WO2003055900A1 - Peptide purification - Google Patents

Peptide purification Download PDF

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Publication number
WO2003055900A1
WO2003055900A1 PCT/IB2002/005581 IB0205581W WO03055900A1 WO 2003055900 A1 WO2003055900 A1 WO 2003055900A1 IB 0205581 W IB0205581 W IB 0205581W WO 03055900 A1 WO03055900 A1 WO 03055900A1
Authority
WO
WIPO (PCT)
Prior art keywords
solvent mixture
nona
decapeptide
precipitation
water
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/IB2002/005581
Other languages
English (en)
French (fr)
Inventor
Jon H. Rasmussen
Palle H. Rasmussen
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.)
Polypeptide Laboratories AS
Original Assignee
Polypeptide Laboratories AS
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
Priority to AT02783479T priority Critical patent/ATE449784T1/de
Priority to KR1020047010363A priority patent/KR100880828B1/ko
Priority to AU2002347550A priority patent/AU2002347550B2/en
Priority to CA2471717A priority patent/CA2471717C/en
Priority to IL16278902A priority patent/IL162789A0/xx
Priority to DE60234535T priority patent/DE60234535D1/de
Priority to US10/500,302 priority patent/US7057014B2/en
Priority to NZ534151A priority patent/NZ534151A/en
Priority to DK02783479.5T priority patent/DK1468009T3/da
Application filed by Polypeptide Laboratories AS filed Critical Polypeptide Laboratories AS
Priority to HK05108061.2A priority patent/HK1076112B/xx
Priority to EP02783479A priority patent/EP1468009B1/en
Priority to JP2003556430A priority patent/JP4378173B2/ja
Publication of WO2003055900A1 publication Critical patent/WO2003055900A1/en
Priority to ZA2004/05135A priority patent/ZA200405135B/en
Priority to IL162789A priority patent/IL162789A/en
Anticipated expiration legal-status Critical
Priority to NO20043046A priority patent/NO329024B1/no
Ceased legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07KPEPTIDES
    • C07K7/00Peptides having 5 to 20 amino acids in a fully defined sequence; Derivatives thereof
    • C07K7/04Linear peptides containing only normal peptide links
    • C07K7/06Linear peptides containing only normal peptide links having 5 to 11 amino acids
    • 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
    • C07K1/30Extraction; Separation; Purification by precipitation

Definitions

  • the present invention relates to the purification of peptides, in particular intermediate-size peptides, more particularly nona- and decapeptides, such as LHRH-antagonists.
  • the LHRH antagonist (I) and nona- and decapeptides of similar structure are essentially pure.
  • the raw product obtained in the last step of a multiple-step synthesis is purified by chromatographic and other methods. To eliminate residual solvent from the chromatography a thus purified product usually has to be dissolved in an aqueous medium and freeze- dried. This is a costly process producing a voluminous product which is not easy to handle.
  • a process of purification of an otherwise pure peptide from residual organic solvent by other means than freeze-drying thus is desirable.
  • a process of purification of an otherwise pure peptide, in particular a nona- or decapeptide, most particularly a nona- or decapeptide which is an LHRH antagonist, from residual organic solvent comprising the following steps: - dissolving said otherwise pure peptide in a dissolution solvent mixture comprising water and at least one alcohol selected from methan ⁇ l, ethanol, propanol, isopropanol;
  • a vigorously stirred precipitation solvent mixture essentially consisting of one or several polar compounds selected from methyl acetate, ethyl acetate, methyl propionate, ethyl propionate, ethyl isopropionate, butyl acetate, isobutyl acetate, t-butyl acetate, ethyl formate, propyl formate, isopropyl formate, and one or several non- polar compounds selected from hexane, heptane, octane, cyclohexane, methylcyclohexane, and, optionally, of up to 5% of acetic or propionic acid;
  • An otherwise pure peptide is a peptide which is sufficiently pure for use in a medicine except for volatile impurities which need to be removed or the content of which needs to be substantially reduced.
  • the otherwise pure peptide will normally be a substance having undergone purification by chromatography.
  • the otherwise pure peptide is N-(2-aminoethyl)-2-aminoethyl-N-(2-aminoethyl)-2-aminoethyl-N-(2-aminoethyl)-2-aminoethyl-N-(2-aminoethyl)-2-aminoethyl-N-(2-aminoethyl)-2-aminoethyl-N-(2-aminoethyl)-2-aminoethyl-N-(2-aminoethyl)-2-aminoethyl-N-(2-aminoethyl)-2-aminoethyl-N-(2-aminoethyl)-2-aminoethyl-N-(2-aminoethyl)-2-aminoethyl-N-(2-aminoethyl)-2-aminoethyl-N
  • the water content of the dissolution solvent mixture is below 5% (v/v) .
  • the volume ratio of the dissolution solvent mixture and the precipitation solvent mixture is at least 15, in particular at least 20.
  • the alcohol of the dissolution solvent mixture is ethanol .
  • the polar component of the precipitation solvent mixture is ethyl acetate.
  • the non-polar component of the precipitation solvent mixture is heptane .
  • Example 1 The fractions containing pure compound (1) (100 g in total) in ethanol-water-acetic acid 40:59:1 (v/v/v) obtained from preparative HPLC by which the synthetically obtained product had been purified were pooled and concentrated in vacuo to an oil which was co-evaporated twice from ethanol. The resulting solid was dissolved in 440 ml of ethanol and the resulting clear solution added over a period of 20 min to 8.8 L of ethyl acetate/heptane 1:1 (v/v). Stirring was continued for 1 hour and filtered. The amorphous product was washed with 3 L of ethyl acetate; it was found that this removed nearly all heptane. The washed product was dried in a vacuum oven at 40oC at 0.3 bar for 48 hrs .
  • Example 2 Variation of the composition of the precipitation solvent or solvent mixture; otherwise, procedure as in Example 1.
  • Precipitation in pure ethyl acetate results in from about 3% to about 5% by weight loss of peptide.
  • Precipitation in pure heptane results in a sticky pr.oduct which is difficult to filter.
  • a 1:1 (v/v) mixture of ethyl-acetate hexane gives a product which is easy to filter and dry; in repeated experiments the loss of peptide was always less than 0.5% by weight.
  • Example 3.Variation of water content of the solution of oily product in the dissolution solvent (absolute ethanol) otherwise, procedure as in Example 1.
  • a water content of 10% (v/v) results in a sticky product on precipitation which is difficult to filter.
  • a water content of 15% (v/v) results in an oily product on precipitation.
  • the water content must not exceed 8% (v/v) but should preferably be kept below 5% (v/v) .
  • a water content below 5% is accomplished by co-evaporating the oily product from the chromatography at least twice with ethanol.
  • Example 4 Variation in precipitation temperature; otherwise, procedure as in Example 1.
  • the precipitation temperature proved to be not critical. It could be varied from 0°C to 20°C without noticeable differences in product yield and morphology.
  • Example 5 Variation of concentration of (I) in the dissolution solvent; otherwise, procedure as in Example 1. It was found that the concentration of the oily product from the chromatography which had been co-evaporated with ethanol in the dissolution solvent should be as high as possible. Even a concentration of 330 g by weight could be used.
  • Example 6 Variation of ratio between dissolution solvent and precipitation solvent volumes and other variations; otherwise, procedure as in Example 1. The optimum ratio was found to be about 1:20. It could be shown that ratios from 1:15 to 1:30 gave satisfactory results. A ratio of 1:10 resulted in a sticky product. Precipitation is very fast. The suspension can be filtered 30 min after the last addition of dissolved substance. Washing with ethyl acetate did not result in loss of product but efficiently removed heptane.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Genetics & Genomics (AREA)
  • Biochemistry (AREA)
  • Biophysics (AREA)
  • General Health & Medical Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Molecular Biology (AREA)
  • Proteomics, Peptides & Aminoacids (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Peptides Or Proteins (AREA)
  • Medicines That Contain Protein Lipid Enzymes And Other Medicines (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
PCT/IB2002/005581 2001-12-29 2002-12-23 Peptide purification Ceased WO2003055900A1 (en)

Priority Applications (15)

Application Number Priority Date Filing Date Title
DK02783479.5T DK1468009T3 (da) 2001-12-29 2002-12-23 Peptidoprensning
AU2002347550A AU2002347550B2 (en) 2001-12-29 2002-12-23 Peptide purification
HK05108061.2A HK1076112B (en) 2001-12-29 2002-12-23 Peptide purification
IL16278902A IL162789A0 (en) 2001-12-29 2002-12-23 Peptide furification
DE60234535T DE60234535D1 (de) 2001-12-29 2002-12-23 Peptid aufreinigung
US10/500,302 US7057014B2 (en) 2001-12-29 2002-12-23 Peptide purification
NZ534151A NZ534151A (en) 2001-12-29 2002-12-23 A process of purification of an otherwise pure nona- or decapeptide from residual organic solvent
AT02783479T ATE449784T1 (de) 2001-12-29 2002-12-23 Peptid aufreinigung
CA2471717A CA2471717C (en) 2001-12-29 2002-12-23 Process of purification of a nona-or deca peptide from residual organic solvent
KR1020047010363A KR100880828B1 (ko) 2001-12-29 2002-12-23 펩타이드 정제
EP02783479A EP1468009B1 (en) 2001-12-29 2002-12-23 Peptide purification
JP2003556430A JP4378173B2 (ja) 2001-12-29 2002-12-23 ペプチド精製
ZA2004/05135A ZA200405135B (en) 2001-12-29 2004-06-28 Peptide purification
IL162789A IL162789A (en) 2001-12-29 2004-06-29 Peptide purification
NO20043046A NO329024B1 (no) 2001-12-29 2004-07-16 Peptidrensing

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
SE0104462A SE0104462D0 (sv) 2001-12-29 2001-12-29 Peptide purifcation (Peptidrening)
SE0104462-7 2001-12-29

Publications (1)

Publication Number Publication Date
WO2003055900A1 true WO2003055900A1 (en) 2003-07-10

Family

ID=20286556

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/IB2002/005581 Ceased WO2003055900A1 (en) 2001-12-29 2002-12-23 Peptide purification

Country Status (18)

Country Link
US (1) US7057014B2 (enExample)
EP (1) EP1468009B1 (enExample)
JP (1) JP4378173B2 (enExample)
KR (1) KR100880828B1 (enExample)
CN (1) CN1272341C (enExample)
AT (1) ATE449784T1 (enExample)
AU (1) AU2002347550B2 (enExample)
CA (1) CA2471717C (enExample)
DE (1) DE60234535D1 (enExample)
DK (1) DK1468009T3 (enExample)
ES (1) ES2350880T3 (enExample)
IL (2) IL162789A0 (enExample)
NO (1) NO329024B1 (enExample)
NZ (1) NZ534151A (enExample)
RU (1) RU2303040C2 (enExample)
SE (1) SE0104462D0 (enExample)
WO (1) WO2003055900A1 (enExample)
ZA (1) ZA200405135B (enExample)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006077428A1 (en) 2005-01-21 2006-07-27 Astex Therapeutics Limited Pharmaceutical compounds
WO2008044045A1 (en) 2006-10-12 2008-04-17 Astex Therapeutics Limited Pharmaceutical combinations
WO2008044041A1 (en) 2006-10-12 2008-04-17 Astex Therapeutics Limited Pharmaceutical combinations
EP2062909A1 (en) * 2007-11-21 2009-05-27 SOLVAY (Société Anonyme) Peptide production and purification process
US9051349B2 (en) 2007-11-21 2015-06-09 Alba Therapeutics Corporation Larazotide acetate compositions

Families Citing this family (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1359722A1 (en) * 2002-03-27 2003-11-05 BRITISH TELECOMMUNICATIONS public limited company Data streaming system and method
EP2280993A1 (en) * 2008-05-15 2011-02-09 Novo Nordisk A/S Purification of peptides prepared by solid phase synthesis
EP2417152B1 (en) * 2009-04-10 2013-10-02 Corden Pharma Colorado, Inc. Process for isolating linaclotide
BR112015013444B1 (pt) 2012-12-13 2022-11-01 Immunomedics, Inc Uso de um imunoconjugado
US9931417B2 (en) 2012-12-13 2018-04-03 Immunomedics, Inc. Antibody-SN-38 immunoconjugates with a CL2A linker
US9107960B2 (en) * 2012-12-13 2015-08-18 Immunimedics, Inc. Antibody-SN-38 immunoconjugates with a CL2A linker
AU2014293670B2 (en) * 2013-07-23 2019-08-01 Immunomedics, Inc. Antibody-SN-38 immunoconjugates with a CL2A linker
AU2017257254B2 (en) 2016-04-27 2022-02-24 Immunomedics, Inc. Efficacy of anti-Trop-2-SN-38 antibody drug conjugates for therapy of tumors relapsed/refractory to checkpoint inhibitors
RU2758234C2 (ru) 2017-03-27 2021-10-26 Иммьюномедикс, Инк. ЛЕЧЕНИЕ ТРИЖДЫ НЕГАТИВНОГО РАКА МОЛОЧНОЙ ЖЕЛЕЗЫ, ХАРАКТЕРИЗУЮЩЕГОСЯ ЭКСПРЕССИЕЙ Trop-2, С ПОМОЩЬЮ САЦИТУЗУМАБА ГОВИТЕКАНА И ИНГИБИТОРА Rad51
CN110352201A (zh) 2017-04-03 2019-10-18 免疫医疗公司 用于癌症疗法的抗体药物缀合物的皮下施用
CN113952944B (zh) * 2021-12-23 2022-03-29 浙江湃肽生物有限公司深圳分公司 一种纯化九肽-1的方法

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0136728A2 (en) * 1983-06-29 1985-04-10 Shell Internationale Researchmaatschappij B.V. Process for the dissolution of peptides and proteins, solutions thereby obtained and their use
WO1991010677A1 (de) * 1990-01-18 1991-07-25 Basf Aktiengesellschaft Verfahren zur anreicherung bzw. reinigung von biomolekülen
EP0955308A1 (de) * 1998-03-27 1999-11-10 Degussa-Hüls Aktiengesellschaft Verfahren zur einstufigen Umsalzung und Aufreinigung von Oligopeptiden
WO2000018423A1 (en) * 1998-09-30 2000-04-06 Laboratoire Theramex Pharmaceutical compositions based on alpha-cyclodextrin for the oral administration of lh-rh analogues
WO2000055190A1 (de) * 1999-03-17 2000-09-21 Zentaris Ag Neue lhrh-antagonisten mit verbesserten löslichkeitseigenschaften

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19544212A1 (de) * 1995-11-28 1997-06-05 Asta Medica Ag Neue LH-RH-Antagonisten mit verbesserter Wirkung

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0136728A2 (en) * 1983-06-29 1985-04-10 Shell Internationale Researchmaatschappij B.V. Process for the dissolution of peptides and proteins, solutions thereby obtained and their use
WO1991010677A1 (de) * 1990-01-18 1991-07-25 Basf Aktiengesellschaft Verfahren zur anreicherung bzw. reinigung von biomolekülen
EP0955308A1 (de) * 1998-03-27 1999-11-10 Degussa-Hüls Aktiengesellschaft Verfahren zur einstufigen Umsalzung und Aufreinigung von Oligopeptiden
WO2000018423A1 (en) * 1998-09-30 2000-04-06 Laboratoire Theramex Pharmaceutical compositions based on alpha-cyclodextrin for the oral administration of lh-rh analogues
WO2000055190A1 (de) * 1999-03-17 2000-09-21 Zentaris Ag Neue lhrh-antagonisten mit verbesserten löslichkeitseigenschaften

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006077428A1 (en) 2005-01-21 2006-07-27 Astex Therapeutics Limited Pharmaceutical compounds
WO2008044045A1 (en) 2006-10-12 2008-04-17 Astex Therapeutics Limited Pharmaceutical combinations
WO2008044041A1 (en) 2006-10-12 2008-04-17 Astex Therapeutics Limited Pharmaceutical combinations
EP2062909A1 (en) * 2007-11-21 2009-05-27 SOLVAY (Société Anonyme) Peptide production and purification process
WO2009065949A3 (en) * 2007-11-21 2009-07-30 Solvay Peptide production and purification process
US9051349B2 (en) 2007-11-21 2015-06-09 Alba Therapeutics Corporation Larazotide acetate compositions

Also Published As

Publication number Publication date
CA2471717A1 (en) 2003-07-10
NO20043046L (no) 2004-08-30
ATE449784T1 (de) 2009-12-15
US20060014694A1 (en) 2006-01-19
EP1468009B1 (en) 2009-11-25
NO329024B1 (no) 2010-08-02
ES2350880T3 (es) 2011-01-27
EP1468009A1 (en) 2004-10-20
IL162789A (en) 2010-04-29
JP2005515217A (ja) 2005-05-26
SE0104462D0 (sv) 2001-12-29
AU2002347550A1 (en) 2003-07-15
CN1625561A (zh) 2005-06-08
US7057014B2 (en) 2006-06-06
DK1468009T3 (da) 2010-04-06
KR20040090966A (ko) 2004-10-27
IL162789A0 (en) 2005-11-20
CA2471717C (en) 2013-06-18
HK1076112A1 (en) 2006-01-06
ZA200405135B (en) 2005-08-31
DE60234535D1 (de) 2010-01-07
JP4378173B2 (ja) 2009-12-02
KR100880828B1 (ko) 2009-01-30
NZ534151A (en) 2007-05-31
RU2303040C2 (ru) 2007-07-20
AU2002347550B2 (en) 2008-01-03
RU2004119965A (ru) 2006-01-10
CN1272341C (zh) 2006-08-30

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