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人凝血因子Ⅷ制备工艺在放大过程中的稳定性研究 被引量:4

Study on the stability of human coagulation factor Ⅷ process during development
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摘要 目的评价人凝血因子Ⅷ制备工艺在放大过程的稳定性。方法人凝血因子Ⅷ工艺放大依次经过BPG50小试阶段、BPG 100中试阶段和BPG 300规模化制备阶段。按《中国药典》2010版三部要求,对工艺放大过程中制品关键质量指标,如蛋白质含量、人凝血因子Ⅷ效价、吐温80残留量、磷酸三丁酯残留量、外观、可见异物、水分、热原和异常毒性等指标进行分析。结果冷沉淀溶解效果稳定,FⅧ回收率依次为(46.8±8.8)%、(46.4±8.2)%和(43.7±5.4)%(P>0.05);S/D处理对FⅧ无显著性影响,FⅧ回收率依次为(95±22)%、(111±20)%和(102±8)%(P>0.05);层析过程对杂蛋白去除效果明显,比活提高倍数分别为(52.4±23.2)、(45.8±17.2)和(55.3±5.6)倍(P>0.05),对吐温80和磷酸三丁酯去除效果稳定,Tween-80残留量分别为(10±1.8)、(8.7±3.5)和(11.3±1.5)μg·m L-1(P>0.05),磷酸三丁酯残留量分别为(0.27±0.31)、(1.2±2.6)和0μg·m L-1(P>0.05);干热处理对FⅧ活性、外观和可见异物指标无显著性影响,FⅧ回收率分别为(90±6)%、(92±4)%和(94±3)%(P>0.05)。3种规模制备的人凝血因子Ⅷ成品关键质量指标稳定。结论该工艺放大过程稳定可靠,适合于人凝血因子Ⅷ规模化制备。 Objective To evaluate the stability of human coagulation factor Ⅷ process during its development. Methods The development process of human coagulation factor Ⅷ included BPG 50 laboratory scale, BPG 100 pilot scale and BPG300 industry scale. The critical test items included protein content,FⅧ activity,Tween 80 content,tri( n-butyl) phosphate( TNBP) content,appearance,visible foreign matter,moisture,pyrogen test and abnormal toxicity test,which were determined according to the requirements in Chinese Pharmacopeia 2010 edition( Volume Ⅲ). Results During scale-up process,cryoprecipitate could be dissolved stably. The recovery rates of FⅧ were 46. 8 ± 8. 8%,46. 4 ± 8. 2% and 43. 7 ± 5. 4%( P 〉0. 05),respectively. The S / D treatment had no significant influence on FⅧ activity. The recovery rates of FⅧ were 95 ± 22%,111 ± 20% and 102 ± 8%( P 〉0. 05),respectively. The chromatographic process could remove hybrid protein,Tween 80 and TNBP obviously. The ratio of the increase in specific activity were 52. 4 ± 23. 2,45. 8 ± 17. 2 and 55. 3 ± 5. 6( P 〉0. 05),respectively. The residual amounts of Tween-80 were 10 ± 1. 8,8. 7 ± 3. 5 and 11. 3 ± 1. 5μg·m L^- 1( P〉 0. 05),respectively. The residual amounts of phosphate were 0. 27 ± 0. 31 and 1. 2 ± 2. 6 and 0μg·m L^- 1( P〉 0. 05),respectively. The dry-heat treatment had no significant influence on FⅧ activity,appearance nor visible foreign matter. The recovery rates of FⅧ were 90 ± 6%,92 ± 4% and 94± 3%( P〉 0. 05),respectively. The critical test items of human coagulation factor Ⅷ remained stable during scale-up process. Conclusion The scale-up process is stable and reliable,and is suitable for FⅧ preparation.
出处 《中国输血杂志》 CAS 北大核心 2015年第11期1366-1369,共4页 Chinese Journal of Blood Transfusion
基金 国家高技术研究发展计划(863计划2012AA021904) 四川省科技计划项目(2014SZ0123) 国药集团新产品基金(2011SW10-3)
关键词 人凝血因子Ⅷ 工艺放大 稳定性 human coagulation factor Ⅷ development process stability
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参考文献15

  • 1赵艳华.凝血因子Ⅷ研究和应用的现状与前景[J].生物技术通讯,2002,13(6):473-475. 被引量:5
  • 2Keeling D,Tait C,Makris M.Guidelines on the selection and use of therapeutic products to treat haemophilia and other hereditary bleeding disorders.Haemophilia,2008,14(4):671-684.
  • 3Srivastava A,Brewer AK,Mauser-Bunschoten EP,et al.Guidelines for the management of hemophilia.Haemophilia,2013,19(1):1-47.
  • 4Wagner RH,Mc Lester WD,Smith M,et al.Purification of anti-hemophilic factor(factorⅧ)by amino acid precipitation.Thromb Diath Haemorrh,1964,11:64-74.
  • 5Burnouf T,Burnouf-Radosevich M,Huart JJ,et al.A highly purified factorⅧ:c concentrate prepared from cryoprecipitate by ion-exchange chromatography.Vox Sang,1991,60(1):8-15.
  • 6Weinstein RE.Immunoaffinity purification of factorⅧ.Ann Clin Lab Sci,1989,19(2):84-91.
  • 7Philipp CS,Monoclate-P Study Group.Viral safety of a pasteurized,monoclonal antibody-purified factorⅧconcentrate in previously untreated haemophilia A patients.Haemophilia,2001,7(2):146-153.
  • 8Mark Brooker.Registry of clotting factor concentrates,9th Edition,World Federation of Hemophilia,2012:5-6.
  • 9牟蕾,袁进,何勤.S/D法用于人凝血因子Ⅷ病毒灭活效果验证[J].中国输血杂志,2001,14(4):222-223. 被引量:3
  • 10余伟,赵辉,刘文芳.病毒灭活/去除工艺与血液制品病毒安全性[J].中国输血杂志,2009,22(7):606-610. 被引量:18

二级参考文献66

  • 1中华人民共和国卫生部.中国生物制品规程[M].北京:卫生部生物制品标准化委员会,1995.212.
  • 2Biesert L. Virus validation studies of immunoglobulin preparations. Clin Exp Rheumatol, 1996,14( Suppl 15) : 47-52.
  • 3Louie RE, Galloway CJ, Dumas ML, et al. Inactivation of hepatitis C virus in low pH intravenous immunoglobulin. Biologicals, 1994, 22( 1 ) : 13-19.
  • 4Kempf C, Jentsch P, Poirier B, et al. Virus inactivation during production of intravenous immunoglobulin. Transfusion, 1991,31 (5) :423-427.
  • 5Bos OJ, Sunye DG, Nieuweboer CE, et al. Virus validation of pH 4-treated human immunoglobulin products produced by the Cohn fractionatlon process. Biologicals, 1998,26 ( 4 ) :267-276.
  • 6Baxter Healthcare Corporation. GAMMAGARD LIQUID [ Immune Globulin Intravenous (Human) 10% ]package insert. Westlake Village, CA: Baxter Heahhcare Corporation, April 2005.
  • 7Boschetti N, Niederhauser I, Kempf C, et al. Different susceptibility of B19 virus and mice minute vires to low pH treatment. Transfusion ,2004,44( 7 ) : 1079-1086.
  • 8Johnston A, Uren E, Johnstone D, et al. Low pH, caprylate incubation as a second viral inactivation step in the manufacture of albumin Parametric and validation studies. Biologicals,2003,31 (3): 213-221.
  • 9Korneyeva M, Hotta J, Lebing W, et al. Enveloped virus inactivation by caprylate: a robust alternative to solvent-detergent treatment in plasma derived intermediates. Biologicals,2002,30 (2) : 153-162.
  • 10Talecris Biotherapeutics, Inc. Gamunex (Immune Globulin Intravenous human, 10% Caprylate/Chromatography Purified ) package insert. Research Triangle Park, USA: Talecris Biotherapeuties, Inc,September 2008.

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