Protein purification method

Abstract: A method of removing a valuable protein from a complex solution and recovering the valuable protein in purified form consists of adding a silica gel sorbant having a pore size approximately the molecular size of the protein to a solution containing the protein, allowing the protein to be sorbed onto the sorbant, separating the sorbant from the solution and then recovering the protein from the sorbant.

Description: The present invention relates to a method of protein purification. More particularly, it relates to a method by which valuable proteins in complex solutions, such as fermentation broths and milk, can be removed and recovered in a purified form. Advances in biotechnology have made it possible to take a gene sequence which is responsible for the expression of a valuable protein in one organism, such as the human gene for insulin, and introduce it into another organism which expresses the valuable protein, for example into a fermentation broth or milk. Unfortunately, it is usually very difficult and expensive to isolate the valuable protein from the other components of the expression system. Isolation and purification are main contributors to the cost of the products. According to its title the publication in World Biotech Reports 2, 1984, pages 175-180 deals with "Concentration & partial purification of proteins by absorption on porous silica". However, the disclosure of this article is incomplete. The protein that was isolated is not identified, the exact elution buffer conditions are not specified and there are no examples for specific elution conditions. There is a need for a simple method of removing and recovering valuable proteins from complex solutions, such as fermentation broths and milk, and also a need for a method of determining which valuable proteins can be removed from such solutions by that method. It is an object of the present invention to disclose a method of removing and recovering valuable proteins from complex solutions, such as fermentation broths and milk. It is a further object to disclose a method of determining whether a valuable protein can be removed and recovered from a complex solution by the method of the present invention. These and other objects are solved by the methods with the features of claims 1 and 2. Preferred embodiments are claimed in dependent claims 3 to 8. The wording of all claims is made to content of the description by reference. The method of the present invention comprises adding to a complex aqueous solution that contains a valuable protein, a safe and effective amount of a silica gel sorbant, namely a silica hydrogel, xerogel or cogel, wherein the pore size of the sorbant is approximately equal to the dimension of the protein to be removed, intimately mixing the silica gel in the complex solution to permit the valuable protein to come into contact with and be sorbed to the sorbant , removing the silica gel with the valuable protein sorbed thereon from the solution, and then desorbing the valuable protein from the sorbant under conditions that minimize the desorption of other sorbed components. A method of avoiding undue experimentation in determining whether a valuable protein in a complex solution can be removed and recovered by the method of the present invention comprises adding a silica gel sorbant as mentioned above which has a pore size approximating that of the valuable protein to be recovered to a complex aqueous solution containing the valuable protein, intimately mixing the sorbant in the solution, allowing the sorbant to remain in the solution for about 10 to 30 minutes so that the protein can be sorbed to the sorbant, then removing the sorbant and treating samples of the sorbant with eluents which can disrupt the various bonds which might exist between the protein and the sorbant. The spent eluents are collected and analyzed to see if they contain the valuable protein. If they do, the method can be used to remove and recover the valuable protein. In the preferred embodiment of the invention, the method of the present invention comprises adding to a complex aqueous solution containing a valuable protein a silica gel sorbant as mentioned above to sorb the valuable protein present in the solution, intimately mixing the sorbant in the solution and allowing said sorbant to remain in the solution for about 10 to 30 minutes until a recoverable amount of the valuable protein has been sorbed onto the sorbant, the silica gel sorbant is then separated from the solution by conventional means, such as filtration. The sorbant with the valuable protein sorbed thereto is then treated with an eluent which disrupts the bonds that exist between the valuable protein and the sorbant so that the valuable protein can be separated from the sorbant and recovered from the eluent. Representative of the valuable proteins which can be removed from a complex solution, such as a fermentation broth or milk, by the practice of the present invention are the following: (a) Proteins, such as Anti Freeze Proteins (AFP), human serum albumin, and Tissue-Type Plasminogen Activator (TPA); (b) Peptide hormones, such as Insulin; (c) Enzymes or similar proteins, such as chymosin and alpha-1-antitrypsin; (d) Other valuable proteins and peptides that can be isolated from fermentation broths, biological fluids, such as milk and, or other liquids or extracts. Examples being growth hormones, and other valuable pharmaceuticals. The silica gel sorbants which can be used in the practice of the present invention are the following: (a) Silica hydrogel, preferably the product having a pore size of about 100 angstroms, such as Britesorb A 100, which is available from P.Q. Corporation, Conshohocken, PA. The Britesorb A100 can be dried to obtain a sorbant that has a smaller pore size, e.g. 25 angstroms. (b) Silica xerogels. (c) Silica cogels, preferably that product available under the tradename DP4660 from P.Q. Corporation. The sorbant selected will have a pore size approximating the molecular dimensions of the protein to be removed. However, if the protein is elliptically shaped or cylindrical the sorbant selected might be one having a smaller pore size that will accommodate that shape molecule. The amount of the sorbant to be added normally will depend upon the protein to be sorbed and its concentration in the solution. The amount used will prefer ably be in excess of that required to sorb all the desired protein. In general, the amount will be much greater than the amounts used in the past in chillproofing beer i.e. substantially in excess of 1000 ppm. The Cohen et al. U.S. Patent No. 4,955,578 discloses a method of making stabilized silica gels useful as sorbants in the method of the present invention. Representative of the eluents that can be used in the practice of the present invention are (a) a hydrophobic interaction bond disrupting eluent, e.g., an eluent containing an alcohol, such as ethanol and/or isopropanol (b) an ion exchange bond disrupting eluent, e.g. an eluent containing salts, buffering agents and/or EDTA, (c) a hydrogen bond disrupting eluent, e.g. containing urea. It was discovered that protein-containing fractions sorbed to silica hydrogel that had been used to chillproof beer could be eluted from the silica hydrogel sequentially with: (1) an eluent with ethanol, salt and the 4.2 pH of beer, (2) an eluent of 0.05 M ammonium bicarbonate, and EDTA with a pH of 8, and (3) an eluent bicarbonate buffer containing 8 M urea and EDTA with a pH of 8. It is believed that the ethanol-containing eluent gently washes the proteins from the pores and matrix of the hydrogel (size-exclusion based elution). Analyses of the eluted material indicated that the proteins had been selectively sorbed, albeit weakly, since the analytical profiles did not correspond to beer profiles. Further elution using an eluent containing EDTA and having a pH of 8 provided evidence for ion-exchange based separation. The EDTA in the eluent also may have disrupted divalent cation interactions that may have directly or indirectly participated in sorption to the hydrogel. The composition of the material eluted using this eluent was different than that of the material desorbed with the ethanol-containing eluent. The final eluent employed contained 8 M urea, an agent that appears to disrupt hydrogen bonding. The composition of the material eluted using the eluent was different than the materials desorbed with the previous two eluents. The results obtained with this sequential elution of hydrogel indicated that the sorption mechanism is complex and can include any one or combination of size-exclusion, ion-exchange, possibly divalent cation interactions, and hydrogen bonding. The materials eluted from the silica hydrogel included surface-active materials, browning products and beer proteins. This suggests that the proteins might not be sorbed directly to the hydrogel matrix, but rather that surface-active fractions might sorb to the matrix and beer proteins might sorb to the surface-active fractions. It also has been suggested that polyphenols might sorb to silica hydrogels and proteins might sorb to the polyphenols. This idea is similar to the idea of surface-active components sorbing to silica hydrogels. Other possible protein-hydrogel interaction modes which might be involved include hydrogen bonding, hydrophilic and hydrophobic interaction, van der Waals, and ionic interactions. In addition, the cogels, such as aluminosilicates or magnesium silicates, that contain metal ions are more ionic in character. In a model experiment employing proteins of defined molecular weight dissolved in a buffer, entrapment appeared to be a mechanism of protein sorption to silica hydrogel, silica cogel, and silica xerogel. Proteins of higher molecular weight were more efficiently sorbed than proteins of lower molecular weight. Lower molecular weight proteins appeared to be less firmly entrapped in the pores of the gel. The proteins examined were aldolase (MW 158,000), bovine serum albumin (MW 67,000), ovalbumin (MW 45,000), chymotrypsinogen A (MW 25,000) and ribonuclease A (MW 13,700). All of these proteins were small enough to enter the pores of the gels. Protein of higher molecular weights would have been excluded from the pores of the gel (100 Angstroms for the silica hydrogel) and would either not have been entrapped (sorbed) or would have been sorbed to the surface of the gel. The entrapment conclusions only directly relate to sorption from a simple buffer containing a few well-defined proteins. Additional sorption mechanisms may occur from complex solutions, such as fermentation broths. No relationship was obvious between protein sorption and the protein parameters of isoelectric point or surface activity. Both of these properties could play a role if there are secondary sorptions or interactions associated with sorption from complex solutions. In general, the proteins and peptides and other molecules that can be purified by the present invention have a molecular weight of about 1,000 to about 250,000 and the preferred sorbant is one having a pore size approximating that of the protein. However, the selection can be affected by the shape of the protein molecule e.g. a smaller pore size can be used with an elliptically shaped protein molecule. A partial listing of peptides and proteins of the type that may be purified by the practice of the present invention and the pore size of the suggested silica gel sorbant appear in Table 1. Protein M.W. Suggested Silica Gel Pore Diameter (Angstroms) Human Epidermal Growth Factor 6,000 25-50 Methionyl Human Growth Hormone 22,000 50 Tissue Plasminogen Activating Factor 64,000 100 Human Gamma Interferon 20,000-25,000 50 Human Interleukin 2 15,000 50 Tumor Necrosis Factor 17,000 50 Streptokinase 47,400 100 Invertase 270,000 200 Bovine Lysozyme 14,400 50 Human Serum Albumin 69,000 100 Human Lysozyme 15,000 50 Superoxide Dismutase 32,600 50 Alcohol Oxidase 148,000 200 A variety of valuable proteins can be removed from complex solutions and recovered in purified form by a relatively simple method employing silica gel sorbants. We have discovered that a recombinant form of a protein present in the body fluids of arctic fish which prevents them from freezing, i.e., Anti-Freeze Protein (AFP), can be sorbed from broths and other solutions onto either DP4660 (a silica cogel containing magnesium) or Britesorb A100 (a silica hydrogel) and selectively desorbed in purified form. Sorption to DP4660 was from either an ultrafiltration concentrate or from the original fermentation broth. Background materials were present in both broth and ultrafiltration concentrate that may influence sorption to, and desorption from, the silica gel. Desorption of the AFP from the cogel DP4660 was achieved with a 50% v/v ethanol eluent, but desorption from the hydrogel Britesorb A100 was achieved with an eluent containing Tris- buffer, pH 8. This is evidence that the sorption methods of the two silica gels may be different. The ability to elute with the ethanol containing eluent indicates that the AFP sorption mechanism with DP4660 is probably due to a hydrophobic interaction. Whereas, elution of the AFP from Britesorb A100 with an eluent that changes the pH is more indicative of an ion-exchange interaction. It is interesting that hydrophobic interaction was indicated for the cogel and ion-exchange interaction for the hydrogel. Some of each type of interaction is probably partially responsible for sorption of AFP with both gels. In another experiment chymosin, a valuable enzyme, was sorbed from an acetate buffer with silica xerogel. Desorption from the xerogel was with an acetate buffer (pH 5.6) eluent containing 25% isopropanol, again indicating that the sorption of chymosin to the xerogel was by a hydrophobic interaction. Sorption and desorption conditions from a fermentation broth could be different because of the influence of background material in the fermentation broth that could also sorb to the silica gel. In still another experiment, insulin, in 0.25M acetic acid, was sorbed to the silica cogel DP4660. Desorption was achieved by using an eluent having a pH of 8 followed by further desorption with an eluent containing urea, a hydrogen-bond breaker. Evidence suggests that both ion-exchange and hydrogen-bonding may play a role in the sorption of insulin to the cogel DP4660. It is possible that sorption and desorption conditions from a complex solution, such as a fermentation broth, could be different because of the influence of background material in the complex solution that would also sorb to the silica gel. To demonstrate the usefulness of the method of the present invention in removing a valuable protein from milk still another experiment was conducted. In this experiment, AFP was mixed with cow's milk to yield a mixture which might be similar to the milk from a transgenic cow producing AFP. The AFP was effectively separated from the casein, whey milk proteins and cream with the silica cogel DP4660. The micellar forms of casein and whey were probably excluded from the cogel pores. The AFP was desorbed from the DP4660 with 50% ethanol. The examples cited above suggest that there probably is no single simple mechanism that is responsible for the sorption of proteins to silica hydrogels, xerogels and cogels. Hydrogen bonding, size-exclusion, hydrophobic and hydrophilic interaction, and ionic and van der Waals interactions all probably play a role. Additionally, the sorption may be influenced by other components in the medium. Additional experiments were done with various proteins of known molecular weight and isoelectric points in a well-defined buffer system. Table 2 lists the protein standards used for the analyses. The molecular weights were provided by the manufacturer. The isoelectric points (pI) were taken from published tables. Aldolase MW 158,000 pI 8.9 (Human) Bovine Serum Albumin MW 67,000 pI 4.98, 5.07, 5.18 (Ox) Ovalbumin MW 43,000 pI 4.6 Chymotrypsinogen A MW 25,000 pI 8.8, 9.2, 9.6 (Beef) Ribonuclease A MW 13,700 pI 8.7, 8.8 (Guinea Pig) Size-exclusion (SE)-HPLC was performed. The mobile phase was pumped at 0.9 mL/min. The mobile phase was pH 5 citrate-phosphate buffer containing 0,17M sodium chloride. The protein standards were individually dissolved in 1 mL aliquots of mobile phase buffer to a concentration of approximately 1 mg/mL. For experiments, aliquots of the protein solutions were mixed. Aldolase, ovalbumin and ribonuclease A were used as a group, and bovine serum albumin and chymotrypsinogen A were used as a second group. Standard curves were prepared for each of the proteins (injected as groups) in the range of approximately 5-15 µg. The amount of aldolase injected was in the range of 11-33 µg because of lower 280 nm absorptivity. The standard mixture was also analyzed at the start of each day that sorption studies were performed to determine an HPLC response factor. Silica gel sorption experiments were performed in 1.5 mL Eppendorf centrifuge tubes. Silica gel was weighed into a tube (0.6 mg to 400 mg). Buffer (less than 1 mL) was added and the tube was mixed on a vortex mixer to wet and disperse the silica gel. Protein solutions (approximately 150 µg each) were then added, increasing the volume to 1 mL. The tubes were placed on a rocking shaker for 20 min. The tubes were then centrifuged for 5 min (14,000 x g). The supernatent was separated, recentrifuged for 2 min and analyzed by HPLC (100 µL injections). The experimental results are summarized in Table 3. Protein / silica hydrogel 0.01g 0.1g 0.4g Aldolase 18% sorb sorb sorb Bovine Serum Albumin 25% sorb sorb sorb Ovalbumin 50% sorb sorb sorb Chymotrypsinogen A 5% sorb 40% sorb 70% sorb Ribonuclease A 14% sorb 70% sorb 80% sorb Protein / silica cogel 0.0008g 0.0014g 0.005g 0.01g 0.2g Aldolase 10% sorb 5% sorb sorb sorb sorb Bovine Serum Albumin 21% sorb 42% sorb sorb sorb sorb Ovalbumin 24% sorb 37% sorb 81% sorb sorb sorb Chymotrypsinogen A 31% sorb 55% sorb sorb sorb sorb Ribonuclease A 22% sorb 32% sorb 81% sorb sorb sorb Protein / silica xerogel 0.0006g 0.001g 0.01g 0.2g Aldolase 16% sorb 35% sorb sorb sorb Bovine Serum Albumin 36% sorb 72% sorb sorb sorb Ovalbumin 38% sorb 63% sorb sorb sorb Chymotrypsinogen A 49% sorb 79% sorb sorb sorb Ribonuclease A 14% sorb 24% sorb 88% sorb sorb The results presented in Table 3 indicate that the proteins examined required higher levels of the silica hydrogel for complete sorption than of the cogel or the xerogel. The results also indicate that the higher molecular weight proteins sorb more strongly to these sorbants than the lower molecular weight proteins, with ribonuclease A being sorbed the least. The current results indicate that the higher molecular weight proteins enter the gel pores and are trapped, but lower molecular weight proteins may enter and then leave the pores. The pore sizes for the silica hydrogel and xerogel are approximately 100 Angstroms each. Proteins for molecular diameters of up to approximately 80 Angstroms (MW 150,000; assuming a globular structure) can be separated by Sephadex G100 (Ref. 7 and 8). Making similar assumptions, proteins of up to a similar molecular weight could be entrapped by the hydrogel or xerogel. The ovalbumin results for sorption to the silica cogel do not fit the pattern of protein entrapment as well as the other proteins and silica hydrogels, but the cogel apparently also contains magnesium. No relationship is obvious between protein sorption and the protein properties of isoelectric point or surface activity which were also analyzed. Both of these properties could play a role if there are secondary sorptions and interactions associated with sorption from complex solutions. The results summarized in Table 3 directly relate to sorption from a simple buffer containing a few well-defined proteins. Substantially higher levels of the silica cogel DP4660 need to be used to quantitatively isolate antifreeze protein from fermentation broths than are used to chillproof beer. As the level of antifreeze protein in the broth increases, the amount of DP4660 used to remove it also has to be increased. Large amounts of DP4660 may also be necessary because of the low molecular weight of the protein (MW < 5,000). Some browning products are coeluted with the protein and need to be separated by a second step in the isolation procedure. The results of the experiments indicate that protein entrapment appears to be the major mechanism of protein sorption to silica hydrogel, silica cogel, and silica xerogel. Proteins of higher molecular weight appear to be more efficiently sorbed than proteins of lower molecular weight. The entrapment conclusions only directly relate to sorption from a simple buffer containing a few well-defined proteins. Additional sorption mechanisms may occur from complex solutions. The complexity of the sorption mechanisms presents an opportunity for selective desorption, as well as a challenge for understanding the mechanism. Many, if not most, of the components in a complex solution, such as a fermentation broth or milk, will not sorb to silica hydrogels, xerogels or cogels. The sorption of other components will be influenced by the composition of the complex solution. Therefore, it is important to have a method such as that previously described for quickly determining the likelihood that a given valuable protein can be removed from a given solution and subsequently recovered in purified form. The methods of the present invention make it possible to recover sorbed components of interest under conditions that are selective enough that most co-sorbed components would not be desorbed. However, even in cases where co-elution cannot be avoided, the valuable protein, or other component of interest can be quickly and inexpensively concentrated and purified to a degree that is difficult to achieve using other technologies. As a result, further purification will have been simplified by use of the method of the present invention. It will be apparent to those skilled in the art that a number of modifications and changes may be made without departing from the spirit and scope of the present invention. As previously stated the terms "sorb" and "sorption" as used herein are intended to describe and include "absorb," "adsorb," "absorption" and "adsorption," as well as, "entrapment" and any other mechanisms by which the protein is bound to the sorbant. In addition, the term "protein" is intended to include other components of interest such as peptides, glycoproteins, and other molecules that can be sorbed and recovered by the practice of the method of the present invention. Therefore, it is intended that the invention not be limited except by the claims.

Claims: A method of removing protein from a solution containing that protein, said method comprising adding to a solution containing at least one protein to be purified an effective amount of a silica hydrogel sorbant, a silica xerogel sorbant or a silica cogel sorbant to sorb at least some of the protein, wherein the pore size of the sorbant is approximately equal to the dimension of the protein to be removed, intimately distributing the sorbant through the solution and permitting the sorbant to remain in the solution until protein has been sorbed thereon, then removing from the solution the sorbant with protein sorbed thereon and treating said sorbant with an eluent which will desorb protein and permit the protein to be separated and recovered. A method of identifying whether a specific protein can be effectively removed from a specific solution containing said protein by treatment with a silica hydrogel sorbant, a silica xerogel sorbant or a silica cogel sorbant, said method comprising adding an effective amount of the sorbant to a sample of the solution containing the protein to be purified to sorb the protein, wherein the pore size of the sorbant is approximately equal to the dimension of the protein to be removed, intimately mixing the sorbant with the solution, allowing the sorbant to remain in the solution long enough for the protein to become sorbed thereon, then removing the sorbant from the solution and treating the sorbant with different eluents to see which, if any, of the eluents desorb protein and allow the protein to be separated and recovered. A method of claim 1 or 2 in which the protein is antifreeze protein. A method according to one of the preceding claims in which the protein is chymosin. A method according to one of the preceding claims in which the protein is insulin. A method according to one of the preceding claims in which the eluent is a hydrophobic solvent. A method according to one of the preceding claims in which the eluent is a solvent that disrupts hydrogen bonds. A method according to one of the preceding claims in which the eluent is a solvent that disrupts ion exchange bonds.

Inventors: GOLDSTEIN HENRY, LUSK LANCE T, GOLDSTEIN, HENRY, LUSK, LANCE T.
Applicants: MILLER BREWING, MILLER BREWING COMPANY
Application year: 1993
Main classification: C07K1
IPC codes: C07K1, C07K14, G01N33, C12N9