JP5882913B2 - 培地およびキレート剤を含む水溶液の調製方法 - Google Patents
培地およびキレート剤を含む水溶液の調製方法 Download PDFInfo
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- JP5882913B2 JP5882913B2 JP2012550988A JP2012550988A JP5882913B2 JP 5882913 B2 JP5882913 B2 JP 5882913B2 JP 2012550988 A JP2012550988 A JP 2012550988A JP 2012550988 A JP2012550988 A JP 2012550988A JP 5882913 B2 JP5882913 B2 JP 5882913B2
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Description
1.粉末培地およびキレート剤を含む水溶液の調製方法であって、該水溶液の最終pH調整よりも先に、且つ、粉末培地よりも先または同時にキレート剤を水溶液に添加することを特徴とする、粉末培地およびキレート剤を含む水溶液の調製方法。
2.キレート剤がクエン酸、リンゴ酸、エチレンジアミン四酢酸、エチレンジアミン四酢酸 鉄(III)ナトリウム塩およびシアル酸、並びにそれらの塩または水和物から選ばれる少なくとも1である、前項1に記載の水溶液の調製方法。
3.粉末培地がさらに金属塩、糖類およびビタミンから選ばれる少なくとも1を含む粉末培地である、前項1または2に記載の水溶液の調製方法。
4.粉末培地が細胞培養用の粉末培地である、前項1〜3のいずれか1項に記載の水溶液の調製方法。
5.粉末培地が動物細胞培養用の粉末培地である、前項4に記載の水溶液の調製方法。
6.粉末培地がチャイニーズハムスター卵巣組織由来のCHO細胞培養用の粉末培地である、前項5に記載の水溶液の調製方法。
7.前項1〜6のいずれか1項に記載の方法により調製された、水溶液。
8.前項1〜6のいずれか1項に記載の方法で調製した水溶液を用いる、細胞の培養方法。
9.細胞が動物細胞である、前項8に記載の細胞の培養方法。
10.細胞がチャイニーズハムスター卵巣組織由来のCHO細胞である、前項9に記載の細胞の培養方法。
11.粉末培地およびキレート剤を含む水溶液を膜ろ過する方法であって、該水溶液が、水溶液の最終pH調整よりも先に、且つ粉末培地よりも先または同時にキレート剤を添加して調製した水溶液である、膜ろ過する方法。
12.キレート剤がクエン酸、リンゴ酸、エチレンジアミン四酢酸、エチレンジアミン四酢酸 鉄(III)ナトリウム塩およびシアル酸、並びにそれらの塩または水和物から選ばれる少なくとも1である、前項11に記載の膜ろ過する方法。
13.粉末培地がさらに金属塩、糖類およびビタミンから選ばれる少なくとも1を含む粉末である、前項11または12に記載の膜ろ過する方法。
14.粉末培地が細胞培養用の粉末培地である、前項11〜13のいずれか1項に記載の膜ろ過する方法。
15.粉末培地が動物細胞培養用の粉末培地である、前項14に記載の膜ろ過する方法。
16.粉末培地がチャイニーズハムスター卵巣組織由来のCHO細胞培養用の粉末培地である、前項15に記載の膜ろ過する方法。
17.膜ろ過に用いるろ過膜の孔径が1nmから100μmである、前項11〜16のいずれか1項に記載の膜ろ過する方法。
18.キレート剤を水溶液に添加してキレート剤を含む水溶液を調製し、該水溶液を膜ろ過する水溶液の膜ろ過性を向上する方法であって、該水溶液が、キレート剤を粉末培地よりも先または同時に添加して調製した水溶液である、水溶液の膜ろ過性を向上する方法。
19.さらに粉末培地を水溶液に添加して粉末培地およびキレート剤を含む水溶液を調製し、該水溶液を膜ろ過する、前項18に記載の水溶液の膜ろ過性を向上する方法。
20.キレート剤を水溶液の最終pH調整よりも先に水溶液に添加してキレート剤を含む水溶液を調製することを特徴とする、前項18または19に記載の水溶液の膜ろ過性を向上する方法。
21.最終pH調整よりも先に、且つ、粉末培地よりも先または同時にキレート剤を水溶液に添加して粉末培地および該キレート剤を含む水溶液を調製し、該水溶液を膜ろ過した後、得られた水溶液を用いて細胞を培養することによって、生理活性物質を製造する方法。
粉末培地を含む水溶液調製時に各種キレート剤を添加したときの該水溶液のろ過性への影響を検討し、Vmax(単位膜面積あたりの最大処理量)の値が向上することを明らかにした。
粉末培地を含む水溶液調製時における、クエン酸3ナトリウム2水和物の添加時期とろ過性への影響を検討し、クエン酸3ナトリウム2水和物をアミノ酸、金属塩、ビタミン等を含む粉末培地と同時または前に添加することにより、Vmax(単位膜面積あたりの最大処理量)が大幅に増加することを明らかにした。さらに、クエン酸3ナトリウム2水和物を最終pH調整工程より前に添加することにより、Vmax(単位膜面積あたりの最大処理量)が増加することを明らかにした。
条件B:SOY HYDROLYSATE UF添加の10分前
条件C:SOY HYDROLYSATE UF添加の1分前
条件D:SOY HYDROLYSATE UF添加と同時
条件E:改良EX−CELL 302添加の10分前
条件F:改良EX−CELL 302添加と同時
条件G:炭酸水素ナトリウム添加の15分前
条件H:PWで1Lに調製した直後
水溶液調製時に添加するクエン酸3ナトリウム2水和物の濃度とろ過性への相関を検討し、濃度依存的にVmax(単位膜面積あたりの最大処理量)が向上することを明らかにした。
粉末培地を含む水溶液調製時におけるキレート剤による水溶液ろ過性向上効果を、複数のろ過膜を用いて検討した。その結果、孔径0.22μmのポリフッ化ビニリデン(以下、PVDFと称す)膜、または、プレフィルターとして孔径0.5μmのポリエーテルスルフォン(以下、PESと称す)膜を組み合わせた孔径0.2μmのPES膜(以下、孔径0.5/0.2μmのPES膜と称す)において、Vmax(単位膜面積あたりの最大処理量)の値が向上することを明らかにした。
最終pH調整よりも先にクエン酸3ナトリウム2水和物を添加し調製された水溶液を用いて、動物細胞の培養を行った。その結果、クエン酸3ナトリウム2水和物を添加した水溶液においても、添加しなかった水溶液と同等以上の細胞増殖、力価が得られることを明らかにした。
粉末培地を含む水溶液調製時にキレート剤として、N−アセチルノイラミン酸二水和物を添加したときの該水溶液のろ過性への影響を検討し、水溶液のVmax(単位膜面積あたりの最大処理量)値が向上することを明らかにした。
Claims (21)
- 粉末培地およびキレート剤を含む水溶液の調製方法であって、該水溶液の最終pH調整よりも先に、且つ、粉末培地よりも先または同時にキレート剤を水溶液に添加することを特徴とする、粉末培地およびキレート剤を含む水溶液の調製方法。
- キレート剤がクエン酸、リンゴ酸、エチレンジアミン四酢酸、エチレンジアミン四酢酸 鉄(III)ナトリウム塩およびシアル酸、並びにそれらの塩または水和物から選ばれる少なくとも1である、請求項1に記載の水溶液の調製方法。
- 粉末培地がさらに金属塩、糖類およびビタミンから選ばれる少なくとも1を含む粉末培地である、請求項1または2に記載の水溶液の調製方法。
- 粉末培地が細胞培養用の粉末培地である、請求項1〜3のいずれか1項に記載の水溶液の調製方法。
- 粉末培地が動物細胞培養用の粉末培地である、請求項4に記載の水溶液の調製方法。
- 粉末培地がチャイニーズハムスター卵巣組織由来のCHO細胞培養用の粉末培地である、請求項5に記載の水溶液の調製方法。
- 請求項1〜6のいずれか1項に記載の方法により調製された、水溶液。
- 請求項1〜6のいずれか1項に記載の方法で調製した水溶液を用いる、細胞の培養方法。
- 細胞が動物細胞である、請求項8に記載の細胞の培養方法。
- 細胞がチャイニーズハムスター卵巣組織由来のCHO細胞である、請求項9に記載の細胞の培養方法。
- 粉末培地およびキレート剤を含む水溶液を膜ろ過する方法であって、該水溶液が、水溶液の最終pH調整よりも先に、且つ粉末培地よりも先または同時にキレート剤を添加して調製した水溶液である、膜ろ過する方法。
- キレート剤がクエン酸、リンゴ酸、エチレンジアミン四酢酸、エチレンジアミン四酢酸 鉄(III)ナトリウム塩およびシアル酸、並びにそれらの塩または水和物から選ばれる少なくとも1である、請求項11に記載の膜ろ過する方法。
- 粉末培地がさらに金属塩、糖類およびビタミンから選ばれる少なくとも1を含む粉末である、請求項11または12に記載の膜ろ過する方法。
- 粉末培地が細胞培養用の粉末培地である、請求項11〜13のいずれか1項に記載の膜ろ過する方法。
- 粉末培地が動物細胞培養用の粉末培地である、請求項14に記載の膜ろ過する方法。
- 粉末培地がチャイニーズハムスター卵巣組織由来のCHO細胞培養用の粉末培地である、請求項15に記載の膜ろ過する方法。
- 膜ろ過に用いるろ過膜の孔径が1nmから100μmである、請求項11〜16のいずれか1項に記載の膜ろ過する方法。
- キレート剤を水溶液に添加してキレート剤を含む水溶液を調製し、該水溶液を膜ろ過する水溶液の膜ろ過性を向上する方法であって、該水溶液が、キレート剤を粉末培地よりも先または同時に添加して調製した水溶液である、水溶液の膜ろ過性を向上する方法。
- さらに粉末培地を水溶液に添加して粉末培地およびキレート剤を含む水溶液を調製し、該水溶液を膜ろ過する、請求項18に記載の水溶液の膜ろ過性を向上する方法。
- キレート剤を水溶液の最終pH調整よりも先に水溶液に添加してキレート剤を含む水溶液を調製することを特徴とする、請求項18または19に記載の水溶液の膜ろ過性を向上する方法。
- 最終pH調整よりも先に、且つ、粉末培地よりも先または同時にキレート剤を水溶液に添加して粉末培地および該キレート剤を含む水溶液を調製し、該水溶液を膜ろ過した後、得られた水溶液を用いて細胞を培養することによって、生理活性物質を製造する方法。
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CN102099468B (zh) | 2008-07-17 | 2014-01-15 | 协和发酵麒麟株式会社 | 抗-系统asc氨基酸转运蛋白2(asct2)抗体 |
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2011
- 2011-12-27 WO PCT/JP2011/080236 patent/WO2012091023A1/ja active Application Filing
- 2011-12-27 ES ES16198419T patent/ES2812923T3/es active Active
- 2011-12-27 JP JP2012550988A patent/JP5882913B2/ja active Active
- 2011-12-27 EP EP16198419.0A patent/EP3147355B1/en not_active Revoked
- 2011-12-27 US US13/976,524 patent/US9611458B2/en active Active
- 2011-12-27 EP EP11854382.6A patent/EP2660315B1/en active Active
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JPS5840331A (ja) * | 1981-08-20 | 1983-03-09 | フアイザ−・インコ−ポレ−テツド | キレート剤を含む安定なキサンタン溶液 |
JP2006500931A (ja) * | 2002-09-30 | 2006-01-12 | ファイザー・プロダクツ・インク | 高レベルのヒト配列抗体を産生するハイブリドーマ |
WO2010036774A1 (en) * | 2008-09-24 | 2010-04-01 | Medimmune, Llc | Methods for purification of viruses |
WO2010036760A1 (en) * | 2008-09-24 | 2010-04-01 | Medimmune, Llc | Methods for cultivating cells, propagating and purifying viruses |
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EP3147355A1 (en) | 2017-03-29 |
EP2660315A4 (en) | 2014-12-31 |
US20130267684A1 (en) | 2013-10-10 |
EP2660315B1 (en) | 2018-11-14 |
EP3147355B1 (en) | 2020-07-22 |
ES2812923T3 (es) | 2021-03-18 |
WO2012091023A1 (ja) | 2012-07-05 |
US9611458B2 (en) | 2017-04-04 |
ES2710543T3 (es) | 2019-04-25 |
EP2660315A1 (en) | 2013-11-06 |
JPWO2012091023A1 (ja) | 2014-06-05 |
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