[go: up one dir, main page]

WO2005077973A1 - Purification of recombinant human proteins - Google Patents

Purification of recombinant human proteins Download PDF

Info

Publication number
WO2005077973A1
WO2005077973A1 PCT/IN2005/000045 IN2005000045W WO2005077973A1 WO 2005077973 A1 WO2005077973 A1 WO 2005077973A1 IN 2005000045 W IN2005000045 W IN 2005000045W WO 2005077973 A1 WO2005077973 A1 WO 2005077973A1
Authority
WO
WIPO (PCT)
Prior art keywords
protein
recombinant
purification
proteins
monomer
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.)
Ceased
Application number
PCT/IN2005/000045
Other languages
French (fr)
Inventor
Sripad Gunwar
Murali Tummuru
Hemanth Nandigala
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.)
VIRCHOW BIOTECH PRIVATE Ltd
Original Assignee
VIRCHOW BIOTECH PRIVATE 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 VIRCHOW BIOTECH PRIVATE Ltd filed Critical VIRCHOW BIOTECH PRIVATE Ltd
Publication of WO2005077973A1 publication Critical patent/WO2005077973A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D15/00Separating processes involving the treatment of liquids with solid sorbents; Apparatus therefor
    • B01D15/08Selective adsorption, e.g. chromatography
    • B01D15/26Selective adsorption, e.g. chromatography characterised by the separation mechanism
    • B01D15/32Bonded phase chromatography
    • B01D15/325Reversed phase
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/281Sorbents specially adapted for preparative, analytical or investigative chromatography
    • B01J20/282Porous sorbents
    • B01J20/285Porous sorbents based on polymers
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07KPEPTIDES
    • C07K1/00General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length
    • C07K1/107General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length by chemical modification of precursor peptides
    • C07K1/113General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length by chemical modification of precursor peptides without change of the primary structure
    • C07K1/1136General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length by chemical modification of precursor peptides without change of the primary structure by reversible modification of the secondary, tertiary or quarternary structure, e.g. using denaturating or stabilising agents
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07KPEPTIDES
    • C07K1/00General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length
    • C07K1/14Extraction; Separation; Purification
    • C07K1/16Extraction; Separation; Purification by chromatography
    • C07K1/20Partition-, reverse-phase or hydrophobic interaction chromatography
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07KPEPTIDES
    • C07K14/00Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof
    • C07K14/435Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof from animals; from humans
    • C07K14/52Cytokines; Lymphokines; Interferons
    • C07K14/54Interleukins [IL]
    • C07K14/55IL-2

Definitions

  • the present invention provides a simple and economical method for the purification of recombinant proteins free from host proteins, wherein at least 90- 95% pure recombinant proteins can be obtained.
  • Biomolecules produced by rDNA technology can be endo or Intracellular proteins ('inside' the cell); Periplasmic (part of the cell wall) or extracellular proteins ('outside' the cell in the culture medium). They can be produced using a variety of organisms like E.coii; S.cerevisiae; P.pastoris etc.
  • the present invention relates specifically to endocellular rDNA derived biomolecules produced in E.coii as 'inclusion bodies'.
  • Endocellular proteins have to be purified from a cell extract containing a complex mixture of molecules (proteins, lipids, nucleic acids) that result from cell lysis. Then isolation, identification, and purification of the factor under investigation require a more or less complex technology that includes extraction, centrifugation and various separation techniques. This calls for different chromatographic techniques when the expected protein has to be highly purified. Chr ⁇ matography is of greatest interest because it produces very good separation and opens way to many prospects. It is based essentially upon the various interactions between the molecules to be separated and the stationary phase constituting the support. These different techniques can be used separately or in combination.
  • the present invention relates to improved RP-HPLC methods for purifying recombinant proteins using simple and novel refolding procedures circumventing the use of complex refolding procedures and purification protocols.
  • Inclusion bodies containing the protein of interest can be produced as a general flow chart as listed in Figure 1.
  • the present invention is limited to the use of Reversed Phase High performance Liquid Chromatography (RP-HPLC) as a purification and subsequently refolding step in the production of highly pure refolded active rDNA derived proteins.
  • RP-HPLC Reversed Phase High performance Liquid Chromatography
  • Ion exchange and gel filtration are widely used in commercial production of recombinant molecules. These are known techniques that practically grew up with protein chemistry.
  • Reversed phase was developed primarily for the analysis of small molecules and its potential was mostly unrealized until the introduction of wide pore RP adsorbents in the 1980's.
  • the present invention relates to improved RP-HPLC methods for purifying recombinant proteins using simple and novel refolding procedures circumventing the use of complex refolding procedures and purification protocols.
  • the RP-HPLC methods comprise using wide pore preparative polystyrene hydrophobic matrix and solvent system consisting of but not limited to acetonitrile; isopropanol; ethano! or methanol as an organic modifier and an organic acid like but not limited to trifluoroacetic; acetic acid; hepta fluorobutaric acid etc.
  • the bonded phase is wide pore polystyrene/divinylbenzene matrix with a pore size of 30um or more preferably 30um using trifluoroacetic as organic acid.
  • the organic acid can also be acetic acid or hepta fluorobutaric acid etc.
  • the concentration can be 0.1 % to 0.3% preferably in the pH range 3-7 more preferably pH 6.
  • the elution can be isocratic or gradient, preferably gradient either linear or nonlinear, wherein the concentration of solvent is 0-100% preferably 20-80%.
  • the solvent consists of but is not limited to acetonitrile; isopropanol; ethano! or methanol.
  • the volume of elution is preferably balanced with the amount of sample loaded on to the column.
  • the process has been demonstrated in at least three rDNA derived biomolecules, like but not limited to recombinant human platelet derived growth factor-B; recombinant human interferon alpha 2b; recombinant human interferon gamma 1 b.
  • a skin wound is defined as a breach in the continuity of any body tissue caused by a minimal direct injury to the skin. There are many instances where a quick closure of the wounded skin will promote a beneficial response. Chronic, nonhealing wounds have plagued healthcare practitioners for decades.
  • PDGF-BB has been shown to be active in promoting wound healing in several " animal models.
  • Human platelet-derived growth factor has been shown to be the major mitogenic protein in serum for mesenchymal derived cells.
  • platelet extracts or purified PDGF-BB induces either cell multiplication or DNA synthesis in cultured smooth muscle ceils, fibroblasts and glial cells.
  • PDGF is a potent chemoattractant for cells that are responsive to it as a mitogen. This is also somewhat unusual in that mitogens generally do not also act as chemotactic agents.
  • PDGF-BB has therapeutic applications for the treatment of injuries, which require the proliferation of fibroblasts or smooth muscle cells to heal.
  • PDGF-BB has been shown to be active in promoting wound healing in several animal models.
  • Lynch et al disclose the use of insulin like growth factor (IGF-1) and purified PDGF- BB to promote healing of dermal wounds in pigs. These two growth factors showed a synergestic effect in promoting the healing.
  • Lynch et al also found that c combination PDGF-BB and IGF-1 promotes bone and cementum formation in a dog model of periodontitis.
  • Interferons are proteins naturally occurring in the body, which has antiviral, anti proliferative and immunoregulatory activity. In particular, it inhibits replication of a variety of RNA- and DNA-containing viruses, inhibits the growth of malignant cells, affects the expression of a variety of oncogenes and activates natural killer cells.
  • Recombinant human interferon alpha is used for the treatment of hairy cell leukemia, AIDS-related Kaposi's sarcoma and chronic hepatitis B and C.
  • interferon alpha leukocyte interferon
  • recombinant interferons are prepared from microbial source, e.g., E.
  • Recombinant DNA derived preparations should be highly pure and homogeneous with required biological activity. The purification of the recombinant material, therefore, plays a particularly important role.
  • the E.coii was used for the manufacture contains an expression vector incorporating the gene for expression of recombinant proteins.
  • E coli cells containing recombinant protein were harvested after fermentation, centrifuged, washed and lysed by sonicator/ bead beater.
  • the inclusion bodies were recovered by centrifugation and washed with buffer containing detergent. Finally, the inclusion bodies were purified by sucrose gradient centrifugation at 6000 rpm and inclusion body pellet was washed with distilled water and stored at -70 deg.C til! further use.
  • the human recombinant protein was extracted with 6M Guanidine Hydrochloride from inclusion body and loaded on to reverse phase polystyrene column (Resource 30 RPC) equilibrated with 30% Acetonitrile containing 0.1% TFA. The column was washed thoroughly with the starting buffer and the bound protein is eluted using 20- 80% Acetonitrile over 60 min. The monomeric form of recombinant protein is analyzed by SDS-PAGE. The pure monomer pooled fractions were concentrated and used for subsequent " purposes. The pooled fraction was diluted ten fold or higher in Tris CI buffer and left overnight for refolding. The refolded solution was concentrated by ultrafiltration and diafiltered extensively. The diafiltered sample was passed through 0.2u filter is almost 95% pure and has the activity comparing to the WHO standards. This protein is taken up for subsequent specific purifications depending on the nature of the biomolecule.
  • the method method herein described in the above examples is not limited to the examples given and is used for a variety of similar rDNA derived molecules like Recombinant Human lnterleukin-2.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Molecular Biology (AREA)
  • Biochemistry (AREA)
  • Biophysics (AREA)
  • General Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Proteomics, Peptides & Aminoacids (AREA)
  • General Chemical & Material Sciences (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Toxicology (AREA)
  • Zoology (AREA)
  • Gastroenterology & Hepatology (AREA)
  • Peptides Or Proteins (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)

Abstract

The present invention provides a simple and economical method for the purification of some recombinant proteins free from host proteins, wherein at least 90-95% pure recombinant proteins can be obtained. The method employs RP-HPLC as primary step using polystyrene based wide pore matrix wherein unfold monomer form of recombinant protein was isolated and used for refolding in a novel way. This process enables the monomer to be converted to active folded form. Depending on the protein, the folded form was further purified by either gel filtration or ion exchange chromatography wherein greater than 98% purity is obtained which meets the criteria for therapeutic proteins.

Description

PURIFICATION OF RECOMBINANT HUMAN PROTEINS.
Filed of the invention:
The present invention provides a simple and economical method for the purification of recombinant proteins free from host proteins, wherein at least 90- 95% pure recombinant proteins can be obtained.
Background of the Invention
Rapid developments in biotechnology, such as genetic engineering and downstream processing have effectively made possible the production of recombinant protein molecules. As the world moves towards more biological protein based therapies and as more companies produce recombinant deoxyribonudeic acid (rDNA) derived molecules the efficiency of the process assumes significance.
In addition to the ideal culture conditions and better expression systems, the importance of simplification of protein purification technology for the production of recombinant protein molecules in commercially viable quantities is necessitated today than ever before. A decrease in the number of purification steps, improvements of the yields, preservation of the biological activity, use of techniques strictly selected on the basis of their simplicity, high performance and reproducibility, and possible use of automated techniques are major objectives in defining conditions.
Biomolecules produced by rDNA technology can be endo or Intracellular proteins ('inside' the cell); Periplasmic (part of the cell wall) or extracellular proteins ('outside' the cell in the culture medium). They can be produced using a variety of organisms like E.coii; S.cerevisiae; P.pastoris etc. The present invention relates specifically to endocellular rDNA derived biomolecules produced in E.coii as 'inclusion bodies'.
Endocellular proteins have to be purified from a cell extract containing a complex mixture of molecules (proteins, lipids, nucleic acids) that result from cell lysis. Then isolation, identification, and purification of the factor under investigation require a more or less complex technology that includes extraction, centrifugation and various separation techniques. This calls for different chromatographic techniques when the expected protein has to be highly purified. Chrαmatography is of greatest interest because it produces very good separation and opens way to many prospects. It is based essentially upon the various interactions between the molecules to be separated and the stationary phase constituting the support. These different techniques can be used separately or in combination.
References
Ross et. All PNAS 71 ; 1207, 1974
Kohler and Lipton, Exp. Cell res. 87:297, 1974
Ross et.al J. Bid. Chem 257:5154, 1982
Grotendorst et al J Cell Physiol. 113:261 , 1982
Seppa et.al. J. Cell Biol, 92:584, 1982
Lynch et al PNAS 84:7696-7700, 1987
Lynch et al J Clin Periodontol 16:545-548, 1989 ''
Greebhalgh et al Am.J.Pathol 136:1235-1246, 1990
Thomason et al EPO 282,317 A2
Ettlin εt al, United States Patent 6005075, 1999.
Ettlin et al, European Patent Application No. 0679718 A2. 1995.
Beldarrain et al., Biotechnol. Appl. Biochem. (2001) 33, 173-182.
Swaminathan and Khanna, Protein Expression and Purification, (1999) 15, 263-242.
Thatcher and Panayotatos, Methods Enzymol. (1986) 119, 166-177.
Tarnowski et al., Methods Enzymol. (1986) 119, 153-165.
Haele yn and Dey Bio. And Mol. Biology Int. 37(6) 1163-1171 , 1995
Arora and Khanna, J. of Biotech. 52, 127-133, 1996
Emlen J Woodruff and Vlasselaer Peter Van US Pat 20010439062001 -11 -22
Ebbesen et al US pat. 5540923, 1996 July 30.
Khanna Navin I 183928, 200-05-20
Zhang and Tong, J. of Chrom. 604, 143-155, 1992
Vandenbroeck et al. EJB 213, 481-486, 1993
Objective of the Invention
The present invention relates to improved RP-HPLC methods for purifying recombinant proteins using simple and novel refolding procedures circumventing the use of complex refolding procedures and purification protocols. Inclusion bodies containing the protein of interest can be produced as a general flow chart as listed in Figure 1. The present invention is limited to the use of Reversed Phase High performance Liquid Chromatography (RP-HPLC) as a purification and subsequently refolding step in the production of highly pure refolded active rDNA derived proteins.
It is aim of this invention to show that this technique can used in the initial stages to provide a simple and trouble free method of purification of some recombinant DNA derived proteins free from host proteins wherein at least 90- 95% pure recombinant proteins can be obtained.
Brief Summary of the Invention:
Ion exchange and gel filtration are widely used in commercial production of recombinant molecules. These are known techniques that practically grew up with protein chemistry.
These previous methods used for the purification of rDNA derived proteins (either from yeast or E.coii) like cationic chromatography, gel filtration (or even reversed phase HPLC for that matter) resulted in yields that were low. Also the purified protein sometimes had clips or cleavages, which were still held together by disulfide bonds. In addition, further refolding parameters like different pH, oxidation and reduction systems using mercaptoethanol, DTT, glutathione and affinity chromatography like heparin sepharose column were also necessitated making the purification process lengthy and complex.
Reversed phase was developed primarily for the analysis of small molecules and its potential was mostly unrealized until the introduction of wide pore RP adsorbents in the 1980's.
Even after this its use was mostly limited to analytical scale due to the misconceptions about its practicality in the process scale and due to the apprehensions of loss of biological activity especially for recombinant proteins. This loss of biological activity is often attributed to the solvents used.
Though many a commercial chromatographic processes use RP today, it is mainly for what are referred colloquially as 'polishing' steps in the tertiary or end stage purification process. It is evident to those skilled in the art that this technique has not been used in the initial stages especially with respect to purification of endocellular recombinant DNA molecules produced in E.coii.
Thus there is need in the art of purification some rDNA derived molecules from E.Coli where in simplified quick procedure is followed leading to highly pure form with good activity and the procedure should be ensured free of problems of purification and refolding. The present invention provides such possibility over other related methods.
It is aim of this invention to show that this technique can used in the initial stages to provide a simple and trouble free method of purification of some recombinant DNA derived proteins free from host proteins wherein at least 90- 95% pure recombinant proteins can be obtained. The method employs RP-HPLC using polystyrene based wide pore matrix wherein unfolded monomer form of recombinant protein was isolated and used for refolding in a novel way. This process enables the monomer to be converted to active folded form in a simplified unique step that greatly increases the yield and reduce the need for elaborate multi stage processes.
This process has demonstrated in three different molecules but is not limited in any way to these three molecules. It is the claim of this invention that this process can be used for a purification of range of rDNA derived inclusion body proteins produced in E.coii. Detailed Description of the invention:
In one aspect, the present invention relates to improved RP-HPLC methods for purifying recombinant proteins using simple and novel refolding procedures circumventing the use of complex refolding procedures and purification protocols.
The RP-HPLC methods comprise using wide pore preparative polystyrene hydrophobic matrix and solvent system consisting of but not limited to acetonitrile; isopropanol; ethano! or methanol as an organic modifier and an organic acid like but not limited to trifluoroacetic; acetic acid; hepta fluorobutaric acid etc.
The bonded phase is wide pore polystyrene/divinylbenzene matrix with a pore size of 30um or more preferably 30um using trifluoroacetic as organic acid. The organic acid can also be acetic acid or hepta fluorobutaric acid etc. The concentration can be 0.1 % to 0.3% preferably in the pH range 3-7 more preferably pH 6.
The elution can be isocratic or gradient, preferably gradient either linear or nonlinear, wherein the concentration of solvent is 0-100% preferably 20-80%. The solvent consists of but is not limited to acetonitrile; isopropanol; ethano! or methanol. The volume of elution is preferably balanced with the amount of sample loaded on to the column.
After obtaining the refolded form of the protein subsequent steps of the purification are undertaken with specific consideration of the protein in particular to obtain >98% pure protein.
The process has been demonstrated in at least three rDNA derived biomolecules, like but not limited to recombinant human platelet derived growth factor-B; recombinant human interferon alpha 2b; recombinant human interferon gamma 1 b.
A skin wound is defined as a breach in the continuity of any body tissue caused by a minimal direct injury to the skin. There are many instances where a quick closure of the wounded skin will promote a beneficial response. Chronic, nonhealing wounds have plagued healthcare practitioners for decades. In this regard PDGF-BB has been shown to be active in promoting wound healing in several" animal models. Human platelet-derived growth factor has been shown to be the major mitogenic protein in serum for mesenchymal derived cells. A number of studies reported that platelet extracts or purified PDGF-BB induces either cell multiplication or DNA synthesis in cultured smooth muscle ceils, fibroblasts and glial cells. Furthermore PDGF is a potent chemoattractant for cells that are responsive to it as a mitogen. This is also somewhat unusual in that mitogens generally do not also act as chemotactic agents.
PDGF-BB has therapeutic applications for the treatment of injuries, which require the proliferation of fibroblasts or smooth muscle cells to heal. In this regard PDGF-BB has been shown to be active in promoting wound healing in several animal models. Lynch et al disclose the use of insulin like growth factor (IGF-1) and purified PDGF- BB to promote healing of dermal wounds in pigs. These two growth factors showed a synergestic effect in promoting the healing. Lynch et al also found that c combination PDGF-BB and IGF-1 promotes bone and cementum formation in a dog model of periodontitis. In addition Greenhalgh et a! demonstrated enhanced healing of full-thickness skin wounds in genetically diabetic mice treated with recombinant PDGF-BB as compared to control animals. Thomason et al disclose that recombinant PDGF-BB accelerates the gain in tensile strength of healing skin wounds in rats and promotes wound healing in diabetic rats.
Interferons are proteins naturally occurring in the body, which has antiviral, anti proliferative and immunoregulatory activity. In particular, it inhibits replication of a variety of RNA- and DNA-containing viruses, inhibits the growth of malignant cells, affects the expression of a variety of oncogenes and activates natural killer cells. Recombinant human interferon alpha is used for the treatment of hairy cell leukemia, AIDS-related Kaposi's sarcoma and chronic hepatitis B and C. Before recombinant DNA technology, interferon alpha (leukocyte interferon) used to be prepared from natural sources, human leukocyte. Today, recombinant interferons are prepared from microbial source, e.g., E. coli and therefore, after their isolation from the micro organism or from the culture medium they are initially contaminated by a series of microbial impurities presence of which is prohibitive for a therapeutic use of the proteins produced this way. Recombinant DNA derived preparations should be highly pure and homogeneous with required biological activity. The purification of the recombinant material, therefore, plays a particularly important role.
Example
The E.coii was used for the manufacture contains an expression vector incorporating the gene for expression of recombinant proteins. E coli cells containing recombinant protein were harvested after fermentation, centrifuged, washed and lysed by sonicator/ bead beater. The inclusion bodies were recovered by centrifugation and washed with buffer containing detergent. Finally, the inclusion bodies were purified by sucrose gradient centrifugation at 6000 rpm and inclusion body pellet was washed with distilled water and stored at -70 deg.C til! further use.
The human recombinant protein was extracted with 6M Guanidine Hydrochloride from inclusion body and loaded on to reverse phase polystyrene column (Resource 30 RPC) equilibrated with 30% Acetonitrile containing 0.1% TFA. The column was washed thoroughly with the starting buffer and the bound protein is eluted using 20- 80% Acetonitrile over 60 min. The monomeric form of recombinant protein is analyzed by SDS-PAGE. The pure monomer pooled fractions were concentrated and used for subsequent "purposes. The pooled fraction was diluted ten fold or higher in Tris CI buffer and left overnight for refolding. The refolded solution was concentrated by ultrafiltration and diafiltered extensively. The diafiltered sample was passed through 0.2u filter is almost 95% pure and has the activity comparing to the WHO standards. This protein is taken up for subsequent specific purifications depending on the nature of the biomolecule.
The method method herein described in the above examples is not limited to the examples given and is used for a variety of similar rDNA derived molecules like Recombinant Human lnterleukin-2.

Claims

1. A method for purification of human recombinant proteins wherein a polystyrene reversed phase column was used to purify unfolded recombinant protein using the unfolded monomeric protein loaded on to this column comprising monomer of recombinant protein was eluted and a organic acid is used.
2. A method of purification according to claim 1 wherein a completely folded form of recombinant proteins of at least 90- 95% purity is obtained in a few simple steps.
3. The method according to claim 1 , wherein monomer of recombinant protein was eluted using 0-100% linear gradient of organic solvent like but not limited to acetonitrile; isopropanol; ethanol or methanol
4. The method according to claim 1 , wherein the organic acid is 0.1 %-0.3%, trifluroacetic acid or any other organic acid like but not limited to acetic acid or hepta fluorobutaric acid was used,
5. The method according to claim 1 , wherein monomer was collected and refolded by diluting to ten fold or higher in TRIS or any other neutral buffer with pH 7-8 at 20 mM-100mM concentration,
6. The method according to claim 1 , wherein the protein concentration was maintained between 10ug-200ug during refolding
7. The method according to claim 1 , wherein refolded protein was concentrated and diafiltered to give at least 90%-95% folded protein.
8. The method of according to claim 1 , wherein, refolded, diafiltered and concentrated was purified recombinant protein further by which at least 98% pure was obtained which the specific activity higher than the WHO standards. The method according to claim 1 , wherein the method is not limited to the examples given and is used for a variety of similar rDNA derived molecules like Recombinant Human lnterleukin-2.
PCT/IN2005/000045 2004-02-11 2005-02-11 Purification of recombinant human proteins Ceased WO2005077973A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
IN107/CHE/2004 2004-02-11
IN107CH2004 2004-02-11

Publications (1)

Publication Number Publication Date
WO2005077973A1 true WO2005077973A1 (en) 2005-08-25

Family

ID=34856858

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/IN2005/000045 Ceased WO2005077973A1 (en) 2004-02-11 2005-02-11 Purification of recombinant human proteins

Country Status (1)

Country Link
WO (1) WO2005077973A1 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10071182B2 (en) 2014-10-14 2018-09-11 Samuel E. Lynch Methods for treating wounds
WO2024264071A1 (en) 2023-06-23 2024-12-26 Lynch Samuel E Methods and compositions for skin repair, rejuvenation and comfort

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1439191A1 (en) * 2004-01-19 2004-07-21 Ares Trading S.A. Process for the purification of bacterially expressed proteins

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1439191A1 (en) * 2004-01-19 2004-07-21 Ares Trading S.A. Process for the purification of bacterially expressed proteins

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
CARR D.: "The Handbook of Analysis and Purification of Peptides and Proteins by Reversed-Phase HPLC.", 2002, GRACEVYDAG. *
MUSACCHIO A. ET AL: "Recombinant Opoc meningococcal protein folded in vitro, elicits bactericidal antibodies after immunization.", VACCINE., vol. 15, no. 6-7, 1997, pages 751 - 758 *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10071182B2 (en) 2014-10-14 2018-09-11 Samuel E. Lynch Methods for treating wounds
WO2024264071A1 (en) 2023-06-23 2024-12-26 Lynch Samuel E Methods and compositions for skin repair, rejuvenation and comfort

Similar Documents

Publication Publication Date Title
US4667016A (en) Erythropoietin purification
EP3398964B1 (en) Chromatographic method for isolating and purifying high-purity recombined human serum albumin
US4432895A (en) Monomeric interferons
KR101831300B1 (en) Method of purifying human granulocyte-colony stimulating factor from recombinant e. coli
JP3894570B2 (en) Methods for purifying IGF-I
EP0401941A2 (en) Hepatitis B virus surface antigen and production thereof
EP0228452B1 (en) Protein purification
JP6742300B2 (en) Novel process for purification of rHu-GCSF
CN103288953A (en) A method for separating and purifying functional proteins in plasma
MXPA02006303A (en) Process for the purification of pharmacologically active proteins through cationic exchange chromatography.
EP2051989A1 (en) One step imac (mcac) purification of proteins
JP2002128795A (en) Method for removing human serum albumin polymer
JP6232130B2 (en) Method for purifying darbepoetin alfa
CN102702341A (en) Recombinant human nerve growth factor purifying method based on CHO cell expression system
Khan et al. Large-scale production of recombinant proteins: human leukocyte interferon
WO2005077973A1 (en) Purification of recombinant human proteins
JP2009501195A (en) Method for purifying G-CSF
JPS6261040B2 (en)
Dasari et al. Optimization of the downstream process for high recovery of rhG-CSF from inclusion bodies expressed in Escherichia coli
WO2020234742A1 (en) Granulocyte colony stimulating factor purification
KR100531670B1 (en) Processes for preparing interferon alpha
Wang et al. Renaturation with simultaneous purification of rhG‐CSF from Escherichia coli by ion exchange chromatography
Misterova et al. Optimization of a Purification Method for the Recombinant Platelet-Derived Growth Factor rhPDGF-BB Expressed in the Methylotrophic Yeast Pichia Pastoris
Wang et al. Chromatographic refolding of proteins: molecular action and column control
CN111434676A (en) A kind of preparation method of hepatitis B virus HBV-derived HBx protein

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A1

Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BW BY BZ CA CH CN CO CR CU CZ DE DK DM DZ EC EE EG ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KP KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NA NI NO NZ OM PG PH PL PT RO RU SC SD SE SG SK SL SY TJ TM TN TR TT TZ UA UG US UZ VC VN YU ZA ZM ZW

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): BW GH GM KE LS MW MZ NA SD SL SZ TZ UG ZM ZW AM AZ BY KG KZ MD RU TJ TM AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LT LU MC NL PL PT RO SE SI SK TR BF BJ CF CG CI CM GA GN GQ GW ML MR NE SN TD TG

121 Ep: the epo has been informed by wipo that ep was designated in this application
NENP Non-entry into the national phase

Ref country code: DE

WWW Wipo information: withdrawn in national office

Country of ref document: DE

122 Ep: pct application non-entry in european phase