ENZYME CATALYSIS IN ORGANIC SOLUTIONS

Abstract: Organic enzyme solutions include an ion pair complex of an enzyme and a surfactant, and an organic solvent in which the enzyme-surfactant ion pair is dissolved, the solution having catalytic activity at least an order of magnitude greater than a suspension of an equal amount of the enzyme and organic solvent without ion pair complexes. The enzyme is preferably a hydrolase with an acyl transferase activity and the surfactant is Aerosol OT (sodium bis(2-ethylhexyl) sulfosuccinate) at low concentrations. The organic enzyme solution may be made by obtaining an aqueous solution of an enzyme at a pH of maximal enzyme activity, adding an ionic surfactant to the aqueous solution in an amount sufficient to form an ion pair, and extracting the enzyme-surfactant ion pair into an organic solvent phase without substantial formation of reversed micelles, to produce an anhydrous organic enzyme solution comprising the enzyme-surfactant ion pair dissolved in the organic solvent such that the enzyme retains native structure and substantial catalytic activity. Catalytic solutions according to the invention can be used to catalyze peptide synthesis from acyl donors and nucleophiles.

Description: ENZYME CATALYSIS IN ORGANIC SOLUTIONS BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to enzyme-surfactant ion pairs with high catalytic activity and solubility in organic solution. More specifically, the invention relates to the solubilization of hydrolases in organic solvents without reversed micelles, and to enzyme- catalyzed reactions such as peptide synthesis with aqueous-like activity. 2. Related Art The longstanding desire to achieve catalysis in organic liquids has led to several approaches. Unlike aqueous-based enzymology, the vast majority of studies involving enzymes in nonaqueous media have employed biocatalyst suspensions. See reviews and references therein by (a) Klibanov, A. M. Trends Biochem. Sci. 1989, 14, 141; (b) Dordick, J. S. Enzyme Microb. Technol. 1989, 11, 194; (c) Dordick, J. S. Biotechnol. Prog. , 1992, 8, 259; and (d) Zaks, A.; Russell, A. J. J. Biotechnol. 1988, 8, 259. For example, some enzymes have been immobilized for suspension in organic solvents. Patel et al. , U.S. patent no. 5,413,935; Persichetti et al., "Cross-linked enzyme crystals (CLECS) of thermolysin in the synthesis of peptides, " J. Am. Chem. Soc. 1995. Suspended catalysts are limited by low mass transfer between the catalyst and substrate, diffusional limitations, masking of active centers, and difficulty in recovering insoluble products. Solubilization is preferred for applications where it is important to avoid these limitations. Some efforts to solubilize enzymes in organic solvents have focused on chemical modification. Inada, Y. ; Katsunobu, T. ; Yoshimoto, T. ; Ajima, A. ; Matsushima, A. ; Saito, Y., Trends Biochem. Technol., 1986, 4, 190; Arseguel, D.; Lattes, A.; Baboulene, M. Biocatafysis, 1990, 3, 227); Levesque et al., U.S. patent no. 4,870,016 (papain); and Arnold et al. , U. S . patent no. 5 ,316,935 (subtilisin) . However, chemical modification is tedious and often results in substantial enzyme inactivation. Another approach has been the use of surfactants to form reversed micelles, (a) Martinek, K.; Levashov, A.V.; Khmelnitsky, Yu.L.; Klyachko, N.L; Berezin, I.V. Ear. J. Biochem. 1986, 155, 453; (b) Luisi, P.L.; Giomini, M.; Pileni, M.P.; Robinson, B.H. Biochim. Biophys. Ada 1988, 947, 209. Reversed micellar systems often consist of a high local water content in organic solvents (thereby destroying the true nonaqueous character of the organic solvent system), and result in excess surfactant that becomes a burden downstream. It has also been shown that non-catalytic substances may form complexes with surfactants, but such complexes have not been demonstrated to have any catalytic activity. Matsuura, Powers, Manning, and Shefter, E. J. Am. Chem. Soc. 1993, 775, 1261; and Okahata and Ijiro, J. Chem. Soc. Chem. Commun. 1988, 1392. The present inventors previously observed that chymotrypsin can be extracted from acidic aqueous solutions into organic solvents at very low surfactant concentrations (e.g., < 2 mM) via ion-pairing of a surfactant with the protein. Paradkar and Dordick, Biotechnol. Bioeng. 1994, 43, 529 ("Paradkar & Dordick 1994"). It was shown in Paradkar & Dordick 1994 that an ion-paired complex of chymotrypsin and an anionic surfactant can be extracted into isooctane in the absence of reversed micelles. It was further shown that protein extraction can be optimized at pH 5 and ionic strength of 0.08 M. Observations via active- site titration indicated that chymotrypsin retained nearly all of its catalytically active centers; and circular dichroism and fluorescence spectroscopy determinations suggested the enzyme was not structurally influenced by the extraction process. This led to the general suggestion that the CT-surfactant complexes of Paradkar & Dordick 1994 may have direct application for preparing biocatalysts active and stable in homogeneous organic solutions. SUMMARY OF THE INVENTION It is an object of the invention to provide stable catalytic enzyme-surfactant complexes that can be dissolved in an orgamc solvent, maintain their native structure, and exhibit high catalytic activities approaching those of aqueous solutions, and exceeding the activity of a catalyst obtained by optimizing extraction variables. It is another object of the invention to provide methods for enzyme catalysis in organic solutions. It is a further object of the invention to catalyze peptide synthesis in organic solutions. According to the invention, catalytic enzyme-surfactant ion pair complexes can be obtained by extraction from aqueous solution into organic solution, in substantially dehydrated form. These catalytic complexes can be obtained at maximal activity and can be used in a wide variety of catalytic reactions requiring homogeneous organic solutions. These complexes remain dissolved, maintain their native structure, and exhibit high catalytic activities which approach that in aqueous solutions. The method of catalysis in an organic solvent according to the invention comprises: (a) obtaining an ion pair complex of an activated enzyme and a surfactant, (b) dissolving the activated enzyme-surfactant ion pair complex in an orgamc reaction solvent without forming a significant quantity of reversed micelles, (c) adding to the orgamc reaction solvent a substrate for the enzyme, (d) allowing a sufficient time for the enzyme to catalyze conversion of the substrate to a product, and (e) recovering the product. The method may be batch or continuous. Conversion of the substrate to the product may be substantially completed before the product is isolated. The enzyme may be precipitated from the organic solvent by removal of the surfactant from the enzyme-surfactant complex. The substrate can be added to, and the product isolated from the organic solvent solution while enzyme catalyzed conversion of substrate to product is continuing. The substrate may comprise an acyl donor and a nucleophile, such as an amino acid, an amino acid ester, an N-blocked amino acid, an N-blocked amino acid ester, an amino acid amide, an N-blocked amino acid amide, a polypeptide, a polypeptide ester, an N-blocked polypeptide, an N-blocked polypeptide ester, a polypeptide amide, an N-blocked polypeptide amide, or a combination thereof. For some hydrolases, the acyl donor is preferably a methyl or ethyl ester of tyrosine, tryptophan, alanine, or phenylalanine; a methyl or ethyl ester of a dipeptide or tripeptide containing tyrosine, tryptophan, alanine, or phenylalanine; or an N-benzoyl, N-acetyl, or N- carbobenzoxy derivative thereof; and the nucleophile is an amino acid amide. The water content of the organic enzyme reaction solution preferably does not exceed the water saturation point for the organic solvent containing the surfactant. The molar ratio of water to enzyme in the organic reaction solvent may be kept less than about 75:1. Alternatively, the method may further comprise adding up to 0.2% v/v water to the reaction solvent. To obtain the ion pair complex of the invention, a method comprises: (1) forming a two-phase aqueous/organic system comprising an activated enzyme solution produced by dissolving an enzyme in an aqueous activating solution at a pH of maximal enzyme activity, an enzyme concentration of from about 1 μg/ml to about 10 mg/ml, and ionic strength less than about 80 mM, preferably less than 30 mM; an organic extraction solvent that is immiscible with water; and an ionic surfactant; the molar ratio of surfactant to enzyme in the two-phase system being in the range of about 15 to about 90 molecules of surfactant per 25,500 dalton enzyme, sufficient to form an enzyme-surfactant ion pair complex, and in a range of from about one tenth to substantially less than the ratio that would form reversed micelles in the organic solvent, (2) then agitating the two-phase system for a period sufficient to produce an ion pair complex of the activated enzyme and the ionic surfactant and to extract the ion pair complex directly from the aqueous solution into solution in the organic extraction solvent, without substantial formation of reversed micelles, (3) then separating the organic phase from the aqueous phase, whereby a homogeneous organic enzyme solution is obtained containing dissolved activated enzyme-surfactant ion pair complex and essentially no reversed micelles, the activated enzyme retaining native structure and having catalytic activity at least an order of magnitude greater than a suspension of an equal amount of the enzyme and organic solvent without surfactant. The organic extraction solvent may be dried after extraction, or evaporated. Preferably, the enzyme is α-chymotrypsin, the surfactant is AOT (aerosol OT, sodium bis(2-ethylhexyl) sulfosuccinate), the pH of the aqueous activating solution is from about 7.0 to about 8.5, the ionic strength is less than about 20 mM, the enzyme: surfactant ratio is about 1:30 and the enzyme surfactant ion pair has a catalytic efficiency k ^ EC,,, in isooctane for the transesterification of N-acetyl-L-phenylalanine ethyl ester with 1-propanol of greater than 3000 M 1 s 1 . Preferably, when the volumes of aqueous solution and organic extraction solvent are about equal, the starting concentration of surfactant in the organic solvent is about 2 mM, and the starting concentration of the enzyme in the aqueous solvent is about 1 mg/ml. The invention encompasses complexes in which the surfactant is cationic and the pH of maximum activity of the enzyme is above the pi. A catalyst of the invention may be an essentially pure solid having water content of about 5% to about 10% by weight. The enzymes include hydrolases with acyl transferase activity in organic solvent, catalytic antibodies, oxidoreductases, transferases, hydrolases, lyases, isomerases, lipases, ligases, a peroxidase catalyzing phenolic polymerizations, a tyrosinase catalyzing aromatic hydroxylations, and an alcohol dehydrogenase catalyzing stereoselective oxidation and reduction. BRIEF DESCRIPTION OF THE DRAWINGS The invention is illustrated by the following detailed description and figures. Fig. 1 illustrates the effect of water content on the product yield, using 5.5 mM acyl donor, 10 mM nucleophile, and 3.6 μM soluble alpha-chymotrypsin. In Fig. IA the acyl donor is Bz-Tyr-OEt (N-benzoyl tyrosine ethyl ester), the nucleophile is LeuNH 2 (leucine amide, in which the carboxyl group is blocked with an amino group to form an amide), and the product is Bz-Tyr-LeuNH 2 (N-benzoyl tyrosine leucine amide). In Fig. IB the acyl donor is the N-blocked dipeptide CBZ-Val-Tyr-OMe (N-carbobenzoxy-valine-tyrosine methyl ester), the nucleophile is LeuNH 2 , and the product is the N-blocked tripeptide CBZ-Val-Tyr- LeuNH 2 . Figure 2 shows the influence of solvent hydrophobicity on peptide synthesis catalyzed by soluble proteases. Fig 2A graphs data for α-chymotrypsin. Fig. 2B shows results for subtilisin Carlsberg. The acyl donor was N-Bz-L-Tyr-OEt, and the acyl acceptor was L-Leu- NH 2 . Solvents: 1 - THF, 2 - ethyl acetate, 3 - methylene chloride, 4 - butyl acetate, 5 - isopropyl ether, 6 - isooctane (containing 30%, v/v THF). Figure 3 shows the effect of added water on peptide synthesis catalyzed by soluble α-chymotrypsin. The acyl donors were N-Bz-L-Tyr-OEt or N-CBZ-L-Val-L-Tyr-OMe, and the acyl acceptor: L-LeuNH 2 . Solvents: Fig. 3A - isooctane (containing 30%, v/v THF), and Fig. 3B - ethyl acetate. Figure 4 demonstrates the effect of added water on peptide synthesis catalyzed by soluble subtilisin Carlsberg. The acyl donor was N-Bz-L-Tyr-OEt, and the acyl acceptor was L-Leu-NH 2 . Solvents: Fig. 4A - isooctane (containing 30%, v/v THF), and Fig. 4B - ethyl acetate. Figure 5 depicts inactivation kinetics of subtilisin BPN' solubilized in dry THF. Soluble enzyme was incubated in THF for indicated periods of time and activity was measured in dry THF (circles), octane (triangles), and aqueous buffer (squares). Also, subtilisin was. incubated in THF for different lengths of time, then transferred to octane, extracted into water after a 30 min further incubation in octane, and the activity assayed in water (diamonds). For the enzyme transferred from THF to octane, no further change in activity was observed for 24 hours in octane. The enzymatic activities are assayed for transesterification reaction between N-Ac-PheOet and 1-propanol in organic solvents, and for hydrolysis of suc-Ala-Ala-Pro-Phe-p-nitroanilide in water. Figure 6 is a schematic mechanism of subtilisin deactivation in THF. Figure 7 shows relative stability of soluble subtilisin in dry THF (squares) and THF containing 0.2% added water (circles). Kinetics of irreversible inactivation was followed by incubating soluble subtilisin in THF (dry or containing 0.2% water) and transferring aliquots to water, measuring activity (filled symbols) and recording near-UN CD spectra (empty symbols) in water. Fraction of the native-like enzyme was estimated from the area under the near-UV CD spectrum. DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS In describing preferred embodiments of the present invention illustrated in the drawings, specific terminology is employed for the sake of clarity. However, the invention is not intended to be limited to the specific terminology so selected, and it is to be understood that each specific element includes all technical equivalents which operate in a similar manner to accomplish a similar purpose. Enzyme-surfactant ion pairs in organic solutions can be obtained according to the invention with catalytic activity approaching the levels in aqueous solution. Preferably, the enzyme is dissolved in the aqueous solution, the surfactant is dissolved in the organic solvent (most surfactants are only slightly soluble in water) and the two phases are then combined. See Paradkar and Dordick, 1994. The method may preferably include selecting an enzyme; determining its pi and pH of maximum activity (pΑ^ in aqueous solution; selecting an anionic surfactant if pH,. ^ < pi, or a cationic surfactant if pH ^ > pi; preparing an aqueous solution buffered to pH^, and including any catalytically required metal ions, or cof actors, ions to provide desired ionic strength, and enzyme in a concentration up to about 10 mg/ml; selecting an organic solvent and a surfactant in a concentration of substantially less than the amount that would lead to substantial formation of reverse micelles, preferably less than about one half that amount (i.e. less than about 90 surfactant molecules, preferably between about 15 and 75, and most preferably about 30, for an average sized enzyme molecule having a molecular weight of about 25,500 daltons, which is completely enclosed by about 110 surfactant molecules), preferably in a range of about 1 to about 2.5 mM surfactant, most preferably about 1.5 mM to about 2 mM for each mg/ml enzyme present; selecting an extraction solvent that is immiscible in water, preferably having a partition coefficient log P > 0.68 (defined as the partitioning of the solvent between water and 1-octanol); and extracting an ion pair complex of the enzyme and surfactant from the aqueous phase solution into the extraction solvent. Any ionic surfactant could be employed to form ion pairs according to the invention. Anionic surfactants such as AOT (aerosol OT, Sodium bis(2-ethylhexyl) sulfosuccinate) and SDS (sodium dodecyl sulfate), and quaternary ammonium salts may be used preferably with enzymes having a pH,. - below the pi. For enzymes forming ion pairs above the pi, cationic surfactants such as CTAB (cetyl trimethylammonium bromide) and DDAB (didodecylammonium bromide) may be employed. The surfactant concentration is kept substantially below the level at which reversed micelles incorporating the enzyme would form (the reversed micelle ratio, or RMR), preferably no more than one half of the RMR, most preferably about one third that amount. The minimum surfactant/enzyme ratio forming soluble ion pairs according to the invention is about one tenth the RMR. For chymotrypsin and AOT in isooctane, the RMR is above about 110 molecules surfactant per molecule of enzyme, well above the preferred amounts of about 2 mM surfactant in the extraction solvent for each mg/ml enzyme in the aqueous solvent to be extracted. In a preferred embodiment, the enzyme is alpha-chymotrypsin (CT) at about 1 mg/ml, the organic solvent is isooctane, and the surfactant is AOT in a concentration of less than about 2 mM. The pH of the aqueous activating solution is from about 7.0 to about 8.5, the ionic strength is less than about 20 mM, and the enzyme surfactant ion pair has a catalytic efficiency ^fK ^ in isooctane for the transesterification of N-acetyl-L-phenylalanine ethyl ester with 1-propanol of greater than 3000 per Molar per second. The enzyme: surfactant molar ratio is about 1:30. The activity of the extracted CT-AOT complex is about 2000 times that of chymotrypsin suspended in isooctane, and the activity is about an order of magnitude higher than chymotrypsin extracted from an aqueous solution at pH 5.0 where extraction is optimal as taught by Paradkar and Dordick 1994. The surfactant concentration is low enough to avoid the formation of any significant quantity of reversed micelles, and the water concentration is no greater than the amount of water soluble in the organic solvent containing the surfactant. Drying of the enzyme-containing isooctane phase by passing a stream of nitrogen gas through the organic liquid results in an extensively dehydrated soluble enzyme in isooctane, with a water content of about 0.03 μl/ml solvent. This soluble enzyme preparation with low surfactant content can then be mixed directly in a wide variety of organic solvents or collected by evaporating the solvent to form a solid preparation containing structural water only, with minimal exogenous water, about 5 to about 10 weight percent water total. The solid preparation can then be dissolved in a reaction solvent. The catalysts and methods of the invention can be applied to most enzymes of the international classification, including oxidoreductases, transferases, hydrolases, lyases, isomerases, and ligases. Single chain enzymes are preferred because they can most easily be extracted with native structure, but any enzyme that can retain its quaternary, tertiary, and secondary structure through the extraction process may be employed. As used here, the term enzyme is meant to include any proteinaceous biocatalyst, including an antibody that has the activity of one of the enzyme classes when acting on an antigen in a non-aqueous solution. Proteins of molecular weight over about 200,000 daltons are too large to easily extract according to the invention. Most preferred are hydrolases catalyzing acyl transfer. Preferred enzymes include α-chymotrypsin, subtilisin BPN' (from Bacillus amyloliquefaciens), subtilisin Carlsberg (from Bacillus licheniformis), and papain. Organic solvents that may be used to extract soluble enzymes according to the invention include hydrophobic organic compounds like isooctane, octane, toluene, hexane, benzene, and the like; hydrophilic water miscible orgamc solvents are not preferred. In general, any organic solvent that is immiscible in water and has a log P greater than about 0.68, the partition coefficient of ethyl acetate, may be used for extraction. This includes the following classes of solvents: hydrocarbons, halogenated hydrocarbons, ethers, esters, aromatics, and so on. The enzyme is extracted from an aqueous solution at the pH of maximal catalytic activity. For CT, that is greater than about pH 6.5, preferably about pH 7-8, most preferably pH 7.8. Surprisingly, the pH at which phase transfer is most efficient, as taught in Paradkar and Dordick 1994, is not the most desirable for enzyme activity. For CT, optimum extraction efficiency occurs from pH 4.0 to 6.5, preferably pH 5.0, but that gives an enzyme whose activity is about an order of magnitude less than the enzyme extracted at pH 7.8, with lower efficiency. The enzyme concentration in the extraction medium is typically about 1 mg/ml, but may range from about 1 μg/ml to about 10 mg/ml. At higher protein concentration emulsification is a problem. The E/S (enzyme/surfactant) ratio may be determined in an organic solvent using methods taught in Paradkar & Dordick 1994, which is incorporated herein by reference. The amount of enzyme in the two phase solvent can be measured directly by standard methods and assays. The amount of complexed surfactant may be readily determined by the difference between the total surfactant in the organic solvent and the amount remaining as free surfactant after the enzyme is in solution. For example, as in Paradkar and Dordick 1994, rhodamine dye can be used to measure free AOT in the organic solvent spectrophotometrically. The characteristic ratio that would form reversed micelles according to the invention may be termed the RMR or reversed micelle ratio, defined as the ratio of surfactant to enzyme in an organic extraction solvent at which significant numbers of reversed micelles form. The RMR may be approximated for a particular enzyme-surfactant-solvent system by calculation, empirical observation, or both. It should be noted that the RMR is only indirectly related to the critical micelle concentration (CMC) of the surfactant in the organic solvent (which is typically about 1 to as high as 3 mM in isooctane). The concentration of enzyme-surfactant (E-S) ion pair in organic solvent can far exceed the CMC. The presence of protein, in effect, raises the concentration of surfactant that would be needed to form micelles. Reversed micelles form when a protein is fully enclosed in hydrophobic surfactant. Apparently, once all available protein is saturated with surfactant, then additional free surfactant begins to form reversed micelles, when the free surfactant reaches the CMC. Thus, the RMR is the concentration of surfactant needed to maintain a critical micelle concentration in a solvent containing extracted protein surfactant ion pairs. These CMCs are known or calculated from the literature. The exact RMR depends on the surface area and surface charge density of the enzyme. In general, however, one can derive the RMR for a particular enzyme from the observed and calculated fact that the RMR for CT is about 110 molecules AOT per molecule enzyme. Thus, it may be stated that RMR = (X 0 /MW CT ) x (110) + CMC in which X 0 is the concentration of enzyme extracted into the organic phase, in mg/ml, MW CT is the molecular weight of chymotrypsin in daltons (25,500), and 110 is the number of moles surfactant per mole of enzyme for a 25,500 MW enzyme (chymotrypsin). The critical micelle concentration for the given surfactant and solvent is added, to give RMR in moles per liter. The constant of 110 may vary somewhat with the size and shape of the enzyme and the size of the surfactant. Therefore, it is desirable to confirm by experiment that no significant reversed micelles are forming. The presence or absence of reversed micelles at a given ratio of surfactant to enzyme may be determined empirically such as by light scattering experiments according to known methods. Another test is to dilute the hydrophobic extraction solvent into a hydrophilic organic solvent such as tetrahydrofuran, which does not support reversed micelles. For example, the RMR can be readily determined by a calibration test. A fixed enzyme concentration, e.g. 1 mg/ml in aqueous solvent, is extracted into an equal volume of extraction solvent containing surfactants ranging from e.g. 0.2 mM to 10 mM. Once the RMR is determined, a range of about one tenth to about half, preferably about one third the RMR is selected to form ion pairs. The key factor in the maximum amount of surfactant selected is avoiding reversed micelle formation. Therefore, it is possible to extract an enzyme according to the invention with up to about 90 of the 110 sites of a standard 25,500 dalton enzyme occupied by surfactant, which would correspond to about 85% of the RMR. In general, though, it is preferred to stay in the range below about half the RMR, corresponding most preferably to about one third to one half the occupied sites. For example, for an enzyme of MW 25,500 in which 0.4 mg/ml extracts into an organic phase containing 2 mM surfactant, the RMR may be calculated as 0.4/25,500 x 110 + CMC = 1.73 mM plus about 1 mM = 2.73. For free micelles to form, the surfactant needs to fully occupy sites on the protein, and additional free surfactant is needed. Thus, according to the invention, a surfactant concentration of 2 mM will not lead to substantial formation of reversed micelles. For extraction of 1 mg/ml of the protein, RMR = 4.33 + 1 = 5.33. Thus, a surfactant concentration up to about 4 mM will not lead to substantial formation of reversed micelles. This is well above the preferred amount of 2 mM. For extraction of 10 mg/ml of the protein, RMR = 43.3 + 1 = 44.3. Thus, a surfactant concentration up to about 30 mM will not lead to substantial formation of reversed micelles. Even at low concentrations, the surfactant can partition into the aqueous phase from the organic phase, complex with the enzyme, and then the complex can partition into the organic phase. The ion pair is unstable and transient in the aqueous phase due to the weak ionic interactions that hold it together, but the complex is stable in the organic phase due to its hydrophobicity. The energy state in the dissociated condition is higher than as a complex. This phenomenon of thermodynamic stabilization occurs at the proper proportions of enzyme, surfactant, water, and organic solvent. Thus, the organic phase is, in effect, a thermodynamic collector for the catalytic ion pair complex according to the invention. The lower limit of protein concentration is primarily based on inconvenience due to dilution and high volumes. The preferred concentration of surfactant at 1 μg/ml enzyme would be about 2 μm. At 10 mg/ml protein, the preferred surfactant concentration would be about 20 mM assuming nearly all enzyme is extracted. Concentration of the enzyme may be accomplished during extraction by using a smaller volume of orgamc solvent than aqueous phase. For example, if the volume ratio of aqueous to orgamc phase is 10:1, about a 10 fold concentration of the enzyme will be achieved. Appropriate buffers may be used to maintain the desired pH, such as bis-Tris propane-HCl buffer. The buffer should be selected for compatibility with the enzyme. The buffer may be in a concentration of from about 1 mM to about 200 mM, preferably about 10 mM. Other components may be present in the aqueous solution to maximize the ultimate activity of the enzyme in organic solution or to increase the efficiency of phase transfer to the organic phase. For example, calcium chloride may be present to maintain the activity of a protease such as chymotrypsin, and to provide desired levels of ionic strength, in a concentration up to about 100 mM, preferably about 2 mM, and salts such as potassium chloride may be present for the latter purpose as well. The ionic strength for CT extraction is preferably less than about 50 mM, or less than 20 mM, and most preferably about 12 mM, when extraction is done to a pH 7.8 solution. Further optional components of the aqueous phase include native components of the enzyme such as metal salts. Extraction can preferably be achieved by mixing the aqueous enzyme solution with an equal volume of organic solvent, preferably isooctane containing a low level of the desired surfactant, e.g. AOT at 2 mM, and effecting phase separation. Agitation enhances mass transfer. The surfactant partitions into the aqueous phase from the organic phase, pairs with the protein and then either dissociates, or causes the protein to emulsify and precipitate, or according to the invention, causes the protein to partition into the organic phase where it is stable. After extraction, the orgamc phase contains enzyme which may be analyzed spectrophotometrically or otherwise. The enzyme-surfactant combination of the invention does not include any significant presence of reversed micelles. The ion pair complex according to the invention includes an enzyme of molecular weight up to about 200,000 daltons, pre-activated by dissolving it in an activating aqueous solution at a pH of maximum activity, and an ionic surfactant. The surfactant and activated enzyme are complexed together as an essentially anhydrous enzyme-surfactant ion pair complex, the proportion of surfactant to pre-activated enzyme in the complex being sufficient to render the complex soluble in an organic solvent and in a range of from about one tenth to about half the proportion that would form reversed micelles in the organic solvent, and the complex, when dissolved in the organic solvent, retaining native structure and catalytic activity an order of magnitude higher than the activity of the enzyme suspended in the organic solvent. The catalyst may further comprise an organic solvent in which the enzyme-surfactant ion pair is dissolved to form a homogeneous organic enzyme solution, the activated enzyme retaining native structure and having catalytic activity at least an order of magnitude greater than a suspension of an equal amount of the enzyme and organic solvent without surfactant. Following drying, the catalyst may be obtained as an essentially pure solid having water content of about 5% to about 10% by weight. The molar ratio of water to enzyme may be from about 50 to 200 and is preferably less than about 75. This is less than the water typically present in lyophilized protein, and less than that trapped in reversed micellar enzyme systems. The soluble enzymes of the invention are highly active in orgamc reaction solvents such as isooctane with activity approaching that in aqueous solutions. Reactions may also be run in water miscible orgamc solvents that are inappropriate for extraction, such as tetrahydrofuran, dimethylformamide, dimethylacetamide, ethanol, methanol, butanol, acetone, dioxane, and the like. Most reactions that can be carried out using activated enzymes in suspension in organic solvents can be carried out according to the invention using enzyme mediated catalysis in a homogeneous organic solution. Enzyme catalysis according to the invention, including such desirable reactions as degradation of toxic substances for bioremediation, and peptide synthesis, may be carried out in a large scale batch mode. Conversion of substrate to product is allowed to go to completion before product is recovered. If the product is soluble, a substance may be added to precipitate the product separate from the enzyme. Alternatively, the enzyme can be precipitated. For example, a strong ion pairing substance like tributylammonium chloride may be added (if an anionic surfactant is used), which releases the surfactant from the enzyme, and leads to precipitation of the enzyme. Soluble product can then be obtained by evaporation. A continuous reaction mode is desirable in certain applications. Substrate is added to the reaction mixture. As the reaction proceeds, the product is removed. For non-soluble product, the product precipitates out and may be collected. This approach is not feasible with enzymes in suspension. Substrate is continuously added until the enzyme catalyst is exhausted. Alternatively, ultrafiltration could be used in a continuous mode with soluble products substantially smaller than the enzyme surfactant ion pair complex, to remove product from the reaction vessel. The method of the invention is suitable for large scale production of dipeptides, tripeptides, and longer polypeptides using alkyl esters of amino acids or short peptides as the acyl donor. N-terminal protection or blocking is preferred but not necessary. Nucleophiles may be carboxyl amides of amino acids or C-terminal amides of short peptides, and amino acids. Reactions are stereospecific for optically pure substrates. The substrate may include an amino acid, an amino acid ester, an N-blocked amino acid, an N-blocked amino acid ester, an amino acid amide, an N-blocked amino acid amide, a polypeptide, a polypeptide ester, an N-blocked polypeptide, an N-blocked polypeptide ester, a polypeptide amide, an N-blocked polypeptide amide, or a combination thereof. The substrate for peptide synthesis in homogenous organic solutions according to the invention may have the formula O II X-HN-CH-C-Y R For the acyl donor, R = side chains of amino acids; X = any N-blocker, other amino acids, peptides, or H Y = -OH, -NH 2 , -O-alkyl, -O-aryl, -N-alkyl, N-aryl or other amino acids. . As used here, the term aryl includes the presence of any substituents on the aryl ring, e.g nitrophenyl, and so on. The same substrates may be used for the acyl acceptor (nucleophile), but X=H, and preferably Y=NH 2 . Preferably for CT or subtilisin, the acyl donor is a methyl or ethyl ester of tyrosine, tryptophan, alanine, or phenylalanine; a methyl or ethyl ester of a dipeptide or tripeptide containing tyrosine, tryptophan, alanine, or phenylalanine; or an N-benzoyl, N-acetyl, or N- carbobenzoxy derivative thereof; and the nucleophile is an amino acid amide. Peptide synthesis may be carried out with roughly equimolar concentrations of acyl donor and nucleophile. A combination of non-polar and polar solvents may be used to achieve solubilization of the enzyme and the substrates. Minor amounts of water, up to about 0.1 % v/v may be added to improve enzyme reactivity without competing with the acyl acceptor (nucleophile). The temperature may preferably range from about 0°C to about 100°C, although certain thermally stable enzymes from hyperthermophilic organisms belonging to the kingdom of Archaea (such as Taq polymerase) may function at even higher temperatures. Preferably the temperature is about 30°C. Reaction times may range from about 10 minutes or less up to about six hours or more. Other subtilisin enzymes that could be used include subtilisin DY from Bacillus subtilis, and related enzymes such as alkaline elastase YaB, minor extracellular protease, intracellular serine protease 1, thermitase, basic protease, extracellular protease, bacillopeptidase, cytolysin component A, epidermin protease, C5a peptidase, SK11 cell wall proteinase, extracellular serine protease, Ca-dependent protease, and alkaline protease. Other proteases that are hydrolases in water may be used according to the invention, such as thermolysin, pepsin, papain, thrombin, and so on. Other enzymes suitable for catalysis while solubilized in organic solvents include: lipases, peroxidases, tyrosinases, glycosidases, nucleases, isomerases, aldolases, phosphatases, sulfatases, dehydrogenases, lyases, etc. Any enzyme may be employed provided it has some charged residues at the pH of maximal activity, so that it can ion pair with a surfactant. This includes some membrane- bound enzymes and most enzymes that typically exist in vivo in solution. The surfactant masks the charges of the enzyme (e.g., for AOT the negative charge of the sulfonate group of the surfactant pairs with the positive charge of an amino group), and also conveys substantial hydrophobic character to the enzyme by virtue of the long hydrophobic hydrocarbon chains of the surfactant. Importantly, no covalent modification of the enzyme is required, and hydrophobic character is imparted to the enzyme in a mild and efficient manner. Thus, most any enzyme may be employed according to the invention if it is able to retain its native components and structure in aqueous solution, complex with an anionic surfactant at a pH of maximum activity and partition into an organic phase as an ion pair, while still retaining native structure and components. Cofactors for a particular enzyme may be added with the substrate to the reaction medium. Water-soluble cofactors could be added to the aqueous solution so that they bind to the enzyme as the latter is extracted. Peptide synthesis reactions using organic soluble enzymes according to the invention are marked by several salient features including: i) high conversions using nearly equimolar concentrations of both the acyl donor and the nucleophile; ii) nearly quantitative yields; and iii) high reaction rates (and therefore relatively low enzyme concentrations required). It is advantageous to keep the concentrations of the acyl donor and nucleophile close, to minimize waste of raw material. According to the invention, the concentrations are in a ratio of acyl donor to nucleophile of about 1 :4 to about 4:1, preferably a range of about 1 :2 to about 2:1, most preferably a range of about 1.5:1 to about 1:1.5. This is an advantage over other approaches to peptide synthesis that utilize high water contents. In such systems, a high (> 10:1) ratio of donor/acceptor is employed to improve peptide yield. The yields achieved may exceed 80%, meaning that only a small fraction of the ester donor is hydrolyzed in the reaction. In many cases the yield is 97% or greater. Yield can be greater than the percent conversion of the ester donor if the reacting ester donor is not hydrolyzed during the reaction. Peptide synthesis according to the invention proceeds at high reaction rates, with most reactions being essentially completed in two to four hours. The homogeneous catalytic reaction solutions of the invention have definite advantages over suspensions and heterogeneous solutions (e.g. , those containing significant quantities of reversed micelles with their inherent water pools). Surprisingly, in a complex that has more surfactant than an enzyme suspension, but less than with reversed micelles, the solubility and activity are significantly enhanced as compared to both prior art systems. Thus, the complexes of the invention allow full realization of the advantages of catalysis in organic solutions: e.g., increased solubility of nonpolar substrates, shifting thermodynamic equilibria to favor synthesis over hydrolysis, suppression of water-dependent side reactions, ease of product recovery, enhanced thermostability, and lack of microbial contamination. This synthetic method could be run at liter scale or larger as a batch or continuous process. There are few problems with scale up because the use of a homogeneous solution essentially eliminates diffusional limitations and mass transfer limitations. A recirculating process can be employed according to the invention. For example, a stream containing the initial acyl donor and nucleophile substrate is continuously added to a reaction vessel containing the solubilized enzyme. The reaction medium is circulated through a filtration device to continuously remove the dipeptide product, which is esterified or amidated and then returned to a reaction vessel as the acyl donor or nucleophile, respectively, for synthesis of a tripeptide. This process is repeated as desired to synthesize longer polypeptides. According to the invention, a peptide having as many residues as desired could be produced. EXAMPLE 1 The catalytic turnover number is defined by k^,. The Michaelis constant is defined by K,,,. The ratio k^/K m reflects the catalytic efficiency for a particular substrate, in terms of the second order rate constant of the interaction of free enzyme and substrate. The highly active soluble CT was used for kinetically-controlled peptide synthesis resulting in efficient synthesis of dipeptides in yields approaching 100 % . In addition to CT, subtilisin Carlsberg was dissolved in isooctane in a similar manner and shows a value of k ca ,/K m for the transesterification of Ac-L-Phe-OEt and n-propanol of 68% of that for hydrolysis in aqueous buffer. The phenomenon of ionogenic memory was previously observed in the context of suspended enzymes which are dried (lyophilized) and then mixed with an organic solution. Zaks, A.; Klibanov, A. M. J. Biol. Chem. 1988, 263, 3194. Pre-activation according to the invention, in contrast, occurs when an enzyme surfactant ion pair complex forms in the pre-activation aqueous solution and then partitions directly into the organic phase. Direct extraction of pre-activated enzyme to the orgamc phase, according to the invention, is preferable not only because the enzyme goes into solution rather than suspension, but also because it avoids the possibility that the activated enzyme might be destabilized or disrupted by lyophilization or subsequent treatment. Moreover, pre-activation is contrary to the teachings of Paradkar & Dordick 1994, p. 531, because the extraction yield at the pH max is significantly lower than at pH 5 which was the optimal extraction pH " observed in the prior art. Pre-activation may lower the extraction yield. In conjunction wtih pre-activation according to the invention, therefore, it is desirable to increase the extraction yield at the pH max to compensate, e.g. by reducing the ionic strength. EXAMPLE 2 This example shows a general method for preparing solubilized enzymes in their catalytically optimized form. The general method for solubilization of enzymes into isooctane is given for subtilisin BPN' (from Bacillus amyloliquefaciens) and the extraction results are below the method. Subtilisin BPN' was extracted from a 1 mg/ml aqueous solution (pH 7.8) into isooctane containing 2 mM Aerosol OT (AOT), yielding 40% extraction. Subtilisin has a molecular weight of 27,500. The pi of the enzyme is 9.4 and maximal activity is at pH 7.8, so an anionic surfactant was applied. The aqueous phase consisted of 10 mM bis- tris propane buffer, pH 7.8, containing 2 mM CaCl 2 and 1 mg/ml subtilisin. This phase was extracted with an equal volume of isooctane containing 2 mM AOT (sodium bis(2-ethylhexyl) sulfosuccinate) by stirring at 250 rpm at 25°C for 2 min. The phases were allowed to settle and then cenrrifuged to obtain clean phase separation. Drying of the organo-soluble enzyme, by bubbling N 2 through the solution, resulted in dried enzyme-AOT ion-paired complex, which can then be diluted in any organic solvent of choice (e.g. THF, acetone, t-amyl alcohol etc.). The concentration of subtilisin in the organic phase was determined spectrophotometrically . Extraction results For subtilisin BPN , the results were as follows: Aqueous phase: 1 mg/ml subtilisin in 10 mM Bis-Tris propane-HCl buffer, pH 7.8, 2 mM CaCl 2 Organic phase: 1 ml isooctane containing 2 mM AOT Extraction Yield: 0.4 mg/ml subtilisin in organic phase EXAMPLE 3 This example provides extraction data for subtilisin Carlsberg (from Bacillus licheniformis). This enzyme has pi of 8.5 and maximum activity at about pH 7.8. The solubilization method and assays were the same as in Example 2. Extraction results: Aqueous phase: 1 mg/ml subtilisin in 10 mM Bis-Tris propane-HCl buffer, pH 7.8, 2 mM CaCl 2 Organic phase: 1 ml isooctane containing 2 mM AOT Extraction Yield: 0.3 mg/ml subtilisin in organic phase EXAMPLE 4 This example provides extraction data for α-chymotrypsin. The solubilization method and assays were the same as in Example 2. This enzyme has a pi of about 8.0 and maximum activity at about 7.8. The results were as follows: Extraction results: Aqueous phase: 1 mg/ml α-chymotrypsin in 10 mM Bis-Tris propane-HCl buffer, pH 7.8, 2 mM CaCl 2 Organic phase: 1 ml isooctane containing 2 mM AOT Extraction Yield: 0.93 mg/ml chymotrypsin in orgamc phase EXAMPLE 5 This example provides extraction data for papain. Papain has a pi of about 8.75 and maximal activity at pH 7.8. Manganese and potassium chloride were added to the aqueous solution because they are helpful to maintain activity. Extraction was performed as in Example 2 at pH 7.8 because this is a pH of maximal activity. Extraction results: Aqueous phase: 0.5 mg/ml papain in 10 mM Bis-Tris propane-HCl buffer, pH 7.8, 3 mM CaCl 2 , 3 mM MnCl 2 , 1 mM KC1 Organic phase: 1 ml isooctane containing 2 mM AOT Extraction Yield: 0.35 mg/ml papain in orgamc phase EXAMPLE 6 Soybean peroxidase has a pi of about 4 and a pH. ^ about 5-7. Therefore, the enzyme has a net negative change in the activating solution, and forms active catalytic ion pairs with a cationic surfactant under the same extraction conditions as in Example 2. EXAMPLE 7 This example compiles peptide synthesis data using chymotrypsin as catalyst. See Table I. Table I shows the acyl donor and the nucleophile (acceptor) which react to form the product. The reaction time and yield are listed. Table I Peptide Synthesis Catalyzed by Soluble Chymotrypsin Acyl donor Nucleo¬ Product Min. Yield phile (%) A. Bz-Tyr-OEt Phe-NH 2 Bz-Tyr-Phe-NH 2 120 99 Bz-Tyr-OEt Tyr-NH 2 Bz-Tyr-Tyr-NH 2 120 98 Bz-Tyr-OEt Leu-NH 2 Bz-Tyr-Leu-NH 2 120 97 Bz-Tyr-OEt Pro-NH 2 Bz-Tyr-Pro-NH 2 240 85 Ac-Trp-OEt Phe-NH 2 Ac-Trp-Phe-NH 2 120 98 Bz-Ala-OMe Phe-NH 2 Bz-Ala-Phe-NH 2 120 98 Bz-Ala-OMe Pro-NH 2 Bz-Ala-Pro-NH 2 360 84 Ac-Phe-OEt Phe-NH 2 Ac-Phe-Phe-NH 2 120 99 Ac-Phe-OEt Leu-NH 2 Ac-Phe-Leu-NH 2 120 94 B. CBZ-Val-Tyr-OMe Leu-NH 2 CBZ-Val-Tyr-Leu-NH 2 120 38 CBZ-Ala-Phe-OMe Leu-NH 2 CBZ-Ala-Phe-Leu-NH 2 120 50 CBZ-Val-Trp-OMe Leu-NH 2 CBZ-Val-Trp-Leu-NH 2 120 51 CBZ-Val-Tyr-OMe Leu-NH 2 CBZ-Val-Tyr-Leu-NH 2 25 97 a CBZ-Ala-Phe-OMe Leu-NH 2 CBZ-Ala-Phe-Leu-NH 2 90 81 a CBZ-Val-Trp-OMe Leu-NH 2 CBZ-Val-Trp-Leu-NH 2 90 76 a CBZ-Val-Phe-OMe Leu-NH 2 CBZ-Val-Phe-Leu-NH 2 90 90 a CBZ-Ile-Phe-OMe Leu-NH 2 CBZ-Ile-Phe-Leu-NH 2 90 49 a C. CBZ-Val-Tyr-OMe L-Leu-NH 2 CBZ-Val-Tyr-L-Leu-NH 2 60 50 3 CBZ-Val-Tyr-OMe L-Phe-NH 2 CBZ-Val-Tyr-L-Phe-NH 2 60 21 a CBZ-Val-Tyr-OMe D-Leu-NH 2 CBZ-Val-Tyr-D-Leu-NH 2 60 67 a CBZ-Val-Tyr-OMe D-Phe-NH 2 CBZ-Val-Tyr-D-Phe-NH 2 60 68 a CBZ-Val-Tyr-OMe L-Leu-NH 2 CBZ-Val-Tyr-L-Leu-NH 2 60 19 CBZ-Val-Tyr-OMe L-Phe-NH 2 CBZ-Val-Tyr-L-Phe-NH 2 60 8 CBZ-Val-Tyr-OMe D-Leu-NH 2 CBZ-Val-Tyr-D-Leu-NH 2 60 24 CBZ-Val-Tyr-OMe D-Phe-NH 2 CBZ-Val-Tyr-D-Phe-NH 2 60 15 D. Tyr-OEt b Leu-NH, Tyr-L-Leu-NH 2 10 89 a The reaction mixture contained 1 μl/ml water b Unblocked (not N-protected) acyl donor was used. The reaction was performed in isooctane-tetrahydrofuran (THF) 70:30 mixture. Acyl donor and nucleophile were dissolved in THF, then isooctane and soluble α-chymotrypsin solution in isooctane were added and the reaction mixture was incubated at room temperature for a certain period of time. Final concentrations of the reactants in the reaction mixture were: 5.0 - 6.5 mM acyl donor, 7.5 - 10.0 mM nucleophile, α-chymotrypsin 3.5 μM. The reaction was terminated by addition of 10% v/v acetic acid, the mixmre was dried, the residue was redissolved in 70:30 mixmre of 0.1 % trifluoroacetic acid (TFA) solution in water and acetonitrile and analyzed by reversed phase HPLC (C18 μBondapak column, Waters) using 0.1% TFA solution in water and acetonitrile mixmre as eluant. The first nine entries under (A) are repeated from Paradkar and Dordick, J. Am. Chem. Soc. 116:5009 (1994) here for comparison, and showing the product. The next group of examples under (B) shows relatively low yields (38-51 %) where the nucleophile is Leu-NH 2 and the acyl donor is the methyl ester of N-CBZ-Val-Tyr, N-CBZ-Ala-Phe, N-CBZ-Val-Trp. To enhance the enzyme activity, 1 μl/ml of water was added to the reaction mixmre to activate the enzymatic reaction. The last three entries in (B) show that this minor amount of water surprisingly increased the yields to the 76-97% range, in shorter reaction times. The addition of 0.1 % water to the reaction medium is believed to enhance activity by maintaining the active structure of the chymotrypsin, and yet is not present at high enough concentrations to compete stoichiometrically with the nucleophile substrate, which leads to hydrolysis. Polar solvents may provide similar structural stabilization without addition of water, or further solubilization of substrates. For example, isopropanol or other alcohols could be used in the reaction medium. Stereospecific catalysis is shown under (C). As can be seen, the addition of 1 μl/ml of water to the reaction medium increased the yields from the 8-24% range to the 21-68% range. Surprisingly, the D-Leu and D-Phe isomers were more reactive than their L- counterparts. Finally, under (D), an unblocked amino acid ester was used as an acyl donor in the reaction. The quick reaction time and high yield demonstrate the feasibility of soluble enzyme catalysis using acyl donors without N-blockers. This is important as it is often desired to use unblocked amino acids as donors and acceptors due to their lower costs. Unblocked acyl donors might include an amino acid or peptide methyl or ethyl ester. Unblocked nucleophiles would include an amino acid itself. EXAMPLE 8 This example demonstrates the effect of added water on reactions catalyzed by chymotrypsin surfactant ion pairs. Two bar graphs for different reactions catalyzed by chymotrypsin are shown in Fig. IA and Fig. IB. The reactions are given above each graph and the effect of added water concentration (from 0 to 1 μl/ml) on each reaction yield is given. With N-benzoyl-L-tyrosine ethyl ester and 1-leucine amide, the maximal yield was obtained at 1 μl/ml. For N-carbobenzoxy-Val-Tyr methyl ester, maximal yields were obtained with water content as low as 0.2 μl/ml. It is clearly demonstrated that addition of very small concentrations of water (1 μl/ml = 0.1 %, v/v) is capable of increasing the reaction yield. EXAMPLE 9 In this and the following examples, the goals were to find improved methods for enzyme solubilization in organic solvents through identification of the most advantageous surfactant ion- paring agents; to provide improved structure, function, and dynamics of solubilized enzymes, particularly in hydrophilic (polar) orgamc solvents which are useful in peptide synthesis; and to provide methods for using solubilized proteases and lipases in the synthesis of peptides in organic solvents, particularly in dehydrated organic solutions. Organic soluble enzymes exhibit extraordinarily high catalytic activities, α-chymotrypsin has catalytic efficiencies over 3-orders of magnimde higher in the solution state as compared to the suspended state in hydrophobic solvents such as octane or hexane for simple transesterification reactions. Surprisingly, this activation is also observed for peptide synthesis according to the invention. Materials α-chymotrypsin from bovine pancreas and subtilisin Carlsberg from Baccillus licheniformis were purchases from Sigma (St. Louis, MO). Aerosol OT (AOT, sodium bis(2- ethylhexyl)sulfosuccinate, > 99% purity) was also obtained from Sigma and was used without further purification. Organic solvents were purchased from Aldrich (Milwaukee, WI) and were of the highest purity available. Solvents were stored over molecular sieves (Type 4 A) for at least 24 hours prior to use. N-CBZ-L- Ala-L-Phe-OMe, N-CBZ-L- Ala-L-Ala-OMe, N-CBZ-L- Val-L-Trp-OMe, and L-Leu-NH 2 were from Bachem Bioscience Inc. (Switzerland). All other amino acid substrates were from Sigma Chem. Co. All reagents used in this work were of the highest grade commercially available. Extraction Procedure Extractions were performed on 1 mg of an enzyme in 1 ml of 10 mM Bis-Tris propane buffer solution, pH 7.8, containing 2 mM CaCl 2 and 1 %, v/v, isopropanol. This solution was contacted with 1 ml of isooctane, containing 2 mM AOT. The biphasic mixmre was stirred in 5 ca. 250 rpm for 2 min. then the phases were allowed to settle for an additional 2 min. Clear phase separation was subsequently achieved by centrifuging at 6000 rpm for 1 min. The enzyme concentrations in the orgamc phase were calculated from the extinction coefficients of the enzymes in water. The organic phase was evaporated to dryness by bubbling N 2 through the isooctane solution. The residue of the soluble enzyme was re-dissolved in the solvent of 10 choice and used for peptide synthesis. The amount of water in the solubilized enzyme preparations was determined by Karl Fisher titration. The organic solution containing the biocatalyst can be dried in vacuo, and the ion-pared enzyme powder can be redissolved in a solvent of choice resulting in a transparent molecular solution of the enzyme in a nearly anhydrous orgamc solvent. 15 Peptide synthesis The standard reaction mixture consisted of an N-protected amino acid ester as acyl donor, an amino acid amide as acyl acceptor, and the solubilized enzyme in 1 ml total volume. The concentrations of the ester and the amide were varied to obtain values of k ∞ /K,,,. In some cases small concentrations of water were added to the reaction mixmre, but in no case did a 20 biphasic system form. The reactions were performed at 3°C under continuous agitation (250 rpm). Periodically, 200 μl aliquots were removed and the reactions terminated by addition of 20 μl glacial acetic acid. The samples were then evaporated to dryness under reduced pressure, the reaction products were dissolved in acetonitrile and quantitatively analyzed by HPLC (Shimadzu LC-10AS, fitted with a YMC-Pack ODS-AQ column and detected by absorbance at 25 280 nm). Elution was carried out isocratically with 40%, v/v, acetonitrile in aqueous solution containing 0.01 %, v/v, trifiuoracetic acid (pH3). Results Orgamc solvent soluble α-chymotrypsin (CT) efficiently catalyzed the synthesis of a variety of dipeptides in isooctane containing 30% (v/v) tetrahydrofuran (THF); the polar solvent 30 was added to aid in substrate solubility. The reaction of N-Bz-L-Tyr-OEt with L-Leu-NH 2 is suitable for both CT and subtilisin Carlsberg (SC) catalysis in a variety of organic solvents. The values of k^/K m for the organic soluble enzymes in isooctane (containing 30%, v/v, THF) was calculated to be 39 and 43 M ' V 1 for CT and SC, respectively. These values were dramatically higher than those for suspended CT and SC (0.04 and 0.02 M ' V 1 , respectively. The activation by the solubilized enzymes is genuine; no reaction was observed in the absence of enzyme or in the presence of heat-inactivated enzyme (by boiling in water for 30 min prior to extraction into isooctane). Thus, the soluble enzymes are sufficiently activated over their suspended counterparts for peptide synthesis. These findings demonstrate that enzymes in orgamc solvents can function with the same activity and selectivity as found in aqueous solutions, albeit with improved potential for commercially relevant syntheses. The activity of both enzymes is strongly affected by the hydrophobicity of the organic solvent. As depicted in Figs. 2A and 2B, both organic soluble CT and SC were strongly activated in hydrophobic orgamc solutions. Indeed, the values of k^/K m are increased over 100- fold for CT and over 300-fold for SC in going from neat THF to isooctane (containing 30%, v/v, THF). This striking solvent effect is more pronounced for orgamc solvent soluble enzymes than for their suspended counterparts for similar reactions. For example, the k- a K π , of the related subtilisin BPN ' -catalyzed transesterification of N-Ac-L-Phe-OEt with n-PrOH is not substantially different in a hydrophobic solvent such as hexane and a hydrophilic solvent such as acetone. Without intending to be limited to this theory, it can be surmised that the suspended enzyme particles act as a buffer between the inactivating effects of hydrophilic organic solvents and the individual enzyme molecules. Soluble enzymes do not have such a protective mechanism. EXAMPLE 10 Enzymatic peptide synthesis using soluble enzymes in organic solvents is dramatically improved upon addition of small concentrations of water. This enables reactions to be performed in ethyl acetate, which was selected as a representative hydrophilic solvent that can aid in dissolving peptidic substrates. The results are summarized in Figs. 3 A and 3B. Water activates CT catalysis in di- and tripeptide synthesis, the latter with CBZ-L-Val-L- Tyr-OMe as ester donor. In isooctane-THF solution, the addition of as little as 0.05%, v/v, water increased the value of k ^ ZR,,, 3.5-fold, and this value was increased over 50-fold upon addition of 0.20%, v/v, water (Figure 3A). Although the activation is not as significant for tripeptide synthesis with CBZ-L-Val-L-Tyr-OMe as the acyl donor, a 12-fold increase in k- a /K,,, was obtained upon addition of 0.20%, v/v, water. The effect of added water is even more pronounced in ethyl acetate for dipeptide synthesis (figure 3B); the addition of 1.0%, v/v, water resulted in greater than a 150-fold activation when compared to the dry ethyl acetate solution. In both isooctane-THF and ethyl acetate, the activation by water did not lead to substantial hydrolysis of the ester donors. For example, even in the presence of 1.0%, v/v, water in ethyl acetate, the k^/K,-, for N-Bz-L-Tyr-OEt hydrolysis was nearly 50-fold lower than that for peptide synthesis. Thus, the reaction selectivity toward peptide synthesis remains high even in the presence of small concentrations of water. The reason for the observed drop in k^/K m above 0.2% and 1.0%, v/v, water in isooctane-THF and ethyl acetate, respectively, is unclear. It is not due to a competing hydrolysis reaction as no increase in the rate of formation of N-Ac-L-Phe is observed. Instead, it is possible that a structural change in the enzyme occurs thereby resulting in a less reactive enzyme. Enzymes become more flexible as the hydration of the solvent increases, but increased flexibility does not always lead to increased activity. A case in point is the hydration of SC in THF: addition of <0.5%, v/v, water strongly activates SC; however, above this hydration level, the activity of SC drops precipitously. Thus, the degree of solvent (and hence enzyme) hydration can result in a complex behavior that is characterized by enhanced and diminished reactivity depending on the level of enzyme hydration. Such behavior is observed for CT catalysis in both isooctane-THF and ethyl acetate. Of great advantage is the dramatic rate enhancement obtained in ethyl acetate in going from dry to 0.5% (v/v) added H 2 O for the synthesis of Bz-Tyr-Leu-NH 2 by CT. The addition of water also has πiinimal effect on reaction selectivity toward peptide synthesis. In both isooctane:THF (7:3) (Fig. 3A), and ethyl acetate (Fig. 3B), the addition of water (up to 0.25% (v/v) in isooctane and 0.5% or 1% (v/v) in ethyl acetate) had a minimal impact in the loss of ester substrate to hydrolysis. Thus, the selectivity of the reaction (toward peptide synthesis) is high. This finding has direct industrial application as it enables use of a solvent that is ideal for peptide synthesis reactions. Unlike CT, the activation of SC upon partial hydration of isooctane-THF or ethyl acetate was not significant (Figs. 4A and 4B), and actually resulted in substantial hydrolysis. Specifically, in isooctane-THF containing 0.25%, v/v, water, the k^/K,. for hydrolysis is nearly as high as for peptide synthesis. Even in dry isooctane-THF, there was a significant fraction ( > 10%) of hydrolysis as compared to CT. Measurements of the water content on CT and SC in dry isooctane-THF indicated that both proteins have bound water contents of 7.5%, w/w. The higher hydrolytic activity of SC relative to CT relates to the proclivity of SC for hydrolysis. SC, due to its more hydrophilic binding pocket, may have greater propensity for water as the nucleophile than for L-Leu-NH 2 as compared with CT. Hence, hydrolysis is a favorable reaction even in the presence of small concentrations of water. The small amount of water bound to the enzyme in the absence of added water is sufficient to promote some background hydrolysis. Thus, according to the invention, the water present in the reaction solution is sufficient to stabilize the enzyme strucmre so as to maximize the rate of peptide synthesis but not so high as to cause substantially increased hydrolysis. The amount of water added to dry organic solvent to provide a reaction solvent thus may be between about 0.025% to about 2.5%, preferably from about 0.05 % to about 0.5 % . With an enzyme having a hydrophobic active site such as CT, the preferred range is about 0.05% to about 0.15%, and in isooctane with 30% THF, v/v, the preferred amount is about 0.1 %. In polar solvents such as ethyl acetate, the range is higher, preferably 0.5% to 2.0%, most preferably about 1.0%. For an enzyme with a hydrophilic active site such as subtilisin Carlsberg in isooctane, the minimum amount of added water is preferred. In a polar solvent, such as ethyl acetate, the range may be from about 0.25% to about 1.0%, preferably about 0.5%. The amount of water added should further be sufficient to provide increased yield of the peptide reaction product as compared to dry reaction conditions. As shown in Figs. IA and IB, the amount of water added to increase yield of a dipeptide and a tripeptide catalyzed by CT in isooctane/THF (70/30) was between about 0.01 % and 0.1%, preferably between about 0.02% and 0.1%. EXAMPLE 11 CT-catalyzed peptide synthesis shows substrate specificity. CT is specific for bulky hydrophobic amino acids. The specificity of CT was examined in isooctane-THF and e yl acetate solutions under optimal solvent hydration levels of 0.2 and 1.0%, v/v, added water, respectively. Values of k^/K m for the ester donor are depicted in Table II for two series of CBZ-dipeptide methyl esters each of them differing in the P, amino acid residue. Table II shows values of k^/K m (M'V 1 ) for organic solvent-soluble α-chymotrypsin-catalyzed peptide synthesis between different dipeptide esters and L-LeuNH 2 . The amide concentration was fixed at 10 mM and the ester concentrations were varied from 1 to 10 mM. The enzyme concentration was 100 μg/ml. All experiments were performed in triplicate and standard errors determined to be < 15% of the values presented in the table. Table II. Ester Isooctane-THF 70:30 Ethyl acetate +0.2%, v/v water + 1 % , v/v water N-CBZ-L-Ala-L-Phe-OMe 141 33.9 N-CBZ-L-Ala-L-Val-OMe 0.017 0.001 N-CBZ-L-Ala-L-Ala-OMe 3.75 0.53 N-CBZ-L- Ala-Gly-OMe 1.10 0.22 N-CBZ-L-Val-L-Tyr-OMe 455 33.2 N-CBZ-L-Val-L-Trp-OMe 75.6 14.3 N-CBZ-L-Val-L-Phe-OMe 71.9 10.4 N-CBZ-L-Val-L-Leu-OMe 6.59 0.71 N-CBZ-L-Val-L-Ala-OMe 2.21 0.52 The aromatic-containing dipeptides were highly reactive in both partially hydrated isooctane-THF and ethyl acetate. Thus, the soluble CT of the invention has hydrolytic specificity with a preference for hydrophobic amino acid residues comparable to CT in aqueous solutions and to CT-catalyzed peptide synthesis in organic solvents using suspended enzyme. A direct comparison of the substrate specificity of the organic solvent soluble CT to the suspended enzyme was made using two of the CBZ-dipeptides in Table II; namely those with a Phe and an Ala in the P [ position. Again using partially hydrated solvents, the values of k- a /K π , for the soluble enzyme were substantially higher (up to three orders of magnitude) than those of the suspended enzyme in isooctane-THF and ethyl acetate, respectively (Table IH). Table D Substrates K M (M-'S- 1 ) Isooctane-THF Ethyl acetate +0.2%, v/v water + 1 %, v/v water α-Chymotrypsin (suspended) N-CBZ-L-Ala-L-Phe-OMe 0.44 0.037 N-CBZ-L-Ala-L-Ala-OMe 0.2 0.011 Ratio 2.2 3.3 α-Chymotrypsin (solubilized) N-CBZ-L-Ala-L-Phe-OMe 141 33.9 N-CBZ-L-Ala-L-Ala-OMe 3.75 0.53 Ratio 37.5 64 Moreover, the specificity ratio between the Phe- and Ala- containing dipeptides was markedly different between the two enzyme forms and between the two organic solvents. Specifically, the ratios of (k cat /K m )p he (k cat /K rn ) Ala for the suspended enzyme in isooctane-THF and ethyl acetate are a modest 2.2 and 3.3 respectively. These ratios are substantially increased with the soluble CT to 37.5 and 64.03 in isooctane-THF and ethyl acetate, respectively. The ion-pared, organic soluble CT is more flexible than its insoluble counterpart. This flexibility provides a binding site tiiat is more native-like (as in water) and capable of eliciting more native-like substrate specificities than the more rigid suspended enzyme form. EXAMPLE 12 A variety of proteases and nonproteases are active in the solubilized state in orgamc solvents. Six different proteases were solubilized in isooctane (containing 1 % isopropanol) in yields ranging from 23 to 70% (0.23 to 0.47 mg/ml), including α-chymotrypsin, subtilisin Carlsberg, subtilisin BPN ' , trypsin, thermolysin, and papain. Also glucose oxidase and soybean peroxidase can be solubilized for other applications including biosensors and bioremediation catalysts, respectively. The solubilization conditions were selected according to the methods of the invention, which provide for solubilizing all these proteins as surfactant ion pairs in organic solvents. EXAMPLE 13 The stability and activity of subtilisin BPN ' is increased in polar orgamc solvents upon the addition of very small concentrations of water. While the stability of soluble subtilisin BPN ' is high in nonpolar solvent such as octane (Table IV), substantial deactivation is observed in polar solvents such as tetrahydrofuran (THF). However, activation of the enzyme in THF is feasible upon addition of small concentrations of water. For example, addition of 0.2% (v/v) water increases the half-life at room temperature from 10 min (in dry solvent) to > 40 min. Water has been shown to stabilize both the secondary and tertiary strucmre of the enzyme in THF. These studies have been extended to tert-amyl alcohol with similar stability enhancements. Thus, the amount of water added to the reaction solvent according to the invention should be sufficient to provide enhanced stability, such as in the range of about 0.1% to about 0.3%, preferably about 0.2% for polar solvents and subtilisin. Table r . Kinetic Constants for Soluble Subtilisin BPN' in Various Solvents Solvent WUMV) 1 . Observed half-life (h) b Octane 370 ± 40 1400 d Aqueous buffer 3500 ± 200 c 2.17 Tetrahydrofuran 0.04 ± 0.01 0.17 THF + 0.2% H 2 O 0.36 ± 0.06 0.67 tert-Amyl alcohol 1.2 ± 0.2 1.67 tøτ-Amyl alcohol + 0.2% 2.8 ± 0.4 n.d. H 2 O Octane (suspended) 0.6 ± 0.1 n.d. "Catalytic constants determined for tranesterification between N-Ac-L-Phe-OEt (0.1 -250 mM) and l-PιOH(0.5M) using 14 - 150 μg/ml subtilisen BPN'. "Observed half-life measured by incubating soluble subtilisin in the given solvent and then assaying the activity in aqueous buffer by transferring small aliquots of subtilisin solution to water. c Catalytic efficiency determined for hydrolysis of N-Ac-L-Phe-OEt (o.1 -1.0 nM) in water using 10 - 50 μg/ml enzyme. d Observed half-life reported in oxane is an estimated value as the enzyme lost only 35% activity in 2 months when incubated in dry octane. Soluble Enzyme Activity and Stability. The k K., of subtilisin BPN' dissolved in octane is nearly three orders of magnimde greater than that of the suspended enzyme in the same solvent (Table IV). This exceptional activation of the enzyme results in a value of k^/K m in octane that is within one order of magnimde of the value in aqueous buffer, and demonstrates that the organic soluble enzyme is highly active in nonpolar, homogeneous organic solutions. Moreover, the enzyme is three orders on magnimde more stable to irreversible inactivation in octane than in aqueous buffer, presumably because of the absence of autolysis in the organic solvent. Therefore, over its active lifetime the productivity of the soluble enzyme is higher in octane than in water. The benefits of solubilization are not observed in all orgamc solvents. For instance, values of k^/K π , are dramatically lower in the more polar tert-amyl alcohol and tetrahydrofuran (THF) solutions (Table IV). Indeed, the four orders of magnitude difference of k^/K π , values between octane and THF correspond to a 7.7 kcal/mol destabilization of the transition state of subtilisin in THF as compared to octane. Whereas the measurable activity of soluble subtilisin is retained after several months storage in octane, activity in THF is lost in minutes. Furthermore, incubation in THF induces severe irreversible inactivation of soluble subtilisin. Specifically, only 50% of the activity can be recovered if soluble subtilisin is incubated in THF for 10 min and then transferred to water. As a practical matter, enzyme stability according to the invention should be greater than that of CT in dry THF, preferably at least about 0.25 hours, more preferably more than about 0.5 hours, and most preferably over an hour. A half life of over 10, 100, or 1000 hours is achievable according to the invention. Effect of solvent hydration on enzyme activity. To compensate for possible stripping of water from the enzyme, causing lower catalytic efficiencies, we observed that additions of small concentrations (0.2%) of water in both THF and tert-a yl alcohol results in an increase in enzymatic activity of soluble subtilisin (Table IV). Coincidentally, the addition of 0.2% water to THF also improves the stability of soluble subtilisin by ca. 4-fold. Thus, addition of water to polar solvents improves activity and stability of soluble subtilisin. EXAMPLE 14 Subtilisin BPN ' can be refolded in octane. It is known that enzymes can be partially denatured in water and still be refolded to the native conformation. This has been extended to nonaqueous systems (Fig. 5). Specifically, subtilisin BPN ' is denatured (loses its tertiary strucmre) in THF for short times (i.e. , before secondary strucmre is lost), and then the enzyme is transferred to water. Refolding occurs and the enzyme regains its activity. Similarly, the denatured enzyme in THF is transferred to octane. As in water, the native enzyme strucmre is obtained and the activity is restored. This demonstrates that water is not required to fold protein-surfactant ion pairs according to the invention. Fig. 5 depicts the fraction of native enzyme as a function of incubation time in both dry THF and THF supplemented with 0.2% (v/v) water. The rapid loss of catalytic activity in dry THF is concomitant with the loss of native teriary strucmre of the enzyme. Hence, the loss of native tertiary strucmre appears to correlate with the loss in catalytic activity in THF, supporting the THF inactivates soluble subtilisin by disrupting the native teritary strucmre. Furthermore, the addition of a small concentration of water is sufficient to stabilize the tertiary strucmre of subtilisin, accompanied by an enhancement of the stability of the enzyme (Table IV). Water appears to stabilize subtilisin in THF by helping to maintain its native strucmre. Reversible and Irreversible Inactivation of Soluble Subtilisin in Organic Solvents. The rapid loss of activity in THF is depicted in Fig. 5. When assayed in THF, subtilisin loses 99% of its activity in less than 10 min. Much of this inactivated enzyme can be regenerated, however, upon transfer of the soluble enzyme to either water or octane. For example, transfer of subtilisin to water (by taking an aliquot of enzyme from the THF solution and diluting into aqueous buffer) after 10 min resulted in the regain of over one-third of d e native enzyme activity (Fig. 5). Thus, soluble subtilisin inactivates quickly in dry THF, but can be partially renatured by transferring the enzyme to water. Similarly, transferring the enzyme from THF to octane also results in a regain of a portion of the active subtilisin, albeit a lesser fraction than that observed in water (Fig. 5, diamonds). After the rapid, partial reactivation, the fraction of active enzyme in octane does not measurably change further for up to 30 min. Subsequent transfer of the partially reactivated enzyme in octane to water, however, results in a fraction of active enzyme similar to that observed for the direct transfer of enzyme from THF to water Thermal inactivation of soluble subtilisin BPN 1 in octane. Similar inactivation and reactivation behavior was observed using elevated temperature as the denaturant in octane. Subtilisin was incubated in octane at 70 °C for various lengths of time and the activity of the enzyme was assayed in octane at 70°C, in octane at 25 °C, and following extraction into water at 25 °C. Three distinct trends were observed at depicted in Fig. 7. First, in contrast to the high stability of soluble subtilisin at 25 °C, over 98% of enzymatic activity is lost after 30 minutes of incubation at 70 °C in octane. Second, the majority of the inactivated enzyme can be renatured by extraction back into aqueous buffer at 25 °C. Third, a significant fraction of the enzyme can also be renatured in octane by rapid cooling of the enzyme solution to 25 °C, albeit a smaller fraction than in water. A hypothetical structural model of subtilisin inactivation has been developed to facilitate understanding of certain applications of the invention. Specifically, five distinct enzyme forms are present at different times during the inactivation process in a solvent such as THF and include the native (N), denatured (D), inactivated (I), unfolded (U), and random coil (R) forms of soluble subtilisin (Fig. 6). The N-form is proposed to be similar to the native structure present in aqueous solutions. The D-form is structurally less compact than the N-form and has no catalytic activity due to the disruption (however slight) of the active-site strucmre. This form exists in equilibrium with the N-form and can be converted back to the N-form in both octane and water. The I-form is even less compact than the N and D forms and can only be converted back to the N-form in water. The I-form can be converted to the U-form by further incubation in dry THF. The U-form has lost its tertiary structure and cannot be converted back to the N- form even in water. Addition of water to THF appears to stabilize the D form, thereby allowing native strucmre and activity to be regained. Partially unfolded subtilisin of the invention is capable of being refolded in an organic solvent. This demonstrates that bulk water is not required for refolding of a partially denatured enzyme-ion pair. Moreover, the reversibility of the N-D, transformation in octane implies that the native subtilisin BPN' ion pair in octane (N-form) is thermodynamically stable. In contrast insoluble enzymes in organic solvents appear to be maintained solely by kinetic limitations to unfolding, presumably due to the rigid nature of an enzyme suspension in the organic milieu (Schulze and Klibanov, 1992). In organic solutions such as octane where such kinetic limitations are removed by solubilization, soluble subtilisin in thermodynamically stable in me native conformation. Possibly the neutralization of some of me charged residues and the introduction of tri-octyl tails of AOT on the surface of the enzyme stabilizes the folded enzyme strucmre in nonpolar solvents. The relative fractions of enzyme renatured upon transferring from THF to water is greater than that renatured in octane. For example, after a 10 min incubation in THF, ca. 30% of the enzyme can be renatured upon transfer to water, whereas, only 10% of the enzyme can be renatured upon transfer to octane (Fig. 5). The difference is not due to continued deactivation of soluble enzyme upon transferring the enzyme to octane (Fig. 5). This suggests the existence of the D 2 form which does not renamre in octane, but can undergo renamration upon transfer to water. The concentration of the D 2 form can be estimated by the difference in fraction of activities recoverable in water and octane. Based on CD spectroscopy, it appears that D 2 unlike D, has lost almost all native tertiary strucmre, but retains full secondary strucmre. Thus, enzyme-surfactant ion pairs according to the invention can refold to native conformation in organic solvents. This approach can only be applied using orgamc solvent- soluble enzymes according to the invention. Preferably, the temperature and polarity of the reaction solution are selected by approaches within the level of ordinary skill to maintain adequate activity and stability, as described above. The high catalytic activity of subtilisin BPN' in nonpolar organic solutions contrasts greatly witfi the activity of the suspended enzyme, and this appears to be due to the maintenance of me secondary and tertiary strucmre of the soluble enzyme when extracted out of an aqueous solution into a nonpolar organic solvent. A major difference between the two preparations is that the suspended enzyme form undergoes lyophilization whereas the soluble enzyme form undergoes a liquid-liquid extraction followed by gaseous drying. Lyophilization can induce conformational changes in a protein which can only reverse to the native strucmre in aqueous solutions. The suspended enzyme, therefore, may be much less active than its soluble counterpart because it exists in the partially denatured form in orgamc solvents. The soluble enzyme is also more conformationally flexible than its insoluble counterpart. Such increased flexibility, particularly at the active site of the enzyme can promote enzyme activity in organic solvents. Subsequent drying of the extracted protein without freezing does not destroy the native strucmre of the enzyme. Soluble subtilisin is very stable in octane, and, presumably because of the absence of autolysis in octane and decreased flexibility, the enzyme is substantially more stable than in aqueous solutions. Assuming substrate saturating conditions, a practical measure of the operational value of an enzyme is its number of turnovers accomplished in a single half- life of the enzyme. This dimensionless term (represented by k^ x τl/2) provides a general measure for the operational power of a biocatalyst. For the soluble enzyme in octane, this value is 1.0 x 10 7 (based on a half life of 2 months) and is greater than the value in water (1.2 x 10 6 ) . Thus, soluble subtilisin BPN' is a practical biocatalyst in octane. The embodiments illustrated and discussed in this specification are intended only to teach those skilled in the art the best way known to the inventors to make and use the invention. Nothing in this specification should be considered as limiting the scope of the present invention. Modifications and variations of the above-described embodiments of the invention are possible without departing from the invention, as appreciated by those skilled in the art in light of the above teachings. Otf er enzymes, surfactants, solvents, and substrates may be used in similar manner or using minor variations according to techniques known in the art. It is therefore to be understood that, widiin the scope of the claims and their equivalents, the invention may be practiced otherwise than as specifically described.

Claims: WHAT IS CLAIMED IS: 1. A method of catalysis in an organic solvent, comprising me steps of: (a) obtaining an ion pair complex of an activated enzyme and a surfactant, (b) dissolving the activated enzyme-surfactant ion pair complex in an orgamc reaction solvent, comprising an organic solvent and water in an amount sufficient to maximize the rate of catalysis and stabilize the activated enzyme without substantially increasing hydrolysis, and ranging from about 0.025% to about 2.5% v/v, (c) adding to the organic reaction solvent a substrate for the enzyme, (d) allowing a sufficient time for the enzyme to catalyze conversion of the substrate to a product, and (e) recovering the product. 2. The method of claim 1, wherein conversion of the substrate to the product is substantially completed before recovering the product. 3. The method of claim 2, further comprising precipitating the enzyme from the orgamc solvent by removal of the surfactant from me enzyme-surfactant complex. 4. The method of claim 1, further comprising adding the substrate to, and recovering the product from the organic reaction solvent while enzyme catalyzed conversion of substrate to product is continuing. 5. The method of claim 1, in which the substrate comprises an acyl donor and a nucleophile. 6. The method of claim 1, in which the substrate comprises at least one of an amino acid, an amino acid ester, an N-blocked amino acid, an N-blocked amino acid ester, an amino acid amide, an N-blocked amino acid amide, a polypeptide, a polypeptide ester, an N-blocked polypeptide, an N-blocked polypeptide ester, a polypeptide amide, an N-blocked polypeptide amide. 7. The method of claim 5 in which the acyl donor is a methyl or ethyl ester of tyrosine, tryptophan, alanine, or phenylalanine; a methyl or ethyl ester of a dipeptide or tripeptide containing any of tyrosine, tryptophan, alanine, or phenylalanine; or an N-benzoyl, N-acetyl, or N-carbobenzoxy derivative thereof; and the nucleophile is an amino acid amide. 8. The method of claim 5, in which the acyl donor and nucleophile are unblocked. 9. The method of claim 5, in which the acyl donor and nucleophile are added in a ratio between about 2:1 and 1:2. 10. The method of claim 1, in which the water content of the organic enzyme reaction solution does not exceed the water samration point for the organic solvent containing the surfactant. 11. The method of claim 1 , in which the molar ratio of water to enzyme in the organic reaction solvent is less than about 75:1. 12. The method of claim 1, further comprising adding up to 0.2% v/v water to the reaction solvent. 13. The method of claim 1, in which the reaction solvent comprises a water miscible hydrophilic organic solvent. 14. The method of claim 1 in which the enzyme is a catalytic antibody, an oxidoreductase, a transferase, a lyase, an isomerase, or a ligase. 15. The method of claim 1 in which the enzyme is a hydrolase with acyl transferase activity in organic solvents. 16. The method of claim 1 in which the enzyme is a peroxidase catalyzing phenolic polymerizations, a tyrosinase catalyzing aromatic hydroxylations, an alcohol dehydrogenase catalyzing stereoselective oxidation and reduction, a lipase, a nuclease, an aldolase, a phosphatase, or a sulfatase. 17. The method of claim 1 in which the enzyme is subtilisin, papain, pepsin, thermolysin, or thrombin. 18. The meti od of claim 1 wherein step (a) comprises: (1) forming a two-phase aqueous/organic system comprising an activated enzyme solution produced by dissolving an enzyme in an aqueous activating solution at a pH of maximal enzyme activity, an enzyme concentration of from about 1 μg/ml to about 10 mg/ml, and ionic strength less than about 80 mM; an organic extraction solvent that is immiscible with water; and an ionic surfactant; the molar ratio of surfactant to enzyme in the two-phase system being sufficient to form an enzyme-surfactant ion pair complex, and substantially less than the ratio that would form reversed micelles in the organic solvent, (2) then agitating the two-phase system for a period sufficient to produce an ion pair complex of the activated enzyme and the ionic surfactant and to extract the ion pair complex directly from the aqueous solution into solution in the organic extraction solvent, without substantial formation of reversed micelles, (3) then separating the organic phase from the aqueous phase, whereby a homogeneous organic enzyme solution is obtained containing dissolved activated enzyme-surfactant ion pair complex and essentially no reversed micelles, the activated enzyme retaining native structure and having catalytic activity at least an order of magnimde greater than a suspension of an equal amount of the enzyme and organic solvent without surfactant. 19. The method of claim 18, further comprising the step of drying the organic extraction solvent after extraction. 20. The method of claim 18, further comprising the step of evaporating the organic extraction solvent. 21. The memod of claim 18, in which the enzyme is α-chymotrypsin, the surfactant is AOT, the pH of the aqueous activating solution is from about 7.0 to about 8.5, me ionic strength is less than about 20 mM, the enzyme: surfactant ratio is about 1:30 and the enzyme surfactant ion pair has a catalytic efficiency k^/K,,, in isooctane for the transesterification of N- acetyl-L-phenylalanine ethyl ester with 1-propanol of greater than 3000 M" 1 s 1 . 22. The method of claim 18, in which the volumes of aqueous solution and organic extraction solvent are about equal, the starting concentration of surfactant in the organic solvent is about 2 mM, and the starting concentration of the enzyme in the aqueous solvent is about 1 mg/ml. 23. The method of claim 18 in which the surfactant is cationic and the pH of maximum activity is above the pi. 24. A catalyst produced by (1) forming a two-phase aqueous/organic system comprising an activated enzyme solution produced by dissolving an enzyme in an aqueous activating solution at a pH of maximal enzyme activity, an enzyme concentration of from about 1 μg/ml to about 10 mg/ml, and ionic strength less than about 80 mM; an organic extraction solvent that is immiscible witii water; and an ionic surfactant; the molar ratio of surfactant to enzyme in the two-phase system being sufficient to form an enzyme-surfactant ion pair complex, and substantially less than the ratio that would form reversed micelles in the organic solvent, (2) then agitating the two-phase system for a period sufficient to produce an ion pair complex of the activated enzyme and the ionic surfactant and to extract the ion pair complex directly from the aqueous solution into solution in the organic extraction solvent, without substantial formation of reversed micelles, (3) then separating the organic phase from the aqueous phase, whereby a homogeneous organic enzyme solution is obtained containing dissolved activated enzyme- surfactant ion pair complex and essentially no reversed micelles, the activated enzyme retaining native strucmre and having catalytic activity at least an order of magnimde greater than a suspension of an equal amount of the enzyme and organic solvent without surfactant. 25. The catalyst of claim 24 as an essentially pure solid having water content of about 5% to about 10% by weight.

Inventors: DORDICK JONATHAN S, PARADKAR VIKRAM M, DORDICK, JONATHAN, S., PARADKAR, VIKRAM, M.
Applicants: BIOTECHNOLOGY RES & DEV, DORDICK JONATHAN S, PARADKAR VIKRAM M, UNIV IOWA RES FOUND, BIOTECHNOLOGY RESEARCH AND DEVELOPMENT CORP., DORDICK, JONATHAN, S., PARADKAR, VIKRAM, M., UNIVERSITY OF IOWA RESEARCH FOUNDATION
Application year: 1996
Main classification: C12P1
IPC codes: C12N9, C12P1, C12P21