A RECOVERY AND ACTIVATION PROCESS FOR MICROBIALLY PRODUCED CALF PROCHYMOSIN

Abstract: There is disclosed: a process for recovering microbially produced bovine prochymosin in a form in which it is capable of being converted to active chymosin which comprises: (a) solubilizing the microbially produced bovine prochy­ mosin in a denaturing solvent; and (b) renaturing the prochymosin by diluting or removing the denaturing agent in the solvent. Further steps leading to the production of active mature chymosin therefrom are also described, these additional steps comprising; (c) activating the renatured prochymosin by reducing the pH of the solution containing the renatured prochymosin to produce active pseudochymosin; and (d) elevating the pH of the solution containing the active pseudochymosin to produce active mature chymosin.

Description: BACKGROUND OF THE INVENTION Chymosin (also called rennin E.C. 3.2.23.4) is an enzyme isolated from the fourth stomach of the calf. It is valued for its ability to produce milk curds by catalyzing the hydrolysis of kappa-casein to para-kappa-casein which, in the presence of calcium ion, precipitates as the insoluble curd calcium paracaseinate. After removal of the whey, the curd is processed to make various types of cheeses. Although several proteolytic enzymes will clot milk, the best cheeses have been produced from milk clotted with preparations rich in chymosin. The availability of chymosin - and ultimately its price - depends upon the demand for veal, since the production of chymosin diminishes, and the production of pepsin increases, as the animal matures and is weaned. Enzymes similar to chymosin have been extracted from microorganisms fungi, especially M. mehei , but the curd and, ultimately, the taste of the cheese are different. The superiority of chymosin for cheese making is probably related to the highly specific manner in which it attacks its substrate, kappa-casein. Bovine calf chymosin exists as two isozymes (designated A and B), which can be resolved by DEAE-cellulose chromatography of the crystalline enzyme. Isozyme B, which may be catalytically less efficient than isozyme A, is the more abundant form in tissue extracts. Bovine calf chymosin isozyme B has been sequenced, and isozyme A has been partially sequenced, to reveal only one amino acid difference at residue 290 (glycine in B and aspartic acid in A) (see Foltmann, B. et al., J. Biol. Chem. , 254: 844-8457 [1976]). Chymosin is synthesized within the cells of the stomach lining in a precursor form known as preprochymosin. The "pre" portion of preprochymosin is a sequence of amino acids located at the amino terminus. These amino acids comprise a signal peptide which appears to be involved in the transport of the protein to the cell wall for secretion into the periplasmic space. The signal peptide is cleaved at the cell wall and the enzyme is secreted as prochymosin. Prochymosin is a zymogen containing 365 amino acids (40,477 Daltons). Prochymosin is converted to chymosin by the specific removal of 42 N-terminal amino acids. The conversion of prochymosin to chymosin is favored by the low pH environment of the stomach. Particular attention has been directed to studying the conversion of prochymosin to chymosin. Prochymosin was first reported by Hammersten in 1872 (Hammersten, O., Upsala Laekarefoeren. Foerh ., 8 , 63 (1872)). It is stable at neutral and alkaline pH and has been isolated by several methods. Foltmann and coworkers have studied the conversion of natural prochymosin to chymosin (Pedersen, V.B. and Foltmann, B., Eur . J . Biochem . 55 , 95 (1975)); (Foltmann, B. et al., Proc . Nat . Acad . Sci . (U.S.) 74 , 2321 (1977)). (Pedersen, V.B., Christensen, K.A. and Foltmann, B., J . Biochem . 94 , 573 (1979); Foltmann, B., C . R . Trav . Lab . Carlsberg , 35 , 143 (1966)). They proposed that at pH2, an intermolecular proteolysis occurs which cleaves the prochymosin at the Phe-Leu[27-28] bond, to produce an active form, "pseudochymosin", which converts to chymosin at pH 4.0 or greater by intramolecular proteolysis. Others have postulated an intramolecular reaction for the generation of pseudochymosin (Al-Janaki et al., J . Biol . Chem ., 247 , 46 28 (1972)). With the advent of recombinant DNA technology, it has become possible to produce prochymosin by the expression, in a transformed microorganism, of cDNA encoding the amino acid sequence of prochymosin under the control of a promoter and regulatory sequence. European Patent Application No. 84304682.9 of Genex Corporation describes a method of producing chymosin which involves expressing a DNA sequence encoding a fusion protein. The fusion protein comprises an N-terminal fragment of a bacterial protein normally associated with the promoter sequence (e.g., the β subunit of tryptophan synthetase) fused to "activatable prochymosin". The activatable prochymosin comprises the amino acid sequence of "mature" chymosin together with a sufficient portion of its presequence (at least about 15 amino acid residues) such that the product can undergo post translational autocatalytic cleavage to produce active chymosin. In addition to a portion of the presequence, the prochymosin fusion product can contain part or all of the signal peptide of preprochymosin and/or a short linker sequence of amino acids, the latter being situated between the N-terminal fragment of the bacterial protein and the amino acid residues of prochymosin (or preprochymosin). The linker sequence in the expressed protein results from the translation of a synthetic DNA linker sequence which serves to fuse the DNA sequence encoding the bacterial protein fragment to the DNA sequence encoding prochymosin (or preprochymosin) in the expression vector and to keep the reading frames of the sequences encoding the two segments in phase. The expression product, i.e., the prochymosin fusion protein, forms an insoluble precipitate within the cells. After cell lysis, this precipitate is both insoluble in conventional solvents for proteins and incapable of undergoing activation by autocatalytic cleavage to produce mature chymosin. The inability of the expression product to self-activate is believed to be related to improper folding of the expressed protein, which in turn is related to the unnatural environment of the microbial host in which it is expressed. Processes for the solubilisation of insoluble chymosin precursor by denaturation, followed by a renaturation to form the native form of the chymosin precursor are e.g. described in EP-A-0068691, EP-A-0122080, No 83/04418 or No 84/03711. The denaturants used in said documents include aqueous solutions of urea or guanidine hydrochloride or alkaline solutions of pH between pH 9.5 and 11.5. SUMMARY OF THE INVENTION This invention is based on our discovery that microbially produced bovine prochymosin can be recovered and activated by a process which comprises: (a) solubilizing the expressed prochymosin in a solution of a strong base at a PH of at least 12.0; (b) renaturing the prochymosin by diluting and/or reducing the pH of the base solution; (c) activating the renatured prochymosin at low pH to produce active pseudochymosin; and (d) elevating the pH and incubating the pseudochymosin to produce active mature chymosin. DETAILED DESCRIPTION OF THE INVENTION The process of the invention provides a method for recovering and activating microbially produced bovine prochymosin. As used herein, the term "microbially produced prochymosin" refers to bovine prochymosin which is produced by expression in a microbial host (e.g., E . coli ) of exogenous DNA encoding the amino acid sequence of chymosin and at least a sufficient amount of its 42-amino acid presequence to allow autocatalytic conversion to active mature chymosin following the process described herein. It has been found that at least about the last 14 amino acids of the prochymosin presequence are necessary to obtain a marginal level of activation. Preferably at least 20 amino acids of the presequence are present, most preferably at least 40. If desired, all or a portion of the signal peptide of preprochymosin may also be present. Further, the microbially produced prochymosin which may be subjected to the process of the invention may be in the form of a fusion protein in which the amino acid sequence of prochymosin is fused, at its N-terminal end to all or a fragment of a microbial protein, such as the β subunit of tryptophan synthetase, the expression of which is normally directed by the particular promoter-operator sequence used to direct the expression of the prochymosin. When the prochymosin is expressed as a fusion protein, a linker sequence of amino acids may also be present. The linker sequence serves to join the amino acid sequence of the bacterial protein to the amino acid sequence of the prochymosin. Since expression of the microbially produced prochymosin is initiated by the presence of an ATG sequence, which is translated at the ribosome as methionine, the microbially produced prochymosin will normally have methionine as its first amino acid residue. Microbially produced prochymosin can be produced by expression, in a transformant, of a DNA sequence, under the control of a trp promoter, encoding an N-terminal fragment of the subunit of tryptophan synthetase fused to the amino acid sequence of prochymosin (less its first two amino acids). The sequence encoding the first 27 amino acids of the β subunit of tryptophan synthetase is linked to the prochymosin-encoding sequence through a linker sequence which encodes the residues PRO-SER-MET-ALA-GLY-ARG-SER-PHE-ASP-GLN An E. coli strain (Gx1670) transformed with a plasmid containing this DNA sequence, pGx 2231, has been deposited with NRRL, Peoria, Illinois, with accession No. B-15571. Another plasmid suitable for use in the microbial production of prochymosin is pGX1049, which contains the fused trp B fragment/prochymosin gene under the control of a hybrid promoter formed from portions of the early leftward and rightward promoters of phage λ. The hybrid promoter is repressed by the cI857 temperature sensitive repressor protein. When the microbially produced bovine prochymosin is expressed in a non-secreting host such as E. coli , the cells must be lysed to release the bovine prochymosin prior to subjecting the prochymosin to the process of our invention. The cells containing the expressed bovine prochymosin are first harvested from the fermentation medium in which the cells are grown, normally by centrifugation. The cells are then lysed to release the bovine prochymosin. When working with small cultures of non-secreting host cells, we prefer to employ a French press to lyse the cells. Other conventional methods for cell lysis may be employed, however, such as the use of mechanical homogenizers or enzymatic or chemical means. The prochymosin, along with other insoluble cellular protein and debris, may be removed from the soluble molecules by any means known to those skilled in the art, as for example, by centrifugation at 10,000 xg. The microbially produced bovine prochymosin, which is contained in the centrifugation pellet, can be employed as the starting material in the process of our invention. The microbially produced bovine prochymosin is solubilized in a strong base such as NaOH, at a pH of about 12.0 or greater. The solution can be produced by resuspending the centrifugation pellet containing the microbially produced bovine prochymosin in a dilute sodium hydroxide solution to the desired protein concentration. The denatured microbially produced bovine prochymosin is then renatured, by diluting the base and/or reducing the pH, this is preferably achieved by diluting the solution with deionized water and adjusting to a pH of about 8.5 to 10.5 and incubating at this pH in the presence of a buffer such as glycine. Incubation is carried out at a temperature which promotes renaturation. The incubation temperature generally ranges from about 4°C to 37°C. Incubation is continued until the microbially produced bovine prochymosin has reconformed so that it is capable of undergoing conversion to active chymosin. The time of incubation will depend somewhat upon the temperature at which the incubation is carried out. We have found that incubation for 48 hours at 4°C effectively restores activity to microbially produced bovine prochymosin. We have found that denaturation by NaOH concentrations equal to or greater than 0.01 M, for periods of time in excess of a few minutes inhibits subsequent renaturation of prochymosin to a form capable of undergoing conversion to active chymosin. The amount of time at which the prochymosin can be held under denaturing conditions without significantly affecting renaturation depends on the concentration of the base and the temperature. When denaturation is effected by addition of 0.1 M NaOH at room temperature, we have found that dilution of the NaOH to renature the prochymosin is preferably carried out immediately after denaturing conditions are achieved. In a preferred embodiment of the invention, the centrifugation pellet is resuspended in a chilled solution of a chelating agent such as tetrasodium ethylenediamine tetraacetic acid (about 10mM) at a protein concentration of about 10 mg/ml or greater. The resulting slurry is solubilized and denatured by the addition of NaOH to a final concentration of about 0.1M . The solubilization product, which is highly viscous, is immediately diluted 10 fold with deionized water and the pH adjusted to 10.0 by the addition of glycine. Final glycine concentrations can be from 10mM to 50mM. Renaturation is then performed by incubating at about 24°C for 20 to 24 hours. Following renaturation, the microbially produced bovine prochymosin, having assumed the configuration of the naturally produced material, can be converted to active chymosin by techniques which serve to cleave the presequences of amino acids from the sequence of mature active chymosin. While this can be achieved using exogenous proteolytic enzymes, we prefer to convert the renatured prochymosin to chymosin by lowering the pH of the solution containing the prochymosin to below about 2.5 to produce active pseudochymosin and then adjusting the pH to about 4.0 to 7.0, preferably about 6.0, which causes the pseudochymosin to convert to active mature chymosin. In the practice of the invention, we have carried out the conversion to pseudochymosin by lowering the pH of the solution to about 2.0 by the addition of a non-oxidizing acid, such as hydrochloric acid, and allowing the solution to stand at 4°C. Since active pseudochymosin is highly soluble at pH 2.0, extraneous proteins from the host cell in which the prochymosin was expressed can be conveniently salted out by adjusting the solution to 0.2-0.3 M sodium chloride, followed by centrifugation at 10,000 xg. to precipitate the extraneous proteins. The active pseudochymosin is present in the final solution in low concentration. Concentrated and more highly purified solutions can be obtained by adsorption of the chymosin on a cation exchange resin with pKa of less than 2.5. The resin may be conveniently washed with pH 2 buffer to remove non-adsorbed contaminating protein and then extracted with a buffer solution with a pH of 6.0 to remove adsorbed chymosin. At pH 6.0, the pseudochymosin undergoes proteolysis to active mature chymosin. Alternatively, following the conversion of prochymosin to pseudochymosin by acidification to pH 2.5 or below, the pseudochymosin may be purified and matured to chymosin by a simple titration to pH 6.0 to 6.5 with sodium phosphate. This titration results in the precipitation of extraneous proteins that can be removed by centrifugation at 10,000 xg. or less. The chymosin containing supernatant from the centrifugation can be concentrated to final form by: adsorption to an anion exchange resin such as DEAE cellulose (Wattman DE-52) followed by elution with 0.5 M NaCl in 50 mM sodium phosphate bufer at pH 6.0 to 6.5; precipitation by ammonium sulfate (60% saturation) or saturated sodium chloride followed by resolubilization in sodium acaetate or sodium phosphate buffer, pH 5.5 to 6.5, or ultrafiltration with a 10,000 nominal molecular weight cutoff. The mature chymosin is stable when refrigerated in pH 6.0 buffer, and may be formulated with stabilizers, coloring agents, etc. or it may be lyophilized to produce a dry powder. The enzyme thus produced may be employed as any conventional rennet extracted from calf stomach, e.g., in cheese making. EXAMPLE I Chymosin recovery from pGX2231 E. coli transformed with the plasmid pGX2231 was grown in 8 liters of LB broth containing 100 µg/ml ampicillin. The plasmid contains an E. coli trp promoter-operator sequence, a sequence encoding a ribosome binding site, an initiation signal, and a DNA sequence, operably linked to the promoter, which encodes a 27-amino acid N-terminal fragment of the β subunit of tryptophan synthetase fused to prochymosin (less the first two amino acids) through the sequence Pro-Ser-Met-Ala-Gly-Arg-Ser-Phe-Asp-Gln. Growth was followed by measurement of the absorbance at 560 nm. The cells were harvested when the A 560 reached 2, followed by centrifugation at 10,000 x G. Gross wet weight of the cells was 27.3 grams. The cells were resuspended in 80 ml of deionized water and lysed in a French press at 18,000 psi. The lysate was immediately centrifuged at approximately 10,000 x G and the supernate discarded. The pellet was extracted with 1600 ml and 0.01 N sodium hydroxide, and titrated to a pH of 12 to solubilize the prochymosin fusion protein. The solution was then diluted to 4 liters with deionized water. Glycine (15.2 grams) was added as a buffer and the solution was titrated to pH 9.5 with 0.1 N hydrochloric acid. The solution was allowed to stand for 48 hours at 4°C to allow renaturation of the prochymosin fusion protein. The solution was then titrated with hydrochloric acid to pH 2, and allowed to stand for four hours to allow conversion of prochymosin fusion protein to chymosin. Sodium chloride (70.13 grams) was added and the suspension centrifuged at 10,000 x G. The supernate containing chymosin was decanted and diluted to 6 liters with deionized water. An ion exchange resin with a pKa near 2.0 (Whatman SE 53) was equilibrated with 0.05 M glycine, pH 2.5, and suspended in the diluted supernate. The suspension was agitated for 30 minutes, allowed to stand overnight and the supernate was decanted. The resin, containing adsorbed chymosin, was resuspended in 100 ml of cold 0.05 M phosphoric acid. After centrifugation, the supernate was discarded and the resin resuspended in a minimal amount of 0.05 M monobasic sodium phosphate, and titrated to pH 6 to desorb the chymosin. The suspension was shaken and then centrifuged at 14,500 x G. The supernate (I) was collected and the resin resuspended in 0.05 M monobasic sodium phosphate (pH 6) including 0.9 M sodium chloride to desorb additional chymosin. After shaking, the suspension was centrifuged and the supernate (II) collected. Supernates I and II were tested for chymosin activity using the method described below. Supernate I was determined to contain 7.5 units of chymosin; supernate (II) had 1.9 units of chymosin. Chymosin activity was assayed by its ability to precipitate Kappa-casein in an acidic environment. Dilutions of the enzyme in 50 mM sodium acetate, 10 mM EDTA, pH 5.5 are incubated at room temperature for 24 hours with 2 mg/ml Kappa-casein purified from either whole milk or dehydrated milk, Zittle, C.A. and Caster, S.H., J. Dairy Sci. , 46 : 1183-1188 (1983). The chymosin activity is quantitated by comparison of the lowest sample dilution yielding paracaseinate precipitate with the lowest dilution of standard single strength calf rennet causing precipitation. 1 unit = 1 ml of single strength calf rennet. EXAMPLE II Chymosin recovery from pGX1049 E. coli strain GX1214 transformed with the plasmid pGX1049 was grown in 9 liters of defined medium at 32°C. Expression of chymosin was induced by a temperature shift to 42°C for one hour. Following the 42°C temperature period, the broth was cooled to 39°C and maintained at that temperature for 2 hours. At that point, the cells were harvested. Growth was followed by measurement of absorbance at 540 nm. When the A540 reached 8.0, the cells were induced. Cells were harvested by concentration to about 2 liters with 0.45 µ Durapore membranes in a Pellicon (Millipore) then centrifuged at 8,000 rpm (≈ 9,000 xg) for 30 minutes. The resulting 209.1 gram cell pellet (wet weight) was resuspended in 836 ml. of deionized water. The cells were lysed by two passes through a Manton-Gaulin cell disrupter at an operating pressure of 9,000 p.s.i. The lysate was centrifuged at about 9,000 x g for 20 minutes and the supernatant was discarded. The pellet was resuspended in approximately 1 liter of deionized water, then centrifuged at about 9,000 x g for 20 minutes and the supernatant discarded. The pellet was resuspended in 126 ml. of chilled 10 mM ethylenediaminetetracetic acid tetrasodium salt. The material was then solubilized by addition of 14 ml. of 1 N NaOH with stirring. The solubilized material was immediately diluted with 1120 ml. of deionized water (room temperature) and neutralized to approximately pH 10.0 by the addition of 140 ml. of 0.1 M glycine. The material was centrifuged at about 10,000 x g for 30 minutes to remove cell debris. The material was allowed to stand at room temperature for approximately 67 hours, then titrated to pH 2.0 by addition of 1.0 N HCl. After three days under refrigeration to allow conversion to active pseudochymosin, 955 ml. of the pH 2.0 solution was brought pH 6.5 by the rapid addition of approximately 85.5 ml. of 0.5 M Na₂HPO₄. The sample was stirred for 30 minutes, then centrifuged at approximately 10,000 x g for 20 minutes. The supernatant was collected and stored under refrigeration. To increase the yield, the centrifugation pellet was redissolved in 500 ml. of 0.05 M glycine, pH 2.0 and refrigerated overnight. The pH 2.0 solution was centrifuged at approximately 9,000 x g for 10 minutes. The supernatant was adjusted to pH 6.5 by rapid addition of 0.5 M Na₂HPO₄ and stirred for 30 minutes, then centrifuged. The supernatant was combined with the previous pH 6.5 supernatant to give a final volume of 1760 ml. The pH 6.5 supernatant (1755 ml.) was brought to 60% saturation with 647.6 grams of ammonium sulfate under refrigeration to precipitate the active chymosin. Chymosin activity of the pH2.0 (prechymosin) solution, the pH 6.5 (chymosin) solution and the (NH₄)₂SO₄ pellet was measured by milk clotting activity, with 1 unit defined as the activity of 1 ml. of single strength rennet. The results are presented below.

Claims: A process for recovering microbially produced bovine prochymosin in a form in which it is capable of being converted to active chymosin which comprises: (a) solubilizing the microbially produced bovine prochymosin in a solution of a strong base at a pH of at least 12.0; (b) renaturing the prochymosin by diluting and/or reducing the pH of the base solution. A process as claimed in claim 1 wherein the renaturation step comprises incubating the solution following the dilution and/or pH reduction. A process as claimed in claim 1 or claim 2, wherein the strong base is NaOH. A process as claimed in claim 3 wherein said NaOH is employed at a concentration equal to or greater than 0.01M. A process as claimed in claim 1, wherein the prochymosin is renatured by diluting a NaOH solution containing the prochymosin and incubating the diluted solution at pH 8.5 to 10.5. A process for producing active mature chymosin from microbially produced bovine prochymosin which comprises: (a) solubilizing the microbially produced bovine prochymosin in a solution of a strong base at a pH of at least 12.0; (b) renaturing the prochymosin by diluting and/or reducing the pH of the base solution; (c) activating the renatured prochymosin by reducing the pH of the solution containing the renatured prochymosin to produce active pseudochymosin; and (d) elevating the pH of the solution containing the active pseudochymosin to produce active mature chymosin. A process as claimed in claim 6, wherein the strong base is NaOH. A process as claimed in claim 7 wherein said NaOH is employed at a concentration equal to or greater than 0.01M. A process as claimed in claim 6, wherein the prochymosin is renatured by diluting an NaOH solution containing the prochymosin and incubating the diluted solution at pH 8.5 to 10.5. A process as claimed in any one of claims 6 to 9 wherein activation of the renatured prochymosin is effected at a pH from about 1.0 to 2.5 and the active pseudochymosin is converted to active mature chymosin by elevating the pH to about 4.0 to 7.0. A process as claimed in claim 10 wherein the activation of the renatured prochymosin is effected at a pH of about 2.0 and the active pseudochymosin is converted to active mature chymosin by elevating the pH to about 6.0. A process as claimed in any one of claims 1 to 11, wherein the microbially produced prochymosin is a fusion protein coprising a N-terminal fragment of a microbial protein fused to a protein comprising chymosin and at least a sufficient amount of its presequence such that it is capable of undergoing autocatalytic cleavage to active chymosin. A process as claimed in claim 12, wherein the protein contains at least about the last 14 amino acid residues of the chymosin presequence. A process as claimed in claim 12, wherein the protein contains at least about the last 20 amino acid residues of the chymosin presequence. A process as claimed in claim 12, wherein the protein contains at least about the last 40 amino acid residues of the chymosin presequence.

Inventors: ROBINSON, DOUGLAS EUGENE, SCANDELLA, CARL JOHN, UREN, JACK RICHARD
Applicants: GENEX CORPORATION
Application year: 1984
Main classification: C12N9
IPC codes: C12N9, C07K1