CN106754839A - A kind of preparation method of human urinary kallidinogenase crude product - Google Patents

A kind of preparation method of human urinary kallidinogenase crude product Download PDF

Info

Publication number
CN106754839A
CN106754839A CN201611101691.XA CN201611101691A CN106754839A CN 106754839 A CN106754839 A CN 106754839A CN 201611101691 A CN201611101691 A CN 201611101691A CN 106754839 A CN106754839 A CN 106754839A
Authority
CN
China
Prior art keywords
crude product
human urinary
urinary kallidinogenase
preparation
human
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201611101691.XA
Other languages
Chinese (zh)
Inventor
王旭
章华
何建国
曾永峰
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
GUANGDONG TIANPU BIOCHEMICAL MEDICINE CO Ltd
Guangdong Techpool Bio Pharma Co Ltd
Original Assignee
GUANGDONG TIANPU BIOCHEMICAL MEDICINE CO Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by GUANGDONG TIANPU BIOCHEMICAL MEDICINE CO Ltd filed Critical GUANGDONG TIANPU BIOCHEMICAL MEDICINE CO Ltd
Priority to CN201611101691.XA priority Critical patent/CN106754839A/en
Publication of CN106754839A publication Critical patent/CN106754839A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12NMICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N9/00Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
    • C12N9/14Hydrolases (3)
    • C12N9/48Hydrolases (3) acting on peptide bonds (3.4)
    • C12N9/50Proteinases, e.g. Endopeptidases (3.4.21-3.4.25)
    • C12N9/64Proteinases, e.g. Endopeptidases (3.4.21-3.4.25) derived from animal tissue
    • C12N9/6421Proteinases, e.g. Endopeptidases (3.4.21-3.4.25) derived from animal tissue from mammals
    • C12N9/6424Serine endopeptidases (3.4.21)
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12YENZYMES
    • C12Y304/00Hydrolases acting on peptide bonds, i.e. peptidases (3.4)
    • C12Y304/21Serine endopeptidases (3.4.21)
    • C12Y304/21008Kallikrein (3.4.21.8)

Landscapes

  • Health & Medical Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Zoology (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Genetics & Genomics (AREA)
  • Wood Science & Technology (AREA)
  • Biochemistry (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Biomedical Technology (AREA)
  • Molecular Biology (AREA)
  • Biotechnology (AREA)
  • Microbiology (AREA)
  • Medicinal Chemistry (AREA)
  • Enzymes And Modification Thereof (AREA)

Abstract

The present invention provides a kind of preparation method of human urinary kallidinogenase crude product, comprises the following steps:Adsorbent is collected, wash-out collects Urine proteins eluting peak;It is concentrated by ultrafiltration, regulation pH is 4~5.8, and electrical conductivity is 20~70mS/cm, obtains concentrate;Loading metal chelate affinity chromatography post, equilibrium liquid rinses metal chelate affinity chromatography post, is then eluted using water as eluent, collects human urokinase-type peptidase eluting peak;Ammonium sulfate is slowly added to, is stirred, stood, collect precipitation, obtain human urinary kallidinogenase crude product.The invention belongs to technical field of chromatography separation, the present invention improves human urinary kallidinogenase crude product yield, reduces production cost, and the human urinary kallidinogenase crude product good product quality of acquisition, KN is higher than work.

Description

A kind of preparation method of human urinary kallidinogenase crude product
Technical field
The invention belongs to technical field of chromatography separation, more particularly to a kind of preparation method of human urinary kallidinogenase crude product.
Background technology
Human urokinase-type peptidase (Urinary Kallidinogenase, KN), be from human urine separation and Extraction by 238 The glycoprotein of amino acid composition, isoelectric point is in 4 or so, molecular weight about 54000D.Human urokinase-type peptidase can activate human plasma and swash Peptide former is converted into kassinin kinin, so as to exercise a series of physiological functions, for example, playing expansion capillary, relax vascular smooth muscle, changes Kind microcirculation, increases the effect such as CBF, anti-freezing, thrombus dissolving, and polarity cerebral infarction is waited indefinitely with significant curative effect.
Human urine trypsin inhibitor (Urinary trypsininhibitor, UTI) is isolated and purified from human urine The glycoprotein being made up of 143 amino acid, 2 or so, molecular weight about 65000D, human urine trypsin inhibitor has isoelectric point Suppress the activity of the enzymes such as multiple protein enzyme, carbohydrase and lipase, so as to suppress the excessive release of inflammatory mediator, suppress systemic inflammatory Reaction, improves microcirculation and perfused tissue, plays the effects such as protection internal organs.
The main production stage of Urine proteins product includes:Urine egg is prepared by steps such as the absorption of Urine proteins, wash-out, precipitations White semifinished product, then Urine proteins semifinished product process is refined, obtains Urine proteins highly finished product.Adsorbent, eluent, equilibrium liquid etc. all can Yield and purity on Urine proteins semifinished product produce influence.
Chinese patent application CN102660525 discloses a kind of method for preparing human urinary kallidinogenase crude product, including such as Lower step:Using anion exchange resin as adsorbent, after collecting the Urine proteins in urine, the NaCl of 0.5-1.0M is used Solution carries out concentration wash-out, and eluent loading metal chelate affinity chromatography is lived, and metal chelate affinity chromatography column equilibration liquid is 0.01-0.2M phosphate buffers, NaCl concentration is 0-2M, pH6.0-9.0, uses the 0.01-0.2M of pH4.5-2.8 Acetic acid-sodium acetate solution as wash-out solution, so as to realize the separation of KN and UTI.With it, can quick adsorption KN simultaneously Central system, improves the advantage of the stability of KN, but the method is in anion exchange resin and metal chelate affinity chromatography post KN yields during wash-out are all relatively low, are unfavorable for industrialized production.
Chinese patent application CN105754977 discloses a kind of method for preparing human urinary kallidinogenase crude product, including such as Lower step:Using anion exchange resin as adsorbent adsorbing urine protein, eluted with NaCl solution, collected eluent;Will Eluent is concentrated by ultrafiltration, and the pH value that regulation is concentrated by ultrafiltration liquid is 3.2-4.2, and conductance is 0.05-8Ms/cm, then loading is The cationic ion-exchange resin balanced with equilibrium liquid, rinses, and equilibrium liquid is the Acetic acid-sodium acetate buffer solution of 0.01-0.5mol/L, Conductance is 0.05-8Ms/cm, and pH value is 3.2-4.2, with elution, collects eluent, and 65% sulphur is added in eluent Sour ammonium powder stirring, collects precipitation, obtains human urinary kallidinogenase crude product.KN yield of the method when resin anion (R.A.) is eluted compared with It is low, it is unfavorable for industrialized production.
Therefore, the preparation method tool of simple to operate, high income, purity human urinary kallidinogenase crude product higher is researched and developed There is important industrialization meaning.
The content of the invention
To solve there are problems that yield is dissatisfactory in the prior art, the present invention provides human urinary kallidinogenase crude product Preparation method, is optimized to anion exchange resin, the eluent of metal chelate affinity chromatography post and equilibrium liquid etc., improves Human urinary kallidinogenase crude product yield, reduces production cost, the human urinary kallidinogenase crude product good product quality of acquisition, KN It is higher than work.
The present invention provides a kind of preparation method of human urinary kallidinogenase crude product, comprises the following steps:
S1 collects the adsorbent after adsorbing urine protein, and wash-out collects Urine proteins eluting peak;
The Urine proteins eluting peak that S2 obtains step S1 is concentrated by ultrafiltration, regulation pH be 4~5.8, electrical conductivity be 20~ 70mS/cm, obtains concentrate;
The concentrate loading metal chelate affinity chromatography post that S3 obtains step S2, equilibrium liquid rinses the affine layer of metal-chelating Analysis post, is then eluted using water as eluent, collects human urokinase-type peptidase eluting peak;The equilibrium liquid by 0.5~ The phosphate buffer of 2mol/L and the acetum of 0.01~0.1mol/L are with 3~5:1 volume ratio composition, the pH of equilibrium liquid It is 4~5.8;
Ammonium sulfate is slowly added in the human urokinase-type peptidase eluting peak that S4 is obtained to step S3, is stirred, stood, collect heavy Form sediment, obtain human urinary kallidinogenase crude product.
Using above-mentioned technical proposal, it is possible to achieve efficiently collect and KN and UTI is efficiently separated, improve human urine kassinin kinin Protoenzyme semifinished product yield, reduces production cost, and the semifinished product good product quality of acquisition, KN is higher than work.
Preferably, in the step S2, regulation pH is 4.5~5.5, and electrical conductivity is 25~60mS/cm.
Preferably, in the step S3, equilibrium liquid by the phosphate buffer of 0.8~1.2mol/L and 0.03~ The acetum of 0.5mol/L is with 3~4:1 volume ratio composition, the pH of equilibrium liquid is 4.2~5.0.
Preferably, in the step S3, equilibrium liquid by 1.0~1.2mol/L phosphate buffer and 0.1~0.3mol/ The acetum of L is with 4:1 volume ratio composition, the pH of equilibrium liquid is 4.4~4.8, and electrical conductivity is 40~55mS/cm.
Preferably, in the step S1, adsorbent is anion exchange resin.It is highly preferred that anion exchange resin is Strong basic type anion-exchange resin, such as:Macroporous type strong anion exchange resin, strong base anion exchange column Q Sepharose H.p、Q Sepharose F.F、Q Sepharose 4F.F、Q Sepharose XL、QAE Sephadex A-25、QAE Sephadex A-50 or STREAMLINE.The macroporous type strong anion exchange resin CAS is 9037-24-5.
Preferably, in the step S1, eluent is the phosphate buffer of 0.3~2mol/L, and pH is 4~6, NaCl's Concentration is 0.01~0.45mol/L.
Preferably, the metal ion of the metal chelate affinity chromatography post is Cu2+、Zn2+Or Ni2+
Preferably, the metal ion of the metal chelate affinity chromatography post is Cu2+
Compared with prior art, the beneficial effects of the invention are as follows:By the present invention in that with 0.3~2mol/L that pH is 4~6 Phosphate buffer as anion exchange resin eluent, it is possible to achieve KN from the abundant wash-out in adsorbent, wash-out Yield is improved;By using the phosphate buffer of 0.5~2mol/L and the acetum of 0.01~0.1mol/L with 3~5:1 Volume ratio constitute metal chelate affinity chromatography post equilibrium liquid, water is used as eluent, it is possible to achieve KN and UTI efficiently point From, human urinary kallidinogenase crude product yield is improve, KN and UTI subsequently refined difficulty is greatly reduced, reduce and be produced into This, the human urinary kallidinogenase crude product good product quality of acquisition, KN is higher than work.
Brief description of the drawings
The HPLC of the human urokinase-type peptidase eluting peak in Fig. 1 embodiment of the present invention one through affinity chromatography schemes.
Specific embodiment
The present invention is described in further details with reference to the accompanying drawings and examples.
The preparation of the human urinary kallidinogenase crude product of embodiment one
The preparation method of human urinary kallidinogenase crude product comprises the following steps:Collect the moon after adsorbing urine protein and water flushing Ion exchange column Q Sepharose F.F 100kg, wash-out, eluent is the phosphate buffer of 0.5mol/L that pH is 4.5, The concentration of NaCl is 0.3mol/L, collects Urine proteins eluting peak;The Urine proteins eluting peak that will be obtained is concentrated by ultrafiltration, and adjusts pH It is 4.5, electrical conductivity is 40mS/cm, obtains concentrate;The Cu that the concentrate loading that will be obtained has been balanced2+Metal-chelating is affine Chromatographic column (Chelating sepharose Fast Flow, purchased from General Electric's Medical Group (GE companies, GE Healthcare), equilibrium liquid rinse metal chelate affinity chromatography post, equilibrium liquid by 1.0mol/L phosphate buffer and The acetum of 0.15mol/L is with 4:1 volume ratio composition, the pH of equilibrium liquid is 4.5, and electrical conductivity is 40mS/cm, is then used Deionized water is eluted as eluent, collects human urokinase-type peptidase eluting peak, carries out HPLC detections, as a result as shown in Figure 1; To ammonium sulfate is slowly added in the human urokinase-type peptidase eluting peak for obtaining, stirring to saturation stands, and adds diatomite 5g, collects Precipitation, obtains human urinary kallidinogenase crude product (KN semifinished products) 41g.Collection loading penetrates liquid and flushing penetrates liquid, is slowly added to Ammonium sulfate, stirring to saturation stands, and adds diatomite 20g, collects precipitation, obtains human urine trypsin inhibitor semifinished product (UTI semifinished products) 303g.
From fig. 1, it can be seen that the human urokinase-type peptidase eluting peak that the equilibrium liquid provided through the present embodiment and elution are collected Human urokinase-type peptidase content be up to 69.02%, and the content of human urine trypsin inhibitor (corresponding retention time is 8.5) It is low.
The preparation of the human urinary kallidinogenase crude product of embodiment two
The preparation method of human urinary kallidinogenase crude product comprises the following steps:It is big after collection adsorbing urine protein and water flushing Pass strong anion exchange resin 100kg, wash-out, eluent is the phosphate buffer of 1mol/L that pH is 4, the concentration of NaCl It is 0.1mol/L, collects Urine proteins eluting peak;The Urine proteins eluting peak that will be obtained is concentrated by ultrafiltration, and regulation pH is 4.5, conductance Rate is 40mS/cm, obtains concentrate;The Cu that the concentrate loading that will be obtained has been balanced2+Metal chelate affinity chromatography post (Chelating sepharose Fast Flow, purchased from General Electric's Medical Group (GE companies, GE Healthcare)), puts down Weighing apparatus liquid rinses metal chelate affinity chromatography post, and equilibrium liquid is molten by the phosphate buffer of 1.0mol/L and the acetic acid of 0.15mol/L Liquid is with 4:1 volume ratio composition, the pH of equilibrium liquid is 4.5, and electrical conductivity is 40mS/cm, then using deionized water as wash-out Liquid is eluted, and collects human urokinase-type peptidase eluting peak;To being slowly added to ammonium sulfate in the human urokinase-type peptidase eluting peak for obtaining, Stirring stands to saturation, adds diatomite 5g, collects precipitation, obtains human urinary kallidinogenase crude product 47g.Loading is collected to penetrate Liquid and flushing penetrate liquid, are slowly added to ammonium sulfate, and stirring to saturation stands, and adds diatomite 20g, collects precipitation, obtains human urine Trypsin inhibitor semifinished product 327g.
The preparation of the human urinary kallidinogenase crude product of comparative example one
The preparation method of human urinary kallidinogenase crude product comprises the following steps:Collect the moon after adsorbing urine protein and water flushing Ion exchange column Q Sepharose F.F 100kg, wash-out, eluent is the NaCl solution of 0.8mol/L, collects Urine proteins and washes De- peak;The Urine proteins eluting peak that will be obtained is concentrated by ultrafiltration, and regulation pH is 4.5, and electrical conductivity is 40mS/cm, obtains concentrate; The Cu that the concentrate loading that will be obtained has been balanced2+Metal chelate affinity chromatography post (Chelating sepharose Fast Flow, purchased from General Electric's Medical Group (GE companies, GE Healthcare)), equilibrium liquid rinses metal chelate affinity chromatography Post, equilibrium liquid is by the phosphate buffer of 1.0mol/L and the acetum of 0.15mol/L with 4:1 volume ratio composition, balance The pH of liquid is 4.5, and electrical conductivity is 40mS/cm, is then eluted using deionized water as eluent, collects human urine kininogen Enzyme eluting peak;To ammonium sulfate is slowly added in the human urokinase-type peptidase eluting peak for obtaining, stirring to saturation stands, and adds diatom Native 5g, collects precipitation, obtains human urinary kallidinogenase crude product 22g.Collection loading penetrates liquid and flushing penetrates liquid, is slowly added to sulphur Sour ammonium, stirring to saturation stands, and adds diatomite 20g, collects precipitation, obtains human urine trypsin inhibitor semifinished product 282g.
Comparative example one is with the difference of embodiment one:The NaCl that the eluent of anion-exchange column is changed to 0.8mol/L is molten Liquid.
The preparation of the human urinary kallidinogenase crude product of comparative example two
The preparation method of human urinary kallidinogenase crude product comprises the following steps:It is big after collection adsorbing urine protein and water flushing Pass strong anion exchange resin 100kg, wash-out, eluent is the phosphate buffer of 0.5mol/L that pH is 4.5, NaCl's Concentration is 0.3mol/L, collects Urine proteins eluting peak;The Urine proteins eluting peak that will be obtained is concentrated by ultrafiltration, and regulation pH is 8.0, Electrical conductivity is 2.2mS/cm, obtains concentrate;The Cu that the concentrate loading that will be obtained has been balanced2+Metal chelate affinity chromatography post (Chelating sepharose Fast Flow, purchased from General Electric's Medical Group (GE companies, GE Healthcare)), puts down Weighing apparatus liquid rinses metal chelate affinity chromatography post, and the pH of equilibrium liquid is 8.0, phosphate buffer and 0.2mol/ containing 0.02mol/L The NaCl solution of L, is then eluted using the Acetic acid-sodium acetate buffer solution of the 20mmol/L of pH3.8 as eluent, is received Collection human urokinase-type peptidase eluting peak;To ammonium sulfate is slowly added in the human urokinase-type peptidase eluting peak for obtaining, stir to saturation, it is quiet Put, add diatomite 5g, collect precipitation, obtain human urinary kallidinogenase crude product 24g.Collection loading penetrates liquid and flushing is penetrated Liquid, is slowly added to ammonium sulfate, and stirring to saturation stands, and adds diatomite 20g, collects precipitation, obtains human urinary trypsin suppression Agent semifinished product 296g.
Comparative example two is with the difference of embodiment one:The Urine proteins eluting peak that will be obtained is concentrated by ultrafiltration, and adjusts pH It is 8.0, electrical conductivity is 2.2mS/cm, obtains concentrate;The pH of equilibrium liquid is 8.0, phosphate buffer containing 0.02mol/L and The NaCl solution of 0.2mol/L;Using pH3.8 20mmol/L Acetic acid-sodium acetate buffer solution as eluent.
Test example:The detection of human urinary kallidinogenase crude product and human urine trypsin inhibitor semifinished product
Embodiment one, embodiment two, comparative example one, KN semifinished products obtained in comparative example two and UTI semifinished products are made respectively Detected with fluorescence method, as a result as shown in table 1.
The KN semifinished products and UTI semifinished product testing result tables of the different embodiments of table 1
As known from Table 1, embodiment one, the ratio of KN is lived as the ratio of UTI in 5.8, UTI semifinished products is lived as 389 in KN semifinished products Embodiment two, the ratio of KN is lived for the ratio work of UTI in 6.2, UTI semifinished products is 426 comparative examples one, in KN semifinished products in KN semifinished products It is 139 comparative examples two that the ratio of KN is lived and lived for the ratio of UTI in 0.8, UTI semifinished products, and the ratio of KN is lived as 1.1, UTI is thick in KN semifinished products It is 152 that the ratio of UTI is lived in product
Therefore, the preparation method of the human urinary kallidinogenase crude product that the present invention is provided can realize the efficient wash-out of KN, realize KN semifinished products and UTI semifinished products are efficiently separated, and UTI is concentrated in UTI semifinished products substantially, and KN concentrates on KN semifinished products substantially In, refined beneficial to KN semifinished products and the follow-up of UTI semifinished products.
Above content is to combine specific preferred embodiment further description made for the present invention, it is impossible to assert Specific implementation of the invention is confined to these explanations.For general technical staff of the technical field of the invention, On the premise of not departing from present inventive concept, some simple deduction or replace can also be made, should be all considered as belonging to of the invention Protection domain.

Claims (9)

1. a kind of preparation method of human urinary kallidinogenase crude product, it is characterised in that:Comprise the following steps:
S1 collects the adsorbent after adsorbing urine protein, and wash-out collects Urine proteins eluting peak;
The Urine proteins eluting peak that S2 obtains step S1 is concentrated by ultrafiltration, and regulation pH is 4~5.8, and electrical conductivity is 20~70mS/ Cm, obtains concentrate;
The concentrate loading metal chelate affinity chromatography post that S3 obtains step S2, equilibrium liquid rinses metal chelate affinity chromatography Post, is then eluted using water as eluent, collects human urokinase-type peptidase eluting peak;The equilibrium liquid is by 0.5~2mol/ The phosphate buffer of L and the acetum of 0.01~0.1mol/L are with 3~5:1 volume ratio composition, the pH of equilibrium liquid for 4~ 5.8;
Ammonium sulfate is slowly added in the human urokinase-type peptidase eluting peak that S4 is obtained to step S3, is stirred, stood, collect precipitation, obtained To human urinary kallidinogenase crude product.
2. the preparation method of human urinary kallidinogenase crude product according to claim 1, it is characterised in that:The step S2 In, regulation pH is 4.5~5.5, and electrical conductivity is 25~60mS/cm.
3. the preparation method of human urinary kallidinogenase crude product according to claim 1, it is characterised in that:The step S3 In, equilibrium liquid is by the phosphate buffer of 0.8~1.2mol/L and the acetum of 0.03~0.5mol/L with 3~4:1 body Than composition, the pH of equilibrium liquid is 4.2~5.0 to product.
4. the preparation method of human urinary kallidinogenase crude product according to claim 3, it is characterised in that:The step S3 In, equilibrium liquid is by the phosphate buffer of 1.0~1.2mol/L and the acetum of 0.1~0.3mol/L with 4:1 volume ratio Composition, the pH of equilibrium liquid is 4.4~4.8, and electrical conductivity is 40~55mS/cm.
5. the preparation method of human urinary kallidinogenase crude product according to claim 1, it is characterised in that:The step S1 In, adsorbent is anion exchange resin.
6. the preparation method of human urinary kallidinogenase crude product according to claim 5, it is characterised in that:The step S1 In, adsorbent is macroporous type strong anion exchange resin.
7. the preparation method of human urinary kallidinogenase crude product according to claim 1, it is characterised in that:The step S1 In, eluent is the phosphate buffer of 0.3~2mol/L, and pH is 0.01~0.45mol/L for the concentration of 4~6, NaCl.
8. the preparation method of human urinary kallidinogenase crude product according to claim 1, it is characterised in that:The metal-chelating The metal ion of affinity column is Cu2+、Zn2+Or Ni2+
9. the preparation method of human urinary kallidinogenase crude product according to claim 8, it is characterised in that:The metal-chelating The metal ion of affinity column is Cu2+
CN201611101691.XA 2016-12-02 2016-12-02 A kind of preparation method of human urinary kallidinogenase crude product Pending CN106754839A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201611101691.XA CN106754839A (en) 2016-12-02 2016-12-02 A kind of preparation method of human urinary kallidinogenase crude product

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201611101691.XA CN106754839A (en) 2016-12-02 2016-12-02 A kind of preparation method of human urinary kallidinogenase crude product

Publications (1)

Publication Number Publication Date
CN106754839A true CN106754839A (en) 2017-05-31

Family

ID=58884567

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201611101691.XA Pending CN106754839A (en) 2016-12-02 2016-12-02 A kind of preparation method of human urinary kallidinogenase crude product

Country Status (1)

Country Link
CN (1) CN106754839A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109091667A (en) * 2018-09-18 2018-12-28 广东天普生化医药股份有限公司 Purposes and combinations thereof of the human urokinase-type peptidase in preparation treatment migraine remedy

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102660525A (en) * 2012-05-15 2012-09-12 扬州艾迪生物科技有限公司 Method for preparing human urinary kallidinogenase crude product
CN105754977A (en) * 2016-04-05 2016-07-13 广东天普生化医药股份有限公司 Method for preparing crude human urine kininogenase product

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102660525A (en) * 2012-05-15 2012-09-12 扬州艾迪生物科技有限公司 Method for preparing human urinary kallidinogenase crude product
CN105754977A (en) * 2016-04-05 2016-07-13 广东天普生化医药股份有限公司 Method for preparing crude human urine kininogenase product

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109091667A (en) * 2018-09-18 2018-12-28 广东天普生化医药股份有限公司 Purposes and combinations thereof of the human urokinase-type peptidase in preparation treatment migraine remedy
CN109091667B (en) * 2018-09-18 2020-05-05 广东天普生化医药股份有限公司 Application of human urinary kallidinogenase in preparing medicine for treating migraine and composition thereof

Similar Documents

Publication Publication Date Title
CN105153297A (en) Method for separating and purifying alpha2-macroglobulin from Cohn component IV precipitate
KR20030005005A (en) Process for the purification of pharmacologically active proteins through cationic exchange chromatography
CN102952187A (en) Preparation method of high-purity bovine serum albumin
CN106349387A (en) Method for purifying alpha1-antitrypsin from Cohn component IV precipitate
CN105968185A (en) Chorionic gonadotrophin purification method
CN107987157A (en) It is a kind of can industrialized production people source blood clotting regulatory protein preparation method
CN106754839A (en) A kind of preparation method of human urinary kallidinogenase crude product
Boggaram et al. Purification of glutathione reductase from porcine erythrocytes by the use of affinity chromatography on 2′, 5′-ADP-Sepharose 4B and crystallization of the enzyme
CN107574214A (en) A kind of preparation method of the whey protein peptide of anti-aging
CN106497903B (en) A kind of technique for purifying blood coagulation proenzyme compound
CN105624134B (en) The preparation method of restricted fibrin ferment
CN106749626A (en) A kind of method and the method using ox blood that albumin and globulin are extracted from cow's serum
CN107033237A (en) A kind of Human Plasma Apolipoprotein A I isolation and purification method
CN103694343A (en) Method for preparing human albumin from urine
WO2020078254A1 (en) Method for isolating recombinant human growth hormone from genetically engineered rice seeds and purifying same
CN102295699B (en) Process for purifying cytochrome C
CN108059673B (en) Method for separating immunoglobulin IgG from human serum
CN105754977B (en) It is a kind of while preparing the method for human urinary kallidinogenase crude product and human urine trypsin inhibitor semifinished product
CN102924586A (en) Method for producing pregnant mare serum gonactotropin by monoclonal antibody technology
CN103694334B (en) A kind of method preparing hEGF raw product
CN103183720B (en) The extracting method of low molecular peptide in a kind of milk and milk products
CN102993267A (en) Preparation method of glossy ganoderma bioactive peptide
Movat et al. A small molecular weight permeability factor in guinea pig serum: adsorption to antigen-antibody aggregates
CN103739692B (en) Method for preparing beta2 microglobulin crude product
CN102660525B (en) Method for preparing human urinary kallidinogenase crude product

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication

Application publication date: 20170531

RJ01 Rejection of invention patent application after publication