CN1504569A - Chromatography purification process of viper venom blood clotting enzyme - Google Patents
Chromatography purification process of viper venom blood clotting enzyme Download PDFInfo
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Abstract
A purification process of venom blood coagulation enzyme for injection comprises, venom dissolution, compatible chromatography segregation to obtain the coarse solution of batroxobin and thrombokinase, hyperconcentration, ion exchange chromatography purification to obtain the pure solution of batroxobin and thrombokinase, hyperconcentration, gel chromatography to obtain the refined pure solution of batroxobin and thrombokinase, mixing the refined pure solution of batroxobin and thrombokinase according to a finite proportion, filling right amount of excipient, stabilizing agent, and filtering, loading, freeze drying, rolling cap, finally obtaining the venom blood coagulation enzyme for injection.
Description
Technical field
The present invention relates to a kind of method of utilizing biochemical means to prepare medicine, refer more particularly to a kind of a kind of enzyme solution of chromatography separation and purification---production technique of snake venom blood coagulation enzyme that adopts with hemostatic function.
Background technology
Reptilase (Reptilase) has another name called Batroxobin (Batroxobin), 1936 by Austrian scholar Klobusitzky first successfully from the venom of Brazilian spearhead pallas pit viper (Bothopsatrox) separation and purification refining and get, it is a kind of zymin based on anastalsis, through the clinical application of many decades, proved that this medical instrument has significant hemostatic function.There are Switzerland, France, Sweden, Japan etc. in the country that produces at present this medicine in the world, and their used raw material is introduced corresponding enzyme purification technology simultaneously all from Brazilian import.The reptilase that China uses (Reptilase) powder pin in 1989 from the import of Switzerland Solco Basle Ltd company, only this item is annual to need millions of dollars of cost.
Walter Kisiel, Mark A.Hermodson and Earl W.Davie equal to filter and strong anion exchanger (QAE-Sephadex A-50) column chromatography with gel (Sephadex G-150) in 1976, separation and purification obtains clauden (Xa factor activator) from adder snake venom (Russell ' s Viper Venom), in the gel electrophoresis of not adding employing 7.5% under the β mercaptoethanol situation, record its full molecular weight and be about 90000 dalton, adopt 10% gel electrophoresis, recording its full molecular weight is 79000 dalton; Adding under the β mercaptoethanol situation, adopt 7.5% gel electrophoresis, record its heavy chain molecule amount and be about 67000 dalton, the light chain molecular weight is about 19000 dalton, adopt 10% gel electrophoresis, record its heavy chain molecule amount and be about 59000 dalton, the light chain molecular weight is about 20000 and 18000 dalton, and this product is not seen listing always.Gel that adopts in this technology and strong anion exchanger are the product of the eighties, because its limitation (flexible glue, flow velocity is slow, the cycle is long, processing is loaded down with trivial details, volume containing the sample is little), are substituted by Bioprocess gel of new generation gradually.
Summary of the invention
In order to address the above problem, the invention provides a kind of production technique of new use purification by chromatography venin for injection hemocoagulase, raw material is the adder snake venom of real estates such as Guangdong, Guangxi, Fujian.This product is made up of two kinds of components: a kind of is the adder Thrombin-like enzyme, a kind of is the adder clauden, and two kinds of enzymes mix the resulting mixed solution in back, every milliliter of hemocoagulase activity that contains a Ke Shi unit by a certain percentage, reptilase medicine composition unanimity with import has equal effect.Experiment showed, that through the animal pharmacodynamics this product has the bleeding time of shortening, reduces blood loss, quickens the hematostatic effect.
The invention provides a kind of chromatography purification method with high resolving power, high carrying capacity, specificity absorption, purifying process is as follows:
(1) with tris-HCl damping fluid or the phosphate buffered saline buffer dissolving of adder snake venom with 0.01～0.1mol/L of pH 7.0～9.0, centrifugal removal precipitation.
(2) carry out affinity chromatography with the high resolving power of two kinds of different ligands, high carrying capacity, narrow spectrum sorbent material, use tris-HCl damping fluid and the NaCl solution linear gradient elution of 0.01～0.05mol/L of pH 7.0～9.0 again, purifying obtains the thick solution of Thrombin-like enzyme and clauden.
(3) the thick solution of ultrafiltration and concentration Thrombin-like enzyme and clauden is put in the refrigerator and is preserved.
(4) the thick solution with gained Thrombin-like enzyme and clauden passes through anion exchange chromatography respectively, and with tris-HCl damping fluid and the NaCl solution linear gradient elution of pH 7.0～9.0, purifying obtains the pure solution of Thrombin-like enzyme and clauden.
(5) the thick solution of ultrafiltration and concentration Thrombin-like enzyme and clauden is put in the refrigerator and is preserved.
(6) the pure solution with gained Thrombin-like enzyme and clauden passes through gel filtration chromatography respectively, with tris-HCl damping fluid (the NaCl solution that the contains 0.15mol/L) wash-out of pH 7.0～9.0, obtains the consummate solution of Thrombin-like enzyme and clauden.
(7) after being mixed by a certain percentage, the consummate solution of gained Thrombin-like enzyme and clauden obtains mixed solution, every milliliter of hemocoagulase activity that contains 1 Ke Shi unit, add again that an amount of vehicle, stablizer filter, can, lyophilize, roll lid, promptly obtain venin for injection hemocoagulase finished product.
In above-mentioned technology, the affinity chromatography sorbent material that the purifying of Thrombin-like enzyme adopts is preferably benzenyl amidine (Benzamidine Sepharose 6B), and the concentration of used damping fluid is 0.01～0.05mol/L, and the gradient of NaCl solution is 0～0.6mol/L; The affinity chromatography sorbent material that the clauden purifying adopts is heparin (Heparin Sepharose CL-6B), and the concentration of used damping fluid is 0.03～0.08mol/L, and the gradient of NaCl solution is 0.1～1.0mol/L.
The advantage of this technology is:
1) this technology so when the first step rough segmentation, can disposablely finish a large amount of enzyme solution apace and slightly obtain through refining work fully, avoids going up repeatedly sample, for next step chromatography has been saved a large amount of time owing to adopt high resolving power, high carrying capacity, specificity sorbent material.
2) this technology is owing to adopt the specificity sorbent material, thus can farthest collect the effective ingredient in the crude product, and the biological activity height.
3) the gained snake venom blood coagulation enzyme is through the animal pharmacodynamic experiment, and the dosage of 0.1～0.2 unit/kg can make rabbit whole blood coagulation time and the preceding reduced in comparison 1/3～1/2 of medication, compares with positive medicine reptilase, and effect is suitable.
4) the gained snake venom blood coagulation enzyme is through the animal pharmacodynamic experiment, 0.1 can making to compare before tame rabbit liver otch blood loss and the medication, the dosage of～0.2 unit/kg reduced 53.84～58.33%, before bleeding time and the medication reduced in comparison 43.5～51.5%, compare with positive medicine reptilase, effect is suitable.
5) the gained snake venom blood coagulation enzyme is measured through hemorrhage poison, and it is subcutaneous that the dosage of 100 units is injected in small white mouse, and small white mouse does not have bleeding.
6) the gained snake venom blood coagulation enzyme is through other several toxin determinations, as phospholipase A
2, alkaline phosphatase, L-amino-acid oxidase etc. determination of activity all negative.Prove thus,
This product can substitute the import reptilase fully, and safe, efficient, cheap.
7) the affinity chromatography sorbent material of this process using can use repeatedly, need not do special processing, when last fresh sample, only needs to get final product with above-mentioned damping fluid balance at every turn.
Embodiment
The following examples will be further explained the present invention, but the present invention is not limited only to these embodiment, the scope that these embodiment do not limit the present invention in any way.Some change that those skilled in the art has done within the scope of the claims and adjust also should be thought and belongs to scope of the present invention.
Embodiment 1
1.1 Thrombin-like enzyme technology
(1) dissolving of thick poison: take by weighing viper venom 5 grams, being dissolved in 30 ml concns is in the tris-HCl damping fluid of 0.02mol/L, pH8.0, puts in 4 refrigerators and spends the night, and dissolving naturally, next day is centrifugal.Centrifugal rotational speed is 4000rpm, and centrifugation time is 10 minutes, and it is stand-by to collect supernatant liquor.
(2) dress post: cut-off directly is one of the glass column of 5.0 * 30cm, with the good benzenyl amidine of the tris-HCl damping fluid balance of 0.02mol/L, pH8.0 (Benzamidine Sepharose 6B) affinity chromatography sorbent material dress post, use the tris-HCl buffer solution elution balance of 0.02mol/L, pH8.0 again.
(3) go up sample, wash-out: the supernatant liquor of getting thick poison dissolving back gained in the step (1) is splined in the step (2) in the Balanced post, carries out linear gradient elution.In the elutriant storage bottle is the tris-HCl damping fluid (including the NaCl solution of 0.6mol/L) of 8000 milliliters of 0.02mol/L, pH8.0, is the tris-HCl damping fluid of 8000 milliliters of 0.02mol/L, pH8.0 in the gradient bottle.Be initiated with slug flow speed, per hour 60 milliliters, detect absorption value at 280nm wavelength place.Last sample changed per hour 300 milliliters into after 5 hours, and elutriant is collected with automatic Fraction Collector, per hour collect 12 pipes, 25 milliliters of every pipes, elution curve contain 6 protein peaks, wherein the 6th peak is the active peak of Thrombin-like enzyme, collects 600 milliliters of Thrombin-like enzyme crude product solution, contains 350 milligrams of protein contents.
(4) ultrafiltration and concentration: the Thrombin-like enzyme crude product solution molecular weight cut-off that step (3) is collected is that 10,000 filter membrane carries out ultrafiltration, and being concentrated into volume is about 100 milliliters, puts preservation in 4 ℃ of refrigerators.
(5) DEAE-Sepharose Fast Flow anion exchange chromatography: the spissated enzyme solution of step (4) is splined on (the pillar diameter is 5.0 * 60cm), carries out the two-way gradient wash-out in the good anion-exchange column of the tris-HCl damping fluid balance of using 0.02mol/L, pH8.2.In the elutriant storage bottle is the tris-HCl damping fluid (including the NaCl solution of 0.5mol/L) of 10000 milliliters of 0.02mol/L, pH6.0, is the tris-HCl damping fluid of 10000 milliliters of 0.02mol/L, pH8.2 in the gradient bottle.Elution flow rate per hour is 480 milliliters, detects absorption value at 280nm wavelength place.Last sample is after 5 hours, and elutriant is collected with automatic Fraction Collector, per hour collects 20 pipes, 24 milliliters of every pipes, and 800 milliliters of the pure product solution of purified acquisition Thrombin-like enzyme contain 180 milligrams of protein contents.
(6) ultrafiltration and concentration: the pure product solution of the Thrombin-like enzyme molecular weight cut-off that step (5) is collected is that 10,000 filter membrane carries out ultrafiltration, and being concentrated into volume is about 50 milliliters, puts preservation in 4 ℃ of refrigerators.
(7) Sephacryl-100HR gel filtration chromatography: the spissated enzyme solution of step (6) is splined on (the pillar diameter is 3.0 * 80cm), carries out chromatography in the good gel column of tris-HCl damping fluid (the including 0.15mol/L NaCl solution) balance of using 0.02mol/L, pH7.6.Flow velocity is per hour 60 milliliters, through being further purified, gets 120 milliliters of consummate Thrombin-like enzyme solution, contains 150 milligrams of protein contents.
(8) purity testing: it is an amount of to get consummate Thrombin-like enzyme solution, and through the SDS-PAGE electrophoresis, recording its molecular weight is 36000 ± 5000, and purity is single component.
1.2 clauden technology
(1) dissolving of thick poison: take by weighing viper venom 5 grams, be dissolved in 30 milliliters of the damping fluids of tris-HCl of 0.05mol/L, pH9.0, put in 4 ℃ of refrigerators and spend the night, dissolve naturally, next day is centrifugal.Rotating speed is 4000rpm when centrifugal, and centrifugation time is 10 minutes, and it is stand-by to collect supernatant liquor.
(2) dress post: cut-off directly is one of the glass column of 5.0 * 30cm, with the good heparin of the tris-HCl damping fluid balance of 0.05mol/L, pH9.0 (Heparin Sepharose CL-6B) affinity chromatography sorbent material dress post, use the tris-HCl buffer solution elution balance of 0.05mol/L, pH9.0 again.
(3) Heparin Sepharose CL-6B affinity chromatography: the supernatant liquor of getting thick poison dissolving back gained in the step (1) is splined in the affinity column that balance is good in the step (2), carries out linear gradient elution.In the elutriant storage bottle is the tris-HCl damping fluid (including the NaCl solution of 0.45mol/L) of 8000 milliliters of 0.05mol/L, pH9.0; It in the gradient bottle tris-HCl damping fluid of 8000 milliliters of 0.05mol/L, pH9.0.Threshold speed is a slug flow speed, per hour 60 milliliters, detects absorption value at 280nm wavelength place.Last sample changed per hour 300 milliliters into after 5 hours.Elutriant is collected with automatic Fraction Collector, per hour collects 12 pipes, 25 milliliters of every pipes.Elution curve contains 7 protein peaks, and wherein the 3rd peak and the 4th peak-to-peak peak valley are active ingredient.Collect 550 milliliters of clauden crude product solution, contain 240 milligrams of protein contents.
(4) ultrafiltration and concentration: with the clauden crude product solution molecular weight cut-off of step (3) is that 10,000 filter membrane carries out ultrafiltration, and being concentrated into volume is about 100 milliliters, puts in 4 ℃ of refrigerators and preserves.
(5) DEAE-Sepharose Fast Flow anion exchange chromatography: the spissated enzyme solution of step (4) is splined on (the pillar diameter is 5.0 * 60cm), carries out linear gradient elution in the good anion-exchange column of the damping fluid balance of the tris-HCl that uses 0.05mol/L, pH8.4.In the elutriant storage bottle is the tris-HCl damping fluid (including the NaCl solution of 0.55mol/L) of 10000 milliliters of 0.05mol/L, pH8.4, is the tris-HCl damping fluid of 10000 milliliters of 0.05mol/L, pH8.4 in the gradient bottle.Flow velocity is per hour 480 milliliters, detects absorption value at 280nm wavelength place.Last sample is after 5 hours, and elutriant is collected with automatic Fraction Collector, per hour collects 20 pipes, 24 milliliters of every pipes.650 milliliters of the pure product solution of purified acquisition clauden, containing protein content is 80 milligrams.
(6) ultrafiltration and concentration: with the pure product solution of the clauden molecular weight cut-off of step (5) is that 10,000 filter membrane carries out ultrafiltration, and being concentrated into volume is about 50 milliliters, puts in 4 ℃ of refrigerators and preserves.
(7) Sephacryl-300HR gel filtration chromatography: (6) spissated enzyme solution is splined on the good gel column of tris-HCl damping fluid (including the NaCl solution of the 0.15mol/L) balance of using 0.02mol/L, pH7.6 is further purified.The pillar diameter is 2.6 * 60cm, and flow velocity is per hour 0.5 milliliter, obtains 80 milliliters of consummate clauden solution, contains 50 milligrams of protein contents.
1.3 the mensuration of congealing activity
The venin for injection hemocoagulase contains two kinds of components: Thrombin-like enzyme and clauden.Thrombin-like enzyme must not be less than 1500IU (international unit) or 1200BU thrombin activity for active every milligram, and clauden must not be less than 150IU (international unit) or 500KU for active every milligram.Two kinds of enzymes mix the solution of back gained by a certain percentage, and every milliliter of hemocoagulase activity that contains 1 Ke Shi unit adds an amount of vehicle, stablizer then, filter, can, lyophilize, roll lid, promptly get venin for injection hemocoagulase finished product.
1.4 pharmacodynamic study
In order to study of the influence of venin for injection hemocoagulase, carried out the animal pharmacodynamics test to inside and outside blood coagulation of animal body and fibrinolytic function.Research unit is the Clinical Researches of New Drugs base of being determined by health ministry-pharmacology teaching and research room of Medical University Of Anhui in 1986.Result of study shows that the venin for injection hemocoagulase can obviously reduce tame rabbit liver otch blood loss, shortens the bleeding time, and can obviously shorten whole blood coagulation time (CT), and concrete parameter sees Table 1:
Table 1: Isodose venin for injection hemocoagulase and reptilase (Reptilase) animal pharmacodynamics relatively
Annotate: with compare before the medication,
*P＜0.05
*P＜0.01
Embodiment 2
2.1 Thrombin-like enzyme technology
Except in step (1) being gets viper venom 5 grams, be dissolved in the phosphate buffered saline buffer China and foreign countries of 0.01mol/L, pH8.5, other working method is identical with embodiment 1, it is used that affinity chromatography sorbent material benzenyl amidine wherein (Benzamidine Sepharose 6B), anionite (DEAE-SepharoseFast Flow) and gel (Sephacryl-100HR) are example 1, through with phosphate buffered saline buffer wash-out balance again, can go up sample.Obtain 550 milliliters of Thrombin-like enzyme solution through separation and purification, contain 275 milligrams of protein contents.
2.2 clauden technology
Except in step (1) being gets viper venom 5 grams, be dissolved in the phosphate buffered saline buffer China and foreign countries of 0.07mol/L, pH8.8, other working method is identical with embodiment 1, wherein to be example 1 used for affinity chromatography sorbent material heparin (Heparin Sepharose CL-6B), anionite (DEAE-Sepharose Fast Flow) and gel (Sephacryl-300HR), through with phosphate buffered saline buffer wash-out balance again, can go up sample.Obtain 520 milliliters of clauden solution through separation and purification, contain 200 milligrams of protein contents.
2.3 congealing activity is measured and the animal pharmacodynamic experiment
This batch used the enzyme solution of phosphate buffered saline buffer purifying, measures and the animal pharmacodynamic experiment all meets the quality standard of clinical application through congealing activity.
Claims (8)
1. the chromatography purification method of a venin for injection hemocoagulase, its step comprises:
(1) the adder snake venom is dissolved centrifugal removal precipitation with damping fluid;
(2) carry out affinity chromatography with the high resolving power of two kinds of different ligands, high carrying capacity, narrow spectrum sorbent material, use tris-HCl damping fluid and the NaCl solution linear gradient elution of 0.01～0.05mol/L of pH 7.0～9.0 again, purifying obtains the thick solution of Thrombin-like enzyme and clauden;
(3) the thick solution of concentrated Thrombin-like enzyme and clauden is put in the refrigerator and is preserved;
(4) the thick solution with gained Thrombin-like enzyme and clauden passes through anion exchange chromatography respectively, and with tris-HCl damping fluid and the NaCl solution linear gradient elution of pH 7.0～9.0, purifying obtains the pure solution of Thrombin-like enzyme and clauden;
(5) the pure solution of concentrated Thrombin-like enzyme and clauden is put in the refrigerator and is preserved;
(6) the pure solution with gained Thrombin-like enzyme and clauden passes through gel filtration chromatography respectively, with the tris-HCl buffer solution elution of pH 7.0～9.0, obtains the consummate solution of Thrombin-like enzyme and clauden;
(7) after being mixed by a certain percentage, the consummate solution of gained Thrombin-like enzyme and clauden obtains mixed solution, every milliliter of hemocoagulase activity that contains 1 Ke Shi unit, add again that an amount of vehicle, stablizer filter, can, lyophilize, roll lid, promptly obtain venin for injection hemocoagulase finished product.
2. the chromatography purification method of snake venom blood coagulation enzyme according to claim 1 is characterized in that the described damping fluid of step (1) is that pH 7.0～9.0, concentration are tris-HCl damping fluid or the phosphate buffered saline buffer of 0.01～0.1mol/L.
3. the chromatography purification method of snake venom blood coagulation enzyme according to claim 1, it is characterized in that in the described affinity chromatography operation of step (2), the sorbent material that the purifying Thrombin-like enzyme adopts is benzenyl amidine (Benzamidine Sepharose 6B), the concentration of used damping fluid is 0.01～0.05mol/L, and the gradient of NaCl solution is 0～0.6mol/L; The sorbent material that the purifying clauden adopts is heparin (Heparin Sepharose CL-6B), and the concentration of used damping fluid is 0.03～0.08mol/L, and the gradient of NaCl solution is 0.1～1.0mol/L.
4. the chromatography purification method of snake venom blood coagulation enzyme according to claim 1 is characterized in that the concentration method that step (3) or step (5) are adopted is ultrafiltration.
5. the chromatography purification method of snake venom blood coagulation enzyme according to claim 4 is characterized in that the molecular weight cut-off of the filter membrane that described ultrafiltration is used is 10,000.
6. the chromatography purification method of snake venom blood coagulation enzyme according to claim 1 is characterized in that the exchanger that the described anion exchange chromatography of step (4) adopts is DEAE-Sepharose Fast Flow.
7. the chromatography purification method of snake venom blood coagulation enzyme according to claim 1, what it is characterized in that the described Thrombin-like enzyme wash-out of step (4) operation adopts is the two-way gradient wash-out, i.e. pH of buffer gradient and NaCl linear gradient.
8. the chromatography purification method of snake venom blood coagulation enzyme according to claim 1 is characterized in that containing the NaCl that concentration is 0.15mol/L in the described tris-HCl damping fluid of step (6).
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| CN100355885C (en) * | 2006-01-18 | 2007-12-19 | 齐鲁制药有限公司 | Method for extracting single ingredient defibrase from snake venom |
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| CX01 | Expiry of patent term |