CN1259336C - Method for purifying composite interferon - Google Patents

Method for purifying composite interferon Download PDF

Info

Publication number
CN1259336C
CN1259336C CN 200310121343 CN200310121343A CN1259336C CN 1259336 C CN1259336 C CN 1259336C CN 200310121343 CN200310121343 CN 200310121343 CN 200310121343 A CN200310121343 A CN 200310121343A CN 1259336 C CN1259336 C CN 1259336C
Authority
CN
China
Prior art keywords
damping fluid
interferon
described step
interferon alfacon
renaturation
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.)
Expired - Fee Related
Application number
CN 200310121343
Other languages
Chinese (zh)
Other versions
CN1626551A (en
Inventor
刘永东
李京京
王芳薇
苏志国
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.)
Institute of Process Engineering of CAS
Original Assignee
Institute of Process Engineering of CAS
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 Institute of Process Engineering of CAS filed Critical Institute of Process Engineering of CAS
Priority to CN 200310121343 priority Critical patent/CN1259336C/en
Publication of CN1626551A publication Critical patent/CN1626551A/en
Application granted granted Critical
Publication of CN1259336C publication Critical patent/CN1259336C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Peptides Or Proteins (AREA)
  • Medicines That Contain Protein Lipid Enzymes And Other Medicines (AREA)

Abstract

The present invention provides a purification method of composite interferon. The method comprises the following procedures: firstly, while the composite interferon is stirred, a buffer solution D is added to the composite interferon obtained by denaturing inclusion bodies obtained by fermentation and collection with a conventional method. Then, the renaturation of composite interferon proteins is carried out in a dialysis bag filled with a buffer solution E, wherein the permeation molecular weight of the dialysis bag is below 50000; finally, a supernatant is separated and treated by gradient elution with a buffer solution F and a buffer solution G on a chromatography column with strong cation exchange mediums, and the purified composite interferon is obtained. With the method, other proteins with the molecular weight of 30000 to 40000 can be completely removed, and renatured intermediates and completely renatured proteins are basically separated; thus, the purity of the obtained composite interferon is high, and the structure of products is more uniform.

Description

A kind of purification process of Interferon alfacon-1
Technical field
The present invention relates to biological technical field, (Consensus interferon, the preparation technology of IFN-α-conl) is particularly with the method for cation exchange medium single step purification recombinant consensus interferon to relate to a kind of recombinant consensus interferon.
Background technology
(IFN is antiviral, antiproliferative and the immunomodulatory that a class has wide spectrum Interferon) to Interferon, rabbit, can activate the general name of the cytokine of natural killer cell multiple functions such as (NK cell).It is that the similar, the function that are produced by multiple inductor inducing cell are close, the low molecular saccharides albumen of biologically active, is a class important cytokine.Interferon, rabbit generally is divided into I type and II type, and the I type comprises IFN-α, IFN-β and IFN-ω, and wherein IFN-α can be divided into the hypotype that primary structure there are differences more than 25 kinds again; The II type comprises IFN- γThese Interferon, rabbit are produced by different genes encodings respectively, and biological activity is different.The Interferon, rabbit that uses clinically mostly is to obtain by gene recombination technology production at present.The advantage that the DNA recombinant technology is produced Interferon, rabbit be this method can high purity, produce Interferon, rabbit in large quantity.
1981, the researchist that (Amgen) company is pacified into by the U.S. synthesized a kind of non-natural I type Interferon, rabbit (Consensus interferon, IFN-α-conl, Interferon alfacon-1) first.Close on this Interferon alfacon-1 structure with common Interferon, rabbit, have 166 amino-acid residues, wherein about 30% locational amino acid is identical with IFN-β, amino acid and IFN-more than 60% γIdentical, have only 20 the locational amino acid and the IFN-α of normal use clinically 2aThe amino acid difference of corresponding position.But the biological activity of Interferon alfacon-1 but is 2～20 times of common Interferon, rabbit.Thereby become the focus of research.United States Patent (USP) 4695623,4897471,5372808 discloses the interferon activity that Interferon alfacon-1 has wide spectrum, has stronger antivirally and antitumor and activate the NK cell activity, can be used for the treatment of disease.Chinese patent 97193506 discloses the method for using composite interference extract for treating hepatitis C, and Chinese patent 98114663 discloses the preparation method of recombinant consensus interferon and the purposes of treatment hepatitis B and hepatitis C.These existing researchs show that all composite interference extract for treating chronic hepatitis C effect is remarkable, particularly aspect reducing the serum-virus load and treating the patient of the invalid or recurrence of other interferon therapy, are better than the Interferon, rabbit of other type.
The preparation method of Interferon alfacon-1 generally comprises the artificial constructed of composite interference gene and by the host cell fermentation that contains this dna sequence dna expression vector, is purification process at last at present.Purification step wherein is most important for the quality product of Interferon alfacon-1.For purification step, adopt at present mostly anionresin and gel-filtration to combine, or the two-step purifying method that combines with hydrophobic chromatography of anionresin.But the effect of these two kinds of purification process is all not good, on the one hand, can not effectively remove the two kind foreign proteins of molecular weight about 3～40,000, so purified product purity is not very high; On the other hand, Interferon alfacon-1 always can contain the not renaturation intermediate of complete renaturation of part in the renaturation supernatant liquor when dilution refolding, use these two kinds of purification process that the renaturation intermediate is not had separating effect substantially, thus the product structure heterogeneity of purifying.
Summary of the invention
The purification process purified product purity that the objective of the invention is to overcome existing Interferon alfacon-1 is not the inhomogenous defective of product structure very high, purifying, thereby provide a kind of molecular weight of can not only removing fully at 3～40,000 foreign protein, and the renaturation intermediate and the protein-based of complete renaturation originally can be separated, thereby products obtained therefrom is the purity height not only, and the also purification process of the Interferon alfacon-1 of homogeneous more of product structure.
The objective of the invention is to realize by the following technical solutions:
The invention provides a kind of purification process of Interferon alfacon-1, comprise the steps:
1) Interferon alfacon-1 that will obtain through the inclusion body sex change of conventional method fermentation and collection adds damping fluid D while stirring, and the damping fluid D that is added and the volume ratio of Interferon alfacon-1 are 40～100: 1, then with the mixed solution standing over night;
2) step 1) is packed into and can be seen through in the dialysis tubing of molecular weight below 50000 through the mixed solution that leaves standstill, dialysed in damping fluid E 12～24 hours, carry out the proteinic renaturation of Interferon alfacon-1, the volume ratio of damping fluid E and mixed solution is 5～20: 1;
3) from step 2) through the mixed solution of dialysis, tell supernatant liquor, obtain the composite interference cellulose solution of renaturation;
4) chromatography column of strong cation exchange medium is housed with damping fluid F balance, the medium loading height is 5～25cm, the composite interference cellulose solution of the renaturation of step 3) is transferred pH to 3.5～6.0 back upper props, applied sample amount is no more than 15mg/ml, use the damping fluid F drip washing of 2 times of column volumes then, the mixed solution that contains damping fluid G and damping fluid F with 5～10 times of column volumes carries out gradient elution again, flow velocity during drip washing is 50～200cm/min, elutriant when collecting second albumen elution peak, at last this elutriant is concentrated, obtain the Interferon alfacon-1 of purifying.
The damping fluid D of described step 1) is 100mM Tris+0.5M arginine+0.2mMEDTA (disodium ethylene diamine tetraacetate), transfers pH to 8.3 with HCl;
Described step 2) damping fluid E is 25mM Tris-HCl, pH8.3;
The strong cation exchange medium of described step 4) comprises SP Sepharose FF, SP-Sepharose XL, and SP-Sepharose Big Bead, SE-Mierocrystalline cellulose or S-dextran are preferably SP Sepharose XL (Aarmacia);
The damping fluid F of described step 4) is 5～50mM Sodium phosphate dibasic-SODIUM PHOSPHATE, MONOBASIC of pH 3.5～6.0, citric acid-sodium citrate, Sodium phosphate dibasic-citric acid, citric acid-sodium hydroxide-hydrochloric acid, sodium acetate-acetate, potassium primary phosphate-sodium hydroxide is preferably Sodium phosphate dibasic-SODIUM PHOSPHATE, MONOBASIC;
The damping fluid G of described step 4) is dissolved among the damping fluid F of described step 4) for 1M NaCl;
The applied sample amount of described step 4) is preferably 8～10mg/ml;
The flow velocity of described step 4) is preferably 150cm/min;
The cocktail buffer damping fluid G that described step 4) is used for gradient elution accounts for 10～60% of cocktail buffer cumulative volume.
Compared with prior art, purification process provided by the invention uses cation exchange medium, more under the tart pH value condition it being adsorbed on the medium than Interferon alfacon-1 iso-electric point, changes the ionic strength of eluent then, and Interferon alfacon-1 is eluted.The Interferon alfacon-1 purity height of present method gained, product structure is homogeneous more also, can remove molecular weight fully at 3～40,000 foreign protein, and the renaturation intermediate and the protein-based of complete renaturation originally can be separated, the gained protein-active rate of recovery is 60%, product purity is greater than 99%, and antiviral activity is 1～2 * 10 9IU/mg.In addition, this method steps is simple, and only a step chromatography can reach purification effect, saves technology and operator than the two step method of prior art, thereby with low cost, is easy to promote.
Description of drawings
Fig. 1 is the chromatography collection of illustrative plates of purification process purifying Interferon alfacon-1 of the present invention.
Embodiment
The production of EXAMPLE l, Interferon alfacon-1
The not purified Interferon alfacon-1 that the present invention uses is to use ordinary method that the composite interference gene is artificial constructed and by the host cell fermentation that contains this dna sequence dna expression vector and get, and specifically fermenting process is as follows:
Selecting e. coli bl21 for use is the host bacterium, and bacterial strain is kept at-80 ℃.Picking Interferon alfacon-1 engineering bacteria (being provided by the Tang Hong researcher of Institute of Micro-biology of the Chinese Academy of Sciences) was rule on ammonia Bian resistance LB flat board, in 37 ℃ of hot-house cultures 12～24 hours.Picking list bacterium colony, be inoculated in 3 milliliters of liquid LB substratum (the ammonia Bian, 1～50mg/ml), cultivated 12～24 hours with the speed of 240rpm in 37 ℃ of shaking tables, survey OD 600Be 2 seed liquor of switching in 1.0～2.0 o'clock, similarity condition is cultivated OD down 600Reach at 1.0～2.0 o'clock and insert fermention medium in 5～10% ratio, 37 ℃, air flow is 0.8～1.2vvm, rotating speed 400～700rpm.In the culturing process, regulate pH at 7.0-7.4 with ammoniacal liquor and hydrochloric acid; The OD value adds supplemented medium 250ml when raising.By regulating feed supplement speed and rotating speed, DO is 20～50% in control.Thalline enters logarithmic growth after date (OD 600=2.0) add 1 ‰ IPTG and begin to induce, induce after 2～8 hours to stop.Centrifugal collection thalline, Interferon alfacon-1 is stored in the cell with the inclusion body form, and SDS-PAGE analyzes its content and accounts for 15% of total protein of cell, freezing preservation.
Described fermention medium is prepared in following ratio: Tryptones 2g/L, yeast extract 2g/L, 12 water Sodium phosphate dibasic 7g/L, potassium primary phosphate 2g/L, dipotassium hydrogen phosphate 4g/L, ammonium sulfate 8g/L, ammonium chloride 0.2g/L, micro-60ml/L; Trace element wherein comprises MnSO 45H 2O 0.001g/L, CaCl 26H 2O 0.004g/L, Na 2MO 42H 2O 0.002g/L, ZnCl 20.002g/L, CuSO 45H 2O 0.001g/L, H 3BO 40.0005g/L, FeSO 47H 2O 0.02g/L, CoCl 22H 2O 0.02g/L, MgSO 47H 2O 0.3g/L.
Described supplemented medium is prepared in following ratio: glycerine 51g/L, yeast extract 10g/L, Tryptones 10g/L, 7 water magnesium sulfate 0.85g/L.
Albumen in the inclusion body exists with aggregate form, and the lifeless matter activity needs sex change dissolving repeatability could recover natural radioactivity.Get a certain amount of thalline, with 1: 5 (W: the buffer A of ratio V) (25mM Tris-HCl, pH8.0) fully suspension.Carrying out ultrasonic bacteria breaking in ice bath.Ultrasonic power 200W, stopped 2 fens at ultrasonic 2 minutes (surpassing 5 seconds, 5 seconds at interval).4 times repeatedly.10000rpm after broken bacterium finishes, 30min is centrifugal, collects inclusion body.Use inclusion body washings (1mM mercaptoethanol+1mM EDTA-Na+0.05%Triton X-100) washing inclusion body afterwards, 10000rpm, centrifugal 30min.The inclusion body of collecting can frozenly be preserved the also dissolving of sex change immediately in-70 degree refrigerators.
In 1: 5 (the inclusion body weight W: denaturing agent volume V) ratio add denaturing agent 100ml (8M urea+0.5mM mercaptoethanol+25mM Tris-HCl, pH8.0).Magnetic agitation a few hours.12000rpm collects supernatant behind the centrifugal 30min, and the Interferon alfacon-1 purity that SDS-PAGE records sex change is 65%.
The purifying of embodiment 2, recombinant consensus interferon
It with the purity that obtains through the fermentation of conventional method and the inclusion body sex change of collecting among the embodiment 1 65% Interferon alfacon-1, add damping fluid D (100mM Tris+0.5M arginine+0.2mM EDTA (disodium ethylene diamine tetraacetate) while stirring, transfer pH to 8.3 with HCl), the damping fluid D that is added and the volume ratio of Interferon alfacon-1 are 40: 1, then with the mixed solution standing over night.
Then this mixed solution being packed into can see through in the dialysis tubing of molecular weight 8000, in damping fluid E (25mMTris-HCl, pH8.3) in dialysis 12 hours, carry out the proteinic renaturation of Interferon alfacon-1, the volume ratio of damping fluid E and mixed solution is 5: 1; Centrifugal or remove by filter white aggregation, tell supernatant liquor, be the solution of the Interferon alfacon-1 of renaturation, recombinant protein concentration is 0.3mg/ml, it is 90% that SDS-PAGE records Interferon alfacon-1 purity, protein renaturation rate 70%.
The chromatography column of self-chambering 2.6 * 20, the medium that adopts is commercial Amarcial SP Sepharose XL strong cation exchange medium, the medium loading height is 5cm, and with damping fluid F (20mM sodium acetate-acetate, pH 3.5) the balance chromatography column, the composite interference cellulose solution of renaturation is transferred pH to 3.5 back upper prop with 1M acetate, applied sample amount is 15mg/ml, use the damping fluid F drip washing of 2 times of column volumes then, use the damping fluid G (20mM sodium acetate-acetate of 5 times of column volumes again, pH 3.5,1M NaCl) and the mixed solution of damping fluid F carry out gradient elution, damping fluid G accounts for the percent by volume of damping fluid G and damping fluid F cumulative volume from 10～60%, flow velocity during drip washing is 50cm/min, collect second albumen elution peak (tomographic map as shown in Figure 1), at last this elutriant is concentrated, be the Interferon alfacon-1 of purifying.
The Interferon alfacon-1 that uses reduced form SDS-PAGE to analyze this purifying is single band, and purity is 99.2%, molecular weight 19200, and the Interferon alfacon-1 that uses oxidized form SDS-PAGE to analyze this purifying is similarly single band.The purification step activity recovery is 75%, and antiviral activity is 1.2 * 10 9IU/mg.
The purifying of embodiment 3, recombinant consensus interferon
It with the purity that obtains through the fermentation of conventional method and the inclusion body sex change of collecting among the embodiment 1 65% Interferon alfacon-1, add damping fluid D (100mM Tris+0.5M arginine+0.2mM EDTA while stirring, transfer pH to 8.3 with HCl), the damping fluid D that is added and the volume ratio of Interferon alfacon-1 are 100: 1, then with the mixed solution standing over night;
Then this mixed solution being packed into can see through in the dialysis tubing of molecular weight 50000, in damping fluid E (25mMTris-HCl, pH8.3) in dialysis 24 hours, carry out the proteinic renaturation of Interferon alfacon-1, the volume ratio of damping fluid E and mixed solution is 20: 1; Centrifugal or remove by filter white aggregation, tell supernatant liquor, be the solution of the Interferon alfacon-1 of renaturation, recombinant protein concentration is 0.8mg/ml, it is 90% that SDS-PAGE records Interferon alfacon-1 purity, protein renaturation rate 70%.
The chromatography column of self-chambering 2.6 * 20, the medium that adopts is commercial SP Sepharose FF strong cation exchange medium, the medium loading height is 25cm, and with damping fluid F (50mM Sodium phosphate dibasic-SODIUM PHOSPHATE, MONOBASIC, pH 6.0) the balance chromatography column, the composite interference cellulose solution of renaturation is transferred pH to 6.0 back upper prop with 1M phosphoric acid, applied sample amount is 10mg/ml, use the damping fluid F drip washing of 2 times of column volumes then, use the damping fluid G (50mM Sodium phosphate dibasic-SODIUM PHOSPHATE, MONOBASIC of 10 times of column volumes again, pH 6.0,1M NaCl) and the mixed solution of damping fluid F carry out gradient elution, damping fluid G accounts for the percent by volume of damping fluid G and damping fluid F cumulative volume from 10～60%, flow velocity during drip washing is 150cm/min, collect second albumen elution peak, at last this elutriant is concentrated, be the Interferon alfacon-1 of purifying.
The Interferon alfacon-1 that uses reduced form SDS-PAGE to analyze this purifying is single band, and purity is 99.6%, molecular weight about 19400, and the Interferon alfacon-1 that uses oxidized form SDS-PAGE to analyze this purifying is similarly single band.The purification step activity recovery is 76%, and antiviral activity is 1.9 * 10 9IU/mg.
The purifying of embodiment 4, recombinant consensus interferon
It with the purity that obtains through the fermentation of conventional method and the inclusion body sex change of collecting among the embodiment 1 65% Interferon alfacon-1, add damping fluid D (100mM Tris+0.5M arginine+0.2mM EDTA while stirring, transfer pH to 8.3 with HCl), the damping fluid D that is added and the volume ratio of Interferon alfacon-1 are 60: 1, then with the mixed solution standing over night;
Then this mixed solution being packed into can see through in the dialysis tubing of molecular weight 20000, in damping fluid E (25mMTris-HCl, pH8.3) in dialysis 18 hours, carry out the proteinic renaturation of Interferon alfacon-1, the volume ratio of damping fluid E and mixed solution is 15: 1; Centrifugal or remove by filter white aggregation, tell supernatant liquor, be the solution of the Interferon alfacon-1 of renaturation, recombinant protein concentration is 0.5mg/ml, it is 90% that SDS-PAGE records Interferon alfacon-1 purity, protein renaturation rate 70%.
The chromatography column of self-chambering 2.6 * 20, the medium that adopts is commercial SP-Sepharose Big Bead strong cation exchange medium, the medium loading height is 15cm, and with damping fluid F (5mM citric acid-sodium citrate, pH 4.0) the balance chromatography column, the composite interference cellulose solution of renaturation is transferred pH to 4.0 back upper prop with 1M phosphoric acid, applied sample amount is 8mg/ml, use the damping fluid F drip washing of 2 times of column volumes then, use damping fluid G (the 5mM citric acid-sodium citrate of 8 times of column volumes again, pH 4.0,1M NaCl) and the mixed solution of damping fluid F carry out gradient elution, damping fluid G accounts for the percent by volume of damping fluid G and damping fluid F cumulative volume from 10～60%, flow velocity during drip washing is 200cm/min, collect second albumen elution peak, at last this elutriant is concentrated, be the Interferon alfacon-1 of purifying.
The Interferon alfacon-1 that uses reduced form SDS-PAGE to analyze this purifying is single band, and purity is 99.1%, molecular weight about 19100, and the Interferon alfacon-1 that uses oxidized form SDS-PAGE to analyze this purifying is similarly single band.The purification step activity recovery is 75%, and antiviral activity is 1.8 * 10 9IU/mg.
Use purification process provided by the invention, the Interferon alfacon-1 purity height that obtains, product structure is homogeneous more also, can remove molecular weight fully at 3～40,000 foreign protein, and the renaturation intermediate and the protein-based of complete renaturation originally can be separated, the gained protein-active rate of recovery reaches more than 60%, and product purity is greater than 99%, and antiviral activity is 1～2 * 10 9IU/mg.

Claims (5)

1, a kind of purification process of recombinant consensus interferon comprises the steps:
1) Interferon alfacon-1 that is will be through the composite interference plain gene artificial constructed and that obtain by the host cell fermentation that contains this dna sequence dna expression vector and the inclusion body sex change of collecting, add damping fluid D while stirring, the damping fluid D that is added and the volume ratio of Interferon alfacon-1 are 40～100: 1, then with the mixed solution standing over night;
2) step 1) is packed into and can be seen through in the dialysis tubing of molecular weight 8000-50000 through the mixed solution that leaves standstill, dialysed in damping fluid E 12～24 hours, carry out the proteinic renaturation of Interferon alfacon-1, the volume ratio of damping fluid E and mixed solution is 5～20: 1;
3) from step 2) through the mixed solution of dialysis, tell supernatant liquor, obtain the composite interference cellulose solution of renaturation;
4) chromatography column of strong cation exchange medium is housed with damping fluid F balance, the medium loading height is 5～25cm, the composite interference cellulose solution of the renaturation of step 3) is transferred pH to 3.5～6.0 back upper props, applied sample amount is 8-15mg/ml, use the damping fluid F drip washing of 2 times of column volumes then, the mixed solution that contains damping fluid G and damping fluid F with 5～10 times of column volumes carries out gradient elution again, flow velocity during drip washing is 50～200cm/min, elutriant when collecting second albumen elution peak, at last this elutriant is concentrated, obtain the Interferon alfacon-1 of purifying;
The damping fluid D of described step 1) is 100mM Tris, 0.5M arginine and 0.2mM disodium ethylene diamine tetraacetate, transfers pH to 8.3 with HCl;
Described step 2) damping fluid E is 25mM Tris-HCl, pH8.3;
The damping fluid F of described step 4) is 5～50mM Sodium phosphate dibasic-SODIUM PHOSPHATE, MONOBASIC of pH3.5～6.0, citric acid-Trisodium Citrate, Sodium phosphate dibasic-citric acid, citric acid-sodium hydroxide-hydrochloric acid, sodium acetate-acetate or potassium primary phosphate-sodium hydroxide;
The damping fluid G of described step 4) is dissolved among the damping fluid F of described step 4) for 1M NaCl;
The cocktail buffer damping fluid G that described step 4) is used for gradient elution accounts for 10～60% of cocktail buffer cumulative volume.
2, the purification process of recombinant consensus interferon as claimed in claim 1, it is characterized in that the strong cation exchange medium of described step 4) is SP Sepharose FF, SP-Sepharose XL, SP-Sepharose Big Bead, SE-Mierocrystalline cellulose or S-dextran.
3, the purification process of recombinant consensus interferon as claimed in claim 1 is characterized in that, the damping fluid F of described step 4) is Sodium phosphate dibasic-SODIUM PHOSPHATE, MONOBASIC.
4, the purification process of recombinant consensus interferon as claimed in claim 1 is characterized in that, the applied sample amount of described step 4) is 8～10mg/ml.
5, the purification process of recombinant consensus interferon as claimed in claim 1 is characterized in that, the flow velocity during described step 4) drip washing is 150cm/min.
CN 200310121343 2003-12-12 2003-12-12 Method for purifying composite interferon Expired - Fee Related CN1259336C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 200310121343 CN1259336C (en) 2003-12-12 2003-12-12 Method for purifying composite interferon

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 200310121343 CN1259336C (en) 2003-12-12 2003-12-12 Method for purifying composite interferon

Publications (2)

Publication Number Publication Date
CN1626551A CN1626551A (en) 2005-06-15
CN1259336C true CN1259336C (en) 2006-06-14

Family

ID=34761578

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 200310121343 Expired - Fee Related CN1259336C (en) 2003-12-12 2003-12-12 Method for purifying composite interferon

Country Status (1)

Country Link
CN (1) CN1259336C (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103804486B (en) * 2014-01-20 2017-05-17 安徽安科生物工程（集团）股份有限公司 Preparation technology for improving native conformation content of recombinant human interferon alpha2b
CN111138523A (en) * 2019-12-10 2020-05-12 天津生机集团股份有限公司 Method for purifying and preparing recombinant chicken interferon α from recombinant chicken interferon α renaturation solution
CN112625115B (en) * 2020-12-25 2022-09-06 山东睿鹰制药集团有限公司 Method and kit for purifying recombinant human interferon-kappa

Also Published As

Publication number Publication date
CN1626551A (en) 2005-06-15

Similar Documents

Publication Publication Date Title
Samuelsson et al. Facilitated in vitro refolding of human recombinant insulin-like growth factor I using a solubilizing fusion partner
WO2005092914A1 (en) Process for promoting proper folding of human serum albumin using a human serum albumin ligand
RU2358980C2 (en) Method of purifying and/or extracting biologically active granulocyte colony-stimulating factor
CN100336825C (en) Renaturation of reconstituted human bone protein-1 and making method of its preparation
CN1259336C (en) Method for purifying composite interferon
CN101514229B (en) Human interferon alpha derivative and polyethylene glycol modified substance thereof
CN104844684A (en) Protein refolding method using metal ion chelate affinity chromatography column as solid phase carrier
CN103014101B (en) Purifying method of interferon
CN102286490B (en) Preparation and renaturation method of chicken interferon gamma
CN1313612C (en) Method for producing recombinant human granulocyte colony stimulating factor
CN1757723A (en) Method of producing recombination human bone morphopoiesis protein
EP2502633A1 (en) Recombinant plasmid DNA pMSIN4, encoding a hybrid polypeptide comprising human insulin precursor, E. coli strain BL21 (DE3) / pMSIN4 - producer of recombinant human insulin, the method for the recombinant human insulin production
CN1844392A (en) Recombinant human ciliary nerve trophic factor mutant and method for preparing same
CN102869767B (en) The preparation method of interferon alpha 5
JP2844484B2 (en) Method for producing recombinant protein
CN102336829B (en) Method for producing recombinant human bone morphogenetic protein-2 mature peptide
EP0529086B1 (en) Process for purifying human bcdf
CN1902224A (en) Process for purifying interferon beta
CN100500841C (en) Expression of soluble TRAIL protein
CN106319001B (en) Industrialized preparation method and application of recombinant interferon gamma
CN1473843A (en) Industrially extracting, renaturation and purifying method for recombined TRAILinclusion body protein
CN1212336C (en) Prepn of recombinant human parathyroid hormone PTH (1-34)
CN1142281C (en) Preparation of recombined erythropoietin preparation
CN1228476A (en) Method for preparing human granulocyte macrophage colony stimulating factor and its expressing carrier and engineering bacteria
CN1259337C (en) Synthesis, expression, preparation and application for human parathyroid hormone gene mutant

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20060614

Termination date: 20131212