A PROCESS FOR THE PURIFICATION OF TPA

Abstract: Tissue plasminogen activator (tPA) species having a molecular weight of about 70,000 daltons is isolated in a purified form from a crude tPA preparation containing various tPA species having different molecular weights, by bringing the crude tPA preparation into contact with a cation exchanger. The desired tPA species is selectively separated from the cation exchanger by means of a salt gradient elution method.

Description: This invention relates to a process for the purification of tissue plasminogen activator (tPA). More particularly, it relates to a process for the purification of tPA which comprises bringing a crude tPA preparation containing various tPA species of different molecular weights into contact with a cation exchanger in advance and separating tPA having a molecular weight of about 70,000 daltons selectively from the cation exchanger by means of the salt gradient elution method. No practical processes have yet been known to refine tPA having a desired molecular weight from a culture medium which has cultured tPA-producing cells and thus contained a crude tPA preparation with various tPA species of different molecular weights. As processes to separate proteins having different molecular weights, it has been known that the gel-filtration process is generally applicable and that cation exchangers are used for the purification of tPA (Japanese Patent Laid-Open No. 174727/1985). However, no purification processes have been known at all, which purify and prepare a tPA species of a desired molecular weight by removing other tPA species than that having the particular molecular weight, for example, about 70,000 daltons as in the process of the present invention. An object of the present invention is to prepare tPA having a molecular weight of about 70,000 daltons selectively from proteins which react with an anti-human tPA antibody and have different molecular weights. When tPA-producing cells are cultured to obtain tPA, the resulting culture both contains, as proteins reactive with an anti-human tPA antibody, various tPA species including tPA species having molecular weights of from 30,000 to 45,000 daltons, tPA species having molecular weights of from 50,000 to 80,000 daltons and tPA species having a molecular weight of 100,000 daltons or higher. The present invention provides a process for isolating and purifying tPA with a molecular weight of about 70,000 daltons from a solution containing those various tPA species of different molecular weights and other proteinaceous impurities. The present inventors have studied the reaction between tPA species of different molecular weights and a cation exchanger with a view to solving the above problems. As a result, it was found that the tPA species of different molecular weights had individually different binding strengths to the cation exchanger. Utilization of this property has led to completion of a process for preparing tPA with a molecular weight of about 70,000 daltons from various tPA species of different molecular weights. Namely, the above object has been accomplished by a purification process of tPA which (a) comprises bringing a crude tPA preparation containing, as impurities, proteins which react with an anti-human tPA antibody and have molecular weights other than about 70,000 daltons into intimate contact with a cation exchanger in advance and (b) separating tPA having a molecular weight of about 70,000 daltons selectively from the cation exchanger by means of a salt gradient elution method. According to one aspect of the present invention, there is provided a process for purifying tPA comprising the steps of: (a) contacting a carboxymethyl agarose exchange resin with a crude tPA preparation containing tPA having a molecular weight of about 70,000 daltons, together with impure tPA species including active degradated products of tPA, polymers of tPA, and complexes of tPA with other proteins, said impure tPA species having molecular weights other than about 70,000 daltons and capable of reacting with an anti-human tPA antibody: (b) treating said exchange resin with an eluant having a salt concentration of less than 0.15M and a pH in the range of 6.0 - 6.4 to elute the impure tPA species having molecular weights of less than about 70,000 daltons; and thereafter (c) treating said exchange resin with an eluant having a salt concentration in the range of 0.175 - 0.375M and a pH in the range of 6.0 - 6.4 to elute the tPA having a molecular weight of about 70,000 daltons and recovering the resultant eluate. According to another aspect of the invention there is provided a process for purifying tPA comprising the steps of: (a) contacting a carboxymethyl acrylamide copolymer exchange resin with a crude tPA preparation containing tPA having a molecular weight of about 70,000 daltons, together with impure tPA species including active degradated products of tPA, polymers of tPA, and complexes of tPA with other proteins, said impure tPA species having molecular weights other than about 70,000 daltons and capable of reacting with an anti-human tPA antibody: (b) treating said exchange resin with an eluant having a salt concentration of at most 0.075M and a pH in the range of 6.0 - 6.4 to elute the impure tPA species having molecular weights of less than about 70,000 daltons; and thereafter (c) treating said exchange resin with an eluant having a salt concentration of 150mM - 200mM, and a pH in the range of 6.0 - 6.4 to elute said tPA having a molecular weight of about 70,000 daltons and recovering the resulting eluate. The following description, which is given by way of example only, explains in more detail the preferred manner of practising the present invention. In the process of the present invention, tissue plasminogen activator (tPA) is produced in the tissue of a higher animal, and is a protein which activates plasminogen, a precursor of plasmin which is a proteolytic enzyme specific to fibrin. When tPA-producing cells are cultured to obtain tPA, the culture medium contains various tPA species of different molecular weights such as those having molecular weights of from 30,000 to 45,000 daltons, those having molecular weights of from 50,000 to 80,000 daltons and that having a molecular weight of 100,000 daltons or higher as proteins reactive with an anti-human tPA antibody. These tPA species include tPA, active degradated products of tPA, polymers of tPA, complexes of tPA and other protein and the like. The culture medium containing the tPA to be purified according to the process of the present invention may include a culture medium of human melanoma cells, culture medium of normal human cells and culture medium of cells carrying the human tPA gene integrated according to the DNA recombinant technique. Culture media formed by partially refining the aforesaid media may also be used. The cation exchanger useful in the practice of the process of the present invention comprises carboxymethyl groups,while the carrier may include agarose or polyacrylamide granules and also a combination thereof. In the process of the present invention, a solution containing various tPA species of different molecular weights and other proteinaceous impurities is first adjusted to be weakly acidic for the purpose of allowing them to be adsorbed onto a cation exchanger. The cation exchanger brought into contact with the solution adsorbs practically all of the tPA species of different molecular weights. After washing the cation exchanger as required, tPA of about 70,000 daltons in molecular weight is allowed to elute selectively at a pH in a specific pH range by means of what is called the salt gradient elution method, in which elution is effected by varying the salt concentration of an eluent that has a pH in the range of 6.0 - 6.4, so that the desired tPA can be separated and purified. Sodium chloride, potassium chloride, sodium phosphate and potassium phosphate are generally used as the salt in most cases. However, the salt to be used is not particularly limited to these compounds. Further, as regards the concentration of the salt, a range of concentration, at which tPA can be eluted, should be applied in accordance with the kind of the functional group of the cation exchanger to be used and the kind of resin. Further, the applicable salt gradient elution method may include, for example, the linear gradient or stepwise method. The invention is now set out in more detail in the following non-limitative Examples. Example 1 : After culturing Bowes melanoma cells (ATCC CRL1424 G361) in RPMI-1640 culture medium supplemented with 10% of thermoinactivated (56°C, 30 minutes) fetal calf serum, the cultured cells were washed once. The washed cells were then cultured for 24 hours in a serum-free medium and the resultant culture supernatant was collected. Phosphoric acid was added to 2 ℓ of the culture supernatant. The collected supernatant was adjusted at a pH of 5.0 by adding phosphoric acid to 2 ℓ of the supernatant, and then allowed to pass through a column containing 10 ml of CM-Sepharose (Pharmacia AB) equilibrated with a 0.05 M sodium dihydrogenphosphate solution (pH 5.0) containing 0.15 M of sodium chloride. The column effluent was collected and its plasminogen-dependent fibrinolytic activity was measured. No activity was however detected. After the whole culture supernatant had been passed through the column, the column was washed with a 25 mM phosphate buffer (pH 6.4) containing 0.1 M of sodium chloride. About 5% of the activity charged into the column was detected in the resulting solution. This solution was subjected to electrophoresis in an SDS polyacrylamide gel and was then analyzed by a zymography. A band corresponding to about 30,000 daltons in molecular weight was observed on the zymograph. The adsorbed proteins were eluted with a 25 mM phosphate buffer (pH 6.0) by varying its sodium chloride concentration from 0.1 M to 0.6 M by means of the linear gradient method. The eluate thus obtained exhibited a single band corresponding to a molecular weight of about 70,000 daltons on the zymograph in the range of 0.2 M - 0.35 M in sodium chloride concentration. About 70% of the activity charged into the column was found to be recovered as the activity of this fraction. Example 2 : Through a column containing 50 ml of an anti-human tPA antibody was passed 2 ℓ of a culture supernatant prepared from the culture of Chinese hamster ovary (CHO) cells with human tPA gene integrated therein (Dr. Chasin, Department of Biological Science, Columbia University) in a medium containing 10% of thermoinactivated (56°C, 30 minutes) fetal calf serum and 40 KIU/ml of aprotinin. The column was washed with a 0.05 M phosphate buffer (pH 7.5) containing 1.0 M sodium chloride and then the adsorbed proteins were eluted with a 0.1 M glycine-HCl buffer (pH 3.5) containing 2.0 M of ammonium thiocyanate. The eluate was collected and its plasminogen-dependent fibrinolytic activity was measured. It was found to be about 95% of the activity charged into the column. This eluted fraction was analyzed by a zymography after subjecting same to electrophoresis in an SDS polyacrylamide gel. Bands were observed in the range corresponding to 30,000 - 150,000 daltons in molecular weight on the zymograph. This solution was added with ammonium sulfate at a rate of 300 g/l, adjusted in pH at 7.0 and allowed to stand at 4°C overnight. The resulting precipitate was collected by centrifugation and dialyzed against a 0.05 M phosphate buffer (pH 6.0). This dialyzed solution was passed through a column containing CM-trisacryl M (LKB Co.) equilibrated with a 0.05 phosphate buffer (pH 6.0). The column was washed with the same buffer as used in the equilibration and the plasminogen-dependent fibrinolytic activity of the effluent was measured. About 5% of the activity charged into the column was found to be recovered and bands were observed in the range corresponding to about 30,000 - 60,000 daltons in molecular weight on a zymograph. The adsorbed proteins were eluted with a 0.05 M phosphate buffer (pH 6.0) containing 0.15 M of sodium chloride. The eluate exhibited an activity about 85% of the activity charged into the column. A band corresponding to about 70,000 daltons in molecular weight was recognized on a zymograph. Example 3 : Two liters of a culture supernatant prepared from the culture of mouse fibroblast cells (Mouse C1271 ATCC CRL 1616) transformed by the human tPA gene in a culture medium containing 2% of thermoinactivated (56°C, 30 minutes) fetal calf serum and 40 KIU/ml of aprotinin were adjusted in pH at 4.5 with phosphoric acid and then passed through a column containing 10 ml of carboxymethyl (CM) Sepharose (Pharmacia AB) equilibrated with 0.05 M sodium dihydrogenphosphate solution (pH 4.5) containing 0.15 M of sodium chloride. The resin containing the proteins adsorbed was washed with a 25 mM phosphate buffer (pH 6.4) containing 50 mM of sodium chloride and thereafter the proteins were eluted with a 50 mM phosphate buffer (pH 6.4) containing 0.5 M of sodium chloride. The plasminogen-dependent fibrinolytic activity of the eluate was measured. It was found to be about 90% of the activity charged into the column. This eluted fraction was subjected to electrophoresis in an SDS polyacrylamide gel and then analyzed by a zymography. Bands were observed as those of tPA in the range corresponding to 30,000 - 15,000 daltons in molecular weight on the zymograph. This fraction was diluted tenfold with a 25 mM phosphate buffer (pH 6.0) and adjusted at a pH of 6.0. The resulting solution was allowed to flow through a column containing CM-trisacryl M equilibrated with a 25 mM phosphate buffer (pH 6.) containing 0.05 M of sodium chloride. The column was washed with the same buffer as used for the equilibration and the plasminogen-dependent fibrinolytic activity of the effluent was measured. About 5% of the activity charged into the column was found to be recovered and bands were observed in the range corresponding to about 30,000 - 60,000 daltons in molecular weight on a zymograph. The proteins adsorbed were eluted with a 0.05 M phosphate buffer (pH 6.4) containing 0.1 M of sodium chloride. The activity of the eluate was about 85% of the activity charged into the column. tPA contained in this fraction was confirmed as a band corresponding to about 70,000 daltons in molecular weight on a zymgraph. Example 4 : Ammonium sulfate was added at a rate of 300 g/ℓ to 2 ℓ of a culture supernatant prepared from the culture of human fetal amniotic cells (FL ATCC CCL-62) carrying the human tPA gene associated with human cytomegalovirus (HCMV) as a promoter for human tPA expression in a culture medium containing 2% of thermoinactivated (56°C, 30 minutes) fetal calf serum and 20 KIU/ml of aprotinin. The resulting solution was adjusted at a pH of 7.0 and then allowed to stand at 4°C overnight. The thus-formed precipitate was collected by centrifugation and dissolved in a 0.04 M phosphate buffer (pH 7.5), followed by dialysis against this buffer for desalting. This solution was allowed to pass through a column containing 10 ml of hydroxyapatite equilibrated with a 0.04 M phosphate buffer (pH 7.5). After the whole solution had been passed through the column, the column was washed with the same buffer as used in the equilibration. Measurement of the plasminogen-dependent fibrinolytic activity of the effluent revealed that it was about 5% of the activity charged into the column. This fraction was subjected to electrophoresis in an SDS polyacrylamide gel and analyzed by a zymography. This effluent exhibited bands in the range corresponding to about 30,000 and 60,000 daltons in molecular weight on the zymograph. The proteins adsorbed was eluted with a 0.3 M phosphate buffer (pH 6.0). The eluate exhibited an activity about 85% of the activity charged into the column, and bands corresponding to about 70,000 daltons and 100,000 daltons or higher in molecular weight were observed on a zymograph. This fraction was diluted sixfold with water and adjusted in pH at 5.5 with phosphoric acid. The resulting solution was passed through a column of CM-Sepharose equilibrated with a 0.05 M phosphate buffer (pH 5.5). After the whole solution had been passed through the column, the adsorbed proteins were eluted with a 25 mM phosphate buffer (pH 6.4) containing 0.15 M of sodium chloride. The recovered activity of the eluate was about 80% of the activity charged into the column. A band corresponding to a molecular weight of about 70,000 daltons was recognized on a zymograph. The remaining adsorbed proteins were eluted with a 25 mM phosphate buffer (pH 6.4) containing 0.5 M of sodium chloride. The eluate exhibited a tPA activity about 15% of the total activity charged into the column. It gave bands corresponding to molecular weights of 70,000 daltons and 100,000 daltons or higher on a zymograph. Example 5 : Ammonium sulfate was added at a rate of 300 g/ℓ to 2 ℓ of a culture supernatant prepared from the culture of mouse myeloma cells (P3 x 63 Ag8 ATCC TIB-9) carrying the human tPA gene associated with immunoglobulin G as a promoter for human tPA expression in a culture medium containing 2% of thermoinactivated (56°C, 30 minutes) fetal calf cerum and 20 KIU/ml of approtinin. The resulting solution was adjusted at a pH of 7.0 and allowed to stand at 4°C overnight. The resulting precipitate was collected by centrifugation and dissolved in 25 mM Tris-HCl buffer (pH 8.0), followed by dialysis against the buffer for desalting. The solution was allowed to flow through a column of DEAE-Sepharose (Pharmacia AB) equilibrated with a 25 mM Tris-HCl buffer (pH 8.0). After the whole solution had been passed through the column, the column was washed with the same buffer as used in the equilibration. The plasminogen-dependent fibrinolytic activity of the effluent and eluate was about 5% of the activity charged into the column. The absorbed proteins were eluted with a 25 mM Tris-HCl buffer (pH 8.0) containing 0.3 M of sodium chloride. The activity of the eluate was about 90% of the activity charged into the column. The eluate was subjected to electrophoresis in an SDS acrylamide gel and analyzed by a zymogaphy. Bands as tPA were observed in the range corresponding to about 30,000 - 150,000 daltons in molecular weight on the zymograph. This fraction was adjusted in pH at 6.0 and diluted threefold with a 25 mM phosphate buffer (pH 6.0). The resulting solution was passed through a column of CM-Sepharose (Pharmacia AB) equilibrated with a 25 mM phosphate buffer (pH 6.0) containing 0.10 M of sodium chloride. After the whole solution had been passed through the column, the column was washed with a 25 mM phosphate buffer (pH 6.0) containing 0.1 M of sodium chloride. In this way, about 5% of the activity charged into the column was detected. The effluent and eluate were subjected to electrophoresis in an SDS-polyacrylamide gel and analyzed by a zymography. Bands were observed in the range corresponding to about 30,000 - 60,000 daltons in molecular weight on the zymograph. The adsorbed proteins were eluted with a 25 mM phosphate buffer (pH 6.0) containing 0.3 M of sodium chloride. The activity of the eluate was about 80% of the activity charged into the column. A single band corresponding to about 70,000 daltons in molecular weight was observed on the zymograph. Subsequently, the column was subjected to elution with a 25 mM phosphate buffer (pH 6.0) containing 0.6 M of sodium chloride. Then, it was found that about 15% of the activity charged into the column was recovered and bands corresponding to 70,000 daltons and 100,000 daltons or higher in molecular weight were observed on a zymograph. Example 6 : Host yeast cells transformed with the human tPA gene therein were allowed to grow in a standard yeast culture medium to which was applied generally the method described in Principles and Practice of Recombinant DNA Research with Yeast in the Molecular Biology of Yeast Saccharomyces: Metabolism and Gene Expression, pp. 603 - 636, Cold Spring Harbor Laboratory, Cold Spring Harbor, NY (1982). The resultant cells were ground with glass beads. tPA was extracted with a 0.04 M phosphate buffer (pH 7.5) containing 0.02% of Tween 80 and 20 KIU/ml of aprotinin. The extract was centrifuged to obtain a supernatant. From this supernatant, tPA was recovered in the same manner as in Example 1. The recovery rate of the tPA was about 60% and its molecular weight was about 70,000 daltons.

Claims: A process for purifying tPA comprising the steps of: (a) contacting a carboxymethyl agarose exchange resin with a crude tPA preparation containing tPA having a molecular weight of about 70,000 daltons, together with impure tPA species including active degradated products of tPA, polymers of tPA, and complexes of tPA with other proteins, said impure tPA species having molecular weights other than about 70,000 daltons and capable of reacting with an anti-human tPA antibody: (b) treating said exchange resin with an eluant having a salt concentration of less than 0.15M and a pH in the range of 6.0 - 6.4 to elute the impure tPA species having molecular weights of less than about 70,000 daltons; and thereafter (c) treating said exchange resin with an eluant having a salt concentration in the range of 0.175 - 0.375M and a pH in the range of 6.0 - 6.4 to elute the tPA having a molecular weight of about 70,000 daltons and recovering the resultant eluate. A process for purifying tPA comprising the steps of: (a) contacting a carboxymethyl acrylamide copolymer exchange resin with a crude tPA preparation containing tPA having a molecular weight of about 70,000 daltons, together with impure tPA species including active degradated products of tPA, polymers of tPA, and complexes of tPA with other proteins, said impure tPA species having molecular weights other than about 70,000 daltons and capable of reacting with an anti-human tPA antibody: (b) treating said exchange resin with an eluant having a salt concentration of at most 0.075M and a pH in the range of 6.0 - 6.4 to elute the impure tPA species having molecular weights of less than about 70,000 daltons; and thereafter (c) treating said exchange resin with an eluant having a salt concentration of 150mM - 200mM, and a pH in the range of 6.0 - 6.4 to elute said tPA having a molecular weight of about 70,000 daltons and recovering the resulting eluate.

Inventors: KAWASHIMA, NOBUHIRO, MORI, KUNIZOU MITSUI TOATSU IIJIMA APAATO 4-43, MORII, MITSUYOSHI, MORII, NORIKO MITSUI TOATSU APAATO 2-4-5, OHOKA, MASAHARU, SUZUKI, KATSUYUKI, SUZUKI, TOSHIHIKO
Applicants: MITSUI TOATSU CHEMICALS, INC.
Application year: 1987
Main classification: C07K3
IPC codes: C12N9, C07K1, C07K16