Patent Application
20120292022
This invention relates to the field of oil recovery from environmental locations. More specifically, compositions including N-lauroyl amino acid-based chemical compounds having oil release activity and oil recovery enhancing microbes are used for improving oil recovery from oil reservoirs.
Hydrocarbons in the form of petroleum deposits and crude oil reservoirs are distributed worldwide. These oil reservoirs are measured in the hundreds of billions of recoverable barrels. Because heavy crude oil has a relatively high viscosity and may adhere to surfaces, it is essentially immobile and cannot be easily recovered by conventional primary and secondary means.
Use of surface active agents or surfactants to increase solubility of oil through reduction in surface and interfacial tensions is another technique for increasing crude oil recovery. A wide variety of surfactants identified thus far are able to significantly reduce surface and interfacial tensions at oil/water and air/water interfaces. Because surfactants partition at oil/water interfaces, they are capable of increasing the solubility and bioavailability of hydrocarbons (Desai and Banat (1997) Microbiol. Mol. Biol. Rev. 61: 47-64; Banat (1995) Bioresource Technol. 51:1-12; Kukukina et al. (2005) Environment International 31:155-161; Mulligan (2005) Environmental Pollution 133:183-198). For example, Doong and Lei ((2003) Journal of Hazardous Materials B96:15-27) found that the addition of surfactants to soil environments contaminated with polyaromatic hydrocarbons increased the mineralization rate of some hydrocarbons.
Microorganisms have been used to enhance oil recovery from subterranean formations using various processes which may improve sweep efficiency and/or oil release. For example, viable microorganisms may be injected into an oil reservoir where they may grow and adhere to the surfaces of pores and channels in the rock or sand matrices in the permeable zones to reduce water channeling, and thereby target injection water flow towards less permeable oil-bearing strata. Processes for promoting growth of indigenous microbes by injecting nutrient solutions into subterranean formations are disclosed in U.S. Pat. No. 4,558,739 and U.S. Pat. No. 5,083,611. Injection of microorganisms isolated from oil recovery sites into subterranean formations along with nutrient solutions has been disclosed, including for Pseudomonas putida and Klebsiella pneumoniae (U.S. Pat. No. 4,800,959), for a Bacillus strain or Pseudomonas strain I-2 (ATCC 30304) isolated from tap water (U.S. Pat. No. 4,558,739), and for Pseudomonas putida, Pseudomonas aeruginosa, Corynebacterium lepus, Mycobacterium rhodochrous, and Mycobacterium vaccae (U.S. Pat. No. 5,163,510). Injection of a surfactant and isolated ultramicrobacteria which, when resuscitated, degrade the surfactant and provide plugging is disclosed in U.S. Pat. No. 5,174,378.
There remains a need for additional methods to improve oil recovery from oil reservoirs that make use of novel compositions.
The method described herein provides for improved recovery of oil from an oil reservoir containing oil-coated surfaces. The method makes use of a composition having one or more N-lauroyl amino acid-based chemical compounds, which promote the release of surface adhered crude oil, and one or more microorganisms which have properties useful for improving oil recovery.
Accordingly, the invention provides a method for improving oil recovery from an oil reservoir comprising:
In another embodiment the invention provides:
An oil recovery enhancing composition comprising:
The invention can be more fully understood from the following detailed description and Figures which form a part of this application.
Applicants specifically incorporate the entire content of all cited references in this disclosure. Unless stated otherwise, all percentages, parts, ratios, etc., are by weight. Trademarks are shown in upper case. Further, when an amount, concentration, or other value or parameter is given as either a range, preferred range or a list of upper preferable values and lower preferable values, this is to be understood as specifically disclosing all ranges formed from any pair of any upper range limit or preferred value and any lower range limit or preferred value, regardless of whether ranges are separately disclosed. Where a range of numerical values is recited herein, unless otherwise stated, the range is intended to include the endpoints thereof, and all integers and fractions within the range. It is not intended that the scope of the invention be limited to the specific values recited when defining a range.
The invention relates to methods for improving oil recovery from an oil reservoir by inoculating an oil reservoir with a microorganism and a minimal growth medium that supports growth of the microorganism in the presence of an electron acceptor in the subterranean location, as well as at least one N-lauroyl amino acid-based compound that has oil releasing properties. These compounds were found to promote release of oil from a surface. Compositions containing one or more of these compounds may be used to contact surfaces in oil reservoirs, and act in combination with microorganisms having activities that improve oil recovery.
The following definitions are provided for the special terms and abbreviations used in this application:
The abbreviation “ASTM” refers to the American Society for Testing and Materials.
The terms “oil well”, “oil reservoir”, and “oil-bearing stratum” may be used herein interchangeably and refer to a subterranean, subsurface, or sea-bed formation from which oil may be recovered. The formation is generally a body of rocks and soil having sufficient porosity and permeability to store and transmit oil.
The term “well bore” refers to a channel from the surface to an oil-bearing stratum with enough size to allow for the pumping of fluids either from the surface into the oil-bearing stratum (injection well) or from the oil-bearing stratum to the surface (production well).
The terms “denitrifying” and “denitrification” mean reducing nitrate for use in respiratory energy generation.
The term “sweep efficiency” refers to the fraction of an oil-bearing stratum that has seen fluid or water passing through it to move oil to production wells. One problem that can be encountered with waterflooding operations is the relatively poor sweep efficiency of the water, i.e., the water can channel through certain portions of a reservoir as it travels from injection well(s) to production well(s), thereby bypassing other portions of the reservoir. Poor sweep efficiency may be due, for example, to differences in the mobility of the water versus that of the oil, and permeability variations within the reservoir which encourage flow through some portions of the reservoir and not others.
The term “pure culture” means a culture derived from a single cell isolate of a microbial species. The pure cultures specifically referred to herein include those that are publicly available in a depository, and those identified herein.
The term “biofilm” means a film or “biomass layer” of microorganisms. Biofilms are often embedded in extracellular polymers, which adhere to surfaces submerged in, or subjected to, aquatic environments. Biofilms consist of a matrix of a compact mass of microorganisms with structural heterogeneity, which may have genetic diversity, complex community interactions, and an extracellular matrix of polymeric substances.
The term “plugging biofilm” means a biofilm that is able to alter the permeability of a porous material, and thus retard the movement of a fluid through a porous material that is associated with the biofilm.
The term “simple nitrates” and “simple nitrites” refer to nitrate (NO3−) and nitrite (NO2−), respectively, as they occur in ionic salts such as potassium nitrate, sodium nitrate, and sodium nitrite.
The term “electron acceptor” refers to a molecular compound that receives or accepts an electron(s) during cellular respiration. Microorganisms obtain energy to grow by transferring electrons from an “electron donor” to an electron acceptor. During this process, the electron acceptor is reduced and the electron donor is oxidized. Examples of acceptors include oxygen, nitrate, fumarate, iron (III), manganese (IV), sulfate or carbon dioxide. Sugars, low molecular weight organic acids, carbohydrates, fatty acids, hydrogen and crude oil or its components such as petroleum hydrocarbons or polycyclic aromatic hydrocarbons are examples of compounds that can act as electron donors.
The term “terrestrial subsurface formation” or “subsurface formation” refers to in ground or underground geological formations and may comprise elements such as rock, soil, sand, shale, clays and mixtures thereof.
The term “terrestrial surface formation” or “surface formation” refers to above ground geological formations and may comprise elements such as rock, soil, sand, shale, clays and mixtures thereof.
The term “environmental site” means a site that has been contaminated with hydrocarbons, and may have other persistent environmental pollutants. Environmental sites may be in surface or subsurface locations.
“Production wells” are wells through which oil is withdrawn from an oil reservoir. An oil reservoir or oil formation is a subsurface body of rock having sufficient porosity and permeability to store and transmit oil.
The term “injection water” refers to fluid injected into oil reservoirs for secondary oil recovery. Injection water may be supplied from any suitable source, and may include, for example, sea water, brine, production water, water recovered from an underground aquifer, including those aquifers in contact with the oil, or surface water from a stream, river, pond or lake. As is known in the art, it may be necessary to remove particulate matter including dust, bits of rock or sand and corrosion by-products such as rust from the water prior to injection into the one or more well bores. Methods to remove such particulate matter include filtration, sedimentation and centrifugation.
The term “production water” means water recovered from production fluids extracted from an oil reservoir. The production fluids contain both water used in secondary oil recovery and crude oil produced from the oil reservoir.
The term “inoculating an oil well” means injecting one or more microorganisms or microbial populations or a consortium into an oil well or oil reservoir such that microorganisms are delivered to the well or reservoir without loss of viability.
The term “irreducible water saturation” refers to the minimal water saturation that occurs in a porous core plug when flooding with oil to saturation. It represents the interstitial water content of the matrix where the water is never completely displaced by the oil because a minimal amount of water is retained to satisfy capillary forces.
The term “remediation” refers to the process used to remove hydrocarbon contaminants from an environmental site containing hydrocarbons and optionally other persistent environmental pollutants.
The term “petroleum” or “crude oil” or “oil” herein refers to a complex mixture of naturally occurring hydrocarbons or various molecular weights, with other organic compounds.
“Interface” as used herein refers to the surface of contact or boundary between immiscible materials, such as oil and water or a liquid and a solid. As used herein “interfaces” may be between a water layer and an oil layer, a water layer and a solid surface layer, or an oil layer and a solid surface layer.
“Hydrocarbon-coated” or “oil-coated” as used herein refer to a coating of hydrocarbons or crude oil (also petroleum or oil) to a solid surface of at least 10% areal coverage.
“Adhered to” refers to the coating or adsorption of a liquid to a solid surface of at least 10% areal coverage.
The term “critical micelle concentration” or “CMC” refers to the concentration of a surfactant above which micelles form spontaneously.
The term “wetting” refers to the ability of a liquid to maintain contact with a solid surface, resulting from intermolecular interactions when the two are brought together. The degree of wetting (expressed as “wettability”) is determined by a force balance between adhesive and cohesive forces.
“Wetting agent” refers to a chemical such as a surfactant that increases the water wettability of a solid or porous surface by changing the hydrophobic surface into one that is more hydrophilic. Wetting agents help spread the wetting phase (e.g., water) onto the surface thereby making the surface more water wet.
“Wettability” refers to the preference of a solid to contact one liquid, known as the wetting phase, rather than another. Solid surfaces can be water wet, oil wet or intermediate wet. “Water wettability” pertains to the adhesion of water to the surface of a solid. In water-wet conditions, a thin film of water coats the solid surface, a condition that is desirable for efficient oil transport.
The term “adhesive forces” refers to the forces between a liquid and solid that cause a liquid drop to spread across the surface.
The term “cohesive forces” refers to forces within the liquid that cause a liquid drop to ball up and avoid contact with the surface.
The term “contact angle” is the angle at which a liquid (oil or water) interface meets a solid surface, such as sand or clay. Contact angle is a quantitative measurement of the wetting of a solid by a liquid and is specific for any given system, and is determined by interactions across three interfaces. The concept is illustrated with a small liquid droplet resting on a flat horizontal solid surface. The shape of the droplet is determined by the “Young Relation” (Bico et al., Colloids and Surfaces A: Physicochemical and Engineering Aspects 206 (2002) 41-46). The theoretical description of contact arises from the consideration of a thermodynamic equilibrium between the three phases: the liquid phase of the droplet (L), the solid phase of the substrate (S), and the gas/vapor phase of the ambient (V) (which will be a mixture of ambient atmosphere and an equilibrium concentration of the liquid vapor). The V phase could also be another (immiscible) liquid phase. At equilibrium, the chemical potential in the three phases should be equal. It is convenient to frame the discussion in terms of interfacial energies. The solid-vapor interfacial energy (see surface energy) is γSV, the solid-liquid interfacial energy is γSL L and the liquid-vapor energy (i.e. the surface tension) is simply γ. The Young equation: 0=γSV−γSL−cos θ is written such that describes an equilibrium where θC is the equilibrium contact angle. In the three phase systems described herein (solid phase, hydrocarbon phase, aqueous phase), the contact angle is described as the angle through the hydrocarbon phase rather than through the aqueous phase.
Chemical compounds are identified herein that are effective for releasing oil from a surface. These compounds are N-lauroyl amino acid-based compounds with the structure:
where:
R1 is H, CH3, or is part of a heterocyclic ring (—CH2—)n, where n=3, 4, or 5, and the ring is directly connected to the rest of the structure at R4, such as that derived from L-proline as shown below:
R3 and R4 are independently H, a straight chain alkyl or branched-chain alkyl group with 1 to 5 carbons, —CH2OH, —CH2CH2SCH3, a cycloalkyl group, a substituted cycloalkyl group, an aryl group, an alkylaryl group; a substituted aryl group; a phenyl group, —CH2Ph where Ph is phenyl, —CH(Ph)Ph; a heterocycle; a substituted heterocycle; or is part of a heterocyclic ring (—CH2—)n, where n=3, 4, or 5 and is directly connected to the rest of the structure at R1; and
R5 is a monovalent cation or H.
The stereochemistry of any asymmetric carbon within the N-acyl amino acid compounds of the structures given above may be either R or S, or a mixture of R and S stereoisomers. In one embodiment the N-acyl amino acid compound contains one or more stereocenters.
In one embodiment R3 and R4 do not have charged groups. It is desirable to maintain the compound at a pH that avoids having a charged group in the R3 and R4 side chains. In one embodiment R3 and R4 are independently a nonpolar alkyl group, an aryl group, or a polar uncharged group. In one embodiment the substituted aryl group contains substituents that are uncharged.
In one embodiment R3 is H or CH3.
In one embodiment R5 is an alkali metal cation, such as Na+ or K+.
In one embodiment the total sum of the number of carbons of R3 and R4 are equal to or between the integers of 1 and 25.
Examples of chemical compounds of Structure (I) that may be used in the present methods include structures (III) through (XXIII) below:
Chemical compounds of the general structure (I) may be used to release oil from a surface. As representatives of general structure (I), compounds of structures (II) through (XXIII) were shown to be active in an oil release assay. Though oil was released, increase in solubility of oil was not observed, thus indicating that an originally oil-coated surface became less oil wet and more water wet to release the oil.
Properties of the representative compound N-lauroyl-L-alanine in decreasing interfacial tension (IFT) do not suggest that this compound would have good surfactant activity. Typical good surfactants, such as surfactin, rhamnolipids, and many nonionic surfactants such as fatty alcohols, Tritons, Brii, and Tergitol would have an IFT drop of orders of magnitude in a standard interfacial tension assay such as in Example 5 herein. Such surfactants would typically be good oil solubilizers for release of oil. N-lauroyl-alanine at a concentration of 0.1% had a decrease in IFT that was less than 5-fold as compared to the medium alone control, a much smaller IFT drop than is characteristic of surfactants good for solubilizing oil.
In addition, a typical good surfactant would have a critical micelle concentration (CMC) in the μM range. The CMC may be determined by the concentration where measurement of drop in surface tension levels out. This is the concentration above which micelles form spontaneously. CMCs of N-lauroyl-L-alanine, N-lauroyl-L-valine, and N-lauroyl-L-phenylalanine were measured to be between about 0.1 mM and 1 mM in a surface tension assay in Example 5 herein.
Thus, although representative compounds of the general structure (I) do not have strong surfactant properties that would provide oil solubilizing activity, these compounds were found herein to have oil release activity. The properties of these compounds are more similar to properties of wetting agents that would typically not be considered to be useful for oil release. However, altering wettability of an oil-coated surface using the present compounds, as assayed in the LOOS test described herein, was shown to provide oil release activity. Oil release obtained using the present compounds may be at least about 5%, 10%, 15%, 20%, 25%, 30%, 35% or greater of oil coated on a surface.
In different environmental conditions, use of specific compounds of structure (I) may be preferred. For example, it was found that activities of different compounds of structure (I) vary in high salts solutions. In solutions with high NaCl, MgCl2, or a combination of NaCl, MgCl2 and CaCl2, with a salts concentration of about 5% to 6%, N-lauroyl-L-alanine (NLA) and N-lauroyl-L-valine (NLV) were active in releasing oil while N-lauroyl-L-phenylalanine (NLP) was not. Compounds of structure (I) that are most effective at the salt concentration and temperature of a specific environment can be readily determined by one of skill in the art. Temperature of production water and temperature in an oil reservoir provide information on conditions at an environmental site. One skilled in the art can readily assess the oil release activity of different compounds of structure (I) under specific environmental conditions, for example using the assay described in General Methods herein, such that compounds effective for a target environment may be chosen. Specifically, a LOOS test or alternate oil release assay is carried out under the target environmental conditions, which may include specific salinity, inclusion of specific salts, use of specific temperature, or other factors that characterize a target environment.
It is contemplated that compounds having structures similar to structure (I), but with shorter or longer carbon chains replacing (CH2)10, would be effective for oil release under conditions in which these compounds are soluble. Such conditions may include, for example, lower salt conditions, and/or temperatures higher than room temperature. In addition, other surfactants may be used to solubilize the shorter or longer carbon chain compounds, that are of structure (I) in other respects, in a water-based system so that they may be effective for oil release.
It is contemplated that compounds of structure (I) are biodegradable and are less toxic than typical chemical surfactants. In addition, compounds of structure (I) are able to release oil from surfaces without greatly dropping the interfacial tension between the hydrocarbons and water, so as to avoid the generation of emulsions which can be difficult to break. These characteristics of compounds of structure (I) provide benefits to their use in the environment relative to other chemical surfactants.
It is contemplated that a compound of structure (I) may be synthesized by an enzymatic pathway in a microorganism. Amino acid and fatty acid biosynthesis is common to microorganisms. Enzymatic activity to combine an amino acid and a fatty acid to produce a compound of structure (I) may be present in a microorganism which synthesizes the amino acid and fatty acid. Alternatively, enzymatic activities may be engineered in a microorganism for synthesis of a compound of structure (I).
The present composition contains one or more compounds of structure (I) and at least one microorganism which grows in the presence of oil and in the presence of an electron acceptor, and which has properties useful for improving oil recovery. The composition may be in any form suitable for introduction to an oil reservoir containing oil-coated surfaces. Typically the composition is a water-based fluid prepared using a source of water such as injection water. In one embodiment the compound added in the composition may be the carboxylic acid form of structure (I), where R5 is H. In this embodiment, the salt form of the compound is formed in the composition under conditions where the carboxylate salt can be formed, such as in the presence of carbonates, such as calcium carbonate. This may occur in the composition itself if the fluid contains salt-forming compounds, or at the location of contact with oil-coated surfaces, described below.
The concentration of the compound of structure (I) in the present composition is determined by the oil release activity of the specific compound in use. For example N-lauroyl-L-phenylglycine is effective at 1 mM and may be used in this concentration, while NLA is used in 10 mM concentration. One of skill in the art can readily determine the effective concentration for the specific compound of use.
A compound of structure (I) may be synthesized chemically. Chemical synthesis of representative compounds of structure (I) is described in the Examples section herein using methods well-known by one skilled in the art. When a compound of structure (I) is synthesized by a microorganism, as described above, the compound may be provided in the medium in which the microorganism is grown. In addition, the compound may be synthesized in situ in an oil reservoir site by a microorganism of the present composition.
Any microorganism which grows in the presence of oil and an electron acceptor, that has properties useful for improving oil recovery, may be included in the present composition. Useful microorganisms have properties such as metabolizing oil, releasing oil from surfaces, forming biofilms, and/or forming plugging biofilms. Microorganisms that may be used include, but are not limited to, species belonging to the genera: Pseudomonas, Bacillus, Actinomycetes, Acinetobacter, Arthrobacter, Schizomycetes, Corynebacteria, Achromobacteria, Enterobacteria, Nocardia, Saccharomycetes, Schizosaccharomyces, Vibrio, Shewanella, Arcobacter, Thauera, Petrotoga, Microbulbifer, Marinobacteria, Klebsiella, Fusibacteria and Rhodotorula. The present composition may include only one species, two or more species of the same genera, or species from a combination of different genera of microorganisms.
The properties of the microorganism(s) of the present composition may enhance the oil release activity of the compound of structure (I) of the composition, may provide a different activity to improve oil release, or may have multiple types of activities. These microorganisms grow in the presence of oil and may use a component of oil as a carbon source. These microorganisms grow in anaerobic and/or microaerophilic conditions.
In one embodiment, one or more Pseudomonas stutzeri strains are included in the present composition. For example, Pseudomonas stutzeri strain LH4:15 (ATCC # PTA-8823) which is disclosed in US Patent Application Publication 20090263887, which has properties of growth on oil as the sole carbon source and biofilm forming activity, is included in the composition. Though strain LH4:15 did not increase oil release activity when combined with NLA in examples herein, a composition containing a compound of structure (I) would benefit from biofilm forming activity of strain LH4:15 to increase oil recovery for example by increasing sweep efficiency. Pseudomonas stutzeri strains BR5311 (ATCC # PTA-11283) and 89AC1-2 (ATCC # PTS-11284), which form plugging biofioms (U.S. patent application Ser. No. 13/280,849, filed Oct. 25, 2011) may be included independently or in combinations.
In one embodiment a Shewanella sp. is included in the present composition. Shewanella is a bacterial genus that has been established, in part through phylogenetic classification by rDNA and is fully described in the literature (see for example Fredrickson et al., Towards Environmental Systems Biology Of Shewanella, Nature Reviews Microbiology (2008), 6 (8), 592-603; Hau et al., Ecology And Biotechnology Of The Genus Shewanella, Annual Review of Microbiology (2007), 61, 237-258). For example, Shewanella putrefaciens strain LH4:18 which is disclosed in U.S. Pat. No. 7,776,795 and US Patent Application Publication 2011/0030956, and has properties of growth on oil as the sole carbon source and oil release activity, is included. Strain LH4:18 was shown to enhance oil release activity of NLA at low concentration. Shewanella sp. L3:3 (ATCC # PTA-10980) disclosed in US Patent Application Publication 2011/0030956, having oil release activity, may be included independently or in combinations with other microorganisms.
In one embodiment an Arcobacter species belonging to a group identified as Clade 1 is included in the present composition. In molecular phylogenetic analysis of Arcobacter strains, Clade 1 is a group that includes the known species Arcobacter marinas, Arcobacter halophilus, and Arcobacter mytili (U.S. patent application Ser. No. 13/280,972, filed Oct. 25, 2011). For example Arcobacter sp. 97AE3-12 (ATCC # PTA-11409) and/or Arcobacter sp. 97AE3-3 (ATCC # PTA-11410) may be included independently or in combinations. These are Arcobacter strains isolated from oil reservoir production water which produce plugging biofilms and belong to Arcobacter Clade 1.
In one embodiment Thauera sp. AL9:8 (ATCC # PTA-9497) is included in the present composition. Thauera sp. AL9:8 was isolated from subsurface soil samples and was shown to be capable of growth under denitrifying conditions using oil or oil components as the sole source of carbon. This microorganism also has oil releasing activity (U.S. Pat. No. 7,708,065).
The present composition includes components of a minimal growth medium, including one or more electron acceptors and at least one carbon source. Electron acceptors may include, for example, nitrate, fumarate, iron (III), manganese (IV), and sulfate. In one embodiment the electron acceptor is nitrate and the microorganism grows in denitrifying conditions. Nitrate is reduced to nitrite and/or to nitrogen during growth of the microorganism.
The carbon source may be a simple or a complex carbon-containing compound. The carbon source may be complex organic matter such as oil or an oil component, peptone, corn steep liquor, or yeast extract. In another embodiment the carbon source is a simple compound such as citrate, fumarate, maleate, pyruvate, succinate, acetate, or lactate.
The compositions may include additional components which promote growth of, oil release by, and/or biofilm formation by the microorganisms of the composition. These components may include, for example, vitamins, trace metals, salts, nitrogen, phosphorus, magnesium, buffering chemicals, and/or yeast extract
The composition may contain additional components such as surfactants that aid oil recovery.
The present method provides for releasing oil from oil-coated surfaces by the compound of structure (I) of the composition, and optionally by microorganisms of the composition. Oil-coated surfaces may be any hard surface (including one or more particle) that is coated or contaminated with hydrocarbons of oil, with at least 10% areal coverage by said hydrocarbons. The hydrocarbons may be adhered to said surfaces. Hydrocarbon-coated surfaces may be in subsurface formations, for example in oil reservoirs, and may include rock, soil, sand, clays, shale, and mixtures thereof.
In the present method, the present composition is used to inoculate an oil reservoir leading to enhancement in oil recovery. The microorganisms in the composition include viable cells that populate and grow in the oil reservoir. Oil reservoirs may be inoculated with the present composition using any introduction method known to one skilled in the art. Typically inoculation is by injecting a composition into an oil reservoir. Injection methods are common and well known in the art and any suitable method may be used (see for example Nontechnical guide to petroleum geology, exploration, drilling, and production, 2nd edition. N. J. Hyne, PennWell Corp. Tulsa, Okla., USA, Freethey, G. W., Naftz, D. L., Rowland, R. C., & Davis, J. A. (2002); and Deep aquifer remediation tools: Theory, design, and performance modeling, In: D. L. Naftz, S. J. Morrison, J. A. Davis, & C. C. Fuller (Eds.) (2002); and Handbook of groundwater remediation using permeable reactive barriers (pp. 133-161), Amsterdam: Academic Press. (2002)).
Injection may be through one or more injection wells, which are in communication underground with one or more production wells from which oil is recovered. The injected composition will flow into an area comprising oil-coated surfaces and fluid containing released oil is recovered at the production well. Alternatively, the present composition may be pumped down a producer well and into the formation containing oil-coated surfaces, followed by back flow of fluid containing released oil out of the producer well (huff and puff).
Improved oil recovery from an oil reservoir may include secondary or tertiary oil recovery of hydrocarbons from subsurface formations. Specifically, hydrocarbons are recovered that are not readily recovered from a production well by water flooding or other traditional secondary oil recovery techniques. Primary oil recovery methods, which use only the natural forces present in an oil reservoir, typically obtain only a minor portion of the original oil in the oil-bearing strata of an oil reservoir. Secondary oil recovery methods such as water flooding may be improved using the present method by promoting oil release from oil-coated surfaces by contact with a composition including at least one compound of structure (I). In addition, oil recovery is improved by the presence of microorganisms that grow and have oil release and/or plugging biofilm formation activity. Biofilm plugging of permeable formations may reroute water used in water flooding towards less permeable, more oil rich areas. Thus enhanced oil recovery from the presence of plugging biofilms is obtained particularly from oil reservoirs where sweep efficiency is low due to, for example, interspersion in the oil-bearing stratum of rock layers that have a substantially higher permeability compared to the rest of the rock layers. The higher permeability layers will channel water and prevent water penetration to the other parts of the oil-bearing stratum. Formation of plugging biofilms by microorganisms will reduce this channeling.
The oil released from oil-coated surfaces and from improved sweep efficiency may be recovered in production water as is the oil from primary and secondary recovery processes. This oil may be further processed by standard petroleum processing methods for commercial use.
The present invention is further defined in the following Examples. It should be understood that these Examples, while indicating preferred embodiments of the invention, are given by way of illustration only. From the above discussion and these Examples, one skilled in the art may ascertain the essential characteristics of this invention, and without departing from the spirit and scope thereof, may make various changes and modifications of the invention to adapt it to various usages and conditions.
The meaning of abbreviations is as follows: “hr” means hour(s); “mL” means millilitre(s); “° C.” means degrees Celsius; “mg” means milligram(s); “mm” means millimeter(s); “g” means gram(s); “GC” means gas chromatography; “g of oil/g of total fluid” means gram of oil per gram of total fluid; “ppm” means parts per million; “mM” means millimolar; “%” means percent; “min” means minute(s); “mL/min means milliliter per minute; “μg/L” means microgram per liter; “nM” means nanomolar; “μM” means micromolar, “Et3N” means triethylamine, “Et2O” means diethyl ether, “EtOAc” means ethyl acetate, “NLA” means N-lauroyl-L-alanine, “SIB” means simulated injection brine, “MHz” means megahertz, “δ” means parts per million, “t” means triplet, “H” means protons, “m” means multiplet, “J” means coupling constant, “q” means quartet, “mN/m” means milliNewton per meter, “OD” means outer diameter.
Unless otherwise stated, the amino acids and other reagents were purchased from Sigma-Aldrich (St. Louis, Mo.). K2CO3 was purchased from EMD Chemicals (Gibbstown, N.J.). L-methionine, L-tyrosine, 2-methylalanine and 3-aminobutanoic acid were purchased from Acros Organics (Morris Plains, N.J.). L-phenylglycine, L-tert-leucine, L-norvaline and L-2-aminobutyric acid were purchased from Alfa Aesar (Ward Hill, Mass.). N-lauroyl-L-serine was purchased from Wilshire Technologies (Princeton, N.J.).
A round bottom flask was charged with an amino acid (1.0 equiv.) and K2CO3 (430 mg/mmol) and dissolved in water. The solution was cooled to 0° C. A solution of lauroyl chloride (1.0 equiv.) in acetone was added dropwise to the cooled solution. After addition was complete, the reaction mixture was allowed to warm up to room temperature over the course of 3 hours. Most of the acetone was then removed under reduced pressure and the remaining solution was acidified with concentrated HCl to pH=1. The white precipitate that formed was collected using vacuum filtration, washed with H2O 3×, and dried. If a precipitate was not observed, then the acidified aqueous layer was extracted using EtOAc or Et2O (3×), the combined organic layers were washed with brine, and the sample was dried over anhydrous Na2SO4. The solvent was removed under reduced pressure to provide the crude product.
The residue was purified by flash column chromatography (4:1 EtOAc/hex→10% MeOH/CHCl3; monitored by TLC using bromocresol green) to provide the product.
The crude product was recrystallized twice from hot toluene.
The N-lauroyl amino acid (1.0 equiv.) was dissolved in ethanol. Sodium hydroxide (1.0 equiv., dissolved in ethanol) was added to the solution. The reaction mixture was allowed to stir at least 30 minutes. The ethanol was removed under reduced pressure and the product was washed with hexane (3×) to remove any residual traces of ethanol.
The acid was prepared as described in General Method for Acylation with L-alanine as the amino acid, and the resulting product was a white solid (5.17 g, 85%). The sodium salt was prepared as described above and yielded 5.17 g (78% over 2 steps). 1H NMR (400 MHz, D2O) δ 0.97 (t, J=6.4 Hz, 3H), 1.35-1.44 (m, 19H), 1.69 (m, 2H), 2.35 (t, J=7.5 Hz, 2H), 2.24 (q, J=7.2 & 14.4 Hz, 1H).
The acid was prepared as described in General Method for Acylation with L-leucine as the amino acid, and the resulting product was a white solid (3.82 g, 80%). The sodium salt was prepared as described above and yielded 3.74 g (73% over 2 steps). 1H NMR (400 MHz, D2O) δ 0.86 (t, J=7.3 Hz, 3H), 0.92 (d, J=5.8 Hz, 3H), 0.95 (d, J=5.8 Hz, 3H), 1.28 (br s, 16H), 1.65 (m, 5H), 2.30 (m, 2H), 4.23 (m, 1H).
The acid was prepared as described in General Method for Acylation with L-valine as the amino acid, and the resulting product was a white solid (4.56 g, 89%). The sodium salt was prepared as described above and yielded 4.9 g (77% over 2 steps). 1H NMR (400 MHz, D2O) δ 0.85-0.90 (m, 6H), 0.94 (d, J=6.8 Hz, 3H), 1.28 (br s, 16H), 1.63 (m, 2H), 2.19 (m, 1H), 2.26-2.40 (m, 2H), 4.16 (d, J=5.1 Hz, 1H).
The acid was prepared as described in General Method for Acylation with L-phenylalanine as the amino acid, and the resulting product was a white solid (3.76 g, 90%). The sodium salt was prepared as described above and yielded 4.0 g (83% over 2 steps). 1H NMR (400 MHz, D2O) δ 0.82-1.51 (m, 21H), 2.04 (t, J=6.3 Hz, 2H), 2.81 (dd, J=9.5 & 13.7 Hz, 1H), 3.19 (dd, J=3.2 & 14.7 Hz, 1H), 4.45 (dd, J=4.1 & 9.8 Hz, 1H), 7.01 (t, J=7.7 Hz, 1H), 7.10-7.17 (m, 4H).
N-methyl-L-alanine (1.0 g, 9.7 mmol) was charged into a 250 mL round bottom flask under N2 and dissolved in anhydrous DMF (20 mL), followed by addition of Et3N (1.48 mL, 10.7 mmol). The reaction was cooled to 0° C. and lauroyl chloride (2.2 mL, 9.7 mmol) was added dropwise via syringe. The reaction was allowed to come to room temperature and stirred for 5 hours. Upon completion, the reaction was quenched by addition of H2O (30 mL) and the pH was adjusted with concentrated HCl until pH=3. The aqueous layer was extracted with Et2O (5×). The combined organic layers were washed with brine, dried over anhydrous Na2SO4, and concentrated under reduced pressure. The residue was purified by flash column chromatography (7:3 EtOAc/hex→10% MeOH/CH2Cl2), followed by recrystallization from hexane to provide the acid (0.25 g, 9%). The sodium salt was prepared as described above and yielded 0.25 g (9% over 2 steps). 1H NMR (400 MHz, D2O; mixture of rotamers) δ 0.97 (t, J=6.0 Hz, 3H), 1.31-1.50 (m, 19H), 1.68 (br s, 2H), 2.39-2.61 (m, 2H), 2.86 and 3.04 (2s, 3H), 4.51 and 4.99 (2q, J=8.0 & 14.0 Hz, 1H).
N-lauroyl-L-serine was purchased from Wilshire Technologies (Princeton, N.J.). The sodium salt was prepared as described above and yielded 0.47 g (93%). 1H NMR (400 MHz, D2O) δ 0.88 (br t, J=6.6 Hz, 3H), 1.29 (br s, 16H), 1.61 (m, 2H), 2.31 (t, J=8.1 Hz, 2H), 3.77-3.88 (m, 2H), 4.26 (t, J=4.4 Hz, 1H).
The acid was prepared as described in General Method for Acylation DL-alanine as the amino acid, and purified as described in Purification Method 1 to provide the product as a white solid (4.08 g, 67%). The sodium salt was prepared as described above and yielded 4.41 g (67% over 2 steps). 1H NMR (400 MHz, D2O) δ 0.88 (t, J=6.8 Hz, 3H), 1.23-1.36 (m, 19H), 1.62 (m, 2H), 2.27 (t, J=8.0 Hz, 2H), 4.17 (q, J=8.0 & 14.8 Hz, 1H).
N-lauroyl-D-alanine was prepared using General Method for Acylation with D-alanine as the amino acid, and Purification Method 1 (white solid, 1.42 g, 54%). The salt was prepared as described (1.28 g, 44% over 2 steps). 1H NMR (400 MHz, D2O) δ 0.95 (t, J=6.9 Hz, 3H), 1.30-1.44 (m, 19H), 1.68 (m, 2H), 2.30 (t, J=8.1 Hz, 2H), 4.23 (q, J=6.3 & 14.4 Hz, 1H).
N-lauroyl-L-proline was prepared using General Method for Acylation with L-proline as the amino acid, and Purification Method 1 (white solid, 1.52 g, 59%). The salt was prepared as described (1.50 g, 52% over 2 steps). 1H NMR (400 MHz, D2O, mixture of rotamers) δ 0.93-1.00 (m, 3H), 1.37 (br s, 16H), 1.67 (m, 2H), 1.91-2.50 (m, 6H), 3.53 (m, 1H), 3.62 and 3.79 (2m, 1H), 4.33 and 4.36 (2dd, J=3.4 & 8.4 Hz, 1H).
N-lauroyl-L-tryptophan was prepared using General Method for Acylation with L-tryptophan as the amino acid, and Purification Method 1 (off-white solid, 1.05 g, 56%). The salt was prepared as described (1.11 g, 56% over 2 steps). 1H NMR (400 MHz, D2O) δ 0.60-1.45 (m, 21H), 1.59 (m, 1H), 1.68 (m 1H), 3.00 (br s, 2H), 4.40 (t, J=5.4 Hz, 1H), 6.80 (m, 2H), 6.89-6.96 (m, 2H), 7.25 (d, J=6.9 Hz, 1H).
N-lauroyl-L-isoleucine was prepared using General Method for Acylation with L-isoleucline as the amino acid, and Purification Method 1 (white solid, 1.40 g, 59%). The salt was prepared as described above (white solid, 1.50 g, 59% over 2 steps). 1H NMR (400 MHz, D2O) δ 0.75-0.90 (m, 9H), 1.08 (m, 1H), 1.21 (br s, 16H), 1.38 (m, 1H) 1.47-1.65 (m, 2H), 1.86 (m, 1H), 2.18-2.34 (m, 2H), 4.12 (d, J=5.6 Hz, 1H).
N-lauroyl-L-methionine was prepared using General Method for Acylation with L-methionine as the amino acid, and Purification Method 1 (white solid, 1.19 g, 54%). The salt was prepared as described above (white solid, 0.65 g, 27% over 2 steps). 1H NMR (400 MHz, D2O) δ 0.81 (t, J=7.1 Hz, 3H), 1.22 (br s, 16H), 1.56 (m, 2H), 1.90 (m, 1H), 2.02-2.12 (m, 4H), 2.21-2.31 (m, 2H), 2.40-2.54 (m, 2H), 4.25 (dd, J=4.0 & 9.0 Hz, 1H).
N-lauroyl-L-(4-dodecanoyloxy)-tyrosine was prepared using General Method for Acylation with L-tyrosine as the amino acid, and Purification Method 1 (white solid, 0.44 g, 15%). The salt was prepared as described (white solid, 0.23 g, 7.4% over 2 steps). 1H NMR (400 MHz, CD3OD) δ 0.90 (t, J=7.1 Hz, 6H), 1.29 (m, 28H), 1.47-1.55 (m, 2H), 1.56-1.63 (m, 2H), 2.13 (t, J=7.6 Hz, 2H), 2.30 (t, J=7.4 Hz, 2H), 2.87 (dd, J=7.3 & 13.8 Hz, 1H), 3.10 (dd, J=4.9 & 13.9 Hz, 1H), 4.47 (q, J=4.8 & 7.2 Hz, 1H), 6.64 (d, J=8.5 Hz, 2H), 6.91 (d, J=8.65 Hz, 2H).
N-lauroyl-2-methylalanine was prepared using General Method for Acylation with 2-methylalanine as the amino acid, and Purification Method 2 (white solid, 0.77 g, 28%). The salt was prepared as described (white solid, 0.75 g, 28% over 2 steps). 1H NMR (400 MHz, CD3OD) δ 0.93 (t, J=7.2 Hz, 3H), 1.25-1.40 (m, 16H), 1.53 (s, 6H), 1.62 (m, 2H), 2.19 (t, J=7.7 Hz, 2H).
N-lauroyl-DL-3-aminobutanoate was prepared using General Method for Acylation with 3-aminobutanoic acid as the amino acid, and Purification Method 2 (white solid, 1.81 g, 65%). The salt was prepared as described (white solid, 1.94 g, 65% over 2 steps). 1H NMR (400 MHz, D2O) δ 0.87 (t, J=6.9 Hz, 3H), 1.17 (d, J=6.5 Hz, 3H), 1.24 (br s, 16H), 1.59 (m, 2H), 2.20 (t, J=7.5 Hz, 2H), 2.28 (dd, J=8.4 & 14.1 Hz, 1H), 2.47 (dd, J=5.9 & 14.1 Hz, 1H), 4.16 (m, 1H).
N-lauroyl-L-norvaline was prepared using General Method for Acylation with L-norvaline used as the amino acid, and Purification Method 2 (white solid, 2.08 g, 81%). The salt was prepared as described above (2.22 g, 81% over 2 steps). 1H NMR (400 MHz, D2O) δ 0.87 (t, J=6.8 Hz, 3H), 0.92 (t, J=7.3 Hz, 3H), 1.21-1.44 (m, 18H), 1.52-1.71 (m, 3H), 1.78 (m, 1H), 2.23-2.37 (m, 2H), 4.19 (dd, J=4.2 & 9.2 Hz, 1H).
N-lauroyl-L-tert-leucine was prepared using General Method for Acylation with L-tert-leucine used as the amino acid, and Purification Method 1 (white solid, 1.39 g, 63%). The salt was prepared as described above (1.47 g, 63% over 2 steps). 1H NMR (400 MHz, CD3OD) δ 0.92 (t, J=7.0 Hz, 3H), 1.02 (s, 9H), 1.24-1.43 (m, 16H), 1.58-1.72 (m, 2H), 2.20-2.35 (m, 2H) 4.23 (s, 1H).
N-lauroyl-L-phenylglycine was prepared using General Method for Acylation with L-phenylglycine used as the amino acid, and Purification Method 1 (white solid, 1.09 g, 50%). The salt was prepared as described above (1.13 g, 50% over 2 steps). 1H NMR (400 MHz, D2O) δ 0.67 (t, J=7.1 Hz, 3H), 0.97-1.18 (m, 16H), 1.32-1.45 (m, 2H), 2.03-2.21 (m, 2H), 5.11-5.14 (m, 1H), 7.12-7.19 (m, 1H), 7.22 (t, J=7.9 Hz, 2H), 7.27 (d, J=7.5 Hz, 2H).
N-lauroyl-L-2-aminobutyric acid was prepared using General Method for Acylation with 2-aminobutyric acid used as the amino acid, and Purification Method 2 (0.45 g, 16%). The salt was prepared as described above (0.46 g, 16% over 2 steps). 1H NMR (400 MHz, D2O) δ 0.96 (t, J=7.1 Hz, 3H), 1.00 (t, J=7.6 Hz, 3H), 1.31-1.45 (m, 16H), 1.65-1.82 (m, 3H), 1.85-1.96 (m, 1H), 2.32-2.44 (m, 2H), 4.2 (dd, J=4.8 & 8.0 Hz, 1H).
The acid was prepared as described in General Method for Acylation with L-β-t-butylalanine as the amino acid, and purified as described in Purification Method 1 to provide the product as a white solid (1.07 g, 47%). The sodium salt was prepared as described above and yielded 1.15 g (47% over 2 steps). 1H NMR (400 MHz, D2O) δ 0.87 (t, J=7.1 Hz, 3H), 0.97 (s, 9H), 1.26 (m, 16H), 1.50-1.70 (m, 3H), 1.78 (dd, J=2.1 & 14.6 Hz, 1H), 2.20-2.36 (m, 2H), 4.24 (dd, J=2.2 & 10.0 Hz, 1H).
The acid was prepared as described in General Method for Acylation with DL-β-β-diphenylalanine as the amino acid, and purified as described in Purification Method 2 to provide the product as a white solid (0.66 g, 38%). The sodium salt was prepared as described above and yielded 0.42 g (23% over 2 steps). 1H NMR (400 MHz, D2O) δ 0.81 (m, 2H), 0.89-1.08 (m, 7H), 1.09-1.39 (m, 12H), 1.97-2.13 (m, 2H), 4.54 (d, J=8.9 Hz, 1H), 5.20 (d, J=8.9 Hz, 1H), 7.00 (t, J=7.3 Hz, 1H), 7.10 (t, J=8.0 Hz, 2H), 7.15 (t, J=7.01, 1H), 7.23 (t, J=7.68 Hz, 2H), 7.27 (d, J=7.68 Hz, 2H), 7.36 (d, J=7.68 Hz, 2H).
The acid was prepared as described in General Method for Acylation with 3-aminoisobutyric acid as the amino acid, and purified as described in Purification Method 2 to provide the product as a white solid (2.33 g, 84%). The sodium salt was prepared as described above and yielded 1.67 g (56% over 2 steps). 1H NMR (400 MHz, D2O) δ 0.87 (t, J=7.0 Hz, 3H), 1.09 (d, J=7.1 Hz, 3H), 1.22-1.33 (m, 16H), 1.59 (m, 2H), 2.23 (t, J=7.9 Hz, 2H), 2.45-2.55 (m, 1H) 3.20 (dd, J=7.9 & 13.4 Hz, 1H), 3.34 (dd, J=6.4 & 13.4 Hz, 1H).
Measuring the Potential for Compounds to Release Oil from Sand Particles:
In order to screen test compounds for the ability to release oil from nonporous silica medium, a microtiter plate assay was developed. The assay, referred to as the LOOS test (Less Oil On Sand), measures the ability of a test compound to release oil from oil-saturated sand by measuring sand released from an oil/sand mixture. Autoclaved sand obtained from the Schrader Bluff formation at the Milne Point Unit of the Alaskan North Slope was dried under vacuum at 160° C. for 48 hr. Twenty grams of the dried sand was then mixed with 5 mL of autoclaved, degassed crude oil obtained from an oil reservoir from either the Milne Point Unit of the Alaskan North Slope or from the Wainwright field in the province of Alberta, Canada. The oil-coated sand was then allowed to age anaerobically at room temperature, in an anaerobic chamber (Coy Laboratories Products, Inc., Grass Lake, Mich.; gas mixture: 5% hydrogen, 10% carbon dioxide and 85% nitrogen), for at least a week. Microtiter plate assays were set up and analyzed in an anaerobic chamber. Specifically, 2 mL of compound-containing test sample was added into each well of a 12-well microtiter plate (Falcon Multiwell 12 well plates, #353225, Becton Dickinson, Franklin Lakes, N.J.). Control wells contained 2 mL of sample medium alone. Approximately 40 mg of oil-coated sand was then added to the center of each well. Samples were monitored over time for release and accumulation of “free” sand that collected in the bottom of the wells. Approximate diameter (in millimeters) of the accumulated total sand released was measured for each sample. A score of 3 mm and above indicates the compound's potential to release oil from the nonporous silica medium.
Oil releasing abilities of N-lauroly-L-alanine (NLA) and other lauroyl amino acid derivatives, which were synthesized as described above in General Methods, were compared. Compounds were diluted to 1 mM and 10 mM in SIB (198 mM NaCl, 1 mM MgCl2, 1.8 mM CaCl2, 1.2 mM KCl, 16 mM NaHCO3, 0.05 mM SrCl2, 0.13 mM BaCl2, 0.14 mM LiCl) and assayed in LOOS tests as described in General Methods. Controls were SIB alone. Salinity of SIB as measured by refractometry was 1.3%.
In another experiment shown in
In another experiment shown in
In another experiment shown in
In all assays where oil was released, no oil slick was visible on top of the solution. The sand was released and the oil formed balls, indicating that the sand became more water wet and less oil wet, without solubilization of the oil.
The oil releasing abilities of NLA and some of the lauroyl amino acid derivatives were tested in the presence of high salts.
LOOS tests were performed as described in General Methods. NLA, N-lauroyl-L-valine, and N-lauroyl-L-phenylalanine were diluted to 10 mM in SIB. An additional salt was added to each of different test samples to bring the final concentration to 924 mM for NaCl, 7.4 mM for MgCl2, or 10.9 mM for CaCl2. A sample labeled “none” had no extra salts added but contained the levels already present in the SIB. An “All Salts” sample had all three salts added to the increased respective concentrations given above.
The results given in
The potential application of NLA for enhanced oil recovery was evaluated using a gravimetric sandpack technique. This was done with an in-house developed Teflon® shrink-wrapped sandpack apparatus. Using a 0.5 inches (1.27 cm) OD and 7 inches (17.78 cm) long Teflon heat shrink tube (McMaster-Carr, Dayton N.J.), an aluminum inlet fitting with Viton® O-ring was attached to one end of the tube by heat with a heat gun. Sterile sand from Milne Point, Ak. was added to the column which was vibrated with an engraver to pack down the sand and release trapped air. A second aluminum inlet fitting with Viton® O-ring was attached to the other end of the tube and sealed with heat a gun. This sandpack was then put in an oven at 275° C. for 7 min to evenly heat and shrink the wrap. The sandpack was removed and allowed to cool to room temperature. A second Teflon® heat shrink tube was installed over the original sandpack and heated in the oven as described above. After the double-layer sandpack had cooled, a hose clamp was attached on the pack on the outer wrap over the O-ring and then tightened.
The sandpack was vertically mounted and secured onto a balance. Weight of the sandpack was continuously logged over time. The sandpack was flooded with four pore volumes (60 mL each) of filter sterilized injection water from the Wainwright oil field (Alberta, Canada) at 10 mL/hr via a syringe pump and a 60 mL (Becton Dickinson, Franklin Lakes, N.J.) sterile plastic polypropylene syringe. The sandpack was then flooded with two pore volumes of anaerobic autoclaved crude oil from the Wainwright oil field (Alberta, Canada) at 10 mL/hr to achieve irreducible water saturation. The crude oil was then aged on the sand for three weeks at room temperature. In order to determine a control de-oiling curve, approximately one pore volume (about 60 ml volume of fluid for each pore volume) of filter sterilized injection water was pumped onto the pack at 10 mL/hr, followed by a 5 day shut in period, then a second pore volume was loaded. The weight change of the saturated sand pack during this water flooding was monitored and is shown in
Thus a change in weight of 0.5 g (pore volume=60 mL, density of water=1.0 g/cm3, density of oil=0.93 g/cm3) translates to a reduction in residual oil saturation of approximately 10% indicating that the presence of NLA resulted in release of additional oil.
Interfacial tension (IFT) between hexadecane and SIB containing NLA, or SIB alone, was measured by the inverted pendant drop method using a Model 500 goniometer with DROPimage Advanced software (Rame-Hart Instrument Co., Netcong, N.J.) following the supplier's protocol. NLA was diluted to 0.1% (3.4 mM) and 0.01% (0.34 mM) in SIB. Hexadecane was used as the organic drop phase. IFT was measured every 5 minutes for 15 minutes.
Surface tensions between a platinum plate and solutions of NLA, N-lauroyl-L-leucine, N-lauroyl-L-valine and N-lauroyl-L-phenylalanine were measured by the Wilhelmy plate method using a Kruss K11 tensiometer with a PL21 Pt-plate (Kruss, Hamburg, Germany) following the supplier's protocol. Samples were diluted into SIB to 0.01 mM, 0.1 mM, 1.0 mM, 10.0 mM, and 100.0 mM concentrations for the measurements.
The results are shown in
A LOOS test was performed as described in General Methods with N-lauroyl-L-alanine (NLA) at different concentrations in the presence of Shewanella putrefaciens strain LH4:18 (ATCC # PTA-8822) or Pseudomonas stutzeri LH4:15 (ATCC # PTA-8823). Shewanella putrefaciens LH4:18, disclosed in U.S. Pat. No. 7,776,795 and U.S. patent application Ser. No. 12/784,518 12/784,518, is able to grow on oil as the sole carbon source and has oil release activity. Pseudomonas stutzeri LH4:15, disclosed in US Patent Application Publication 20090263887, is able to grow on oil as the sole carbon source and has biofilm forming activity.
LH4:18 and LH4:15 were each grown overnight in SIB supplemented with 1% peptone (SIB/peptone). Two milliliters of the cultures were added into separate wells for the LOOS test. Negative control wells contained SIB/peptone without any added microbes. NLA was added in 0, 0.01%, or 0.1% concentration in individual wells with LH4:18 or LH4:15 cultures. The results shown in
Oil releasing abilities of additional lauroyl amino acid derivatives, which were synthesized as described above in General Methods, were compared as described in Example 1.
The following additional compounds were found to be effective for oil release at the 10 mM concentration: N-lauroyl-4-methyl-L-leucine and N-lauroyl-DL-3,3-diphenylalanine, as shown in
In another experiment shown in
This application claims the benefit of U.S. Provisional Application 61/416,031, filed Nov. 22, 2010, and is incorporated by reference in its entirety.
| Number | Date | Country | |
|---|---|---|---|
| 61416031 | Nov 2010 | US |
