Patent Application
20100009403
Not applicable.
The invention relates to increased production of products by engineered bacteria by limiting respiration, thus conserving carbon for production even in the presence of excess oxygen. Specifically, the invention relates to a ΔubiCA bacteria and its uses.
The energetic state of microbial cells is very important during cell growth and product production. Currently, significant numbers of valuable products are produced through anaerobic fermentation. However, productivity, mainly production rate, of these processes is usually hampered by slow cell growth and low culture density. This is because under anaerobic conditions the cell generates much less energy from the nutrient; it mostly derives its energy through glycolysis that only yields two moles of ATP per mole of glucose consumed. This ATP yield is much lower than that of aerobic respiration, however, the remaining carbon is conserved for product formation. Certainly, a higher energy yield through aerobic respiration can be achieved, but only at the expense of releasing carbon atoms stored in the feedstock (hence lower product yields).
The aerobic respiratory chain of Escherichia coli (E. coli) is composed of a number of membrane-bound, multisubunit enzymes located within the cytoplasmic membrane. Dehydrogenases such as NADH dehydrogenase or succinate dehydrogenase reduce ubiquinone to ubiquinol within the cytoplasmic membrane. Ubiquinol diffuses within the membrane bilayer and is oxidized by either of two quinol oxidase complexes: the cytochrome O complex or the cytochrome D complex. For a complete review of E. coli respiration, see Ingledew and Poole (1984) incorporated herein by reference.
Two operating procedures have been developed in an attempt to strike an ideal balance between energy generation through aerobic respiration (for better cell growth and cell “fitness”) and carbon conservation. One approach is to operate the bioreactor under microaerobic conditions. This reactor configuration provides a slight increase in ATP supply and limits the amount of carbon lost during aerobic respiration. However, it is technically difficult to maintain a constant microaerobic environment in real processes, especially for large bioreactors. Variation in extent of aeration is a problem even in those situations where near complete oxygen saturation is desired. Any increased supply of oxygen will favor cell growth and subsequently decrease the product yield.
A second strategy is to perform the process in two stages. The first stage is to grow the cell under aerobic conditions and then switch to anaerobic conditions for product formation. This strategy avoids the possibility of oxygen oversupply and guarantees a certain product yield for the second stage. However, the supply of ATP still is low during the product formation stage. There are also biological complexities that arise during the transition (proper synthesis and activation of required proteins and cofactors, triggering of cellular stress responses).
What is required to improve production in engineered bacterial cells is a balance between energy generation through aerobic respiration and carbon atom conservation by limited respiration. By limiting respiration, the cell will not “waste” carbon atoms even when the oxygen supply is abundant. At the same time, a sufficient supply of ATP will be available for cell growth and product formation throughout the fermentation processes. Strain respiration can be maintained at levels required for specific bioproduction needs, thus optimizing respiration and carbon conservation.
The Invention is generally directed to engineered bacterial cells having a balance between energy generation through aerobic respiration and carbon atom conservation by limited respiration. Disruption, mutation, inactivation, or complete deletion of electron transfer genes can be used to control respiration. The invention improves the performance of anaerobic processes, particularly those processes requiring significant energy for substrate uptake, product formation, or processes that do not perform well due to a lack of electron acceptors.
In one embodiment, ATP is limited through control of aerobic respiration. This approach provides a limited carbon flow for energy generation independent of oxygen supply; thus this approach also conserves substrate carbon atoms for product formation (hence be able to maintain high product yield). Aerobic respiration can be limited in two ways:
For example, the invention can be achieved by reducing activity of one or more NDH, SDH, UbiCA, CytO, or CytD. In one embodiment, ubiCA is deleted, and in another embodiment a mutant ubiCA with reduced activity is expressed. Deletion of the ubiCA operon prevents production of ubiquinone. Electron transfer can then be regulated by adding ubiquinone or controlling exogenous ubiCA expression.
Ubiquinone (Coenzyme Q) is an essential component of bacterial respiratory chains. The first committed step in the biosynthetic pathway is the formation of 4-hydroxybenzoate from chorismate by the enzyme chorismate pyruvate-lyase encoded by the ubiC gene. The 4-hydroxybenzoate is prenylated by 4-hydroxybenzoate octaprenyltransferase encoded by the ubiA gene. The two genes are linked at 91.5 min in the E. coli chromosome (see e.g, AP—004540 and AP—004541), and are found in all bacterial species with homologies ranging from to as low as 33% (while still being recognized as chorismate-pyruvate lyase, see e.g., NP—932913) and 24% (while still being recognized as polyprenyltransferase, see e.g., ZP—00987621).
NADH-CoQ reductase in E. coli is encoded by either of two different membrane-bound NADH dehydrogenases (NDH-1 and NDH-2). Succinate dehydrogenase (SDH) reduces succinate to fumarate and reduces ubiquinone to ubiquinol. The Cyto complex is encoded by cyoABCDE operon and Cytd encoded by the cydAB operon.
Carboxylic acids described herein can be a salt, acid, base, or derivative depending on structure, pH, and ions present. For example, the terms “succinate” and “succinic acid” are used interchangeably herein. Chemicals used herein, including formate, glyoxylate, lactate, malate, oxaloacetate (OAA), phosphoenolpyruvate (PEP), and pyruvate, can be found in the NATIONAL LIBRARY OF MEDICINE® PUBCHEM™ database (pubchem.ncbi.nlm.nih.gov) incorporated herein by reference Bacterial metabolic pathways including the Krebs cycle (also called citric acid, tricarboxylic acid, or TCA cycle) can be found in Principles of Biochemistry 2nd ed., by Lehninger (1993), incorporated herein by reference, as well as other biochemistry texts.
The terms “operably associated” or “operably linked,” as used herein, refer to functionally coupled nucleic acid sequences.
“Reduced activity” is defined herein to be at least a 75% reduction in protein activity, as compared with an appropriate control species. Preferably, at least 80, 85, 90, or 95% reduction in activity is attained, and in the most preferred embodiment, the activity is eliminated (100% or “inactivation”). Proteins can be inactivated with inhibitors, by mutation, or by suppression of expression or translation, and the like. By “null mutant” or “null mutation” what is meant is that protein activity is completely inactivated. In one example, the control plasmid is inserted without the gene of interest. In another example, the gene of interest is completely removed by recombination. Additionally, the gene of interest may be removed by inactivation, mutation, or truncation which eliminates activity.
“Overexpression” or “overexpressed” is defined herein to be greater than wild type activity, preferably above 125% increase, more preferably above 150% increase in protein activity as compared with an appropriate control species. Preferably, the activity is increased 100-500%. Overexpression is achieved by mutating the protein to produce a more active form, a more stable form, or a form that is resistant to inhibition, by removing inhibitors, adding activators, and the like. Overexpression can also be achieved by removing repressors, adding multiple copies of a gene to the cell, up-regulating an existing gene, adding an exogenous gene, and the like.
The terms “disruption” and “disruption strains,” as used herein, refer to cell strains in which the native gene is mutated, deleted, interrupted, or down-regulated in such a way as to decrease the activity of the gene. A gene is completely (100%) reduced by knockout or removal of a portion or the entire gene sequence. Use of a frame shift mutation, early stop codon, point mutations of critical residues, or deletions or insertions, and the like, can completely inactivate (100%) gene product by completely preventing transcription and/or translation of active protein.
The term “exogenous” indicates that the protein or nucleic acid is a non-native molecule introduced from outside the organism or system without regard to species of origin. For example, an exogenous peptide may be applied to the cell culture; an exogenous RNA may be expressed from a recombinant DNA transfected into a cell; or a native gene may be under the control of exogenous regulatory sequences.
As used herein “recombinant” is relating to, derived from, or containing genetically engineered material.
A gene or cDNA may be “optimized” for expression in E. coli or other bacterial species using the codon bias for the species. Various nucleotides can encode a single peptide sequence. Understanding the inherent degeneracy of the genetic code allows one of ordinary skill in the art to design multiple nucleotides which encode the same amino acid sequence. NCBI™ provides codon usage databases for optimizing DNA sequences for protein expression in various species.
In calculating “% identity” the unaligned terminal portions of the query sequence are not included in the calculation. The identity is calculated over the entire length of the reference sequence; thus short local alignments with a query sequence are not relevant (e.g., % identity =number of aligned residues in the query sequence/length of reference sequence). Alignments are performed using BLAST homology alignment as described by Tatusova TA & Madden TL (1999) FEMS Microbiol. Lett. 174:247-50. The default parameters were used, except the filters were turned OFF. As of Jan. 1, 2001 the default parameters were as follows: BLASTN or BLASTP as appropriate; Matrix=none for BLASTN, BLOSUM62 for BLASTP; G Cost to open gap default=5 for nucleotides, 11 for proteins; E Cost to extend gap [Integer] default=2 for nucleotides, 1 for proteins; q Penalty for nucleotide mismatch [Integer] default=−3; r reward for nucleotide match [Integer] default=1; e expect value [Real] default=10; W word size [Integer] default=11 for nucleotides, 3 for proteins; y Dropoff (X) for blast extensions in bits (default if zero) default=20 for blastn, 7 for other programs; X dropoff value for gapped alignment (in bits) 30 for blastn, 15 for other programs; Z final X dropoff value for gapped alignment (in bits) 50 for blastn, 25 for other programs. This program is available online at NCBI™ (www.ncbi.nlm.nih.gov/BLAST/).
Common restriction enzymes and restriction sites are found at NEB® (New England Biolabs®, www.neb.com) and Invitrogen® (www.invitrogen.com). ATCC®, American Type Culture Collection™ (www.atcc.org) has an extensive collection of cell strains that are publicly available and incorporated herein by reference.
Plasmids and strains used in certain embodiments of the invention are set forth in Table 2.
When plasmids are used, the effect of host/plasmid interaction is minimized by comparing three different systems consisting of: the host only, a plasmid expressing biologically active enzyme, and a control system with the expression vector alone.
We sought to study the effect of exogenous supplementation of ubiquinone-1 (UQ-1) to a ΔubiCA mutant strain, AMS001 on cell respiration by measuring both cell growth and lactate yield, as an example of product formation. This mutant cannot produce ubiquinone due to a disruption (deletion) in ubiCA.
Aerobic shake flask experiments with this mutant strain were carried out in 125-ml shake flasks containing 10 ml of LB medium supplemented with 20 g/L of glucose in a rotary shaker at 37° C. and 250 rpm. The final optical density and the specific lactate yield after 24 hours are summarized in
The ΔubiCA mutant strain grows very poorly and produces a large amount of lactate. The ΔubiCA mutant, due to the disruption in the electron chain, cannot use oxygen as the electron receptor even grown under aerobic conditions. Instead, the cell opted to recycle the NADH to NAD+ through the formation of lactate (the ethanol pathway is not active aerobically). Thus, the metabolic pattern of the ΔubiCA mutant strain behaves similar to one that is grown anaerobically, even in the presence of air.
Addition of different amounts of ubiquinone to the culture increased the final optical density and reduced the amount of lactate accumulated. The mutant strain responded to ubiquinone supplementation in a graded manner. The reduction in lactate formation suggests that the electron transfer chain is partially recovered and the cells are capable using oxygen as the electron acceptor. However, the mutant strain did not fully recover even when the concentration was increased to 400 μM. It is possible that the low solubility of UQ-1 in the medium limits the uptake of this molecule. Another explanation might be that some intermediate products in the ubiquinone biosynthesis pathway are necessary for full recovery and restoration of the cell. These experiments demonstrate recovery by the exogenous addition of ubiquinone and control of cellular respiration rates using ubiquinone supplementation.
Complementation experiments were performed by transforming AMS001 with pUBICA. The growth characteristics and metabolic patterns were fully recovered by the introduction of a plasmid carrying a normal ubiCA gene to the ΔubiCA mutant (data not shown). Expression of exogenous UbiCA demonstrates influence of growth behavior and metabolic patterns in an aerobic E. coli culture by manipulating the supply of the ubiquinone. By manipulating expression of the ubiCA operon, the amount of ubiquinone can be controlled and respiration can be tailored to the production process.
All references are listed herein for the convenience of the reader. Each is incorporated by reference in its entirety.
This application claims priority to U.S. Provisional Application 60/824,879 filed Sep. 7, 2006, and incorporated by reference in its entirety.
This invention may have been sponsored in part by funds from the U.S. Government. Therefore, the U.S. Government may have certain rights in the invention.
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/US07/77947 | 9/7/2007 | WO | 00 | 2/27/2009 |
| Number | Date | Country | |
|---|---|---|---|
| 60824879 | Sep 2006 | US |
