Patent Application
20160186102
Disclosed are compositions and methods relating to α-amylase enzymes from a subset of Exiguobacterium. The α-amylases are useful, for example, for starch liquefaction and saccharification, cleaning starchy stains, textile desizing, baking, and brewing.
Starch consists of a mixture of amylose (15-30% w/w) and amylopectin (70-85% w/w). Amylose consists of linear chains of α-1,4-linked glucose units having a molecular weight (MW) from about 60,000 to about 800,000. Amylopectin is a branched polymer containing α-1,6 branch points every 24-30 glucose units; its MW may be as high as 100 million.
α-amylases hydrolyze starch, glycogen, and related polysaccharides by cleaving internal α-1,4-glucosidic bonds at random. α-amylases, particularly from Bacilli, have been used for a variety of different purposes, including starch liquefaction and saccharification, textile desizing, starch modification in the paper and pulp industry, brewing, baking, production of syrups for the food industry, production of feedstocks for fermentation processes, and in animal feed to increase digestability. α-amylases have also been used to remove starchy soils and stains during dishwashing and laundry washing.
The present compositions and methods relate to α-amylase polypeptides, and methods of use, thereof. Aspects and embodiments of the present compositions and methods are summarized in the following separately-numbered paragraphs:
1. In one aspect, a recombinant Exiguobacterium Group II-like α-amylase is provided, having α-amylase activity and comprising at least two of the following structural features: (i) the amino acid sequence X1NLRGKGIG at residues corresponding to positions 89-97, where X1 is S or T; (ii) the amino acid sequence ADSLGL at residues corresponding to positions 223-228; (iii) the amino acid sequence QX2TGK at residues corresponding to positions 253-257, where X2 is A or T; (iv) the amino acid sequence GYTH at residues corresponding to positions 281-284; and/or; (v) the amino acid sequence VX3DRX4K at residues corresponding to positions 419-224, where X3 is T, S, or A and X4 is A or T; wherein any one of SEQ ID NOs: 1-4, 9-11, and 15-17 are used for numbering; wherein the recombinant α-amylase does not have an amino acid sequence identical to any of SEQ ID NOs: 1, 3, 11 or, 15; and wherein optionally the recombinant α-amylase has at least 95% amino acid sequence identity to SEQ ID NO: 4 or at least 96% amino acid sequence identity to SEQ ID NO: 11.
2. In some embodiments, the α-amylase of paragraph 1, comprises: (i) an amino acid sequence having at least 80% amino acid sequence identity to the amino acid sequence of any one of SEQ ID NOs: 1-4, 9-11, and 15-17; (ii) an amino acid sequence derived from a parental α-amylase having at least 80% amino acid sequence identity to the amino acid sequence of any one of SEQ ID NOs: 1-4, 9-11, and 15-17 by amino acid substitution, deletion or insertion; (iii) an amino acid sequence that differs from the amino acid sequence of any one of SEQ ID NOs: 1-4, 9-11, and 15-17 by one or a few residues; or (iv) an amino acid sequence that is derived from a parental α-amylase having the amino acid sequence of any one of SEQ ID NOs: 1-4, 9-11, and 15-17 by substitution, deletion or insertion of one or a few residues.
3. In some embodiments, the α-amylase of paragraph 1 or 2, further comprised a deletion of one of more residues corresponding to K179, S180, T181, or G182, and/or the substitutions S242Q, E188P, and/or G477K, refering to any one of SEQ ID NOs: 1-4, 9-11, and 15-17 for numbering.
4. In some embodiments, the α-amylase of any of paragraphs 1-3, is encoded by a nucleic acid that hybridizes under stringent conditions to a nucleic acid that is complementary to a nucleic acid that encodes any one of SEQ ID NOs: 1-4, 9-11, and 15-17.
5. In some embodiments, the α-amylase of any of paragraphs 1-4, is encoded by a nucleic acid that hybridizes under stringent conditions to a nucleic acid that is complementary to the nucleic acid of any of SEQ ID NOs: 18-23.
6. In another apsect, a composition comprising the α-amylase of any of paragraphs 1-5 is provided.
7. In some embodiments, the composition of paragraph 6 further comprises a surfactant.
8. In some embodiments, the composition of paragraph 6 or 7 is a detergent composition.
9. In some embodiments, the composition of any of paragraphs 6-8 is a laundry detergent, a laundry detergent additive, or a manual or automatic dishwashing detergent.
10. In some embodiments, the composition of any of paragraphs 6-9 further comprises one or more additional enzymes selected from the group consisting of protease, hemicellulase, cellulase, peroxidase, lipolytic enzyme, metallolipolytic enzyme, xylanase, lipase, phospholipase, esterase, perhydrolase, cutinase, pectinase, pectate lyase, mannanase, keratinase, reductase, oxidase, phenoloxidase, lipoxygenase, ligninase, pullulanase, tannase, pentosanase, malanase, β-glucanase, arabinosidase, hyaluronidase, chondroitinase, laccase, metalloproteinase, amadoriase and an amylase other than a recombinant Exiguobacterium α-amylase.
11. In some embodiments, the composition of paragraph 6 is for saccharifying a composition comprising starch, for SSF post liquefaction, or for direct SSF without prior liquefaction.
12. In some embodiments, the composition of paragraph 6 is for producing a fermented beverage or a baked food product.
13. In some embodiments, the composition of paragraph 6 or 7 is for textile desizing.
14. In another apsect, a recombinant polynucleotide encoding a polypeptide of any of paragraphs 1-5 is provided.
15. In some embodiments, the polynucleotide of paragraph 14 has at least 80% nucleic acid sequence identity to the polynucleotide of any one of SEQ ID NOs: 18-23.
16. In another aspect, an expression vector comprising the polynucleotide of paragraph 14 or 15 is provided.
17. In another apsect, a host cell comprising the expression vector of paragraph 16 is provided.
18. In another apsect, the use of the α-amylase of any of paragraphs 1-5 in the production of a composition comprising glucose, in the production of a liquefied starch, in the production of a foodstuff or beverage, in cleaning starchy stains, or in textile desizing is provided.
19. In another aspect, a method for removing a starchy stain or soil from a surface is provided, comprising: contacting the surface with a composition comprising an effective amount of a recombinant Exiguobacterium Group II-like α-amylase of any of paragraphs 1-5; and allowing the α-amylase to hydrolyze starch components present in the starchy stain to produce smaller starch-derived molecules that dissolve in aqueous solution; thereby removing the starchy stain from the surface.
20. In some embodiments of the method of paragraph 19 the aqueous composition further comprises a surfactant.
21. In some embodiments of the method of paragraph 19 or 20 the surface is a textile surface or a surface on dishware.
22. In some embodiments, of the method for any of paragraphs 19-21, the composition further comprises at least one additional enzymes selected from the group consisting of protease, hemicellulase, cellulase, peroxidase, lipolytic enzyme, metallolipolytic enzyme, xylanase, lipase, phospholipase, esterase, perhydrolase, cutinase, pectinase, pectate lyase, mannanase, keratinase, reductase, oxidase, phenoloxidase, lipoxygenase, ligninase, pullulanase, tannase, pentosanase, malanase, β-glucanase, arabinosidase, hyaluronidase, chondroitinase, laccase, metalloproteinase, amadoriase, and an amylase other than an Exiguobacterium Group II-like α-amylase.
23. In another aspect, a method for desizing a textile is provided, comprising: contacting a sized textile with an effective amount of an Exiguobacterium Group II-like α-amylase of any of paragraphs 1-5; and allowing the α-amylase to hydrolyze starch components in the size to produce smaller starch-derived molecules that dissolve in aqueous solution; thereby removing the size from the textile.
24. In another aspect, a method for saccharifying a composition comprising starch to produce a composition comprising glucose is provided, the method comprising: contacting the composition comprising starch with effective amount of an Exiguobacterium Group II-like α-amylase of any of paragraphs 1-5; and saccharifying the composition comprising starch to produce the composition comprising glucose; wherein the α-amylase catalyzes the saccharification of the starch solution to glucose.
25. In some embodiments of the method of paragraph 24 the composition comprising starch comprises liquefied starch, gelatinized starch, or granular starch.
26. In another aspect, a method for preparing a foodstuff or beverage is provided, comprising: contacting a foodstuff or beverage comprising starch with an Exiguobacterium Group II-like α-amylase of any of paragraphs 1-5; and allowing the α-amylase to hydrolyze the starch to produce smaller starch-derived molecules.
27. In some embodiments, the method of paragraph 26 further comprises contacting the foodstuff or beverage with glucoamylase, hexokinase, xylanase, glucose isomerase, xylose isomerase, phosphatase, phytase, pullulanase, β-amylase, α-amylase that is not the variant α-amylase, protease, cellulase, hemicellulase, lipase, cutinase, isoamylase, redox enzyme, esterase, transferase, pectinase, α-glucosidase, beta-glucosidase, or a combination thereof.
28. In some embodiments of the method of any one of paragraphs 19-27 the α-amylase is expressed and secreted by a host cell.
29. In some embodiments of the method of paragraph 28 the composition comprising starch is contacted with the host cell.
30. In some embodiments of the method of paragraph 28 or 29 the host cell further expresses and secretes a glucoamylase or other enzyme.
31. In some embodiments of the method of any one of paragraphs 28-30 the host cell is capable of fermenting the composition.
32. In another aspect, a composition comprising glucose produced by the method of any one of paragraphs 24-31 is provided.
33. In another aspect, liquefied starch produced by the method of any one of paragraphs 24-31 is provided.
34. In another aspect, a foodstuff or beverage produced by the method of any one of paragraphs 26-31 is provided.
These and other aspects and embodiments of the compositions and methods will be apparent from the present description and drawings.
Described are compositions and methods relating to α-amylase enzymes from a subset of Exiguobacterium. Exemplary applications for the α-amylase enzymes are for starch liquefaction and saccharification, for cleaning starchy stains in laundry, dishwashing, and other applications, for textile processing (e.g., desizing), in animal feed for improving digestibility, and for baking and brewing. These and other aspects of the compositions and methods are described in detail, below.
Prior to describing the various aspects and embodiments of the present compositions and methods, the following definitions and abbreviations are described.
In accordance with this detailed description, the following abbreviations and definitions apply. Note that the singular forms “a,” “an,” and “the” include plural referents unless the context clearly dictates otherwise. Thus, for example, reference to “an enzyme” includes a plurality of such enzymes, and reference to “the dosage” includes reference to one or more dosages and equivalents thereof known to those skilled in the art, and so forth.
The present document is organized into a number of sections for ease of reading; however, the reader will appreciate that statements made in one section may apply to other sections. In this manner, the headings used for different sections of the disclosure should not be construed as limiting.
Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art. The following terms are provided below.
1.1. Abbreviations and Acronyms
The following abbreviations/acronyms have the following meanings unless otherwise specified:
ABTS 2,2-azino-bis-3-ethylbenzothiazoline-6-sulfonic acid
AE or AEO alcohol ethoxylate
AES or AEOS alcohol ethoxysulfate
AkAA Aspergillus kawachii α-amylase
AnGA Aspergillus niger glucoamylase
AOS α-olefinsulfonate
AS alkyl sulfate
cDNA complementary DNA
CMC carboxymethylcellulose
DE dextrose equivalent
DNA deoxyribonucleic acid
DPn degree of saccharide polymerization having n subunits
ds or DS dry solids
DTMPA diethylenetriaminepentaacetic acid
EC Enzyme Commission
EDTA ethylenediaminetetraacetic acid
EO ethylene oxide (polymer fragment)
EOF End of Fermentation
GA glucoamylase
GAU/g ds glucoamylase activity unit/gram dry solids
HFCS high fructose corn syrup
HgGA Humicola grisea glucoamylase
IPTG isopropyl β-D-thiogalactoside
IRS insoluble residual starch
kDa kiloDalton
LAS linear alkylbenzenesulfonate
LAT, BLA B. licheniformis amylase
MW molecular weight
MWU modified Wohlgemuth unit; 1.6×10−5 mg/MWU=unit of activity
NCBI National Center for Biotechnology Information
NOBS nonanoyloxybenzenesulfonate
NTA nitriloacetic acid
OxAm Purastar HPAM 5000L (Danisco US Inc.)
PAHBAH p-hydroxybenzoic acid hydrazide
PEG polyethyleneglycol
pI isoelectric point
PI performance index
ppm parts per million, e.g., μg protein per gram dry solid
PVA poly(vinyl alcohol)
PVP poly(vinylpyrrolidone)
RCF relative centrifugal/centripetal force (i.e., x gravity)
RNA ribonucleic acid
SAS alkanesulfonate
SDS-PAGE sodium dodecyl sulfate polyacrylamide gel electrophoresis
SSF simultaneous saccharification and fermentation
SSU/g solid soluble starch unit/gram dry solids
sp. species
TAED tetraacetylethylenediamine
Tm melting temperature
TrGA Trichoderma reesei glucoamylase
w/v weight/volume
w/w weight/weight
v/v volume/volume
wt % weight percent
° C. degrees Centigrade
H2O water
dH2O or DI deionized water
dIH2O deionized water, Milli-Q filtration
g or gm grams
μg micrograms
mg milligrams
kg kilograms
μL and μl microliters
mL and ml milliliters
mm millimeters
μm micrometer
M molar
mM millimolar
μM micromolar
U units
sec seconds
min(s) minute/minutes
hr(s) hour/hours
DO dissolved oxygen
Ncm Newton centimeter
ETOH ethanol
eq. equivalents
N normal
MWCO molecular weight cut-off
SSRL Stanford Synchrotron Radiation Lightsource
PDB Protein Database
CAZy Carbohydrate-Active Enzymes database
Tris-HCl tris(hydroxymethyl)aminomethane hydrochloride
HEPES 4-(2-hydroxyethyl)-1-piperazineethanesulfonic acid
mS/cm milli-Siemens/cm
CV column volumes
1.2. Definitions
The terms “amylase” or “amylolytic enzyme” refer to an enzyme that is, among other things, capable of catalyzing the degradation of starch. α-amylases are hydrolases that cleave the α-D-(1→4) 0-glycosidic linkages in starch. Generally, α-amylases (EC 3.2.1.1; α-D-(1→4)-glucan glucanohydrolase) are defined as endo-acting enzymes cleaving α-D-(1→4) 0-glycosidic linkages within the starch molecule in a random fashion yielding polysaccharides containing three or more (1-4)-α-linked D-glucose units. In contrast, the exo-acting amylolytic enzymes, such as β-amylases (EC 3.2.1.2; α-D-(1→4)-glucan maltohydrolase) and some product-specific amylases like maltogenic α-amylase (EC 3.2.1.133) cleave the polysaccharide molecule from the non-reducing end of the substrate. β-amylases, α-glucosidases (EC 3.2.1.20; α-D-glucoside glucohydrolase), glucoamylase (EC 3.2.1.3; α-D-(1→4)-glucan glucohydrolase), and product-specific amylases like the maltotetraosidases (EC 3.2.1.60) and the maltohexaosidases (EC 3.2.1.98) can produce malto-oligosaccharides of a specific length or enriched syrups of specific maltooligosaccharides.
“Enzyme units” herein refer to the amount of product formed per time under the specified conditions of the assay. For example, a “glucoamylase activity unit” (GAU) is defined as the amount of enzyme that produces 1 g of glucose per hour from soluble starch substrate (4% DS) at 60° C., pH 4.2. A “soluble starch unit” (SSU) is the amount of enzyme that produces 1 mg of glucose per minute from soluble starch substrate (4% DS) at pH 4.5, 50° C. DS refers to “dry solids.”
The term “starch” refers to any material comprised of the complex polysaccharide carbohydrates of plants, comprised of amylose and amylopectin with the formula (C6H10O5)x, wherein X can be any number. The term includes plant-based materials such as grains, cereal, grasses, tubers and roots, and more specifically materials obtained from wheat, barley, corn, rye, rice, sorghum, brans, cassava, millet, milo, potato, sweet potato, and tapioca. The term “starch” includes granular starch. The term “granular starch” refers to raw, i.e., uncooked starch, e.g., starch that has not been subject to gelatinization.
The terms, “wild-type,” “parental,” or “reference,” with respect to a polypeptide, refer to a naturally-occurring polypeptide that does not include a man-made substitution, insertion, or deletion at one or more amino acid positions. Similarly, the terms “wild-type,” “parental,” or “reference,” with respect to a polynucleotide, refer to a naturally-occurring polynucleotide that does not include a man-made nucleoside change. However, note that a polynucleotide encoding a wild-type, parental, or reference polypeptide is not limited to a naturally-occurring polynucleotide, and encompasses any polynucleotide encoding the wild-type, parental, or reference polypeptide.
Reference to the wild-type polypeptide is understood to include the mature form of the polypeptide. A “mature” polypeptide or variant, thereof, is one in which a signal sequence is absent, for example, cleaved from an immature form of the polypeptide during or following expression of the polypeptide.
The term “variant,” with respect to a polypeptide, refers to a polypeptide that differs from a specified wild-type, parental, or reference polypeptide in that it includes one or more naturally-occurring or man-made substitutions, insertions, or deletions of an amino acid. Similarly, the term “variant,” with respect to a polynucleotide, refers to a polynucleotide that differs in nucleotide sequence from a specified wild-type, parental, or reference polynucleotide. The identity of the wild-type, parental, or reference polypeptide or polynucleotide will be apparent from context.
In the case of the present α-amylases, “activity” refers to α-amylase activity, which can be measured as described, herein.
The term “recombinant,” when used in reference to a subject cell, nucleic acid, protein or vector, indicates that the subject has been modified from its native state. Thus, for example, recombinant cells express genes that are not found within the native (non-recombinant) form of the cell, or express native genes at different levels or under different conditions than found in nature. Recombinant nucleic acids differ from a native sequence by one or more nucleotides and/or are operably linked to heterologous sequences, e.g., a heterologous promoter in an expression vector. Recombinant proteins may differ from a native sequence by one or more amino acids and/or are fused with heterologous sequences. A vector comprising a nucleic acid encoding an amylase is a recombinant vector.
The terms “recovered,” “isolated,” and “separated,” refer to a compound, protein (polypeptides), cell, nucleic acid, amino acid, or other specified material or component that is removed from at least one other material or component with which it is naturally associated as found in nature. An “isolated” polypeptides, thereof, includes, but is not limited to, a culture broth containing secreted polypeptide expressed in a heterologous host cell.
The term “purified” refers to material (e.g., an isolated polypeptide or polynucleotide) that is in a relatively pure state, e.g., at least about 90% pure, at least about 95% pure, at least about 98% pure, or even at least about 99% pure.
The term “enriched” refers to material (e.g., an isolated polypeptide or polynucleotide) that is in about 50% pure, at least about 60% pure, at least about 70% pure, or even at least about 70% pure.
The terms “thermostable” and “thermostability,” with reference to an enzyme, refer to the ability of the enzyme to retain activity after exposure to an elevated temperature. The thermostability of an enzyme, such as an amylase enzyme, is measured by its half-life (t112) given in minutes, hours, or days, during which half the enzyme activity is lost under defined conditions. The half-life may be calculated by measuring residual α-amylase activity following exposure to (i.e., challenge by) an elevated temperature.
A “pH range,” with reference to an enzyme, refers to the range of pH values under which the enzyme exhibits catalytic activity.
The terms “pH stable” and “pH stability,” with reference to an enzyme, relate to the ability of the enzyme to retain activity over a wide range of pH values for a predetermined period of time (e.g., 15 min., 30 min., 1 hour).
The term “amino acid sequence” is synonymous with the terms “polypeptide,” “protein,” and “peptide,” and are used interchangeably. Where such amino acid sequences exhibit activity, they may be referred to as an “enzyme.” The conventional one-letter or three-letter codes for amino acid residues are used, with amino acid sequences being presented in the standard amino-to-carboxy terminal orientation (i.e., N→C).
The term “nucleic acid” encompasses DNA, RNA, heteroduplexes, and synthetic molecules capable of encoding a polypeptide. Nucleic acids may be single stranded or double stranded, and may be chemical modifications. The terms “nucleic acid” and “polynucleotide” are used interchangeably. Because the genetic code is degenerate, more than one codon may be used to encode a particular amino acid, and the present compositions and methods encompass nucleotide sequences that encode a particular amino acid sequence. Unless otherwise indicated, nucleic acid sequences are presented in 5′-to-3′ orientation.
“Hybridization” refers to the process by which one strand of nucleic acid forms a duplex with, i.e., base pairs with, a complementary strand, as occurs during blot hybridization techniques and PCR techniques. Stringent hybridization conditions are exemplified by hybridization under the following conditions: 65° C. and 0.1×SSC (where 1×SSC=0.15 M NaCl, 0.015 M Na3 citrate, pH 7.0). Hybridized, duplex nucleic acids are characterized by a melting temperature (Tm), where one-half of the hybridized nucleic acids are unpaired with the complementary strand. Mismatched nucleotides within the duplex lower the Tm.
A “synthetic” molecule is produced by in vitro chemical or enzymatic synthesis rather than by an organism.
The terms “transformed,” “stably transformed,” and “transgenic,” used with reference to a cell means that the cell contains a non-native (e.g., heterologous) nucleic acid sequence integrated into its genome or carried as an episome that is maintained through multiple generations.
The term “introduced” in the context of inserting a nucleic acid sequence into a cell, means “transfection”, “transformation” or “transduction,” as known in the art.
A “host strain” or “host cell” is an organism into which an expression vector, phage, virus, or other DNA construct, including a polynucleotide encoding a polypeptide of interest (e.g., an amylase) has been introduced. Exemplary host strains are microorganism cells (e.g., bacteria, filamentous fungi, and yeast) capable of expressing the polypeptide of interest and/or fermenting saccharides. The term “host cell” includes protoplasts created from cells.
The term “heterologous” with reference to a polynucleotide or protein refers to a polynucleotide or protein that does not naturally occur in a host cell.
The term “endogenous” with reference to a polynucleotide or protein refers to a polynucleotide or protein that occurs naturally in the host cell.
The term “expression” refers to the process by which a polypeptide is produced based on a nucleic acid sequence. The process includes both transcription and translation.
A “selective marker” or “selectable marker” refers to a gene capable of being expressed in a host to facilitate selection of host cells carrying the gene. Examples of selectable markers include but are not limited to antimicrobials (e.g., hygromycin, bleomycin, or chloramphenicol) and/or genes that confer a metabolic advantage, such as a nutritional advantage on the host cell.
A “vector” refers to a polynucleotide sequence designed to introduce nucleic acids into one or more cell types. Vectors include cloning vectors, expression vectors, shuttle vectors, plasmids, phage particles, cassettes and the like.
An “expression vector” refers to a DNA construct comprising a DNA sequence encoding a polypeptide of interest, which coding sequence is operably linked to a suitable control sequence capable of effecting expression of the DNA in a suitable host. Such control sequences may include a promoter to effect transcription, an optional operator sequence to control transcription, a sequence encoding suitable ribosome binding sites on the mRNA, enhancers and sequences which control termination of transcription and translation.
The term “operably linked” means that specified components are in a relationship (including but not limited to juxtaposition) permitting them to function in an intended manner. For example, a regulatory sequence is operably linked to a coding sequence such that expression of the coding sequence is under control of the regulatory sequences.
A “signal sequence” is a sequence of amino acids attached to the N-terminal portion of a protein, which facilitates the secretion of the protein outside the cell. The mature form of an extracellular protein lacks the signal sequence, which is cleaved off during the secretion process.
“Biologically active” refer to a sequence having a specified biological activity, such an enzymatic activity.
The term “specific activity” refers to the number of moles of substrate that can be converted to product by an enzyme or enzyme preparation per unit time under specific conditions. Specific activity is generally expressed as units (U)/mg of protein.
As used herein, “water hardness” is a measure of the minerals (e.g., calcium and magnesium) present in water.
As used herein, an “effective amount of amylase,” or similar expressions, refers to an amount of amylase sufficient to produce a visible, or otherwise measurable amount of starch hydrolysis in an particular application. Starch hydrolysis may result in, e.g., a visible cleaning of fabrics or dishware, reduced viscosity of a starch slurry or mash, and the like.
A “swatch” is a piece of material such as a fabric that has a stain applied thereto. The material can be, for example, fabrics made of cotton, polyester or mixtures of natural and synthetic fibers. The swatch can further be paper, such as filter paper or nitrocellulose, or a piece of a hard material such as ceramic, metal, or glass. For amylases, the stain is starch based, but can include blood, milk, ink, grass, tea, wine, spinach, gravy, chocolate, egg, cheese, clay, pigment, oil, or mixtures of these compounds.
A “smaller swatch” is a section of the swatch that has been cut with a single hole punch device, or has been cut with a custom manufactured 96-hole punch device, where the pattern of the multi-hole punch is matched to standard 96-well microtiter plates, or the section has been otherwise removed from the swatch. The swatch can be of textile, paper, metal, or other suitable material. The smaller swatch can have the stain affixed either before or after it is placed into the well of a 24-, 48- or 96-well microtiter plate. The smaller swatch can also be made by applying a stain to a small piece of material. For example, the smaller swatch can be a stained piece of fabric ⅝″ or 0.25″ in diameter. The custom manufactured punch is designed in such a manner that it delivers 96 swatches simultaneously to all wells of a 96-well plate. The device allows delivery of more than one swatch per well by simply loading the same 96-well plate multiple times. Multi-hole punch devices can be conceived of to deliver simultaneously swatches to any format plate, including but not limited to 24-well, 48-well, and 96-well plates. In another conceivable method, the soiled test platform can be a bead made of metal, plastic, glass, ceramic, or another suitable material that is coated with the soil substrate. The one or more coated beads are then placed into wells of 96-, 48-, or 24-well plates or larger formats, containing suitable buffer and enzyme.
“A cultured cell material comprising an amylase” or similar language, refers to a cell lysate or supernatant (including media) that includes an amylase as a component. The cell material may be from a heterologous host that is grown in culture for the purpose of producing the amylase.
“Percent sequence identity” means that a particular sequence has at least a certain percentage of amino acid residues identical to those in a specified reference sequence, when aligned using the CLUSTAL W algorithm with default parameters. See Thompson et al. (1994) Nucleic Acids Res. 22:4673-4680. Default parameters for the CLUSTAL W algorithm are:
Deletions are counted as non-identical residues, compared to a reference sequence. Deletions occurring at either termini are included. For example, a variant 500-amino acid residue polypeptide with a deletion of five amino acid residues from the C-terminus would have a percent sequence identity of 99% (495/500 identical residues×100) relative to the parent polypeptide. Such a variant would be encompassed by the language, “a variant having at least 99% sequence identity to the parent.”
“Fused” polypeptide sequences are connected, i.e., operably linked, via a peptide bond between two subject polypeptide sequences.
The term “filamentous fungi” refers to all filamentous forms of the subdivision Eumycotina, particularly Pezizomycotina species.
The term “degree of polymerization” (DP) refers to the number (n) of anhydro-glucopyranose units in a given saccharide. Examples of DP1 are the monosaccharides glucose and fructose. Examples of DP2 are the disaccharides maltose and sucrose. The term “DE,” or “dextrose equivalent,” is defined as the percentage of reducing sugar, i.e., D-glucose, as a fraction of total carbohydrate in a syrup.
The term “dry solids content” (ds) refers to the total solids of a slurry in a dry weight percent basis. The term “slurry” refers to an aqueous mixture containing insoluble solids.
The phrase “simultaneous saccharification and fermentation (SSF)” refers to a process in the production of biochemicals in which a microbial organism, such as an ethanologenic microorganism, and at least one enzyme, such as an amylase, are present during the same process step. SSF includes the contemporaneous hydrolysis of starch substrates (granular, liquefied, or solubilized) to saccharides, including glucose, and the fermentation of the saccharides into alcohol or other biochemical or biomaterial in the same reactor vessel.
An “ethanologenic microorganism” refers to a microorganism with the ability to convert a sugar or oligosaccharide to ethanol.
The term “fermented beverage” refers to any beverage produced by a method comprising a fermentation process, such as a microbial fermentation, e.g., a bacterial and/or fungal fermentation. “Beer” is an example of such a fermented beverage, and the term “beer” is meant to comprise any fermented wort produced by fermentation/brewing of a starch-containing plant material. Often, beer is produced exclusively from malt or adjunct, or any combination of malt and adjunct.
The term “malt” refers to any malted cereal grain, such as malted barley or wheat.
The term “adjunct” refers to any starch and/or sugar containing plant material that is not malt, such as barley or wheat malt. Examples of adjuncts include common corn grits, refined corn grits, brewer's milled yeast, rice, sorghum, refined corn starch, barley, barley starch, dehusked barley, wheat, wheat starch, torrified cereal, cereal flakes, rye, oats, potato, tapioca, cassava and syrups, such as corn syrup, sugar cane syrup, inverted sugar syrup, barley and/or wheat syrups, and the like.
The term “mash” refers to an aqueous slurry of any starch and/or sugar containing plant material, such as grist, e.g., comprising crushed barley malt, crushed barley, and/or other adjunct or a combination thereof, mixed with water later to be separated into wort and spent grains.
The term “wort” refers to the unfermented liquor run-off following extracting the grist during mashing.
“Iodine-positive starch” or “IPS” refers to (1) amylose that is not hydrolyzed after liquefaction and saccharification, or (2) a retrograded starch polymer. When saccharified starch or saccharide liquor is tested with iodine, the high DPn amylose or the retrograded starch polymer binds iodine and produces a characteristic blue color. The saccharide liquor is thus termed “iodine-positive saccharide,” “blue saccharide,” or “blue sac.”
The terms “retrograded starch” or “starch retrogradation” refer to changes that occur spontaneously in a starch paste or gel on ageing.
The term “about” refers to ±15% to the referenced value.
An aspect of the present compositions and methods relates to α-amylase enzymes from bacteria of the genus Exiguobacterium. Exiguobacterium are low G+C content, Gram-positive, facultative anaerobes isolated from diverse environment ranging from ancient Siberian permafrost to hot springs at Yellowstone National Park (Vishnivetskaya, T. A. et al. (2009) Extremophiles_13:541-55). While some Exiguobacterium have been studied, the use of α-amylases from these organisms in industrial applications does not appear to have been contemplated.
The first (1) structural feature is the amino acid sequence X1NLRGKGIG (SEQ ID NO: 24), where X1 is S or T, at residues corresponding to positions 89-97, referring to any of SEQ ID NOs: 1-4, 9-11, and 15-17 for numbering. This sequence represents a significant departure from the corresponding amino acid sequences of Bacillus sp. α-amylases, such as B. licheniformis (KSLHSRDIN; SEQ ID NO: 25) and B. stearothermophilus (QAAHAAGMQ; SEQ ID NO: 26), as well as the amino acid sequences of other known α-amylases.
The second (2) structural feature is the amino acid sequence ADSLGL (SEQ ID NO: 27) at residues corresponding to positions 223-228, referring to any of SEQ ID NOs: 1-4, 9-11, and 15-17 for numbering. This sequence represents a significant departure from the corresponding amino acid sequences of Bacillus sp. α-amylases, such as B. licheniformis (ANELQL; SEQ ID NO: 28) and B. stearothermophilus (VNTTNI; SEQ ID NO: 29), as well as the amino acid sequences of other known α-amylases.
The third (3) structural feature is the amino acid sequence QX2TGK (SEQ ID NO: 30) at residues corresponding to positions 253-257, where X2 is A or T, referring to any of SEQ ID NOs: 1-4, 9-11, and 15-17 for numbering. This sequence represents a significant departure from the corresponding amino acid sequences of Bacillus sp. α-amylases, such as B. licheniformis (EKTGK; SEQ ID NO: 31) and B. stearothermophilus (SQTGK; SEQ ID NO: 32), as well as the amino acid sequences of other known α-amylases.
The fourth (4) structural feature is the amino acid sequence GYTH (SEQ ID NO: 33) at residues corresponding to positions 281-284, referring to any of SEQ ID NOs: 1-4, 9-11, and 15-17 for numbering. This sequence represents a significant departure from the corresponding amino acid sequences of Bacillus sp. α-amylases, such as B. licheniformis (NFNH; SEQ ID NO: 34) and B. stearothermophilus (NGTM or DGTM, depending on the particular molecule; SEQ ID NOs: 35 and 36, respectively), as well as the amino acid sequences of other known α-amylases.
The fifth (5) structural feature is the amino acid sequence VX3DRX4K (SEQ ID NO: 37) at residues corresponding to positions 419-224, where X3 is T, S, or A and X4 is A or T, referring to any of SEQ ID NOs: 1-4, 9-11, and 15-17 for numbering. This sequence represents a significant departure from the corresponding amino acid sequences of Bacillus sp. α-amylases, such as B. licheniformis (DSSVAN; SEQ ID NO: 38) and B. stearothermophilus (VTEKPG; SEQ ID NO: 39), as well as the amino acid sequences of other known α-amylases.
The sixth (6) structural feature is the amino acid sequence KS at residues corresponding to positions 179-180, referring to any of SEQ ID NOs: 1-4, 9-11, and 15-17 for numbering. Only one of the present Exiguobacterium Group II-like α-amylases does not have KS at these positions, specifically the α-amylase have the amino acid sequence of SEQ ID NO: 16, which has RS. Most α-amylases have the amino acid sequence RG at this location, although some α-amylases have RS (e.g., the α-amylase from Bacillus sp. TS-23).
The first five of the above-mentioned structural features are in loops on the surface of Exiguobacterium Group II-like α-amylases, on the back side of the molecule relative to the active site. Without being limited to a theory, it is postulated that these structural features, which generally result in a more negative charge, are responsible for interacting with solvent (which may include surfactant) to direct the amylase molecules to substrate thereby increasing starch hydrolysis. The sixth motif is in the calcium-sodium binding loop between domains one and two, and is postulated to increase the detergent stability of the amylase at low calcium concentrations.
The present Exiguobacterium Group II-like α-amylases preferably include any two or more of the first five structural features, optionally along with the sixth structural feature, for example, features 1 and 2, 1 and 3, 1 and 4, 1 and 5, 2 and 3, 2 and 4, 2 and 5, 3 and 4, 3 and 5, and 4 and 5, features 1, 2, and 3, 1, 2, and 4, 1, 2, and 5, 1, 3, and 4, 1, 3, and 5, 1, 4, and 5, 2, 3, and 4, 2, 3, and 5, 2, 4, and 5, and 3, 4, and 5, features 1, 2, 3, and 4, 1, 2, 3, and 5, 1, 2, 4, and 5, 1, 3, 4, and 5, and 2, 3, 4, and 5, and 1, 2, 3, 4, and 5, all optionally with feature 6.
In some embodiments, the present α-amylases have a defined degree of amino acid sequence identity to any of SEQ ID NOs: 1-17, for example, at least 80%, at least 85%, at least 90%, at least 95%, at least 96%, at least 97%, at least 98%, or even at least 99%, amino acid sequence identity. In some embodiments, the present α-amylase are derived from a parental amylase having a defined degree of amino acid sequence identity to SEQ ID NOs: 1-17, for example, at least 80%, at least 85%, at least 90%, at least 95%, at least 96%, at least 97%, at least 98%, or even at least 99%, amino acid sequence identity.
In some embodiments, the present α-amylases comprise conservative substitution of one or several amino acid residues relative to the amino acid sequence of SEQ ID NOs: 1-17. Exemplary conservative amino acid substitutions are listed in the Table 1. Some conservative mutations can be produced by genetic manpulation, while others are produced by introducing synthetic amino acids into a polypeptide other means.
In some embodiments, the present α-amylases comprises a deletion, substitution, insertion, or addition of one or a few amino acid residues relative to the amino acid sequence of SEQ ID NOs: 1-17. Exemplary deletions, substitutions, and insertions correspond to those that have been made in Bacillus CAZy Family 13 α-amylases. In some embodiments, the present α-amylases are derived from the amino acid sequence of SEQ ID NOs: 1-17 by conservative substitution of one or several amino acid residues. In some embodiments, the present α-amylases are derived from the amino acid sequence of SEQ ID NOs: 1-17 by deletion, substitution, insertion, or addition of one or a few amino acid residues relative to the amino acid sequence of SEQ ID NOs: 1-17. In all cases, the expression “one or a few amino acid residues” refers to 10 or less, i.e., 1, 2, 3, 4, 5, 6, 7, 8, 9, or 10, amino acid residues.
In some embodiments, the present α-amylases are characterized by having a deletion at one or more of positions K179, S180, T181, and G182, referring to any of SEQ ID NOs: 1-4, 9-11, and 15-17, for numbering. In particular embodiments, the deletion is a pair-wise deletion of residues K179 and S180 or T181 and G182, referring to any of SEQ ID NOs: 1-4, 9-11, and 15-17.
In some embodiments, the present α-amylases are characterized by having one or more of the substitutions S242Q, E188P, D188P, and G477K, referring to any of SEQ ID NOs: 1-4, 9-11, and 15-17, for numbering, which substitutions may be in combination with the aforementioned deletions. Examples of Exiguobacterium Group II-like α-amylase having deletions and substitutions include SEQ ID NOs: 5-8. In some embodiments, the present α-amylases are characterized by having one or a few additional N-terminal and/or C-terminal residues that do not adversely affect stability or activity. Examples of Exiguobacterium Group II-like α-amylase having additional N-terminal residues that do not interfere with stability or activity include SEQ ID NOs: 12-14.
In some embodiments, the present α-amylases have a defined amount of amino acid sequence identity to any of SEQ ID NOs: 1-4, 9-11, and 15-17, but expressly exclude the exact amino acid sequences of any of SEQ ID NOs: 1-4, 9-11, and 15-17. Such embodiments exclude α-amylases that occur in nature.
In some embodiments, the present α-amylases are encoded by a nucleic acid that hybridizes under stringent conditions to a nucleic acid sequence that is complementary to a nucleic acid that encodes any of SEQ ID NOs: 1-17.
The present amylases may be “precursor,” “immature,” or “full-length,” in which case they include a signal sequence, or “mature,” in which case they lack a signal sequence. Mature forms of the polypeptides are generally the most useful. Unless otherwise noted, the amino acid residue numbering used herein refers to the mature forms of the respective amylase polypeptides. The present amylase polypeptides may also be truncated to remove the N or C-termini, so long as the resulting polypeptides retain amylase activity.
The present amylase may be a “chimeric” or “hybrid” polypeptide, in that it includes at least a portion of a first amylase polypeptide, and at least a portion of a second amylase polypeptide (such chimeric amylases have recently been “rediscovered” as domain-swap amylases). The present amylases may further include heterologous signal sequence, an epitope to allow tracking or purification, or the like. Exemplary heterologous signal sequences are from B. licheniformis amylase (LAT), B. subtilis (AmyE or AprE), and Streptomyces CelA.
In another aspect, nucleic acids encoding an α-amylase polypeptide is provided. The nucleic acid may encode the amylase having the amino acid sequence of any of SEQ ID NOs: 1-17, or an amylase having a specified degree of amino acid sequence identity to the amylase having the amino acid sequence of any of SEQ ID NOs: 1-17. In some embodiments, the nucleic acid encodes an amylase having at least 80%, at least 81%, at least 82%, at least 83%, at least 84%, at least 85%, at least 86%, at least 87%, at least 88%, at least 89%, at least 90%, at least 91%, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or even at least 99%, amino acid sequence identity to any of SEQ ID NOs: 1-17. In some embodiments, the nucleic acid has at least 80%, at least 85%, at least 90%, at least 95%, or even at least 98% nucleotide sequence identity to any of SEQ ID NOs: 18-23.
In some embodiments, the present compositions and methods include nucleic acids that encode any recombinant Exiguobacterium Group II-like α-amylases having deletions, insertions, or substitutions, such as those mentioned, above. It will be appreciated that due to the degeneracy of the genetic code, a plurality of nucleic acids may encode the same polypeptide.
In another example, the nucleic acid hybridizes under stringent or very stringent conditions to a nucleic acid complementary to a nucleic acid encoding an amylase having at least 80%, at least 81%, at least 82%, at least 83%, at least 84%, at least 85%, at least 86%, at least 87%, at least 88%, at least 89%, at least 90%, at least 91%, at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98%, or even at least 99%, amino acid sequence identity to any of SEQ ID NOs: 1-17. In some embodiments, the nucleic acid hybridizes under stringent or very stringent conditions to a nucleic acid complementary to a nucleic acid having the sequence of any of SEQ ID NOs: 18-23. Such hybridization conditions are described herein but are also well known in the art.
Nucleic acids may encode a “full-length” (“fl” or “FL”) amylase, which includes a signal sequence, only the mature form of an amylase, which lacks the signal sequence, or a truncated form of an amylase, which lacks the N or C-terminus of the mature form. Preferrably, the nucleic acids are of sufficient length to encode an active amylase enzyme.
A nucleic acid that encodes an α-amylase can be operably linked to various promoters and regulators in a vector suitable for expressing the α-amylase in host cells. Exemplary promoters are from B. licheniformis amylase (LAT), B. subtilis (AmyE or AprE), and Streptomyces CelA. Such a nucleic acid can also be linked to other coding sequences, e.g., to encode a chimeric polypeptide.
The present α-amylases can be produced in host cells, for example, by secretion or intracellular expression. A cultured cell material (e.g., a whole-cell broth) comprising an α-amylase can be obtained following secretion of the α-amylase into the cell medium. Optionally, the α-amylase can be isolated from the host cells, or even isolated from the cell broth, depending on the desired purity of the final α-amylase. A gene encoding an α-amylase can be cloned and expressed according to methods well known in the art. Suitable host cells include bacterial, fungal (including yeast and filamentous fungi), and plant cells (including algae). Particularly useful host cells include Aspergillus niger, Aspergillus oryzae or Trichoderma reesei. Other host cells include bacterial cells, e.g., Bacillus subtilis or B. licheniformis, as well as Streptomyces.
The host cell further may express a nucleic acid encoding a homologous or heterologous glucoamylase, i.e., a glucoamylase that is not the same species as the host cell, or one or more other enzymes. The glucoamylase may be a variant glucoamylase, such as one of the glucoamylase variants disclosed in U.S. Pat. No. 8,058,033 (Danisco US Inc.), for example. Additionally, the host may express one or more accessory enzymes, proteins, peptides. These may benefit liquefaction, saccharification, fermentation, SSF etc. processes. Furthermore, the host cell may produce biochemicals in addition to enzymes used to digest the various feedstock(s). Such host cells may be useful for fermentation or simultaneous saccharification and fermentation processes to reduce or eliminate the need to add enzymes.
3.1. Vectors
A DNA construct comprising a nucleic acid encoding α-amylases can be constructed to be expressed in a host cell. Because of the well-known degeneracy in the genetic code, different polynucleotides that encode an identical amino acid sequence can be designed and made with routine skill. It is also well-known in the art to optimize codon use for a particular host cell. Nucleic acids encoding α-amylases can be incorporated into a vector. Vectors can be transferred to a host cell using well-known transformation techniques, such as those disclosed below.
The vector may be any vector that can be transformed into and replicated within a host cell. For example, a vector comprising a nucleic acid encoding an α-amylase can be transformed and replicated in a bacterial host cell as a means of propagating and amplifying the vector. The vector also may be transformed into an expression host, so that the encoding nucleic acids can be expressed as a functional amylase. Host cells that serve as expression hosts can include filamentous fungi, for example. The Fungal Genetics Stock Center (FGSC) Catalogue of Strains lists suitable vectors for expression in fungal host cells. See FGSC, Catalogue of Strains, University of Missouri, at www.fgsc.net (last modified Jan. 17, 2007). A representative vector is pJG153, a promoterless Cre expression vector that can be replicated in a bacterial host. See Harrison et al. (2011) Applied Environ. Microbiol. 77:3916-22. pJG153 can be modified with routine skill to comprise and express a nucleic acid encoding an amylase variant.
A nucleic acid encoding an α-amylase can be operably linked to a suitable promoter, which allows transcription in the host cell. The promoter may be any DNA sequence that shows transcriptional activity in the host cell of choice and may be derived from genes encoding proteins either homologous or heterologous to the host cell. Exemplary promoters for directing the transcription of the DNA sequence encoding an α-amylase, especially in a bacterial host, are the promoter of the lac operon of E. coli, the Streptomyces coelicolor agarase gene dagA or celA promoters, the promoters of the Bacillus licheniformis α-amylase gene (amyL), the promoters of the Bacillus stearothermophilus maltogenic amylase gene (amyM), the promoters of the Bacillus amyloliquefaciens α-amylase (amyQ), the promoters of the Bacillus subtilis xylA and xylB genes etc. For transcription in a fungal host, examples of useful promoters are those derived from the gene encoding Aspergillus oryzae TAKA amylase, Rhizomucor miehei aspartic proteinase, Aspergillus niger neutral α-amylase, A. niger acid stable α-amylase, A. niger glucoamylase, Rhizomucor miehei lipase, A. oryzae alkaline protease, A. oryzae triose phosphate isomerase, or A. nidulans acetamidase. When a gene encoding an amylase is expressed in a bacterial species such as E. coli, a suitable promoter can be selected, for example, from a bacteriophage promoter including a T7 promoter and a phage lambda promoter. Examples of suitable promoters for the expression in a yeast species include but are not limited to the Gal 1 and Gal 10 promoters of Saccharomyces cerevisiae and the Pichia pastoris AOX1 or AOX2 promoters. cbh1 is an endogenous, inducible promoter from T. reesei. See Liu et al. (2008) “Improved heterologous gene expression in Trichoderma reesei by cellobiohydrolase I gene (cbh1) promoter optimization,” Acta Biochim. Biophys. Sin (Shanghai) 40(2): 158-65.
The coding sequence can be operably linked to a signal sequence. The DNA encoding the signal sequence may be the DNA sequence naturally associated with the amylase gene to be expressed or from a different Genus or species. A signal sequence and a promoter sequence comprising a DNA construct or vector can be introduced into a fungal host cell and can be derived from the same source. For example, the signal sequence is the cbh1 signal sequence that is operably linked to a cbh1 promoter.
An expression vector may also comprise a suitable transcription terminator and, in eukaryotes, polyadenylation sequences operably linked to the DNA sequence encoding an α-amylase. Termination and polyadenylation sequences may suitably be derived from the same sources as the promoter.
The vector may further comprise a DNA sequence enabling the vector to replicate in the host cell. Examples of such sequences are the origins of replication of plasmids pUC19, pACYC177, pUB110, pE194, pAMB1, and pIJ702.
The vector may also comprise a selectable marker, e.g., a gene the product of which complements a defect in the isolated host cell, such as the dal genes from B. subtilis or B. licheniformis, or a gene that confers antibiotic resistance such as, e.g., ampicillin, kanamycin, chloramphenicol or tetracycline resistance. Furthermore, the vector may comprise Aspergillus selection markers such as amdS, argB, niaD and xxsC, a marker giving rise to hygromycin resistance, or the selection may be accomplished by co-transformation, such as known in the art. See e.g., International PCT Application WO 91/17243.
Intracellular expression may be advantageous in some respects, e.g., when using certain bacteria or fungi as host cells to produce large amounts of amylase for subsequent enrichment or purification. Extracellular secretion of amylase into the culture medium can also be used to make a cultured cell material comprising the isolated amylase.
The expression vector typically includes the components of a cloning vector, such as, for example, an element that permits autonomous replication of the vector in the selected host organism and one or more phenotypically detectable markers for selection purposes. The expression vector normally comprises control nucleotide sequences such as a promoter, operator, ribosome binding site, translation initiation signal and optionally, a repressor gene or one or more activator genes. Additionally, the expression vector may comprise a sequence coding for an amino acid sequence capable of targeting the amylase to a host cell organelle such as a peroxisome, or to a particular host cell compartment. Such a targeting sequence includes but is not limited to the sequence, SKL. For expression under the direction of control sequences, the nucleic acid sequence of the amylase is operably linked to the control sequences in proper manner with respect to expression.
The procedures used to ligate the DNA construct encoding an amylase, the promoter, terminator and other elements, respectively, and to insert them into suitable vectors containing the information necessary for replication, are well known to persons skilled in the art (see, e.g., Sambrook et al., M
3.2. Transformation and Culture of Host Cells
An isolated cell, either comprising a DNA construct or an expression vector, is advantageously used as a host cell in the recombinant production of an amylase. The cell may be transformed with the DNA construct encoding the enzyme, conveniently by integrating the DNA construct (in one or more copies) in the host chromosome. This integration is generally considered to be an advantage, as the DNA sequence is more likely to be stably maintained in the cell. Integration of the DNA constructs into the host chromosome may be performed according to conventional methods, e.g., by homologous or heterologous recombination. Alternatively, the cell may be transformed with an expression vector as described above in connection with the different types of host cells.
Examples of suitable bacterial host organisms are Gram positive bacterial species such as Bacillaceae including Bacillus subtilis, Bacillus licheniformis, Bacillus lentus, Bacillus brevis, Geobacillus (formerly Bacillus) stearothermophilus, Bacillus alkalophilus, Bacillus amyloliquefaciens, Bacillus coagulans, Bacillus lautus, Bacillus megaterium, and Bacillus thuringiensis; Streptomyces species such as Streptomyces murinus; lactic acid bacterial species including Lactococcus sp. such as Lactococcus lactis; Lactobacillus sp. including Lactobacillus reuteri; Leuconostoc sp.; Pediococcus sp.; and Streptococcus sp. Alternatively, strains of a Gram negative bacterial species belonging to Enterobacteriaceae including E. coli, or to Pseudomonadaceae can be selected as the host organism.
A suitable yeast host organism can be selected from the biotechnologically relevant yeasts species such as but not limited to yeast species such as Pichia sp., Hansenula sp., or Kluyveromyces, Yarrowinia, Schizosaccharomyces species or a species of Saccharomyces, including Saccharomyces cerevisiae or a species belonging to Schizosaccharomyces such as, for example, S. pombe species. A strain of the methylotrophic yeast species, Pichia pastoris, can be used as the host organism. Alternatively, the host organism can be a Hansenula species. Suitable host organisms among filamentous fungi include species of Aspergillus, e.g., Aspergillus niger, Aspergillus oryzae, Aspergillus tubigensis, Aspergillus awamori, or Aspergillus nidulans. Alternatively, strains of a Fusarium species, e.g., Fusarium oxysporum or of a Rhizomucor species such as Rhizomucor miehei can be used as the host organism. Other suitable strains include Thermomyces and Mucor species. In addition, Trichoderma sp. can be used as a host. A suitable procedure for transformation of Aspergillus host cells includes, for example, that described in EP 238023. An amylase expressed by a fungal host cell can be glycosylated, i.e., will comprise a glycosyl moiety. The glycosylation pattern can be the same or different as present in the wild-type amylase. The type and/or degree of glycosylation may impart changes in enzymatic and/or biochemical properties.
It is advantageous to delete genes from expression hosts, where the gene deficiency can be cured by the transformed expression vector. Known methods may be used to obtain a fungal host cell having one or more inactivated genes. Gene inactivation may be accomplished by complete or partial deletion, by insertional inactivation or by any other means that renders a gene nonfunctional for its intended purpose, such that the gene is prevented from expression of a functional protein. Any gene from a Trichoderma sp. or other filamentous fungal host that has been cloned can be deleted, for example, cbh1, cbh2, egl1, and egl2 genes. Gene deletion may be accomplished by inserting a form of the desired gene to be inactivated into a plasmid by methods known in the art.
Introduction of a DNA construct or vector into a host cell includes techniques such as transformation; electroporation; nuclear microinjection; transduction; transfection, e.g., lipofection mediated and DEAE-Dextrin mediated transfection; incubation with calcium phosphate DNA precipitate; high velocity bombardment with DNA-coated microprojectiles; and protoplast fusion. General transformation techniques are known in the art. See, e.g., Sambrook et al. (2001), supra. The expression of heterologous protein in Trichoderma is described, for example, in U.S. Pat. No. 6,022,725. Reference is also made to Cao et al. (2000) Science 9:991-1001 for transformation of Aspergillus strains. Genetically stable transformants can be constructed with vector systems whereby the nucleic acid encoding an amylase is stably integrated into a host cell chromosome. Transformants are then selected and purified by known techniques.
The preparation of Trichoderma sp. for transformation, for example, may involve the preparation of protoplasts from fungal mycelia. See Campbell et al. (1989) Curr. Genet. 16: 53-56. The mycelia can be obtained from germinated vegetative spores. The mycelia are treated with an enzyme that digests the cell wall, resulting in protoplasts. The protoplasts are protected by the presence of an osmotic stabilizer in the suspending medium. These stabilizers include sorbitol, mannitol, potassium chloride, magnesium sulfate, and the like. Usually the concentration of these stabilizers varies between 0.8 M and 1.2 M, e.g., a 1.2 M solution of sorbitol can be used in the suspension medium.
Uptake of DNA into the host Trichoderma sp. strain depends upon the calcium ion concentration. Generally, between about 10-50 mM CaCl2 is used in an uptake solution. Additional suitable compounds include a buffering system, such as TE buffer (10 mM Tris, pH 7.4; 1 mM EDTA) or 10 mM MOPS, pH 6.0 and polyethylene glycol. The polyethylene glycol is believed to fuse the cell membranes, thus permitting the contents of the medium to be delivered into the cytoplasm of the Trichoderma sp. strain. This fusion frequently leaves multiple copies of the plasmid DNA integrated into the host chromosome.
Usually transformation of Trichoderma sp. uses protoplasts or cells that have been subjected to a permeability treatment, typically at a density of 105 to 107/mL, particularly 2×106/mL. A volume of 100 μL of these protoplasts or cells in an appropriate solution (e.g., 1.2 M sorbitol and 50 mM CaCl2) may be mixed with the desired DNA. Generally, a high concentration of PEG is added to the uptake solution. From 0.1 to 1 volume of 25% PEG 4000 can be added to the protoplast suspension; however, it is useful to add about 0.25 volumes to the protoplast suspension. Additives, such as dimethyl sulfoxide, heparin, spermidine, potassium chloride and the like, may also be added to the uptake solution to facilitate transformation. Similar procedures are available for other fungal host cells. See, e.g., U.S. Pat. No. 6,022,725.
3.3. Expression
A method of producing an amylase may comprise cultivating a host cell as described above under conditions conducive to the production of the enzyme and recovering the enzyme from the cells and/or culture medium.
The medium used to cultivate the cells may be any conventional medium suitable for growing the host cell in question and obtaining expression of an amylase. Suitable media and media components are available from commercial suppliers or may be prepared according to published recipes (e.g., as described in catalogues of the American Type Culture Collection).
An enzyme secreted from the host cells can be used in a whole broth preparation. In the present methods, the preparation of a spent whole fermentation broth of a recombinant microorganism can be achieved using any cultivation method known in the art resulting in the expression of an α-amylase. Fermentation may, therefore, be understood as comprising shake flask cultivation, small- or large-scale fermentation (including continuous, batch, fed-batch, or solid state fermentations) in laboratory or industrial fermenters performed in a suitable medium and under conditions allowing the amylase to be expressed or isolated. The term “spent whole fermentation broth” is defined herein as unfractionated contents of fermentation material that includes culture medium, extracellular proteins (e.g., enzymes), and cellular biomass. It is understood that the term “spent whole fermentation broth” also encompasses cellular biomass that has been lysed or permeabilized using methods well known in the art.
An enzyme secreted from the host cells may conveniently be recovered from the culture medium by well-known procedures, including separating the cells from the medium by centrifugation or filtration, and precipitating proteinaceous components of the medium by means of a salt such as ammonium sulfate, followed by the use of chromatographic procedures such as ion exchange chromatography, affinity chromatography, or the like.
The polynucleotide encoding an amylase in a vector can be operably linked to a control sequence that is capable of providing for the expression of the coding sequence by the host cell, i.e. the vector is an expression vector. The control sequences may be modified, for example by the addition of further transcriptional regulatory elements to make the level of transcription directed by the control sequences more responsive to transcriptional modulators. The control sequences may in particular comprise promoters.
Host cells may be cultured under suitable conditions that allow expression of an amylase. Expression of the enzymes may be constitutive such that they are continually produced, or inducible, requiring a stimulus to initiate expression. In the case of inducible expression, protein production can be initiated when required by, for example, addition of an inducer substance to the culture medium, for example dexamethasone or IPTG or Sophorose. Polypeptides can also be produced recombinantly in an in vitro cell-free system, such as the TNT™ (Promega) rabbit reticulocyte system.
An expression host also can be cultured in the appropriate medium for the host, under aerobic conditions. Shaking or a combination of agitation and aeration can be provided, with production occurring at the appropriate temperature for that host, e.g., from about 25° C. to about 75° C. (e.g., 30° C. to 45° C.), depending on the needs of the host and production of the desired α-amylase. Culturing can occur from about 12 to about 100 hours or greater (and any hour value there between, e.g., from 24 to 72 hours). Typically, the culture broth is at a pH of about 4.0 to about 8.0, again depending on the culture conditions needed for the host relative to production of an amylase.
3.4. Identification of Amylase Activity
To evaluate the expression of an amylase in a host cell, assays can measure the expressed protein, corresponding mRNA, or α-amylase activity. For example, suitable assays include Northern blotting, reverse transcriptase polymerase chain reaction, and in situ hybridization, using an appropriately labeled hybridizing probe. Suitable assays also include measuring amylase activity in a sample, for example, by assays directly measuring reducing sugars such as glucose in the culture media. For example, glucose concentration may be determined using glucose reagent kit No. 15-UV (Sigma Chemical Co.) or an instrument, such as Technicon Autoanalyzer. α-Amylase activity also may be measured by any known method, such as the PAHBAH or ABTS assays, described below.
3.5. Methods for Enriching and Purifying α-Amylases
Fermentation, separation, and concentration techniques are well known in the art and conventional methods can be used in order to prepare a concentrated an α-α-amylase polypeptide-containing solution.
After fermentation, a fermentation broth is obtained, the microbial cells and various suspended solids, including residual raw fermentation materials, are removed by conventional separation techniques in order to obtain an amylase solution. Filtration, centrifugation, microfiltration, rotary vacuum drum filtration, ultrafiltration, centrifugation followed by ultrafiltration, extraction, or chromatography, or the like, are generally used.
It is desirable to concentrate an α-amylase polypeptide-containing solution in order to optimize recovery. Use of unconcentrated solutions requires increased incubation time in order to collect the enriched or purified enzyme precipitate.
The enzyme containing solution is concentrated using conventional concentration techniques until the desired enzyme level is obtained. Concentration of the enzyme containing solution may be achieved by any of the techniques discussed herein. Exemplary methods of enrichment and purification include but are not limited to rotary vacuum filtration and/or ultrafiltration.
The enzyme solution is concentrated into a concentrated enzyme solution until the enzyme activity of the concentrated α-amylase polypeptide-containing solution is at a desired level.
Concentration may be performed using, e.g., a precipitation agent, such as a metal halide precipitation agent. Metal halide precipitation agents include but are not limited to alkali metal chlorides, alkali metal bromides and blends of two or more of these metal halides. Exemplary metal halides include sodium chloride, potassium chloride, sodium bromide, potassium bromide and blends of two or more of these metal halides. The metal halide precipitation agent, sodium chloride, can also be used as a preservative.
The metal halide precipitation agent is used in an amount effective to precipitate an amylase. The selection of at least an effective amount and an optimum amount of metal halide effective to cause precipitation of the enzyme, as well as the conditions of the precipitation for maximum recovery including incubation time, pH, temperature and concentration of enzyme, will be readily apparent to one of ordinary skill in the art, after routine testing.
Generally, at least about 5% w/v (weight/volume) to about 25% w/v of metal halide is added to the concentrated enzyme solution, and usually at least 8% w/v. Generally, no more than about 25% w/v of metal halide is added to the concentrated enzyme solution and usually no more than about 20% w/v. The optimal concentration of the metal halide precipitation agent will depend, among others, on the nature of the specific α-amylase polypeptide and on its concentration in the concentrated enzyme solution.
Another alternative way to precipitate the enzyme is to use organic compounds. Exemplary organic compound precipitating agents include: 4-hydroxybenzoic acid, alkali metal salts of 4-hydroxybenzoic acid, alkyl esters of 4-hydroxybenzoic acid, and blends of two or more of these organic compounds. The addition of the organic compound precipitation agents can take place prior to, simultaneously with or subsequent to the addition of the metal halide precipitation agent, and the addition of both precipitation agents, organic compound and metal halide, may be carried out sequentially or simultaneously.
Generally, the organic precipitation agents are selected from the group consisting of alkali metal salts of 4-hydroxybenzoic acid, such as sodium or potassium salts, and linear or branched alkyl esters of 4-hydroxybenzoic acid, wherein the alkyl group contains from 1 to 12 carbon atoms, and blends of two or more of these organic compounds. The organic compound precipitation agents can be, for example, linear or branched alkyl esters of 4-hydroxybenzoic acid, wherein the alkyl group contains from 1 to 10 carbon atoms, and blends of two or more of these organic compounds. Exemplary organic compounds are linear alkyl esters of 4-hydroxybenzoic acid, wherein the alkyl group contains from 1 to 6 carbon atoms, and blends of two or more of these organic compounds. Methyl esters of 4-hydroxybenzoic acid, propyl esters of 4-hydroxybenzoic acid, butyl ester of 4-hydroxybenzoic acid, ethyl ester of 4-hydroxybenzoic acid and blends of two or more of these organic compounds can also be used. Additional organic compounds also include but are not limited to 4-hydroxybenzoic acid methyl ester (named methyl PARABEN), 4-hydroxybenzoic acid propyl ester (named propyl PARABEN), which also are both amylase preservative agents. For further descriptions, see, e.g., U.S. Pat. No. 5,281,526.
Addition of the organic compound precipitation agent provides the advantage of high flexibility of the precipitation conditions with respect to pH, temperature, α-amylase concentration, precipitation agent concentration, and time of incubation.
The organic compound precipitation agent is used in an amount effective to improve precipitation of the enzyme by means of the metal halide precipitation agent. The selection of at least an effective amount and an optimum amount of organic compound precipitation agent, as well as the conditions of the precipitation for maximum recovery including incubation time, pH, temperature and concentration of enzyme, will be readily apparent to one of ordinary skill in the art, in light of the present disclosure, after routine testing.
Generally, at least about 0.01% w/v of organic compound precipitation agent is added to the concentrated enzyme solution and usually at least about 0.02% w/v. Generally, no more than about 0.3% w/v of organic compound precipitation agent is added to the concentrated enzyme solution and usually no more than about 0.2% w/v.
The concentrated polypeptide solution, containing the metal halide precipitation agent, and the organic compound precipitation agent, can be adjusted to a pH, which will, of necessity, depend on the enzyme to be enriched or purified. Generally, the pH is adjusted at a level near the isoelectric point of the amylase. The pH can be adjusted at a pH in a range from about 2.5 pH units below the isoelectric point (pI) up to about 2.5 pH units above the isoelectric point.
The incubation time necessary to obtain an enriched or purified enzyme precipitate depends on the nature of the specific enzyme, the concentration of enzyme, and the specific precipitation agent(s) and its (their) concentration. Generally, the time effective to precipitate the enzyme is between about 1 to about 30 hours; usually it does not exceed about 25 hours. In the presence of the organic compound precipitation agent, the time of incubation can still be reduced to less about 10 hours and in most cases even about 6 hours.
Generally, the temperature during incubation is between about 4° C. and about 50° C. Usually, the method is carried out at a temperature between about 10° C. and about 45° C. (e.g., between about 20° C. and about 40° C.). The optimal temperature for inducing precipitation varies according to the solution conditions and the enzyme or precipitation agent(s) used.
The overall recovery of enriched or purified enzyme precipitate, and the efficiency with which the process is conducted, is improved by agitating the solution comprising the enzyme, the added metal halide and the added organic compound. The agitation step is done both during addition of the metal halide and the organic compound, and during the subsequent incubation period. Suitable agitation methods include mechanical stirring or shaking, vigorous aeration, or any similar technique.
After the incubation period, the enriched or purified enzyme is then separated from the dissociated pigment and other impurities and collected by conventional separation techniques, such as filtration, centrifugation, microfiltration, rotary vacuum filtration, ultrafiltration, press filtration, cross membrane microfiltration, cross flow membrane microfiltration, or the like. Further enrichment or purification of the enzyme precipitate can be obtained by washing the precipitate with water. For example, the enriched or purified enzyme precipitate is washed with water containing the metal halide precipitation agent, or with water containing the metal halide and the organic compound precipitation agents.
During fermentation, an α-amylase polypeptide accumulates in the culture broth. For the isolation, enrichment, or purification of the desired α-amylase, the culture broth is centrifuged or filtered to eliminate cells, and the resulting cell-free liquid is used for enzyme enrichment or purification. In one embodiment, the cell-free broth is subjected to salting out using ammonium sulfate at about 70% saturation; the 70% saturation-precipitation fraction is then dissolved in a buffer and applied to a column such as a Sephadex G-100 column, and eluted to recover the enzyme-active fraction. For further enrichment or purification, a conventional procedure such as ion exchange chromatography may be used.
Enriched or purified enzymes are useful for laundry and cleaning applications. For example, they can be used in laundry detergents and spot removers. They can be made into a final product that is either liquid (solution, slurry) or solid (granular, powder).
A more specific example of enrichment or purification, is described in Sumitani et al. (2000) “New type of starch-binding domain: the direct repeat motif in the C-terminal region of Bacillus sp. 195 α-amylase contributes to starch binding and raw starch degrading,” Biochem. J. 350: 477-484, and is briefly summarized here. The enzyme obtained from 4 liters of a Streptomyces lividans TK24 culture supernatant was treated with (NH4)2SO4 at 80% saturation. The precipitate was recovered by centrifugation at 10,000×g (20 min. and 4° C.) and re-dissolved in 20 mM Tris/HCl buffer (pH 7.0) containing 5 mM CaCl2. The solubilized precipitate was then dialyzed against the same buffer. The dialyzed sample was then applied to a Sephacryl S-200 column, which had previously been equilibrated with 20 mM Tris/HCl buffer, (pH 7.0), 5 mM CaCl2, and eluted at a linear flow rate of 7 mL/hr with the same buffer. Fractions from the column were collected and assessed for activity as judged by enzyme assay and SDS-PAGE. The protein was further purified as follows. A Toyopearl HW55 column (Tosoh Bioscience, Montgomeryville, Pa.; Cat. No. 19812) was equilibrated with 20 mM Tris/HCl buffer (pH 7.0) containing 5 mM CaCl2 and 1.5 M (NH4)2SO4. The enzyme was eluted with a linear gradient of 1.5 to 0 M (NH4)2SO4 in 20 mM Tris/HCL buffer, pH 7.0 containing 5 mM CaCl2. The active fractions were collected, and the enzyme precipitated with (NH4)2SO4 at 80% saturation. The precipitate was recovered, re-dissolved, and dialyzed as described above. The dialyzed sample was then applied to a Mono Q HR5/5 column (Amersham Pharmacia; Cat. No. 17-5167-01) previously equilibrated with 20 mM Tris/HCl buffer (pH 7.0) containing 5 mM CaCl2, at a flow rate of 60 mL/hour. The active fractions are collected and added to a 1.5 M (NH4)2SO4 solution. The active enzyme fractions were re-chromatographed on a Toyopearl HW55 column, as before, to yield a homogeneous enzyme as determined by SDS-PAGE. See Sumitani et al. (2000) Biochem. J. 350: 477-484, for general discussion of the method and variations thereon.
For production scale recovery, α-amylase polypeptides can be enriched or partially purified as generally described above by removing cells via flocculation with polymers. Alternatively, the enzyme can be enriched or purified by microfiltration followed by concentration by ultrafiltration using available membranes and equipment. However, for some applications, the enzyme does not need to be enriched or purified, and whole broth culture can be lysed and used without further treatment. The enzyme can then be processed, for example, into granules.
4. Compositions and Uses of α-Amylases
The present α-amylases are useful for a variety of industrial applications. For example, α-amylases are useful in a starch conversion process, particularly in a saccharification process of a starch that has undergone liquefaction. The desired end-product may be any product that may be produced by the enzymatic conversion of the starch substrate. For example, the desired product may be a syrup rich in glucose and maltose, which can be used in other processes, such as the preparation of HFCS, or which can be converted into a number of other useful products, such as ascorbic acid intermediates (e.g., gluconate; 2-keto-L-gulonic acid; 5-keto-gluconate; and 2,5-diketogluconate); 1,3-propanediol; aromatic amino acids (e.g., tyrosine, phenylalanine and tryptophan); organic acids (e.g., lactate, pyruvate, succinate, isocitrate, and oxaloacetate); amino acids (e.g., serine and glycine); antibiotics; antimicrobials; enzymes; vitamins; and hormones.
The starch conversion process may be a precursor to, or simultaneous with, a fermentation process designed to produce alcohol for fuel or drinking (i.e., potable alcohol). One skilled in the art is aware of various fermentation conditions that may be used in the production of these end-products. α-amylases are also useful in compositions and methods of food preparation. These various uses of α-amylases are described in more detail below.
4.1. Preparation of Starch Substrates
Those of general skill in the art are well aware of available methods that may be used to prepare starch substrates for use in the processes disclosed herein. For example, a useful starch substrate may be obtained from tubers, roots, stems, legumes, cereals or whole grain.
More specifically, the granular starch may be obtained from corn, cobs, wheat, barley, rye, triticale, milo, sago, millet, cassava, tapioca, sorghum, rice, peas, bean, banana, or potatoes. Corn contains about 60-68% starch; barley contains about 55-65% starch; millet contains about 75-80% starch; wheat contains about 60-65% starch; and polished rice contains 70-72% starch. Specifically contemplated starch substrates are corn starch and wheat starch. The starch from a grain may be ground or whole and includes corn solids, such as kernels, bran and/or cobs. The starch may also be highly refined raw starch or feedstock from starch refinery processes. Various starches also are commercially available. For example, corn starch is available from Cerestar, Sigma, and Katayama Chemical Industry Co. (Japan); wheat starch is available from Sigma; sweet potato starch is available from Wako Pure Chemical Industry Co. (Japan); and potato starch is available from Nakaari Chemical Pharmaceutical Co. (Japan).
The starch substrate can be a crude starch from milled whole grain, which contains non-starch fractions, e.g., germ residues and fibers. Milling may comprise either wet milling or dry milling or grinding. In wet milling, whole grain is soaked in water or dilute acid to separate the grain into its component parts, e.g., starch, protein, germ, oil, kernel fibers. Wet milling efficiently separates the germ and meal (i.e., starch granules and protein) and is especially suitable for production of syrups. In dry milling or grinding, whole kernels are ground into a fine powder and often processed without fractionating the grain into its component parts. In some cases, oils from the kernels are recovered. Dry ground grain thus will comprise significant amounts of non-starch carbohydrate compounds, in addition to starch. Dry grinding of the starch substrate can be used for production of ethanol and other biochemicals. The starch to be processed may be a highly refined starch quality, for example, at least 90%, at least 95%, at least 97%, or at least 99.5% pure.
4.2. Gelatinization and Liquefaction of Starch
As used herein, the term “liquefaction” or “liquefy” means a process by which starch is converted to less viscous and shorter chain dextrins. Generally, this process involves gelatinization of starch simultaneously with or followed by the addition of an α-amylase, although additional liquefaction-inducing enzymes optionally may be added. In some embodiments, the starch substrate prepared as described above is slurried with water. The starch slurry may contain starch as a weight percent of dry solids of about 10-55%, about 20-45%, about 30-45%, about 30-40%, or about 30-35%. α-Amylase (EC 3.2.1.1) may be added to the slurry, with a metering pump, for example. The α-amylase typically used for this application is a thermally stable, bacterial α-amylase, such as a Geobacillus stearothermophilus α-amylase. The α-amylase is usually supplied, for example, at about 1500 units per kg dry matter of starch. To optimize α-amylase stability and activity, the pH of the slurry typically is adjusted to about pH 5.5-6.5 and about 1 mM of calcium (about 40 ppm free calcium ions) can also be added. Geobacillus stearothermophilus variants or other α-amylases may require different conditions. Bacterial α-amylase remaining in the slurry following liquefaction may be deactivated via a number of methods, including lowering the pH in a subsequent reaction step or by removing calcium from the slurry in cases where the enzyme is dependent upon calcium.
The slurry of starch plus the α-amylase may be pumped continuously through a jet cooker, which is steam heated to 105° C. Gelatinization occurs rapidly under these conditions, and the enzymatic activity, combined with the significant shear forces, begins the hydrolysis of the starch substrate. The residence time in the jet cooker is brief. The partly gelatinized starch may be passed into a series of holding tubes maintained at 105-110° C. and held for 5-8 min. to complete the gelatinization process (“primary liquefaction”). Hydrolysis to the required DE is completed in holding tanks at 85-95° C. or higher temperatures for about 1 to 2 hours (“secondary liquefaction”). These tanks may contain baffles to discourage back mixing. As used herein, the term “minutes of secondary liquefaction” refers to the time that has elapsed from the start of secondary liquefaction to the time that the Dextrose Equivalent (DE) is measured. The slurry is then allowed to cool to room temperature. This cooling step can be 30 minutes to 180 minutes, e.g. 90 minutes to 120 minutes. The liquefied starch typically is in the form of a slurry having a dry solids content (w/w) of about 10-50%; about 10-45%; about 15-40%; about 20-40%; about 25-40%; or about 25-35%.
Liquefaction with α-amylases advantageously can be conducted at low pH, eliminating the requirement to adjust the pH to about pH 5.5-6.5. α-amylases can be used for liquefaction at a pH range of 2 to 7, e.g., pH 3.0-7.5, pH 4.0-6.0, or pH 4.5-5.8. α-amylases can maintain liquefying activity at a temperature range of about 85° C.-95° C., e.g., 85° C., 90° C., or 95° C. For example, liquefaction can be conducted with 800 μg an amylase in a solution of 25% DS corn starch for 10 min at pH 5.8 and 85° C., or pH 4.5 and 95° C., for example. Liquefying activity can be assayed using any of a number of known viscosity assays in the art.
In particular embodiments using the present α-amylases, starch liquifaction is performed at a temperature range of 90-115° C., for the purpose of producing high-purity glucose syrups, HFCS, maltodextrins, etc.
4.3. Saccharification
The liquefied starch can be saccharified into a syrup rich in lower DP (e.g., DP1+DP2) saccharides, using α-amylases, optionally in the presence of another enzyme(s). The exact composition of the products of saccharification depends on the combination of enzymes used, as well as the type of granular starch processed. Advantageously, the syrup obtainable using the provided α-amylases may contain a weight percent of DP2 of the total oligosaccharides in the saccharified starch exceeding 30%, e.g., 45%-65% or 55%-65%. The weight percent of (DP1+DP2) in the saccharified starch may exceed about 70%, e.g., 75%-85% or 80%-85%. The present amylases also produce a relatively high yield of glucose, e.g., DP1>20%, in the syrup product.
Whereas liquefaction is generally run as a continuous process, saccharification is often conducted as a batch process. Saccharification typically is most effective at temperatures of about 60-65° C. and a pH of about 4.0-4.5, e.g., pH 4.3, necessitating cooling and adjusting the pH of the liquefied starch. Saccharification may be performed, for example, at a temperature between about 40° C., about 50° C., or about 55° C. to about 60° C. or about 65° C. Saccharification is normally conducted in stirred tanks, which may take several hours to fill or empty. Enzymes typically are added either at a fixed ratio to dried solids as the tanks are filled or added as a single dose at the commencement of the filling stage. A saccharification reaction to make a syrup typically is run over about 24-72 hours, for example, 24-48 hours. When a maximum or desired DE has been attained, the reaction is stopped by heating to 85° C. for 5 min., for example.
Further incubation will result in a lower DE, eventually to about 90 DE, as accumulated glucose re-polymerizes to isomaltose and/or other reversion products via an enzymatic reversion reaction and/or with the approach of thermodynamic equilibrium. When using an amylase, saccharification optimally is conducted at a temperature range of about 30° C. to about 75° C., e.g., 45° C.-75° C. or 47° C.-74° C. The saccharifying may be conducted over a pH range of about pH 3 to about pH 7, e.g., pH 3.0-pH 7.5, pH 3.5-pH 5.5, pH 3.5, pH 3.8, or pH 4.5.
An amylase may be added to the slurry in the form of a composition. Amylase can be added to a slurry of a granular starch substrate in an amount of about 0.6-10 ppm ds, e.g., 2 ppm ds. An amylase can be added as a whole broth, clarified, enriched, partially purified, or purified enzyme. The specific activity of the amylase may be about 300 U/mg of enzyme, for example, measured with the PAHBAH assay. The amylase also can be added as a whole broth product.
An amylase may be added to the slurry as an isolated enzyme solution. For example, an amylase can be added in the form of a cultured cell material produced by host cells expressing an amylase. An amylase may also be secreted by a host cell into the reaction medium during the fermentation or SSF process, such that the enzyme is provided continuously into the reaction. The host cell producing and secreting amylase may also express an additional enzyme, such as a glucoamylase. For example, U.S. Pat. No. 5,422,267 discloses the use of a glucoamylase in yeast for production of alcoholic beverages. For example, a host cell, e.g., Trichoderma reesei or Aspergillus niger, may be engineered to co-express an amylase and a glucoamylase, e.g., HgGA, TrGA, or a TrGA variant, during saccharification. The host cell can be genetically modified so as not to express its endogenous glucoamylase and/or other enzymes, proteins or other materials. The host cell can be engineered to express a broad spectrum of various saccharolytic enzymes. For example, the recombinant yeast host cell can comprise nucleic acids encoding a glucoamylase, an alpha-glucosidase, an enzyme that utilizes pentose sugar, an α-amylase, a pullulanase, an isoamylase, and/or an isopullulanase. See, e.g., WO 2011/153516 A2.
4.4. Isomerization
The soluble starch hydrolysate produced by treatment with amylase can be converted into high fructose starch-based syrup (HFSS), such as high fructose corn syrup (HFCS). This conversion can be achieved using a glucose isomerase, particularly a glucose isomerase immobilized on a solid support. The pH is increased to about 6.0 to about 8.0, e.g., pH 7.5 (depending on the isomerase), and Ca2+ is removed by ion exchange. Suitable isomerases include SWEETZYME®, IT (Novozymes A/S); G-ZYME® IMGI, and G-ZYME® G993, KETOMAX®, G-ZYME® G993, G-ZYME® G993 liquid, and GENSWEET® IGI. Following isomerization, the mixture typically contains about 40-45% fructose, e.g., 42% fructose.
4.5. Fermentation
The soluble starch hydrolysate, particularly a glucose rich syrup, can be fermented by contacting the starch hydrolysate with a fermenting organism typically at a temperature around 32° C., such as from 30° C. to 35° C. for alcohol-producing yeast. The temperature and pH of the fermentation will depend upon the fermenting organism. EOF products include metabolites, such as citric acid, lactic acid, succinic acid, monosodium glutamate, gluconic acid, sodium gluconate, calcium gluconate, potassium gluconate, itaconic acid and other carboxylic acids, glucono delta-lactone, sodium erythorbate, lysine and other amino acids, omega 3 fatty acid, butanol, isoprene, 1,3-propanediol and other biomaterials.
Ethanologenic microorganisms include yeast, such as Saccharomyces cerevisiae and bacteria, e.g., Zymomonas moblis, expressing alcohol dehydrogenase and pyruvate decarboxylase. The ethanologenic microorganism can express xylose reductase and xylitol dehydrogenase, which convert xylose to xylulose. Improved strains of ethanologenic microorganisms, which can withstand higher temperatures, for example, are known in the art and can be used. See Liu et al. (2011) Sheng Wu Gong Cheng Xue Bao 27:1049-56. Commercial sources of yeast include ETHANOL RED® (LeSaffre); THERMOSACC® (Lallemand); RED STAR® (Red Star); FERMIOL® (DSM Specialties); and SUPERSTART® (Alltech). Microorganisms that produce other metabolites, such as citric acid and lactic acid, by fermentation are also known in the art. See, e.g., Papagianni (2007) Biotechnol. Adv. 25:244-63; John et al. (2009) Biotechnol. Adv. 27:145-52.
The saccharification and fermentation processes may be carried out as an SSF process. Fermentation may comprise subsequent enrichment, purification, and recovery of ethanol, for example. During the fermentation, the ethanol content of the broth or “beer” may reach about 8-18% v/v, e.g., 14-15% v/v. The broth may be distilled to produce enriched, e.g., 96% pure, solutions of ethanol. Further, CO2 generated by fermentation may be collected with a CO2 scrubber, compressed, and marketed for other uses, e.g., carbonating beverage or dry ice production. Solid waste from the fermentation process may be used as protein-rich products, e.g., livestock feed.
As mentioned above, an SSF process can be conducted with fungal cells that express and secrete amylase continuously throughout SSF. The fungal cells expressing amylase also can be the fermenting microorganism, e.g., an ethanologenic microorganism. Ethanol production thus can be carried out using a fungal cell that expresses sufficient amylase so that less or no enzyme has to be added exogenously. The fungal host cell can be from an appropriately engineered fungal strain. Fungal host cells that express and secrete other enzymes, in addition to amylase, also can be used. Such cells may express glucoamylase and/or a pullulanase, phytase, alpha-glucosidase, isoamylase, beta-amylase cellulase, xylanase, other hemicellulases, protease, beta-glucosidase, pectinase, esterase, redox enzymes, transferase, or other enzyme.
A variation on this process is a “fed-batch fermentation” system, where the substrate is added in increments as the fermentation progresses. Fed-batch systems are useful when catabolite repression may inhibit the metabolism of the cells and where it is desirable to have limited amounts of substrate in the medium. The actual substrate concentration in fed-batch systems is estimated by the changes of measurable factors such as pH, dissolved oxygen and the partial pressure of waste gases, such as CO2. Batch and fed-batch fermentations are common and well known in the art.
Continuous fermentation is an open system where a defined fermentation medium is added continuously to a bioreactor, and an equal amount of conditioned medium is removed simultaneously for processing. Continuous fermentation generally maintains the cultures at a constant high density where cells are primarily in log phase growth. Continuous fermentation permits modulation of cell growth and/or product concentration. For example, a limiting nutrient such as the carbon source or nitrogen source is maintained at a fixed rate and all other parameters are allowed to moderate. Because growth is maintained at a steady state, cell loss due to medium being drawn off should be balanced against the cell growth rate in the fermentation. Methods of optimizing continuous fermentation processes and maximizing the rate of product formation are well known in the art of industrial microbiology.
4.6. Compositions Comprising α-Amylases
α-amylases may be combined with a glucoamylase (EC 3.2.1.3), e.g., a Trichoderma glucoamylase or variant thereof. An exemplary glucoamylase is Trichoderma reesei glucoamylase (TrGA) and variants thereof that possess superior specific activity and thermal stability. See U.S. Published Applications Nos. 2006/0094080, 2007/0004018, and 2007/0015266 (Danisco US Inc.). Suitable variants of TrGA include those with glucoamylase activity and at least 80%, at least 90%, or at least 95% sequence identity to wild-type TrGA. α-amylases advantageously increase the yield of glucose produced in a saccharification process catalyzed by TrGA.
Alternatively, the glucoamylase may be another glucoamylase derived from plants (including algae), fungi, or bacteria. For example, the glucoamylases may be Aspergillus niger G1 or G2 glucoamylase or its variants (e.g., Boel et al. (1984) EMBO J. 3:1097-1102; WO 92/00381; WO 00/04136 (Novo Nordisk A/S)); and A. awamori glucoamylase (e.g., WO 84/02921 (Cetus Corp.)). Other contemplated Aspergillus glucoamylase include variants with enhanced thermal stability, e.g., G137A and G139A (Chen et al. (1996) Prot. Eng. 9:499-505); D257E and D293E/Q (Chen et al. (1995) Prot. Eng. 8:575-582); N182 (Chen et al. (1994) Biochem. J. 301:275-281); A246C (Fierobe et al. (1996) Biochemistry, 35: 8698-8704); and variants with Pro residues in positions A435 and S436 (Li et al. (1997) Protein Eng. 10:1199-1204). Other contemplated glucoamylases include Talaromyces glucoamylases, in particular derived from T. emersonii (e.g., WO 99/28448 (Novo Nordisk A/S), T. leycettanus (e.g., U.S. Pat. No. RE 32,153 (CPC International, Inc.)), T. duponti, or T. thermophilus (e.g., U.S. Pat. No. 4,587,215). Contemplated bacterial glucoamylases include glucoamylases from the genus Clostridium, in particular C. thermoamylolyticum (e.g., EP 135138 (CPC International, Inc.) and C. thermohydrosulfuricum (e.g., WO 86/01831 (Michigan Biotechnology Institute)). Suitable glucoamylases include the glucoamylases derived from Aspergillus oryzae, such as a glucoamylase shown in SEQ ID NO:2 in WO 00/04136 (Novo Nordisk A/S). Also suitable are commercial glucoamylases, such as AMG 200L; AMG 300 L; SAN™ SUPER and AMG™ E (Novozymes); OPTIDEX® 300 and OPTIDEX L-400 (Danisco US Inc.); AMIGASE™ and AMIGASE™ PLUS (DSM); G-ZYME® G900 (Enzyme Bio-Systems); and G-ZYME® G990 ZR (A. niger glucoamylase with a low protease content). Still other suitable glucoamylases include Aspergillus fumigatus glucoamylase, Talaromyces glucoamylase, Thielavia glucoamylase, Trametes glucoamylase, Thermomyces glucoamylase, Athelia glucoamylase, or Humicola glucoamylase (e.g., HgGA). Glucoamylases typically are added in an amount of about 0.1-2 glucoamylase units (GAU)/g ds, e.g., about 0.16 GAU/g ds, 0.23 GAU/g ds, or 0.33 GAU/g ds.
Other suitable enzymes that can be used with amylase include a phytase, protease, pullulanase, β-amylase, isoamylase, a different α-amylase, alpha-glucosidase, cellulase, xylanase, other hemicellulases, beta-glucosidase, transferase, pectinase, lipase, cutinase, esterase, redox enzymes, or a combination thereof. For example, a debranching enzyme, such as an isoamylase (EC 3.2.1.68), may be added in effective amounts well known to the person skilled in the art. A pullulanase (EC 3.2.1.41), e.g., PROMOZYME®, is also suitable. Pullulanase typically is added at 100 U/kg ds. Further suitable enzymes include proteases, such as fungal and bacterial proteases. Fungal proteases include those obtained from Aspergillus, such as A. niger, A. awamori, A. oryzae; Mucor (e.g., M. miehei); Rhizopus; and Trichoderma. β-Amylases (EC 3.2.1.2) are exo-acting maltogenic amylases, which catalyze the hydrolysis of 1,4-α-glucosidic linkages into amylopectin and related glucose polymers, thereby releasing maltose. β-Amylases have been isolated from various plants and microorganisms. See Fogarty et al. (1979) in P
Compositions comprising the present amylases may be aqueous or non-aqueous formulations, granules, powders, gels, slurries, pastes, etc., which may further comprise any one or more of the additional enzymes listed, herein, along with buffers, salts, preservatives, water, co-solvents, surfactants, and the like. Such compositions may work in combination with endogenous enzymes or other ingredients already present in a slurry, water bath, washing machine, food or drink product, etc, for example, endogenous plant (including algal) enzymes, residual enzymes from a prior processing step, and the like.
The present invention also relates to a “food composition,” including but not limited to a food product, animal feed and/or food/feed additives, comprising an amylase, and methods for preparing such a food composition comprising mixing α-amylase with one or more food ingredients, or uses thereof.
Furthermore, the present invention relates to the use of an amylase in the preparation of a food composition, wherein the food composition is baked subsequent to the addition of the polypeptide of the invention. As used herein the term “baking composition” means any composition and/or additive prepared in the process of providing a baked food product, including but not limited to bakers flour, a dough, a baking additive and/or a baked product. The food composition or additive may be liquid or solid.
As used herein, the term “flour” means milled or ground cereal grain. The term “flour” also may mean Sago or tuber products that have been ground or mashed. In some embodiments, flour may also contain components in addition to the milled or mashed cereal or plant matter. An example of an additional component, although not intended to be limiting, is a leavening agent. Cereal grains include wheat, oat, rye, and barley. Tuber products include tapioca flour, cassava flour, and custard powder. The term “flour” also includes ground corn flour, maize-meal, rice flour, whole-meal flour, self-rising flour, tapioca flour, cassava flour, ground rice, enriched flower, and custard powder.
For the commercial and home use of flour for baking and food production, it is important to maintain an appropriate level of α-amylase activity in the flour. A level of activity that is too high may result in a product that is sticky and/or doughy and therefore unmarketable. Flour with insufficient α-amylase activity may not contain enough sugar for proper yeast function, resulting in dry, crumbly bread, or baked products. Accordingly, an amylase, by itself or in combination with another α-amylase(s), may be added to the flour to augment the level of endogenous α-amylase activity in flour.
An amylase can further be added alone or in a combination with other amylases to prevent or retard staling, i.e., crumb firming of baked products. The amount of anti-staling amylase will typically be in the range of 0.01-10 mg of enzyme protein per kg of flour, e.g., 0.5 mg/kg ds. Additional anti-staling amylases that can be used in combination with an amylase include an endo-amylase, e.g., a bacterial endo-amylase from Bacillus. The additional amylase can be another maltogenic α-amylase (EC 3.2.1.133), e.g., from Bacillus. NOVAMYL® is an exemplary maltogenic α-amylase from B. stearothermophilus strain NCIB 11837 and is described in Christophersen et al. (1997) Starch 50:39-45. Other examples of anti-staling endo-amylases include bacterial α-amylases derived from Bacillus, such as B. licheniformis or B. amyloliquefaciens. The anti-staling amylase may be an exo-amylase, such as β-amylase, e.g., from plant sources, such as soybean, or from microbial sources, such as Bacillus.
The baking composition comprising an amylase further can comprise a phospholipase or enzyme with phospholipase activity. An enzyme with phospholipase activity has an activity that can be measured in Lipase Units (LU). The phospholipase may have A1 or A2 activity to remove fatty acid from the phospholipids, forming a lysophospholipid. It may or may not have lipase activity, i.e., activity on triglyceride substrates. The phospholipase typically has a temperature optimum in the range of 30-90° C., e.g., 30-70° C. The added phospholipases can be of animal origin, for example, from pancreas, e.g., bovine or porcine pancreas, snake venom or bee venom. Alternatively, the phospholipase may be of microbial origin, e.g., from filamentous fungi, yeast or bacteria, for example.
The phospholipase is added in an amount that improves the softness of the bread during the initial period after baking, particularly the first 24 hours. The amount of phospholipase will typically be in the range of 0.01-10 mg of enzyme protein per kg of flour, e.g., 0.1-5 mg/kg. That is, phospholipase activity generally will be in the range of 20-1000 LU/kg of flour, where a Lipase Unit is defined as the amount of enzyme required to release 1 μmol butyric acid per minute at 30° C., pH 7.0, with gum arabic as emulsifier and tributyrin as substrate.
Compositions of dough generally comprise wheat meal or wheat flour and/or other types of meal, flour or starch such as corn flour, cornstarch, rye meal, rye flour, oat flour, oatmeal, soy flour, sorghum meal, sorghum flour, potato meal, potato flour or potato starch. The dough may be fresh, frozen or par-baked. The dough can be a leavened dough or a dough to be subjected to leavening. The dough may be leavened in various ways, such as by adding chemical leavening agents, e.g., sodium bicarbonate or by adding a leaven, i.e., fermenting dough. Dough also may be leavened by adding a suitable yeast culture, such as a culture of Saccharomyces cerevisiae (baker's yeast), e.g., a commercially available strain of S. cerevisiae.
The dough may also comprise other conventional dough ingredients, e.g., proteins, such as milk powder, gluten, and soy; eggs (e.g., whole eggs, egg yolks or egg whites); an oxidant, such as ascorbic acid, potassium bromate, potassium iodate, azodicarbonamide (ADA) or ammonium persulfate; an amino acid such as L-cysteine; a sugar; or a salt, such as sodium chloride, calcium acetate, sodium sulfate or calcium sulfate. The dough further may comprise fat, e.g., triglyceride, such as granulated fat or shortening. The dough further may comprise an emulsifier such as mono- or diglycerides, diacetyl tartaric acid esters of mono- or diglycerides, sugar esters of fatty acids, polyglycerol esters of fatty acids, lactic acid esters of monoglycerides, acetic acid esters of monoglycerides, polyoxyethylene stearates, or lysolecithin. In particular, the dough can be made without addition of emulsifiers.
The dough product may be any processed dough product, including fried, deep fried, roasted, baked, steamed and boiled doughs, such as steamed bread and rice cakes. In one embodiment, the food product is a bakery product. Typical bakery (baked) products include bread—such as loaves, rolls, buns, bagels, pizza bases etc. pastry, pretzels, tortillas, cakes, cookies, biscuits, crackers etc.
Optionally, an additional enzyme may be used together with the anti-staling amylase and the phospholipase. The additional enzyme may be a second amylase, such as an amyloglucosidase, a β-amylase, a cyclodextrin glucanotransferase, or the additional enzyme may be a peptidase, in particular an exopeptidase, a transglutaminase, a lipase, a cellulase, a xylanase, a protease, a protein disulfide isomerase, e.g., a protein disulfide isomerase as disclosed in WO 95/00636, for example, a glycosyltransferase, a branching enzyme (1,4-α-glucan branching enzyme), a 4-α-glucanotransferase (dextrin glycosyltransferase) or an oxidoreductase, e.g., a peroxidase, a laccase, a glucose oxidase, an amadoriase, a metalloproteinase, a pyranose oxidase, a lipooxygenase, an L-amino acid oxidase or a carbohydrate oxidase. The additional enzyme(s) may be of any origin, including mammalian and plant, and particularly of microbial (bacterial, yeast or fungal) origin and may be obtained by techniques conventionally used in the art.
The xylanase is typically of microbial origin, e.g., derived from a bacterium or fungus, such as a strain of Aspergillus. Xylanases include PENTOPAN® and NOVOZYM 384®, for example, which are commercially available xylanase preparations produced from Trichoderma reesei. The amyloglucosidase may be an A. niger amyloglucosidase (such as AMG®). Other useful amylase products include GRINDAMYL® A 1000 or A 5000 (Grindsted Products, Denmark) and AMYLASE HTM or AMYLASE PTM (DSM). The glucose oxidase may be a fungal glucose oxidase, in particular an Aspergillus niger glucose oxidase (such as GLUZYME®). An exemplary protease is NEUTRASE®.
The process may be used for any kind of baked product prepared from dough, either of a soft or a crisp character, either of a white, light or dark type. Examples are bread, particularly white, whole-meal or rye bread, typically in the form of loaves or rolls, such as, but not limited to, French baguette-type bread, pita bread, tortillas, cakes, pancakes, biscuits, cookies, pie crusts, crisp bread, steamed bread, pizza and the like.
An amylase may be used in a pre-mix, comprising flour together with an anti-staling amylase, a phospholipase, and/or a phospholipid. The pre-mix may contain other dough-improving and/or bread-improving additives, e.g., any of the additives, including enzymes, mentioned above. An amylase can be a component of an enzyme preparation comprising an anti-staling amylase and a phospholipase, for use as a baking additive.
The enzyme preparation is optionally in the form of a granulate or agglomerated powder. The preparation can have a narrow particle size distribution with more than 95% (by weight) of the particles in the range from 25 to 500 p.m. Granulates and agglomerated powders may be prepared by conventional methods, e.g., by spraying an amylase onto a carrier in a fluid-bed granulator. The carrier may consist of particulate cores having a suitable particle size. The carrier may be soluble or insoluble, e.g., a salt (such as NaCl or sodium sulfate), a sugar (such as sucrose or lactose), a sugar alcohol (such as sorbitol), starch, rice, corn grits, or soy.
Enveloped particles, i.e., α-amylase particles, can comprise an amylase. To prepare enveloped α-amylase particles, the enzyme is contacted with a food grade lipid in sufficient quantity to suspend all of the α-amylase particles. Food grade lipids, as used herein, may be any naturally organic compound that is insoluble in water but is soluble in non-polar organic solvents such as hydrocarbon or diethyl ether. Suitable food grade lipids include, but are not limited to, triglycerides either in the form of fats or oils that are either saturated or unsaturated.
Examples of fatty acids and combinations thereof which make up the saturated triglycerides include, but are not limited to, butyric (derived from milk fat), palmitic (derived from animal and plant fat), and/or stearic (derived from animal and plant fat). Examples of fatty acids and combinations thereof which make up the unsaturated triglycerides include, but are not limited to, palmitoleic (derived from animal and plant fat), oleic (derived from animal and plant fat), linoleic (derived from plant oils), and/or linolenic (derived from linseed oil). Other suitable food grade lipids include, but are not limited to, monoglycerides and diglycerides derived from the triglycerides discussed above, phospholipids and glycolipids.
The food grade lipid, particularly in the liquid form, is contacted with a powdered form of the α-amylase particles in such a fashion that the lipid material covers at least a portion of the surface of at least a majority, e.g., 100% of the α-amylase particles. Thus, each α-amylase particle is individually enveloped in a lipid. For example, all or substantially all of the α-amylase particles are provided with a thin, continuous, enveloping film of lipid. This can be accomplished by first pouring a quantity of lipid into a container, and then slurrying the α-amylase particles so that the lipid thoroughly wets the surface of each α-amylase particle. After a short period of stirring, the enveloped α-amylase particles, carrying a substantial amount of the lipids on their surfaces, are recovered. The thickness of the coating so applied to the particles of α-amylase can be controlled by selection of the type of lipid used and by repeating the operation in order to build up a thicker film, when desired.
The storing, handling and incorporation of the loaded delivery vehicle can be accomplished by means of a packaged mix. The packaged mix can comprise the enveloped α-amylase. However, the packaged mix may further contain additional ingredients as required by the manufacturer or baker. After the enveloped α-amylase has been incorporated into the dough, the baker continues through the normal production process for that product.
The advantages of enveloping the α-amylase particles are two-fold. First, the food grade lipid protects the enzyme from thermal denaturation during the baking process for those enzymes that are heat labile. Consequently, while the α-amylase is stabilized and protected during the proving and baking stages, it is released from the protective coating in the final baked good product, where it hydrolyzes the glucosidic linkages in polyglucans. The loaded delivery vehicle also provides a sustained release of the active enzyme into the baked good. That is, following the baking process, active α-amylase is continually released from the protective coating at a rate that counteracts, and therefore reduces the rate of, staling mechanisms.
In general, the amount of lipid applied to the α-amylase particles can vary from a few percent of the total weight of the α-amylase to many times that weight, depending upon the nature of the lipid, the manner in which it is applied to the α-amylase particles, the composition of the dough mixture to be treated, and the severity of the dough-mixing operation involved.
The loaded delivery vehicle, i.e., the lipid-enveloped enzyme, is added to the ingredients used to prepare a baked good in an effective amount to extend the shelf-life of the baked good. The baker computes the amount of enveloped α-amylase, prepared as discussed above, that will be required to achieve the desired anti-staling effect. The amount of the enveloped α-amylase required is calculated based on the concentration of enzyme enveloped and on the proportion of α-amylase to flour specified. A wide range of concentrations has been found to be effective, although, as has been discussed, observable improvements in anti-staling do not correspond linearly with the α-amylase concentration, but above certain minimal levels, large increases in α-amylase concentration produce little additional improvement. The α-amylase concentration actually used in a particular bakery production could be much higher than the minimum necessary to provide the baker with some insurance against inadvertent under-measurement errors by the baker. The lower limit of enzyme concentration is determined by the minimum anti-staling effect the baker wishes to achieve.
A method of preparing a baked good may comprise: a) preparing lipid-coated α-amylase particles, where substantially all of the α-amylase particles are coated; b) mixing a dough containing flour; c) adding the lipid-coated α-amylase to the dough before the mixing is complete and terminating the mixing before the lipid coating is removed from the α-amylase; d) proofing the dough; and e) baking the dough to provide the baked good, where the α-amylase is inactive during the mixing, proofing and baking stages and is active in the baked good.
The enveloped α-amylase can be added to the dough during the mix cycle, e.g., near the end of the mix cycle. The enveloped α-amylase is added at a point in the mixing stage that allows sufficient distribution of the enveloped α-amylase throughout the dough; however, the mixing stage is terminated before the protective coating becomes stripped from the α-amylase particle(s). Depending on the type and volume of dough, and mixer action and speed, anywhere from one to six minutes or more might be required to mix the enveloped α-amylase into the dough, but two to four minutes is average. Thus, several variables may determine the precise procedure. First, the quantity of enveloped α-amylase should have a total volume sufficient to allow the enveloped α-amylase to be spread throughout the dough mix. If the preparation of enveloped α-amylase is highly concentrated, additional oil may need to be added to the pre-mix before the enveloped α-amylase is added to the dough. Recipes and production processes may require specific modifications; however, good results generally can be achieved when 25% of the oil specified in a bread dough formula is held out of the dough and is used as a carrier for a concentrated enveloped α-amylase when added near the end of the mix cycle. In bread or other baked goods, particularly those having a low fat content, e.g., French-style breads, an enveloped α-amylase mixture of approximately 1% of the dry flour weight is sufficient to admix the enveloped α-amylase properly with the dough. The range of suitable percentages is wide and depends on the formula, finished product, and production methodology requirements of the individual baker. Second, the enveloped α-amylase suspension should be added to the mix with sufficient time for complete mixture into the dough, but not for such a time that excessive mechanical action strips the protective lipid coating from the enveloped α-amylase particles.
In a further aspect of the invention, the food composition is an oil, meat, lard, composition comprising an amylase. In this context the term “oil, meat, lard, composition” means any composition, based on, made from and/or containing oil, meat or lard, respectively. Another aspect the invention relates to a method of preparing an oil or meat or lard composition and/or additive comprising an amylase, comprising mixing the polypeptide of the invention with a oil/meat/lard composition and/or additive ingredients.
In a further aspect of the invention, the food composition is an animal feed composition, animal feed additive and/or pet food comprising an amylase and variants thereof. The present invention further relates to a method for preparing such an animal feed composition, animal feed additive composition and/or pet food comprising mixing an amylase and variants thereof with one or more animal feed ingredients and/or animal feed additive ingredients and/or pet food ingredients. Furthermore, the present invention relates to the use of an amylase in the preparation of an animal feed composition and/or animal feed additive composition and/or pet food.
The term “animal” includes all non-ruminant and ruminant animals. In a particular embodiment, the animal is a non-ruminant animal, such as a horse and a mono-gastric animal. Examples of mono-gastric animals include, but are not limited to, pigs and swine, such as piglets, growing pigs, sows; poultry such as turkeys, ducks, chicken, broiler chicks, layers; fish such as salmon, trout, tilapia, catfish and carps; and crustaceans such as shrimps and prawns. In a further embodiment the animal is a ruminant animal including, but not limited to, cattle, young calves, goats, sheep, giraffes, bison, moose, elk, yaks, water buffalo, deer, camels, alpacas, llamas, antelope, pronghorn and nilgai.
In the present context, it is intended that the term “pet food” is understood to mean a food for a household animal such as, but not limited to dogs, cats, gerbils, hamsters, chinchillas, fancy rats, guinea pigs; avian pets, such as canaries, parakeets, and parrots; reptile pets, such as turtles, lizards and snakes; and aquatic pets, such as tropical fish and frogs.
The terms “animal feed composition,” “feedstuff” and “fodder” are used interchangeably and may comprise one or more feed materials selected from the group comprising a) cereals, such as small grains (e.g., wheat, barley, rye, oats and combinations thereof) and/or large grains such as maize or sorghum; b) by products from cereals, such as corn gluten meal, Distillers Dried Grain Solubles (DDGS) (particularly corn based Distillers Dried Grain Solubles (cDDGS), wheat bran, wheat middlings, wheat shorts, rice bran, rice hulls, oat hulls, palm kernel, and citrus pulp; c) protein obtained from sources such as soya, sunflower, peanut, lupin, peas, fava beans, cotton, canola, fish meal, dried plasma protein, meat and bone meal, potato protein, whey, copra, sesame; d) oils and fats obtained from vegetable and animal sources; e) minerals and vitamins.
Also contemplated are compositions and methods of treating fabrics (e.g., to desize a textile) using an amylase. Fabric-treating methods are well known in the art (see, e.g., U.S. Pat. No. 6,077,316). For example, the feel and appearance of a fabric can be improved by a method comprising contacting the fabric with an an amylase in a solution. The fabric can be treated with the solution under pressure.
An amylase can be applied during or after the weaving of a textile, or during the desizing stage, or one or more additional fabric processing steps. During the weaving of textiles, the threads are exposed to considerable mechanical strain. Prior to weaving on mechanical looms, warp yarns are often coated with sizing starch or starch derivatives to increase their tensile strength and to prevent breaking. An amylase can be applied during or after the weaving to remove these sizing starch or starch derivatives. After weaving, an amylase can be used to remove the size coating before further processing the fabric to ensure a homogeneous and wash-proof result.
An amylase can be used alone or with other desizing chemical reagents and/or desizing enzymes to desize fabrics, including cotton-containing fabrics, as detergent additives, e.g., in aqueous compositions. An amylase also can be used in compositions and methods for producing a stonewashed look on indigo-dyed denim fabric and garments. For the manufacture of clothes, the fabric can be cut and sewn into clothes or garments, which are afterwards finished. In particular, for the manufacture of denim jeans, different enzymatic finishing methods have been developed. The finishing of denim garment normally is initiated with an enzymatic desizing step, during which garments are subjected to the action of amylolytic enzymes to provide softness to the fabric and make the cotton more accessible to the subsequent enzymatic finishing steps. An amylase can be used in methods of finishing denim garments (e.g., a “bio-stoning process”), enzymatic desizing and providing softness to fabrics, and/or finishing process.
An aspect of the present compositions and methods is a cleaning composition that includes an amylase as a component. An amylase polypeptide can be used as a component in detergent compositions for hand washing, laundry washing, dishwashing, and other hard-surface cleaning.
7.1. Overview
Preferably, an amylase is incorporated into detergents at or near a concentration conventionally used for amylase in detergents. For example, an amylase polypeptide may be added in amount corresponding to 0.00001-1 mg (calculated as pure enzyme protein) of amylase per liter of wash/dishwash liquor. Exemplary formulations are provided herein, as exemplified by the following:
An amylase polypeptide may be a component of a detergent composition, as the only enzyme or with other enzymes including other amylolytic enzymes. As such, it may be included in the detergent composition in the form of a non-dusting granulate, a stabilized liquid, or a protected enzyme. Non-dusting granulates may be produced, e.g., as disclosed in U.S. Pat. Nos. 4,106,991 and 4,661,452 and may optionally be coated by methods known in the art. Examples of waxy coating materials are poly(ethylene oxide) products (polyethyleneglycol, PEG) with mean molar weights of 1,000 to 20,000; ethoxylated nonylphenols having from 16 to 50 ethylene oxide units; ethoxylated fatty alcohols in which the alcohol contains from 12 to 20 carbon atoms and in which there are 15 to 80 ethylene oxide units; fatty alcohols; fatty acids;
and mono- and di- and triglycerides of fatty acids. Examples of film-forming coating materials suitable for application by fluid bed techniques are given in, for example, GB 1483591. Liquid enzyme preparations may, for instance, be stabilized by adding a polyol such as propylene glycol, a sugar or sugar alcohol, lactic acid or boric acid according to established methods. Other enzyme stabilizers are known in the art. Protected enzymes may be prepared according to the method disclosed in for example EP 238 216. Polyols have long been recognized as stabilizers of proteins, as well as improving protein solubility.
The detergent composition may be in any useful form, e.g., as powders, granules, pastes, or liquid. A liquid detergent may be aqueous, typically containing up to about 70% of water and 0% to about 30% of organic solvent. It may also be in the form of a compact gel type containing only about 30% water.
The detergent composition comprises one or more surfactants, each of which may be anionic, nonionic, cationic, or zwitterionic. The detergent will usually contain 0% to about 50% of anionic surfactant, such as linear alkylbenzenesulfonate (LAS); α-olefinsulfonate (AOS); alkyl sulfate (fatty alcohol sulfate) (AS); alcohol ethoxysulfate (AEOS or AES); secondary alkanesulfonates (SAS); α-sulfo fatty acid methyl esters; alkyl- or alkenylsuccinic acid; or soap. The composition may also contain 0% to about 40% of nonionic surfactant such as alcohol ethoxylate (AEO or AE), carboxylated alcohol ethoxylates, nonylphenol ethoxylate, alkylpolyglycoside, alkyldimethylamineoxide, ethoxylated fatty acid monoethanolamide, fatty acid monoethanolamide, or polyhydroxy alkyl fatty acid amide (as described for example in WO 92/06154).
The detergent composition may additionally comprise one or more other enzymes, such as proteases, another amylolytic enzyme, cutinase, lipase, cellulase, pectate lyase, perhydrolase, xylanase, peroxidase, and/or laccase in any combination.
The detergent may contain about 1% to about 65% of a detergent builder or complexing agent such as zeolite, diphosphate, triphosphate, phosphonate, citrate, nitrilotriacetic acid (NTA), ethylenediaminetetraacetic acid (EDTA), diethylenetriaminepentaacetic acid (DTMPA), alkyl- or alkenylsuccinic acid, soluble silicates or layered silicates (e.g., SKS-6 from Hoechst). The detergent may also be unbuilt, i.e. essentially free of detergent builder. The enzymes can be used in any composition compatible with the stability of the enzyme. Enzymes generally can be protected against deleterious components by known forms of encapsulation, for example, by granulation or sequestration in hydro gels. Enzymes, and specifically amylases, either with or without starch binding domains, can be used in a variety of compositions including laundry and dishwashing applications, surface cleaners, as well as in compositions for ethanol production from starch or biomass.
The detergent may comprise one or more polymers. Examples include carboxymethylcellulose (CMC), poly(vinylpyrrolidone) (PVP), polyethyleneglycol (PEG), poly(vinyl alcohol) (PVA), polycarboxylates such as polyacrylates, maleic/acrylic acid copolymers and lauryl methacrylate/acrylic acid copolymers.
The detergent may contain a bleaching system, which may comprise a H2O2 source such as perborate or percarbonate, which may be combined with a peracid-forming bleach activator such as tetraacetylethylenediamine (TAED) or nonanoyloxybenzenesulfonate (NOBS). Alternatively, the bleaching system may comprise peroxyacids (e.g., the amide, imide, or sulfone type peroxyacids). The bleaching system can also be an enzymatic bleaching system, for example, perhydrolase, such as that described in International PCT Application WO 2005/056783.
The enzymes of the detergent composition may be stabilized using conventional stabilizing agents, e.g., a polyol such as propylene glycol or glycerol; a sugar or sugar alcohol; lactic acid; boric acid or a boric acid derivative such as, e.g., an aromatic borate ester; and the composition may be formulated as described in, e.g., WO 92/19709 and WO 92/19708.
The detergent may also contain other conventional detergent ingredients such as e.g., fabric conditioners including clays, foam boosters, suds suppressors, anti-corrosion agents, soil-suspending agents, anti-soil redeposition agents, dyes, bactericides, tarnish inhibiters, optical brighteners, or perfumes.
The pH (measured in aqueous solution at use concentration) is usually neutral or alkaline, e.g., pH about 7.0 to about 11.0.
Particular forms of detergent compositions for inclusion of the present α-amylase are described, below.
7.2. Heavy Duty Liquid (HDL) Laundry Detergent Composition
Exemplary HDL laundry detergent compositions includes a detersive surfactant (10%-40% wt/wt), including an anionic detersive surfactant (selected from a group of linear or branched or random chain, substituted or unsubstituted alkyl sulphates, alkyl sulphonates, alkyl alkoxylated sulphate, alkyl phosphates, alkyl phosphonates, alkyl carboxylates, and/or mixtures thereof), and optionally non-ionic surfactant (selected from a group of linear or branched or random chain, substituted or unsubstituted alkyl alkoxylated alcohol, for example a C8-C18 alkyl ethoxylated alcohol and/or C6-C12 alkyl phenol alkoxylates), wherein the weight ratio of anionic detersive surfactant (with a hydrophilic index (HIc) of from 6.0 to 9) to non-ionic detersive surfactant is greater than 1:1. Suitable detersive surfactants also include cationic detersive surfactants (selected from a group of alkyl pyridinium compounds, alkyl quarternary ammonium compounds, alkyl quarternary phosphonium compounds, alkyl ternary sulphonium compounds, and/or mixtures thereof); zwitterionic and/or amphoteric detersive surfactants (selected from a group of alkanolamine sulpho-betaines); ampholytic surfactants; semi-polar non-ionic surfactants and mixtures thereof.
The composition may optionally include, a surfactancy boosting polymer consisting of amphiphilic alkoxylated grease cleaning polymers (selected from a group of alkoxylated polymers having branched hydrophilic and hydrophobic properties, such as alkoxylated polyalkylenimines in the range of 0.05 wt %-10 wt %) and/or random graft polymers (typically comprising of hydrophilic backbone comprising monomers selected from the group consisting of: unsaturated C1-C6 carboxylic acids, ethers, alcohols, aldehydes, ketones, esters, sugar units, alkoxy units, maleic anhydride, saturated polyalcohols such as glycerol, and mixtures thereof; and hydrophobic side chain(s) selected from the group consisting of: C4-C25 alkyl group, polypropylene, polybutylene, vinyl ester of a saturated C1-C6 mono-carboxylic acid, C1-C6 alkyl ester of acrylic or methacrylic acid, and mixtures thereof.
The composition may include additional polymers such as soil release polymers (include anionically end-capped polyesters, for example SRP1, polymers comprising at least one monomer unit selected from saccharide, dicarboxylic acid, polyol and combinations thereof, in random or block configuration, ethylene terephthalate-based polymers and co-polymers thereof in random or block configuration, for example Repel-o-tex SF, SF-2 and SRP6, Texcare SRA100, SRA300, SRN100, SRN170, SRN240, SRN300 and SRN325, Marloquest SL), anti-redeposition polymers (0.1 wt % to 10 wt %, include carboxylate polymers, such as polymers comprising at least one monomer selected from acrylic acid, maleic acid (or maleic anhydride), fumaric acid, itaconic acid, aconitic acid, mesaconic acid, citraconic acid, methylenemalonic acid, and any mixture thereof, vinylpyrrolidone homopolymer, and/or polyethylene glycol, molecular weight in the range of from 500 to 100,000 Da); cellulosic polymer (including those selected from alkyl cellulose, alkyl alkoxyalkyl cellulose, carboxyalkyl cellulose, alkyl carboxyalkyl cellulose examples of which include carboxymethyl cellulose, methyl cellulose, methyl hydroxyethyl cellulose, methyl carboxymethyl cellulose, and mixures thereof) and polymeric carboxylate (such as maleate/acrylate random copolymer or polyacrylate homopolymer).
The composition may further include saturated or unsaturated fatty acid, preferably saturated or unsaturated C12-C24 fatty acid (0 wt % to 10 wt %); deposition aids (examples for which include polysaccharides, preferably cellulosic polymers, poly diallyl dimethyl ammonium halides (DADMAC), and co-polymers of DAD MAC with vinyl pyrrolidone, acrylamides, imidazoles, imidazolinium halides, and mixtures thereof, in random or block configuration, cationic guar gum, cationic cellulose such as cationic hydoxyethyl cellulose, cationic starch, cationic polyacylamides, and mixtures thereof.
The composition may further include dye transfer inhibiting agents, examples of which include manganese phthalocyanine, peroxidases, polyvinylpyrrolidone polymers, polyamine N-oxide polymers, copolymers of N-vinylpyrrolidone and N-vinylimidazole, polyvinyloxazolidones and polyvinylimidazoles and/or mixtures thereof; chelating agents, examples of which include ethylene-diamine-tetraacetic acid (EDTA), diethylene triamine penta methylene phosphonic acid (DTPMP), hydroxy-ethane diphosphonic acid (HEDP), ethylenediamine N,N′-disuccinic acid (EDDS), methyl glycine diacetic acid (MGDA), diethylene triamine penta acetic acid (DTPA), propylene diamine tetracetic acid (PDT A), 2-hydroxypyridine-N-oxide (HPNO), or methyl glycine diacetic acid (MGDA), glutamic acid N,N-diacetic acid (N,N-dicarboxymethyl glutamic acid tetrasodium salt (GLDA), nitrilotriacetic acid (NTA), 4,5-dihydroxy-m-benzenedisulfonic acid, citric acid and any salts thereof, N-hydroxyethylethylenediaminetri-acetic acid (HEDTA), triethylenetetraaminehexaacetic acid (TTHA), N-hydroxyethyliminodiacetic acid (HEIDA), dihydroxyethylglycine (DHEG), ethylenediaminetetrapropionic acid (EDTP), and derivatives thereof.
The composition preferably included enzymes (generally about 0.01 wt % active enzyme to 0.03 wt % active enzyme) selected from proteases, amylases, lipases, cellulases, choline oxidases, peroxidases/oxidases, pectate lyases, mannanases, cutinases, laccases, phospholipases, lysophospholipases, acyltransferases, perhydrolases, arylesterases, and any mixture thereof. The composition may include an enzyme stabilizer (examples of which include polyols such as propylene glycol or glycerol, sugar or sugar alcohol, lactic acid, reversible protease inhibitor, boric acid, or a boric acid derivative, e.g., an aromatic borate ester, or a phenyl boronic acid derivative such as 4-formylphenyl boronic acid).
The composition optionally include silicone or fatty-acid based suds suppressors; heuing dyes, calcium and magnesium cations, visual signaling ingredients, anti-foam (0.001 wt % to about 4.0 wt %), and/or structurant/thickener (0.01 wt % to 5 wt %, selected from the group consisting of diglycerides and triglycerides, ethylene glycol distearate, microcrystalline cellulose, cellulose based materials, microfiber cellulose, biopolymers, xanthan gum, gellan gum, and mixtures thereof).
The composition can be any liquid form, for example a liquid or gel form, or any combination thereof. The composition may be in any unit dose form, for example a pouch.
7.3. Heavy Duty Dry/Solid (HDD) Laundry Detergent Composition
Exemplary HDD laundry detergent compositions includes a detersive surfactant, including anionic detersive surfactants (e.g., linear or branched or random chain, substituted or unsubstituted alkyl sulphates, alkyl sulphonates, alkyl alkoxylated sulphate, alkyl phosphates, alkyl phosphonates, alkyl carboxylates and/or mixtures thereof), non-ionic detersive surfactant (e.g., linear or branched or random chain, substituted or unsubstituted C8-C18 alkyl ethoxylates, and/or C6-C12 alkyl phenol alkoxylates), cationic detersive surfactants (e.g., alkyl pyridinium compounds, alkyl quaternary ammonium compounds, alkyl quaternary phosphonium compounds, alkyl ternary sulphonium compounds, and mixtures thereof), zwitterionic and/or amphoteric detersive surfactants (e.g., alkanolamine sulpho-betaines), ampholytic surfactants, semi-polar non-ionic surfactants, and mixtures thereof; builders including phosphate free builders (for example zeolite builders examples which include zeolite A, zeolite X, zeolite P and zeolite MAP in the range of 0 wt % to less than 10 wt %), phosphate builders (for example sodium tri-polyphosphate in the range of 0 wt % to less than 10 wt %), citric acid, citrate salts and nitrilotriacetic acid, silicate salt (e.g., sodium or potassium silicate or sodium meta-silicate in the range of 0 wt % to less than 10 wt %, or layered silicate (SKS-6)); carbonate salt (e.g., sodium carbonate and/or sodium bicarbonate in the range of 0 wt % to less than 80 wt %); and bleaching agents including photobleaches (e.g., sulfonated zinc phthalocyanines, sulfonated aluminum phthalocyanines, xanthenes dyes, and mixtures thereof) hydrophobic or hydrophilic bleach activators (e.g., dodecanoyl oxybenzene sulfonate, decanoyl oxybenzene sulfonate, decanoyl oxybenzoic acid or salts thereof, 3,5,5-trimethy hexanoyl oxybenzene sulfonate, tetraacetyl ethylene diamine-TAED, nonanoyloxybenzene sulfonate-NOBS, nitrile quats, and mixtures thereof), sources of hydrogen peroxide (e.g., inorganic perhydrate salts examples of which include mono or tetra hydrate sodium salt of perborate, percarbonate, persulfate, perphosphate, or persilicate), preformed hydrophilic and/or hydrophobic peracids (e.g., percarboxylic acids and salts, percarbonic acids and salts, perimidic acids and salts, peroxymonosulfuric acids and salts, and mixtures thereof), and/or bleach catalysts (e.g., imine bleach boosters (examples of which include iminium cations and polyions), iminium zwitterions, modified amines, modified amine oxides, N-sulphonyl imines, N-phosphonyl imines, N-acyl imines, thiadiazole dioxides, perfluoroimines, cyclic sugar ketones, and mixtures thereof, and metal-containing bleach catalysts (e.g., copper, iron, titanium, ruthenium, tungsten, molybdenum, or manganese cations along with an auxiliary metal cations such as zinc or aluminum and a sequestrate such as ethylenediaminetetraacetic acid, ethylenediaminetetra(methylenephosphonic acid), and water-soluble salts thereof).
The composition preferably includes enzymes, e.g., proteases, amylases, lipases, cellulases, choline oxidases, peroxidases/oxidases, pectate lyases, mannanases, cutinases, laccases, phospholipases, lysophospholipases, acyltransferase, perhydrolase, arylesterase, and any mixture thereof.
The composition may optionally include additional detergent ingredients including perfume microcapsules, starch encapsulated perfume accord, hueing agents, additional polymers, including fabric integrity and cationic polymers, dye-lock ingredients, fabric-softening agents, brighteners (for example C.I. Fluorescent brighteners), flocculating agents, chelating agents, alkoxylated polyamines, fabric deposition aids, and/or cyclodextrin.
7.4. Automatic Dishwashing (ADW) Detergent Composition
Exemplary ADW detergent composition includes non-ionic surfactants, including ethoxylated non-ionic surfactants, alcohol alkoxylated surfactants, epoxy-capped poly(oxyalkylated) alcohols, or amine oxide surfactants present in amounts from 0 to 10% by weight; builders in the range of 5-60% including phosphate builders (e.g., mono-phosphates, di-phosphates, tri-polyphosphates, other oligomeric-poylphosphates, sodium tripolyphosphate-STPP) and phosphate-free builders (e.g., amino acid-based compounds including methyl-glycine-diacetic acid (MGDA) and salts and derivatives thereof, glutamic-N,N-diacetic acid (GLDA) and salts and derivatives thereof, iminodisuccinic acid (IDS) and salts and derivatives thereof, carboxy methyl inulin and salts and derivatives thereof, nitrilotriacetic acid (NTA), diethylene triamine penta acetic acid (DTPA), B-alaninediacetic acid (B-ADA) and their salts, homopolymers and copolymers of poly-carboxylic acids and their partially or completely neutralized salts, monomeric polycarboxylic acids and hydroxycarboxylic acids and their salts in the range of 0.5% to 50% by weight; sulfonated/carboxylated polymers in the range of about 0.1% to about 50% by weight to to provide dimensional stability; drying aids in the range of about 0.1% to about 10% by weight (e.g., polyesters, especially anionic polyesters, optionally together with further monomers with 3 to 6 functionalities—typically acid, alcohol or ester functionalities which are conducive to polycondensation, polycarbonate-, polyurethane- and/or polyurea-polyorganosiloxane compounds or precursor compounds, thereof, particularly of the reactive cyclic carbonate and urea type); silicates in the range from about 1% to about 20% by weight (including sodium or potassium silicates for example sodium disilicate, sodium meta-silicate and crystalline phyllosilicates); inorganic bleach (e.g., perhydrate salts such as perborate, percarbonate, perphosphate, persulfate and persilicate salts) and organic bleach (e.g., organic peroxyacids, including diacyl and tetraacylperoxides, especially diperoxydodecanedioc acid, diperoxytetradecanedioc acid, and diperoxyhexadecanedioc acid); bleach activators (i.e., organic peracid precursors in the range from about 0.1% to about 10% by weight); bleach catalysts (e.g., manganese triazacyclononane and related complexes, Co, Cu, Mn, and Fe bispyridylamine and related complexes, and pentamine acetate cobalt(III) and related complexes); metal care agents in the range from about 0.1% to 5% by weight (e.g., benzatriazoles, metal salts and complexes, and/or silicates); enzymes in the range from about 0.01 to 5.0 mg of active enzyme per gram of automatic dishwashing detergent composition (e.g., proteases, amylases, lipases, cellulases, choline oxidases, peroxidases/oxidases, pectate lyases, mannanases, cutinases, laccases, phospholipases, lysophospholipases, acyltransferase, perhydrolase, arylesterase, and mixtures thereof); and enzyme stabilizer components (e.g., oligosaccharides, polysaccharides, and inorganic divalent metal salts).
7.5. Additional Detergent Compositions
Additional exemplary detergent formulations to which the present amylase can be added are described, below, in the numbered paragraphs.
1) A detergent composition formulated as a granulate having a bulk density of at least 600 g/L comprising linear alkylbenzenesulfonate (calculated as acid) about 7% to about 12%; alcohol ethoxysulfate (e.g., C12-18 alcohol, 1-2 ethylene oxide (EO)) or alkyl sulfate (e.g., C16-18) about 1% to about 4%; alcohol ethoxylate (e.g., C14-15 alcohol, 7 EO) about 5% to about 9%; sodium carbonate (e.g., Na2CO3) about 14% to about 20%; soluble silicate (e.g., Na2O, 2SiO2) about 2 to about 6%; zeolite (e.g., NaAlSiO4) about 15% to about 22%; sodium sulfate (e.g., Na2SO4) 0% to about 6%; sodium citrate/citric acid (e.g., C6H5Na3O7/C6H8O7) about 0% to about 15%; sodium perborate (e.g., NaBO3H2O) about 11% to about 18%; TAED about 2% to about 6%; carboxymethylcellulose (CMC) and 0% to about 2%; polymers (e.g., maleic/acrylic acid, copolymer, PVP, PEG) 0-3%; enzymes (calculated as pure enzyme) 0.0001-0.1% protein; and minor ingredients (e.g., suds suppressors, perfumes, optical brightener, photobleach) 0-5%.
2) A detergent composition formulated as a granulate having a bulk density of at least 600 g/L comprising linear alkylbenzenesulfonate (calculated as acid) about 6% to about 11%; alcohol ethoxysulfate (e.g., C12-18 alcohol, 1-2 EO) or alkyl sulfate (e.g., C16-18) about 1% to about 3%; alcohol ethoxylate (e.g., C14-15 alcohol, 7 EO) about 5% to about 9%; sodium carbonate (e.g., Na2CO3) about 15% to about 21%; soluble silicate (e.g., Na2O, 2SiO2) about 1% to about 4%; zeolite (e.g., NaAlSiO4) about 24% to about 34%; sodium sulfate (e.g., Na2SO4) about 4% to about 10%; sodium citrate/citric acid (e.g., C6H5Na3O7/C6H8O7) 0% to about 15%; carboxymethylcellulose (CMC) 0% to about 2%; polymers (e.g., maleic/acrylic acid copolymer, PVP, PEG) 1-6%; enzymes (calculated as pure enzyme protein) 0.0001-0.1%; minor ingredients (e.g., suds suppressors, perfume) 0-5%.
3) A detergent composition formulated as a granulate having a bulk density of at least 600 g/L comprising linear alkylbenzenesulfonate (calculated as acid) about 5% to about 9%; alcohol ethoxylate (e.g., C12-15 alcohol, 7 EO) about 7% to about 14%; Soap as fatty acid (e.g., C16-22 fatty acid) about 1% to about 3%; sodium carbonate (as Na2CO3) about 10% to about 17%; soluble silicate (e.g., Na2O, 2SiO2) about 3% to about 9%; zeolite (as NaAlSiO4) about 23% to about 33%; sodium sulfate (e.g., Na2SO4) 0% to about 4%; sodium perborate (e.g., NaBO3H2O) about 8% to about 16%; TAED about 2% to about 8%; phosphonate (e.g., EDTMPA) 0% to about 1%; carboxymethylcellulose (CMC) 0% to about 2%; polymers (e.g., maleic/acrylic acid copolymer, PVP, PEG) 0-3%; enzymes (calculated as pure enzyme protein) 0.0001-0.1%; minor ingredients (e.g., suds suppressors, perfume, optical brightener) 0-5%.
4) A detergent composition formulated as a granulate having a bulk density of at least 600 g/L comprising linear alkylbenzenesulfonate (calculated as acid) about 8% to about 12%; alcohol ethoxylate (e.g., C12-15 alcohol, 7 EO) about 10% to about 25%; sodium carbonate (as Na2CO3) about 14% to about 22%; soluble silicate (e.g., Na2O, 2SiO2) about 1% to about 5%; zeolite (e.g., NaAlSiO4) about 25% to about 35%; sodium sulfate (e.g., Na2SO4) 0% to about 10%; carboxymethylcellulose (CMC) 0% to about 2%; polymers (e.g., maleic/acrylic acid copolymer, PVP, PEG) 1-3%; enzymes (calculated as pure enzyme protein) 0.0001-0.1%; and minor ingredients (e.g., suds suppressors, perfume) 0-5%.
5) An aqueous liquid detergent composition comprising linear alkylbenzenesulfonate (calculated as acid) about 15% to about 21%; alcohol ethoxylate (e.g., C12-15 alcohol, 7 EO or C12-15 alcohol, 5 EO) about 12% to about 18%; soap as fatty acid (e.g., oleic acid) about 3% to about 13%; alkenylsuccinic acid (C12-14) 0% to about 13%; aminoethanol about 8% to about 18%; citric acid about 2% to about 8%; phosphonate 0% to about 3%; polymers (e.g., PVP, PEG) 0% to about 3%; borate (e.g., B4O7) 0% to about 2%; ethanol 0% to about 3%; propylene glycol about 8% to about 14%; enzymes (calculated as pure enzyme protein) 0.0001-0.1%; and minor ingredients (e.g., dispersants, suds suppressors, perfume, optical brightener) 0-5%.
6) An aqueous structured liquid detergent composition comprising linear alkylbenzenesulfonate (calculated as acid) about 15% to about 21%; alcohol ethoxylate (e.g., C12-15 alcohol, 7 EO, or C12-15 alcohol, 5 EO) 3-9%; soap as fatty acid (e.g., oleic acid) about 3% to about 10%; zeolite (as NaAlSiO4) about 14% to about 22%; potassium citrate about 9% to about 18%; borate (e.g., B4O7) 0% to about 2%; carboxymethylcellulose (CMC) 0% to about 2%; polymers (e.g., PEG, PVP) 0% to about 3%; anchoring polymers such as, e.g., lauryl methacrylate/acrylic acid copolymer; molar ratio 25:1, MW 3800) 0% to about 3%; glycerol 0% to about 5%; enzymes (calculated as pure enzyme protein) 0.0001-0.1%; and minor ingredients (e.g., dispersants, suds suppressors, perfume, optical brighteners) 0-5%.
7) A detergent composition formulated as a granulate having a bulk density of at least 600 g/L comprising fatty alcohol sulfate about 5% to about 10%; ethoxylated fatty acid monoethanolamide about 3% to about 9%; soap as fatty acid 0-3%; sodium carbonate (e.g., Na2CO3) about 5% to about 10%; Soluble silicate (e.g., Na2O, 2SiO2) about 1% to about 4%; zeolite (e.g., NaAlSiO4) about 20% to about 40%; Sodium sulfate (e.g., Na2SO4) about 2% to about 8%; sodium perborate (e.g., NaBO3H2O) about 12% to about 18%; TAED about 2% to about 7%; polymers (e.g., maleic/acrylic acid copolymer, PEG) about 1% to about 5%; enzymes (calculated as pure enzyme protein) 0.0001-0.1%; and minor ingredients (e.g., optical brightener, suds suppressors, perfume) 0-5%.
8) A detergent composition formulated as a granulate comprising linear alkylbenzenesulfonate (calculated as acid) about 8% to about 14%; ethoxylated fatty acid monoethanolamide about 5% to about 11%; soap as fatty acid 0% to about 3%; sodium carbonate (e.g., Na2CO3) about 4% to about 10%; soluble silicate (Na2O, 2SiO2) about 1% to about 4%; zeolite (e.g., NaAlSiO4) about 30% to about 50%; sodium sulfate (e.g., Na2SO4) about 3% to about 11%; sodium citrate (e.g., C6H5Na3O7) about 5% to about 12%; polymers (e.g., PVP, maleic/acrylic acid copolymer, PEG) about 1% to about 5%; enzymes (calculated as pure enzyme protein) 0.0001-0.1%; and minor ingredients (e.g., suds suppressors, perfume) 0-5%.
9) A detergent composition formulated as a granulate comprising linear alkylbenzenesulfonate (calculated as acid) about 6% to about 12%; nonionic surfactant about 1% to about 4%; soap as fatty acid about 2% to about 6%; sodium carbonate (e.g., Na2CO3) about 14% to about 22%; zeolite (e.g., NaAlSiO4) about 18% to about 32%; sodium sulfate (e.g., Na2SO4) about 5% to about 20%; sodium citrate (e.g., C6H5Na3O7) about 3% to about 8%; sodium perborate (e.g., NaBO3H2O) about 4% to about 9%; bleach activator (e.g., NOBS or TAED) about 1% to about 5%; carboxymethylcellulose (CMC) 0% to about 2%; polymers (e.g., polycarboxylate or PEG) about 1% to about 5%; enzymes (calculated as pure enzyme protein) 0.0001-0.1%; and minor ingredients (e.g., optical brightener, perfume) 0-5%.
10) An aqueous liquid detergent composition comprising linear alkylbenzenesulfonate (calculated as acid) about 15% to about 23%; alcohol ethoxysulfate (e.g., C12-15 alcohol, 2-3 EO) about 8% to about 15%; alcohol ethoxylate (e.g., C12-15 alcohol, 7 EO, or C12-15 alcohol, 5 EO) about 3% to about 9%; soap as fatty acid (e.g., lauric acid) 0% to about 3%; aminoethanol about 1% to about 5%; sodium citrate about 5% to about 10%; hydrotrope (e.g., sodium toluensulfonate) about 2% to about 6%; borate (e.g., B4O7) 0% to about 2%; carboxymethylcellulose 0% to about 1%; ethanol about 1% to about 3%; propylene glycol about 2% to about 5%; enzymes (calculated as pure enzyme protein) 0.0001-0.1%; and minor ingredients (e.g., polymers, dispersants, perfume, optical brighteners) 0-5%.
11) An aqueous liquid detergent composition comprising linear alkylbenzenesulfonate (calculated as acid) about 20% to about 32%; alcohol ethoxylate (e.g., C12-15 alcohol, 7 EO, or C12-15 alcohol, 5 EO) 6-12%; aminoethanol about 2% to about 6%; citric acid about 8% to about 14%; borate (e.g., B4O7) about 1% to about 3%; polymer (e.g., maleic/acrylic acid copolymer, anchoring polymer such as, e.g., lauryl methacrylate/acrylic acid copolymer) 0% to about 3%; glycerol about 3% to about 8%; enzymes (calculated as pure enzyme protein) 0.0001-0.1%; and minor ingredients (e.g., hydrotropes, dispersants, perfume, optical brighteners) 0-5%.
12) A detergent composition formulated as a granulate having a bulk density of at least 600 g/L comprising anionic surfactant (linear alkylbenzenesulfonate, alkyl sulfate, α-olefinsulfonate, α-sulfo fatty acid methyl esters, alkanesulfonates, soap) about 25% to about 40%; nonionic surfactant (e.g., alcohol ethoxylate) about 1% to about 10%; sodium carbonate (e.g., Na2CO3) about 8% to about 25%; soluble silicates (e.g., Na2O, 2SiO2) about 5% to about 15%; sodium sulfate (e.g., Na2SO4) 0% to about 5%; zeolite (NaAlSiO4) about 15% to about 28%; sodium perborate (e.g., NaBO34H2O) 0% to about 20%; bleach activator (TAED or NOBS) about 0% to about 5%; enzymes (calculated as pure enzyme protein) 0.0001-0.1%; minor ingredients (e.g., perfume, optical brighteners) 0-3%.
13) Detergent compositions as described in compositions 1)-12) supra, wherein all or part of the linear alkylbenzenesulfonate is replaced by (C12-C18) alkyl sulfate.
14) A detergent composition formulated as a granulate having a bulk density of at least 600 g/L comprising (C12-C18) alkyl sulfate about 9% to about 15%; alcohol ethoxylate about 3% to about 6%; polyhydroxy alkyl fatty acid amide about 1% to about 5%; zeolite (e.g., NaAlSiO4) about 10% to about 20%; layered disilicate (e.g., SK56 from Hoechst) about 10% to about 20%; sodium carbonate (e.g., Na2CO3) about 3% to about 12%; soluble silicate (e.g., Na2O, 2SiO2) 0% to about 6%; sodium citrate about 4% to about 8%; sodium percarbonate about 13% to about 22%; TAED about 3% to about 8%; polymers (e.g., polycarboxylates and PVP) 0% to about 5%; enzymes (calculated as pure enzyme protein) 0.0001-0.1%; and minor ingredients (e.g., optical brightener, photobleach, perfume, suds suppressors) 0-5%.
15) A detergent composition formulated as a granulate having a bulk density of at least 600 g/L comprising (C12-C18) alkyl sulfate about 4% to about 8%; alcohol ethoxylate about 11% to about 15%; soap about 1% to about 4%; zeolite MAP or zeolite A about 35% to about 45%; sodium carbonate (as Na2CO3) about 2% to about 8%; soluble silicate (e.g., Na2O, 2SiO2) 0% to about 4%; sodium percarbonate about 13% to about 22%; TAED 1-8%; carboxymethylcellulose (CMC) 0% to about 3%; polymers (e.g., polycarboxylates and PVP) 0% to about 3%; enzymes (calculated as pure enzyme protein) 0.0001-0.1%; and minor ingredients (e.g., optical brightener, phosphonate, perfume) 0-3%.
16) Detergent formulations as described in 1)-15) supra, which contain a stabilized or encapsulated peracid, either as an additional component or as a substitute for already specified bleach systems.
17) Detergent compositions as described supra in 1), 3), 7), 9), and 12), wherein perborate is replaced by percarbonate.
18) Detergent compositions as described supra in 1), 3), 7), 9), 12), 14), and 15), which additionally contain a manganese catalyst. The manganese catalyst for example is one of the compounds described in “Efficient manganese catalysts for low-temperature bleaching,” Nature 369: 637-639 (1994).
19) Detergent composition formulated as a non-aqueous detergent liquid comprising a liquid nonionic surfactant such as, e.g., linear alkoxylated primary alcohol, a builder system (e.g., phosphate), an enzyme(s), and alkali. The detergent may also comprise anionic surfactant and/or a bleach system.
As above, the present amylase polypeptide may be incorporated at a concentration conventionally employed in detergents. It is at present contemplated that, in the detergent composition, the enzyme may be added in an amount corresponding to 0.00001-1.0 mg (calculated as pure enzyme protein) of amylase polypeptide per liter of wash liquor.
The detergent composition may also contain other conventional detergent ingredients, e.g., deflocculant material, filler material, foam depressors, anti-corrosion agents, soil-suspending agents, sequestering agents, anti-soil redeposition agents, dehydrating agents, dyes, bactericides, fluorescers, thickeners, and perfumes.
The detergent composition may be formulated as a hand (manual) or machine (automatic) laundry detergent composition, including a laundry additive composition suitable for pre-treatment of stained fabrics and a rinse added fabric softener composition, or be formulated as a detergent composition for use in general household hard surface cleaning operations, or be formulated for manual or automatic dishwashing operations.
Any of the cleaning compositions described, herein, may include any number of additional enzymes. In general the enzyme(s) should be compatible with the selected detergent, (e.g., with respect to pH-optimum, compatibility with other enzymatic and non-enzymatic ingredients, and the like), and the enzyme(s) should be present in effective amounts. The following enzymes are provided as examples.
Proteases:
Suitable proteases include those of animal, vegetable or microbial origin. Chemically modified or protein engineered mutants are included, as well as naturally processed proteins. The protease may be a serine protease or a metalloprotease, an alkaline microbial protease, a trypsin-like protease, or a chymotrypsin-like protease. Examples of alkaline proteases are subtilisins, especially those derived from Bacillus, e.g., subtilisin Novo, subtilisin Carlsberg, subtilisin 309, subtilisin 147, and subtilisin 168 (see, e.g., WO 89/06279). Examples of trypsin-like proteases are trypsin (e.g., of porcine or bovine origin), and Fusarium proteases (see, e.g., WO 89/06270 and WO 94/25583). Examples of useful proteases also include but are not limited to the variants described in WO 92/19729, WO 98/20115, WO 98/20116, and WO 98/34946. Commercially available protease enzymes include but are not limited to: ALCALASE®, SAVINASE®, PRIMASE™, DURALASE™, ESPERASE®, KANNASE™, and BLAZE™ (Novo Nordisk A/S and Novozymes A/S); MAXATASE®, MAXACAL™, MAXAPEM™, PROPERASE®, PURAFECT®, PURAFECT OXP™, FN2™, and FN3™ (Danisco US Inc.). Other exemplary proteases include NprE from Bacillus amyloliquifaciens and ASP from Cellulomonas sp. strain 69B4.
Lipases: Suitable lipases include those of bacterial or fungal origin. Chemically modified, proteolytically modified, or protein engineered mutants are included. Examples of useful lipases include but are not limited to lipases from Humicola (synonym Thermomyces), e.g., from H. lanuginosa (T. lanuginosus) (see e.g., EP 258068 and EP 305216), from H. insolens (see e.g., WO 96/13580); a Pseudomonas lipase (e.g., from P. alcaligenes or P. pseudoalcaligenes; see, e.g., EP 218 272), P. cepacia (see e.g., EP 331 376), P. stutzeri (see e.g., GB 1,372,034), P. fluorescens, Pseudomonas sp. strain SD 705 (see e.g., WO 95/06720 and WO 96/27002), P. wisconsinensis (see e.g., WO 96/12012); a Bacillus lipase (e.g., from B. subtilis; see e.g., Dartois et al. Biochemica et Biophysica Acta, 1131: 253-360 (1993)), B. stearothermophilus (see e.g., JP 64/744992), or B. pumilus (see e.g., WO 91/16422). Additional lipase variants contemplated for use in the formulations include those described for example in: WO 92/05249, WO 94/01541, WO 95/35381, WO 96/00292, WO 95/30744, WO 94/25578, WO 95/14783, WO 95/22615, WO 97/04079, WO 97/07202, EP 407225, and EP 260105. Some commercially available lipase enzymes include LIPOLASE® and LIPOLASE ULTRA™ (Novo Nordisk A/S and Novozymes A/S).
Polyesterases:
Suitable polyesterases can be included in the composition, such as those described in, for example, WO 01/34899, WO 01/14629, and U.S. Pat. No. 6,933,140.
Amylases:
The compositions can be combined with other amylases, such as non-production enhanced amylase. These can include commercially available amylases, such as but not limited to STAINZYME®, NATALASE®, DURAMYL®, TERMAMYL®, FUNGAMYL® and BAN™ (Novo Nordisk A/S and Novozymes A/S); RAPIDASE®, POWERASE®, and PURASTAR® (from Danisco US Inc.).
Cellulases:
Cellulases can be added to the compositions. Suitable cellulases include those of bacterial or fungal origin. Chemically modified or protein engineered mutants are included. Suitable cellulases include cellulases from the genera Bacillus, Pseudomonas, Humicola, Fusarium, Thielavia, Acremonium, e.g., the fungal cellulases produced from Humicola insolens, Myceliophthora thermophila and Fusarium oxysporum disclosed for example in U.S. Pat. Nos. 4,435,307; 5,648,263; 5,691,178; 5,776,757; and WO 89/09259. Exemplary cellulases contemplated for use are those having color care benefit for the textile. Examples of such cellulases are cellulases described in for example EP 0495257, EP 0531372, WO 96/11262, WO 96/29397, and WO 98/08940. Other examples are cellulase variants, such as those described in WO 94/07998; WO 98/12307; WO 95/24471; PCT/DK98/00299; EP 531315; U.S. Pat. Nos. 5,457,046; 5,686,593; and 5,763,254. Commercially available cellulases include CELLUZYME® and CAREZYME® (Novo Nordisk A/S and Novozymes A/S); CLAZINASE® and PURADAX HA® (Danisco US Inc.); and KAC-500(B)™ (Kao Corporation).
Peroxidases/Oxidases:
Suitable peroxidases/oxidases contemplated for use in the compositions include those of plant, bacterial or fungal origin. Chemically modified or protein engineered mutants are included. Examples of useful peroxidases include peroxidases from Coprinus, e.g., from C. cinereus, and variants thereof as those described in WO 93/24618, WO 95/10602, and WO 98/15257. Commercially available peroxidases include for example GUARDZYME™ (Novo Nordisk A/S and Novozymes A/S).
The detergent composition can also comprise 2,6-β-D-fructan hydrolase, which is effective for removal/cleaning of biofilm present on household and/or industrial textile/laundry.
The detergent enzyme(s) may be included in a detergent composition by adding separate additives containing one or more enzymes, or by adding a combined additive comprising all of these enzymes. A detergent additive, i.e. a separate additive or a combined additive, can be formulated e.g., as a granulate, a liquid, a slurry, and the like. Exemplary detergent additive formulations include but are not limited to granulates, in particular non-dusting granulates, liquids, in particular stabilized liquids or slurries.
Non-dusting granulates may be produced, e.g., as disclosed in U.S. Pat. Nos. 4,106,991 and 4,661,452 and may optionally be coated by methods known in the art. Examples of waxy coating materials are poly(ethylene oxide) products (e.g., polyethyleneglycol, PEG) with mean molar weights of 1,000 to 20,000; ethoxylated nonylphenols having from 16 to 50 ethylene oxide units; ethoxylated fatty alcohols in which the alcohol contains from 12 to 20 carbon atoms and in which there are 15 to 80 ethylene oxide units; fatty alcohols; fatty acids; and mono- and di- and triglycerides of fatty acids. Examples of film-forming coating materials suitable for application by fluid bed techniques are given in, for example, GB 1483591. Liquid enzyme preparations may, for instance, be stabilized by adding a polyol such as propylene glycol, a sugar or sugar alcohol, lactic acid or boric acid according to established methods. Protected enzymes may be prepared according to the method disclosed in EP 238,216.
The detergent composition may be in any convenient form, e.g., a bar, a tablet, a powder, a granule, a paste, or a liquid. A liquid detergent may be aqueous, typically containing up to about 70% water, and 0% to about 30% organic solvent. Compact detergent gels containing about 30% or less water are also contemplated. The detergent composition can optionally comprise one or more surfactants, which may be non-ionic, including semi-polar and/or anionic and/or cationic and/or zwitterionic. The surfactants can be present in a wide range, from about 0.1% to about 60% by weight.
When included therein the detergent will typically contain from about 1% to about 40% of an anionic surfactant, such as linear alkylbenzenesulfonate, α-olefinsulfonate, alkyl sulfate (fatty alcohol sulfate), alcohol ethoxysulfate, secondary alkanesulfonate, α-sulfo fatty acid methyl ester, alkyl- or alkenylsuccinic acid, or soap.
When included therein, the detergent will usually contain from about 0.2% to about 40% of a non-ionic surfactant such as alcohol ethoxylate, nonylphenol ethoxylate, alkylpolyglycoside, alkyldimethylamineoxide, ethoxylated fatty acid monoethanolamide, fatty acid monoethanolamide, polyhydroxy alkyl fatty acid amide, or N-acyl-N-alkyl derivatives of glucosamine (“glucamides”).
The detergent may contain 0% to about 65% of a detergent builder or complexing agent such as zeolite, diphosphate, triphosphate, phosphonate, carbonate, citrate, nitrilotriacetic acid, ethylenediaminetetraacetic acid (EDTA), diethylenetriaminepentaacetic acid, alkyl- or alkenylsuccinic acid, soluble silicates or layered silicates (e.g., SKS-6 from Hoechst).
The detergent may comprise one or more polymers. Exemplary polymers include carboxymethylcellulose (CMC), poly(vinylpyrrolidone) (PVP), poly(ethylene glycol) (PEG), poly(vinyl alcohol) (PVA), poly(vinylpyridine-N-oxide), poly(vinylimidazole), polycarboxylates e.g., polyacrylates, maleic/acrylic acid copolymers), and lauryl methacrylate/acrylic acid copolymers.
The enzyme(s) of the detergent composition may be stabilized using conventional stabilizing agents, e.g., as polyol (e.g., propylene glycol or glycerol), a sugar or sugar alcohol, lactic acid, boric acid, or a boric acid derivative (e.g., an aromatic borate ester), or a phenyl boronic acid derivative (e.g., 4-formylphenyl boronic acid). The composition may be formulated as described in WO 92/19709 and WO 92/19708.
It is contemplated that in the detergent compositions, in particular the enzyme variants, may be added in an amount corresponding to about 0.01 to about 100 mg of enzyme protein per liter of wash liquor (e.g., about 0.05 to about 5.0 mg of enzyme protein per liter of wash liquor or 0.1 to about 1.0 mg of enzyme protein per liter of wash liquor).
Yet additional exemplary detergent formulations to which the present amylase can be added are described in, e.g., WO2010065455, WO2011072099, WO2011130222, WO2011140364, WO2011156297, WO2011156298, WO2011130076, WO2011133381, WO2011156297, WO2011156298, EP1794295B1, US20110195481, US20110212876, US20110257063, WO2010039958, WO2011072117, WO2011098531, WO2011100410, WO2011130076, WO2011133381, WO2011140316, US20070215184, US20070251545, US20090075857, US20090137444, US20090143271, US20100011513, US20100093588, US20110201536, US20110232004, US20110237482, US20110312868, US20120003326, US20120004155, WO2011131585, EP707628B1, U.S. Pat. No. 5,719,115, EP736084B1, U.S. Pat. No. 5,783,545, EP767830B1, U.S. Pat. No. 5,972,668, EP746599B1, U.S. Pat. No. 5,798,328, EP662117B1, U.S. Pat. No. 5,898,025, U.S. Pat. No. 6,380,140, EP898613B1, U.S. Pat. No. 3,975,280, U.S. Pat. No. 6,191,092, U.S. Pat. No. 6,329,333, U.S. Pat. No. 6,530,386, EP1307547B1, U.S. Pat. No. 7,153,818, EP1421169B1, U.S. Pat. No. 6,979,669, EP1529101B1, U.S. Pat. No. 7,375,070, EP1385943B1, U.S. Pat. No. 7,888,104, EP1414977B1, U.S. Pat. No. 5,855,625, EP1921147B1, EP1921148B1, EP701605B1, EP1633469B1, EP1633470B1, EP1794293B1, EP171007B1, U.S. Pat. No. 4,692,260, U.S. Pat. No. 7,569,226, EP1165737B1, U.S. Pat. No. 6,391,838, U.S. Pat. No. 6,060,441, US2009017074, U.S. Pat. No. 7,320,887, EP1737952B1, U.S. Pat. No. 7,691,618, US20070256251, US20050261156, US20050261158, US20100234267, US20110136720, US20110201536, U.S. Pat. No. 7,811,076, U.S. Pat. No. 5,929,017, U.S. Pat. No. 5,156,773, EP2343310A1, WO2011083114, EP214761B1, U.S. Pat. No. 4,876,024, EP675944B1, U.S. Pat. No. 5,763,383, EP517761B1, U.S. Pat. No. 6,624,129, EP1054956B1, U.S. Pat. No. 6,939,702, U.S. Pat. No. 6,964,944, EP832174B1, US20060205628, US20070179076, US20080023031, US20110015110, US20110028372, U.S. Pat. No. 4,973,417, U.S. Pat. No. 5,447,649, U.S. Pat. No. 5,840,677, U.S. Pat. No. 5,965,503, U.S. Pat. No. 5,972,873, U.S. Pat. No. 5,998,344, U.S. Pat. No. 6,071,356, WO9009428, EP1661978A1, EP1698689A1, EP1726636A1, EP1867707A1, EP1876226A1, EP1876227A1, EP0205208A2, EP0206390A2, EP0271152, EP0271154, EP0341999, EP0346136, EP2135934, US20120208734, WO2011127102, WO2012142087, WO2012145062, EP1790713B1, U.S. Pat. No. 8,066,818B2, U.S. Pat. No. 8,163,686B2, U.S. Pat. No. 8,283,300B2, U.S. Pat. No. 8,354,366B2, US20120125374, U.S. Pat. No. 3,929,678, and U.S. Pat. No. 5,898,025.
7.6. Methods of Assessing Amylase Activity in Detergent Compositions
Numerous α-amylase cleaning assays are known in the art, including swatch and micro-swatch assays. The appended Examples describe only a few such assays.
In order to further illustrate the compositions and methods, and advantages thereof, the following specific examples are given with the understanding that they are illustrative rather than limiting.
The present α-amylase may be a component of a brewing composition used in a process of brewing, i.e., making a fermented malt beverage. Non-fermentable carbohydrates form the majority of the dissolved solids in the final beer. This residue remains because of the inability of malt amylases to hydrolyze the alpha-1,6-linkages of the starch. The non-fermentable carbohydrates contribute about 50 calories per 12 ounces of beer. an amylase, in combination with a glucoamylase and optionally a pullulanase and/or isoamylase, assist in converting the starch into dextrins and fermentable sugars, lowering the residual non-fermentable carbohydrates in the final beer.
The principal raw materials used in making these beverages are water, hops and malt. In addition, adjuncts such as common corn grits, refined corn grits, brewer's milled yeast, rice, sorghum, refined corn starch, barley, barley starch, dehusked barley, wheat, wheat starch, torrified cereal, cereal flakes, rye, oats, potato, tapioca, and syrups, such as corn syrup, sugar cane syrup, inverted sugar syrup, barley and/or wheat syrups, and the like may be used as a source of starch.
For a number of reasons, the malt, which is produced principally from selected varieties of barley, has the greatest effect on the overall character and quality of the beer. First, the malt is the primary flavoring agent in beer. Second, the malt provides the major portion of the fermentable sugar. Third, the malt provides the proteins, which will contribute to the body and foam character of the beer. Fourth, the malt provides the necessary enzymatic activity during mashing. Hops also contribute significantly to beer quality, including flavoring. In particular, hops (or hops constituents) add desirable bittering substances to the beer. In addition, the hops act as protein precipitants, establish preservative agents and aid in foam formation and stabilization.
Grains, such as barley, oats, wheat, as well as plant components, such as corn, hops, and rice, also are used for brewing, both in industry and for home brewing. The components used in brewing may be unmalted or may be malted, i.e., partially germinated, resulting in an increase in the levels of enzymes, including α-amylase. For successful brewing, adequate levels of α-amylase enzyme activity are necessary to ensure the appropriate levels of sugars for fermentation. An amylase, by itself or in combination with another α-amylase(s), accordingly may be added to the components used for brewing.
As used herein, the term “stock” means grains and plant components that are crushed or broken. For example, barley used in beer production is a grain that has been coarsely ground or crushed to yield a consistency appropriate for producing a mash for fermentation. As used herein, the term “stock” includes any of the aforementioned types of plants and grains in crushed or coarsely ground forms. The methods described herein may be used to determine α-amylase activity levels in both flours and stock.
Processes for making beer are well known in the art. See, e.g., Wolfgang Kunze (2004) “Technology Brewing and Malting,” Research and Teaching Institute of Brewing, Berlin (VLB), 3rd edition. Briefly, the process involves: (a) preparing a mash, (b) filtering the mash to prepare a wort, and (c) fermenting the wort to obtain a fermented beverage, such as beer. Typically, milled or crushed malt is mixed with water and held for a period of time under controlled temperatures to permit the enzymes present in the malt to convert the starch present in the malt into fermentable sugars. The mash is then transferred to a mash filter where the liquid is separated from the grain residue. This sweet liquid is called “wort,” and the left over grain residue is called “spent grain.” The mash is typically subjected to an extraction, which involves adding water to the mash in order to recover the residual soluble extract from the spent grain. The wort is then boiled vigorously to sterilizes the wort and help develop the color, flavor and odor. Hops are added at some point during the boiling. The wort is cooled and transferred to a fermentor.
The wort is then contacted in a fermentor with yeast. The fermentor may be chilled to stop fermentation. The yeast flocculates and is removed. Finally, the beer is cooled and stored for a period of time, during which the beer clarifies and its flavor develops, and any material that might impair the appearance, flavor and shelf life of the beer settles out. The beer usually contains from about 2% to about 10% v/v alcohol, although beer with a higher alcohol content, e.g., 18% v/v, may be obtained. Prior to packaging, the beer is carbonated and, optionally, filtered and pasteurized.
The brewing composition comprising an amylase, in combination with a glucoamylase and optionally a pullulanase and/or isoamylase, may be added to the mash of step (a) above, i.e., during the preparation of the mash. Alternatively, or in addition, the brewing composition may be added to the mash of step (b) above, i.e., during the filtration of the mash. Alternatively, or in addition, the brewing composition may be added to the wort of step (c) above, i.e., during the fermenting of the wort.
A fermented beverage, such as a beer, can be produced by one of the methods above. The fermented beverage can be a beer, such as full malted beer, beer brewed under the “Reinheitsgebot,” ale, IPA, lager, bitter, Happoshu (second beer), third beer, dry beer, near beer, light beer, low alcohol beer, low calorie beer, porter, bock beer, stout, malt liquor, non-alcoholic beer, non-alcoholic malt liquor and the like, but also alternative cereal and malt beverages such as fruit flavored malt beverages, e.g., citrus flavored, such as lemon-, orange-, lime-, or berry-flavored malt beverages, liquor flavored malt beverages, e.g., vodka-, rum-, or tequila-flavored malt liquor, or coffee flavored malt beverages, such as caffeine-flavored malt liquor, and the like.
α-amylases may reduce the iodine-positive starch (IPS), when used in a method of liquefaction and/or saccharification. One source of IPS is from amylose that escapes hydrolysis and/or from retrograded starch polymer. Starch retrogradation occurs spontaneously in a starch paste, or gel on ageing, because of the tendency of starch molecules to bind to one another followed by an increase in crystallinity. Solutions of low concentration become increasingly cloudy due to the progressive association of starch molecules into larger articles. Spontaneous precipitation takes place and the precipitated starch appears to be reverting to its original condition of cold-water insolubility. Pastes of higher concentration on cooling set to a gel, which on ageing becomes steadily firmer due to the increasing association of the starch molecules. This arises because of the strong tendency for hydrogen bond formation between hydroxy groups on adjacent starch molecules. See J. A. Radley, ed., S
The presence of IPS in saccharide liquor negatively affects final product quality and represents a major issue with downstream processing. IPS plugs or slows filtration system, and fouls the carbon columns used for purification. When IPS reaches sufficiently high levels, it may leak through the carbon columns and decrease production efficiency. Additionally, it may result in hazy final product upon storage, which is unacceptable for final product quality. The amount of IPS can be reduced by isolating the saccharification tank and blending the contents back. IPS nevertheless will accumulate in carbon columns and filter systems, among other things. The use of α-amylases is expected to improve overall process performance by reducing the amount of IPS.
All references cited herein are herein incorporated by reference in their entirety for all purposes. In order to further illustrate the compositions and methods, and advantages thereof, the following specific examples are given with the understanding that they are illustrative rather than limiting.
A search of the NCBI databases for amylases in the genus Exiguobacterium revealed the presence of an alpha-amylase belonging to GH13 subfamily 5: Exiguobacterium sp. AT1b alpha-amylase (NCBI Reference Sequence: YP_002885778.1; SEQ ID NO: 1). The amylase carries a signal peptide as predicted by as predicted by SignalP version 4.0 (Nordahl Petersen et al. (2011) Nature Methods, 8:785-786) indicating that it is a secreted enzyme.
The amino acid sequence of the mature chain of Exiguobacterium sp. AT1b alpha-amylase (EspAmy3) is set forth below as SEQ ID NO: 1:
Sequencing of the genome of Exiguobacterium sp. GICC#1337 (natural isolate from Yellowstone, Culture Collection Genencor International) resulted in the discovery of another Exiguobacterium amylase belonging to GH13 subfamily 5. The nucleotide sequence of espAmy6 amylase gene is set forth below as SEQ ID NO: 18:
The amino acid sequence of the mature protein EspAmy6 is set forth below as SEQ ID NO: 2:
Sequencing of the genome of Exiguobacterium sp. GICC#1347 (natural isolate from Yellowstone, Culture Collection Genencor International) resulted in the discovery of yet another Exiguobacterium amylase belonging to the same subfamily (GH13-5). The amino acid sequence of the mature protein EspAmy7 is set forth below as SEQ ID NO: 3:
Sequencing of the genome of Exiguobacterium aurantiacum DSM 6208 (obtained from DSMZ: Deutsche Sammlung von Mikroorganismen and Zellkulturen, Braunschweig, GERMANY) resulted in the discovery of alpha-amylase EauAmy1, another member of Cazy family GH13, subfamily 5. The nucleotide sequence of eauAmyl amylase gene is set forth below as SEQ ID NO: 19:
The amino acid sequence of the mature protein EauAmy1 is set forth below as SEQ ID NO: 4:
The amylases EspAmy3 (SEQ ID NO: 1), EspAmy6 (SEQ ID NO: 2), EspAmy7 (SEQ ID NO: 3) and EauAmy1 (SEQ ID NO: 4) were expressed in B. subtilis by using the pHPLT expression vector (Solingen et al. (2001) Extremophiles 5:333-341; US Patent Application 20100021587). Synthetic genes encoding these amylases were synthesized as Pst I Hpa I fragments at Geneart/Life Technologies (Regensburg, Germany) and fused in-frame to the amyL (B. licheniformis alpha-amylase) signal peptide sequence and in front of the amyL transcription terminator, both present in the pHPLT vector.
A suitable two-protease-deleted B. subtilis strain was transformed with the resulting expression plasmids and transformants were selected on plates containing Heart infusion agar (Difco, Cat. No. 244400) and 10 mg/L neomycin sulphate (Sigma, Neomycin sulphate Cat. No. N-1876). Selective growth of B. subtilis transformants harbouring the pHPLT amylase expression plasmids was performed in shake flasks containing MBD medium (a MOPS based defined medium), 5 mM CaCl2 and 10 mg/L neomycin. MBD medium was made essentially as known in the art (See, Neidhardt et al. (1974) J. Bacteriol., 119:736-747), except that NH4Cl2, FeSO4, and CaCl2 were omitted from the base medium, 3 mM K2HPO4 was used, and the base medium was supplemented with 60 mM urea, 75 g/L glucose, and 1% soytone. The micronutrients were made up as a 100× stock solution containing in one liter, 400 mg FeSO4.7H2O, 100 mg MnSO4.H2O, 100 mg ZnSO4.7H2O, 50 mg CuCl2.2H2O, 100 mg CoCl2.6H2O, 100 mg NaMoO4.2H2O, 100 mg Na2B4O7.10H2O, 10 ml of 1M CaCl2, and 10 ml of 0.5 M sodium citrate. Growth resulted in the production of secreted amylase with starch hydrolyzing activity.
Suzuki et al. ((1989) J. Biol. Chem., 264:18933-38) showed that deletion of R176 and G177 (i.e., the “RG deletion”) in B. amyloliquefaciens amylase enhances the stability of the enzyme. The substitution of serine at position 242 in G. stearothermophilus amylase into glutamine was shown to enhance the stability of the enzyme (U.S. Pat. No. 8,206,966). Mutation G475K in Bacillus sp. TS-23 amylase enhanced cleaning performance of the enzyme (US20120045817). Equivalent mutations were made in the Exiguobacterium amylases described in Example 2.
The amino acid sequence of a mature form of variant of EspAmy3 amylase having deletions of K179 and S180 and the substitutions S242Q and G477K (i.e., EspAmy3-V1) is set forth below as SEQ ID NO: 5:
The amino acid sequence of a mature form of variant of EspAmy6 amylase having deletions of K179 and S180 and the substitutions A242Q and G477K (i.e., EspAmy6-V1) is set forth below as SEQ ID NO: 6:
The amino acid sequence of a mature form of variant of EspAmy7 amylase having deletions of K179 and S180 and the substitutions S242Q and G477K (i.e., EspAmy7-V1) is set forth below as SEQ ID NO: 7:
The amino acid sequence of a mature form of variant of EauAmy1 amylase having deletions of K179 and S180 and the substitutions S242Q and G477K (i.e., EauAmy1-V1) is set forth below as SEQ ID NO: 8:
Synthetic genes encoding these amylase variants were also synthesized as Pst I-Hpa I fragments at Geneart/Life Technologies (Regensburg, Germany) and fused in-frame to the amyL (B. licheniformis alpha-amylase) signal peptide sequence and in front of the amyL transcription terminator, both present in the pHPLT vector.
The variants were expressed as in Example 2.
The cleaning performance of EspAmy3 (SEQ ID NO: 1), EspAmy6 (SEQ ID NO: 2), EspAmy7 (SEQ ID NO: 3), EauAmy1 (SEQ ID NO: 4), EspAmy3-V1 (SEQ ID NO: 5), EspAmy6-V1 (SEQ ID NO: 6), EspAmy7-V1 (SEQ ID NO: 7), and EauAmy1-V1 (SEQ ID NO: 8) was analyzed in a microswatch assay. Two samples of Bacillus licheniformis amylase (LAT, PURASTAR®) were included as a benchmark. CFT CS-28 rice starch on cotton swatches (Center for Testmaterials BV, Vlaardingen, Netherlands) containing an indicator dye bound to the starch, were pre-punched by the manufacturer to form discs measuring 5.5 mm in diameter. Two discs were placed in each well of flat-bottom non-binding 96-well assay plates.
The cleaning assay was carried out in a buffer consisting of 25 mM HEPES (pH 8.2), with 2 mM CaCl2 and 0.005% Tween-80 added. Filtered culture supernatants were diluted 1:100 in an enzyme dilution buffer (10 mM NaCl, 0.1 mM CaCl2, 0.005% TWEEN 80). An appropriate volume of HEPES buffer (162 to 180 μL) was added to each well, and then varying amounts of the diluted enzyme solution, from 0 μL to 18 μL were added for a total volume of 180 μL in every well. The plates were incubated at 25° C. with agitation at 1150 rpm for 15 minutes. Color release was quantified spectrophotometrically at 488 nm by the transfer of 100 μL of the final wash solution to a fresh medium-binding microtiter plate. Enzyme performance was judged by the amount of colour released into the wash liquor. Performances of enzymes were compared to each other by subtracting the blank wells and fitting curves based on the actual concentration of each amylase, as determined by reversed phase HPLC.
The cleaning performances of the Exiguobacterium amylases and their respective V1 variants are shown graphically in
Sequencing of the genome of Exiguobacterium sp DSM17349 (obtained from DSMZ: Deutsche Sammlung von Mikroorganismen and Zellkulturen, Braunschweig, GERMANY) resulted in the discovery of alpha-amylase EspAmy5, another member of Cazy family GH13, subfamily 5. The nucleotide sequence of the espAmy5 gene is set forth below as SEQ ID NO: 20. The sequence encoding the native signal peptide, as predicted by SignalP-NN (Emanuelsson et al. (2007) Nature Protocols, 2:953-971), is shown in bold:
ATGATGTTGAAGAAACGACAAGGGATTGCCGTGCTGGCTGGAGTGACATC
GATTGCACTGCTTTCAGGACAACCGGTCGCACAAGCGGCAACTCCACAGA
The amino acid sequence of the predicted mature EspAmy5 protein encoded by the espAmy5 gene is set forth below as SEQ ID NO: 9.
A bacterial strain previously characterized as a Bacillus sp. was selected as a potential source for various alpha-amylases and other enzymes, useful for industrial applications. Genomic DNA for sequencing was obtained by first growing the presumptive Bacillus sp. on LB agar plates at 37° C. for 24 h. Cell material was scraped from the plates and used to prepare genomic DNA using phenol/chloroform extraction. The genomic DNA was used for sequencing. The entire genome of Bacillus sp was sequenced using ILLUMINA® sequencing by synthesis (SBS) technology. Genome sequencing and assembly of the sequence data was performed by BaseClear (Leiden, The Netherlands). Contigs were annotated by BioXpr (Namur, Belgium). One of genes identified in this way encodes an alpha-amylase that showed homology by BLASTP to alpha-amylases of various other bacteria. At the N-terminus, the protein is predicted to have a signal peptide with a length of 28 amino acids as determined by the Signal P 3.0 program set to SignalP-NN system (Emanuelsson et al., Nature Protocols, 2: 953-971, 2007). The presence of a signal sequence suggests that the alpha amylase is a secreted enzyme. The presence of hallmark Exiguobacterium amylase sequence motifs (discussed infra) suggests that the Bacillus sp. is in fact an Exiguobacterium sp. The nucleotide sequence of the espAmy8 coding region is set forth below as SEQ ID NO: 21 (the coding region of the predicted signal peptide sequence is underlined):
ATGATGAAGAGACGGCAAGGGTTTGCGGTCATCGCTGGTGTCACGGCTGT
TGCACTGCTCGCGGGGCAACCGGTCGCACAAGCAGCAACAACTCAAAACG
The amino acid sequence of the predicted mature EspAmy8 protein is set forth below as SEQ ID NO: 10:
Sequencing of the genome of Exiguobacterium mexicanum DSM16483 (obtained from DSMZ: Deutsche Sammlung von Mikroorganismen and Zellkulturen, Braunschweig, GERMANY) resulted in the discovery of alpha-amylase) resulted in the discovery of another amylase EmeAmy1, another member of Cazy family GH13, subfamily 5. The amino acid sequence of the EmeAmy1 precursor protein encoded by the gene emeAmy1 is set forth below as SEQ ID NO: 11:
The amino acid sequence of the predicted mature form of EspAmy9 protein from Exiguobacterium sp. DAUS (NCBI Reference Sequence: AFZ41193.1) is set forth below as SEQ ID NO: 15
The amino acid sequence of the predicted mature form of EspAmy10 protein Exiguobacterium sp. DSM 17357 (EspB02846), obtained from DSMZ: Deutsche Sammlung von Mikroorganismen and Zellkulturen, Braunschweig, GERMANY, is set forth below as SEQ ID NO: 16:
The nucleotide sequence of the espAmy10 coding region is set forth below as SEQ ID NO: 22 (the coding region of the predicted signal peptide sequence is underlined):
ATGATGTTGAAGAAACGACAAGGAATTGCCGTGCTGGCAGGAGTGACATC
GATTGCACTGCTTTCGGGGCAACCGGTCGCGCAAGCGGCAACTCCGCAGA
The amino acid sequence of the predicted mature form of EprAmy1 protein from Exiguobacterium profundum DSM 17289 (EprA01468), obtained from DSMZ: Deutsche Sammlung von Mikroorganismen and Zellkulturen, Braunschweig, GERMANY, is set forth below as SEQ ID NO: 17:
The nucleotide sequence of the eprAmy1 coding region is set forth below as SEQ ID NO: 23 (the coding region of the predicted signal peptide sequence is underlined):
ATGTTGAAGAAACGACAAGGGATTGCTGTCCTAGCTGGAGTGACATCGA
TTGCACTGCTTTCGGGGCAACCGGTCGCACAGGCAGCGACCCCACAGAA
The nucleotide sequences of the EspAmy5, EspAmy8, and EmeAmy1 were synthesized by GeneRay Biotech Co., Ltd (Shanghai, China). The synthetic constructs were digested with the restriction enzymes BssHII and XhoI and ligated into the Bacillus subtilis expression vector p2JM103BBI (Vogtentanz, Protein Expr Purif, 55:40-52, 2007), to obtain the expression plasmids pLGQ0015 (aprE-EspAmy8) (
The amino acid sequence of the mature form of EspAmy5 amylase expressed from plasmid p2JM858 (aprE-EspAmy5) is set forth below as SEQ ID NO: 12. The three residue addition (AGK) is shown in bold.
AGKATPQNGTMMQYFEWYVPNDGLHWNRLSNDSQHLKDIGISTVWIPPA
The amino acid sequence of the mature form of EspAmy8 protein expressed from pLGQ0015 is set forth below as SEQ ID NO: 13 (the three residue amino-terminal extension based on the predicted cleavage site shown in bold):
AGKATTQNGTMMQYFEWYVPNDGLHWNRLSNDSQNLKDIGVTTVWIPP
The amino acid sequence of the mature form of EmeAmy1 amylase expressed from plasmid p2JM855 (aprE-EmeAmy1) is set forth below as SEQ ID NO: 14. The three residue addition (AGK) is shown in bold.
AGKATPQNGTMMQYFEWYVPNDGLHWNRLSNDSQHLKDIGVTTVWIPP
A seed culture of a Bacillus subtilis strain expressing EspAmy8 protein (SEQ ID NO: 13) was grown in two 250-mL shake flasks, each flask contained 50 mL of LBG media consisting of 10 g/L soytone, 5 g/L yeast extract, 10 g/L NaCl, 11 g/L glucose. 1 aq, 1.67 drop/L Mazu 6000, and 5 ug/mL chloramphenicol. The seed culture was grown at 37° C. and 250 rpm. OD550 was checked after 5 hours growth and 100 mL of the culture was transferred to fermentor when OD550 was between 0.8˜1.2. The fermentation medium in a 7-L fermenter (Applikon) consisted of 2 g/kg soytone, 1.4 g/kg yeast extract, 8 g/kg KH2PO4, 8 g/kg NaH2PO4.H2O, 2.8 g/kg MgSO4.7H2O, 0.1 g/kg CaCl2.2H2O, 0.25 FeCl2.4H2O, 0.22 g/kg MnSO4.4H2O, 13.9 mL/kg 4 N H2SO4, 5.7 g/kg glucose, 2 mL Mazu 6000, and 10 mL/kg Trace metals 100× stock (52.5 g/kg citric acid. 1H2O, 2.18 g/kg ZnSO4.7H2O, 2.0 g/kg CoCl2.6H2O, 2.0 g/kg Na2MoO4.H2O, 1.9 g/kg CuSO4.5H2O and 0.5 g/kg H3BO3).
Following inoculation with 100 mL of the seed culture, the fermentation was initiated with working volume of 3.5 kg and controlled at pH 6.9 and temperature 37° C. The dissolved oxygen was controlled above 20% by adjusting aeration and agitation. The feed of sterile 600 g/kg glucose solution was started at elapsed fermentation time of 5 h with feed rate of 0.30 g/min. The feed rate was increased to 0.40 g/min, 0.63 g/min at elapsed fermentation times of 19.6 h and 23.7 h, respectively. Fermentation broth was sampled at 16.7 h, 21.7 h and 41 h to run residual glucose, cell mass, protein concentration measurement and SDS-PAGE analysis. Fermentation was terminated at elapsed fermentation time of 41 h. Following centrifugation, filtration and ultrafiltration, 480 mL concentrated sample was obtained. BCA assay (protein quantification kit, Shanghai Generay Biotech CO., Ltd) illustrated that protein concentration in concentrated sample was 42.12 g/L.
EspAmy8 amylase was purified via three steps purification. Ammonium sulfate was added into 240 mL concentrated fermentation broth with a final concentration of 40% saturation. The precipitant was centrifuged, collected, and resuspended in 20 mM Tris-HCl pH 8.5 (buffer A). The suspended solution was then loaded onto a 40-mL Anion Exchange chromatography column Q HP that was pre-equilibrated with buffer A. The column was washed step-wise with buffer A containing 50 mM NaCl, 100 mM NaCl, 200 mM NaCl, 300 mM NaCl, and 1 M NaCl. The target protein was eluted in the flow through. The flow through was dialysed with 40% glycerol, 20 mM Tris, pH 8.0 and loaded onto a gel filtration column Superdex GF200 that was pre-equilibrated with 20 mM Tris-HCl, pH 8.0, with 150 mM NaCl (buffer B). The active fractions from the gel filtration column were concentrated using a 10K Amicon Ultra-15 device. The purity of the final product was above 98% and the sample was stored in 40% glycerol at −80° C. for further studies.
EspAmy5 (SEQ ID NO: 12) was purified by ammonium sulphate precipitation and anion-exchange and size-exclusion chromatography columns. Ammonium sulphate was added to fermentation broth containing EspAmy5 to a final saturation of 70%. The solution was stirred at 4° C. overnight, and then centrifuged at 14,000×g for 1 hour. The target protein-containing pellet was resuspended in 20 mM HEPES, pH 8 with 2 mM CaCl2 (buffer A), and then loaded onto a Q-Sepharose column pre-equilibrated with buffer A. After column washing, the protein was eluted by gradient elution of 0-50% 20 mM HEPES pH 8 with 1 M NaCl (buffer B). The flow-through fraction was concentrated and applied to a Superdex in 20 mM sodium phosphate buffer pH 7 with 0.15 M NaCl. Fractions containing target protein were pooled and concentrated using 10 KDa Amicon Ultra-15 devices. The sample was above 90% pure and stored in 40% glycerol at −80° C. until usage.
EmeAmy1 amylase (SEQ ID NO: 14) was purified via two chromatography steps: anion-exchange and size exclusion chromatography. Fermentation broth containing EmeAmy1 was buffer exchanged to 20 mM HEPES, pH 8 with 2 mM CaCl2, and then loaded onto a 50 ml Q-Sepharose column pre-equilibrated with 20 mM HEPES, pH 8 with 2 mM CaCl2 (buffer A). After sample loading, the column was washed with the same buffer for 2 column volumes (CVs), followed by gradient elution of 0-50% 20 mM HEPES pH 8 with 1 M NaCl (buffer B) in 4 CVs and then 100% of buffer B in 2 CVs. Fractions were analyzed by SDS-PAGE and alpha-amylase activity assay. The target protein was found in the flow through fraction. This fraction was concentrated down to less than 10 mL, and applied onto a Superdex 75 XK 26×60 column in 20 mM sodium phosphate buffer pH 7 with 0.15 M NaCl. The fractions containing the target protein were pooled and concentrated using 10 KDa Amicon Ultra-15 devices. The sample was above 95% pure and stored in 40% glycerol at −80° C. until usage.
Alpha-amylase activity of EmeAmy1 (SEQ ID NO: 14) and EspAmy5 SEQ ID NO: 12) was determined using a colorimetric assay to monitor the release of reducing sugars from potato amylopectin. The activity is reported as equivalents of glucose released per minute. Substrate solutions were prepared by mixing 9 mL of 1% potato amylopectin w/w, in water (Sigma, Cat. No. 10118), 1 mL of 0.5 M buffer (pH 5.0 sodium acetate or pH 8.0 HEPES), and 40 μL of 0.5 M CaCl2 into a 15-mL conical tube. Stock solutions of purified alpha-amylase samples were made by diluting original samples to 0.4 mg/mL (400 ppm) in water. Serial dilutions of enzyme samples and glucose standard were prepared in water in non-binding microtiter plates (MTP, Corning 3641). Then 90 μL of substrate solution (preincubated at 50° C. for 5 min at 600 rpm) and 10 μL of the enzyme serial dilution were added and mixed into in non-binding microtiter plates (MTP, Corning 3641). All the incubations were done at 50° C. for 10 min at 600 rpm in a thermomixer (Eppendorf). After incubation, 50 μL of 0.5 N NaOH were added to each well to stop the reaction. Total reducing sugars present in each well were measured using a PAHBAH method (Lever, M. et al. (1973) 82:649-655): 80 μL of 0.5 N NaOH was aliquoted into a microtiter plate, followed by the addition of 20 μL of PAHBAH reagent (5% w/v 4-hydroxybenzoic acid hydrazide in 0.5 N HCl) and 10 μL of each reaction mixture. Plates were incubated at 95° C. for 5 min and cooled down at 4° C. for 5 sec. Samples (80 μL) were then transferred to polystyrene microtiter plates (Costar 9017) and absorbance was measured at 410 nm. Resulting absorbance values were plotted against enzyme concentration and linear regression was used to determine the slope of the line. The α-amylase activities are as shown in Table 2 when calculated using the following equation:
Specific Activity(U/mg)=Slope(enzyme)/slope(std)*100
The effect of pH on the on α-amylase activity of EspAmy8 (SEQ ID NO: 13), EmeAmy1 (SEQ ID NO: 14) and EspAmy5 SEQ ID NO: 12) was monitored using the PAHBAH assay protocol as described above, with a pH range from 3.0 to 10.0. Working buffers consisted of the combination of glycine/sodium acetate/HEPES (250 mM), with pH varying from 3.0 to 10.0. Substrate solutions were prepared by mixing 896 μL of 1% potato amylopectin w/w, in water (Sigma, Cat. No. 10118), 100 μL of 250 mM buffer working solutions at various pH values, and 4 μL of 0.5 M CaCl2. Enzyme working solutions were prepared in water. All the incubations were done using the protocol described for alpha-amylase activity assay. The absorbance from the control (water-only) sample was subtracted, and the resulting values were converted to percentages of relative activity, by defining the activity at the optimal pH as 100%. The pH profiles (Table 3A) and the pH optima and approximate pH range for ≧70% of activities (Table 3B) for EspAmy5 and EmeAmy1, under the conditions of this assay, are shown below.
The effect of temperature on alpha-amylase activity of EmeAmy1 (SEQ ID NO: 14) and EspAmy5 SEQ ID NO: 12) was monitored using the PAHBAH assay protocol as described above at temperatures ranging from 30° C. to 95° C. Substrate solutions were prepared by mixing 3.6 mL of 1% potato amylopectin w/w, in water (Sigma, Cat. No. 10118), 0.4 mL of 0.5 M buffer (pH 5.0 sodium acetate), and 16 μL of 0.5 M CaCl2 into a 15-mL conical tube. Enzyme working solutions were prepared in water. Incubations were done at temperatures ranging from 30° C. to 95° C. for 10 min at 600 rpm in a thermomixer (Eppendorf). After incubation, samples were quenched and measured using the protocol described for alpha-amylase activity assay. The absorbance from the control (water-only) sample was subtracted, and the resulting values were converted to percentages of relative activity, by defining the activity at the optimal temperature as 100%. The temperature profiles (Table 4A) and temperature optima and approximate temperature range for ≧70% of activity (Table 4B) for EspAmy5 and EmeAmy1 are shown below.
The thermostability of EmeAmy1 (SEQ ID NO: 14) and EspAmy5 SEQ ID NO: 12) was measured by monitoring the enzyme activity before and after incubation at temperatures ranging from 40° C. to 95° C. for 2 h. Enzyme samples were diluted in 50 mM of sodium acetate buffer (pH 5.0) containing 2 mM of CaCl2 to appropriate concentration (showing signal within linear range as per dose response curve) and 40 uL was aliquots were added to PCR strip tubes. The tubes were transferred to a PCR machine at the desired temperature ranging from 40° C. to 95′C. After incubation for 2 h, residual enzyme activity was assayed using the amylopectin/PAHBAH method as described previously. The residual activities were converted to percentages of relative activity (Table 5), by defining the activity of the sample kept on ice as 100%.
In order to understand the action pattern of EmeAmy1 (SEQ ID NO: 14) and EspAmy5 SEQ ID NO: 12), a product profile analysis with oligosaccharides maltoheptaose (DP7), amylopectin, and maltodextrin (DE10) was performed using an HPLC method coupled with a refractive index detector. The amylase was incubated with 0.5% (w/v) substrate in 50 mM pH 5.3 sodium citrate buffer (or 50 mM pH 8.2 HEPES buffer) containing 50 mM NaCl and 2 mM CaCl2 at a final concentration of 10 ppm for 120 min at 50° C. Following incubation, the reaction was stopped by adding equal volume of ethanol and the tubes centrifuged for 10 min at 14,000 rpm. The supernatant was diluted 10-fold using MilliQ water, and 10 μL of the diluted supernatant was loaded onto an HPLC column (Aminex HPX-42A, 300 mm*7.8 mm) equipped with a refractive index detector. The mobile phase was MilliQ water, and the flow rate was 0.6 mL/min at 85° C.
Table 6 shows the oligosaccharide product compositions of the amylases. The numbers in the Table depict the peak area percentage of each DPn as a fraction of the total DP1-DP7. Both amylases showed a product profile distribution from DP1 to DP5, with DP5 as the major product produced under acidic and basic conditions of these assays.
The liquefying performance of EmeAmy1 (SEQ ID NO: 14) and EspAmy5 SEQ ID NO: 12) was evaluated by a Rapid Viscosity Analyzer (RVA) assay using a viscometer for measuring the peak and final viscosity of corn flour slurry after incubation with the enzyme dosed at 70 μg at 85° C./pH 5.8 for 10 minutes.
33 g of corn flour slurry substrate (25% dry solids (ds), 9.16% moisture content) was prepared fresh in MilliQ water for the assay and 5 μL of 2 N sulfuric acid was added into slurry to adjust its pH to 5.8, followed by adding the enzyme sample (70 μg) to start the RVA run. A typical RVA run was 10 min total run time by keeping the temperature at 70° C. for 1 min, ramping to 85° C. for 1 min 20 sec, and holding at 85° C. for 7 min 40 sec (
The cleaning performances of EmeAmy1 (SEQ ID NO: 14) and EspAmy5, (SEQ ID NO: 12) were analyzed in a microswatch assay. A sample of BASE (i.e., SEQ ID NO: 2 in U.S. Pat. No. 8,153,412) was included as a benchmark. The assay was performed as described in Example 4 with the following changes: Prior to the assay, the swatches were pre-washed in Milli-Q water at 25° C. with shaking at 350 rpm for 1 hour (water was changed every 20 minutes) and the reactions were incubated at 30° C. Enzyme performance was judged by the amount of color released into the wash liquor (
Although the foregoing compositions and methods have been described in some detail by way of illustration and examples for purposes of clarity of understanding, it will be apparent to those skilled in the art that certain changes and modifications may be made. Therefore, the description should not be construed as limiting the scope of the invention, which is delineated by the appended claims.
All publications, patents, and patent applications cited herein are hereby incorporated by reference in their entireties for all purposes and to the same extent as if each individual publication, patent, or patent application were specifically and individually indicated to be so incorporated by reference.
| Number | Date | Country | Kind |
|---|---|---|---|
| PCT/CN2013/084809 | Oct 2013 | CN | national |
This application claims benefit of priority from international patent application number PCT/CN2013/084809, filed 3 Oct. 2013, which is incorporated herein by reference in its entirety.
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/US2014/056650 | 9/19/2014 | WO | 00 |
