JP5855564B2 - オルソポックスウイルスの製造および精製方法 - Google Patents
オルソポックスウイルスの製造および精製方法 Download PDFInfo
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- JP5855564B2 JP5855564B2 JP2012510276A JP2012510276A JP5855564B2 JP 5855564 B2 JP5855564 B2 JP 5855564B2 JP 2012510276 A JP2012510276 A JP 2012510276A JP 2012510276 A JP2012510276 A JP 2012510276A JP 5855564 B2 JP5855564 B2 JP 5855564B2
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- orthopoxvirus
- cell
- anion exchange
- packaging
- exchange adsorbent
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Description
a)パッケージング細胞の培養物を用意し、
b)培養パッケージング細胞にオルソポックスウイルスを感染させ、
c)感染させたパッケージング細胞を、子孫オルソポックスウイルスが製造されるまで培養し、
d)1以上のヌクレアーゼの存在下でインキュベートし、
e)培養上清および/またはパッケージング細胞からオルソポックスウイルスを回収し、
f)単数または複数のヌクレアーゼの活性を阻害し、かつ工程e)で回収されたオルソポックスウイルスが工程g)において陰イオン交換吸着剤へ吸着することを避けるのに適切な条件下で、前記オルソポックスウイルスに一価の塩を添加し、
g)核酸の捕捉を可能にするのに適切な条件下で、工程f)で得られた混合物と陰イオン交換吸着剤とを接触させ、
h)細胞片の除去を可能にするのに適切な条件下で、工程g)で得られた混合物を清澄化し、
i)陰イオン交換吸着剤に残るオルソポックスウイルスを、通過画分(flow through)中に回収するのに適切な条件下で、陰イオン交換吸着剤を一価の塩を含んでなる溶液により洗浄し、
j)工程h)で得られた通過画分と工程i)で得られた通過画分を濃縮し、
k)工程j)で得られたオルソポックスウイルスを含んでなる画分を透析濾過(diafiltrating)すること。
−受託番号08060502により欧州細胞培養収集機関(European Collection of Cell Cultures:ECACC)に寄託されるT3−17490(図2、3、および4を参照)またはその誘導体;
−受託番号08060501により欧州細胞培養収集機関(ECACC)に寄託されるT6−17490(図5、6、および7を参照)またはその誘導体。
−米国特許第5,879,924号に記載される、10日齢のイーストランシング系統(ELL−O)卵由来の自然発生不死化ニワトリ細胞株である、DF1細胞株;
−国際公開第2005/007840号に記載される、増殖因子および支持細胞層から徐々に分離した胚性幹細胞由来のEbxニワトリ細胞株;
−カモ胚永久細胞株である、DEC99細胞株(Ivanov et al. Experimental Pathology and Parasitology, 4/2000 Bulgarian Academy of Sciences)である。
パッケージング細胞の培養物を用意する工程a)は当業者に公知である。
−7.0ないし9.0、好ましくは7.5ないし8.5、より好ましくは8.0のpH;
−1ないし2mMの範囲、好ましくは2mMである、Mg2+およびMn2+、好ましくはMg2+から選択される補助因子の濃度である(実施例1に記載される)。
1.好ましくは高速ホモジナイザーを用いてまたは超音波処理によって、パッケージング細胞膜を破壊し、
2.工程1)で得られる混合物を少なくとも1時間インキュベートし、工程d)において添加された単数または複数のヌクレアーゼにより、パッケージング細胞から放出された核酸(例えばDNA)を分解する。
−単数または複数のヌクレアーゼ活性を阻害すること;および
−工程g)においてオルソポックスウイルスの陰イオン交換吸着剤への吸着を避けること、すなわち、10%を超えるオルソポックスウイルスの陰イオン交換吸着剤への吸着を避けることを可能にする。従って、工程g)では核酸(例えばDNA)のみが陰イオン交換吸着剤へ吸着され得る。
1.ゲル濾過工程(すなわち工程l));および
2.透析濾過工程(すなわち工程m))をさらに含んでいてよい。
・エチレングリコール/メタクリル酸塩ゲル濾過クロマトグラフィー支持体(例えば、20ないし60μmのビーズ直径を有するToyopearl(登録商標)HW 55、Toyopearl(登録商標)HW 65、およびToyopearl(登録商標)HW 75、Tosohaas);
・アリルデキストラン/メチレンビスアクリルアミドゲル濾過クロマトグラフィー支持体(例えば、25ないし75μmのビーズ直径を有するSephacryl(商標)S300 HR;25ないし75μmのビーズ直径を有するSephacryl(商標)S400 HR;25ないし75μmのビーズ直径を有するSephacryl(商標)S500 HR;40ないし105μmのビーズ直径を有するSephacryl(商標)S1000 SF、全てPharmaciaから市販される);
・N−アクリルアミノヒドロキシプロパンジオールゲル濾過クロマトグラフィー支持体(例えば、80ないし160μmのビーズ直径を有するTrisacryl、Biosepra);
・アガロースゲル濾過クロマトグラフィー支持体(例えば、20ないし80μmのビーズ直径を有するMacro-Prep SE、Bio-Rad)
として市販される。
−200mMないし2Mの範囲、好ましくは200mMないし1Mの範囲、より好ましくは500mMである、NaClおよびKClから選択され、好ましくはNaClである一価の塩の濃度;
−7.0ないし9.0、好ましくは7.5ないし8.5、より好ましくは8.0のpHである。
a’)パッケージング細胞の培養物を用意すること;
b’)培養パッケージング細胞にオルソポックスウイルスを感染させること;
c’)感染させたパッケージング細胞を、子孫オルソポックスウイルスが製造されるまで培養すること;
d’)1以上のヌクレアーゼの存在下でインキュベートすること;
e’)培養上清および/またはパッケージング細胞からオルソポックスウイルスを回収すること;
f’)工程e’)で回収されたオルソポックスウイルスを、
1.単数または複数のヌクレアーゼの活性を阻害できる1以上の薬剤、および所望により
2.1以上の安定剤
の存在下でインキュベートすること;
g’)オルソポックスウイルスおよび核酸の捕捉を可能にするため、工程f’)で得られた混合物と陰イオン交換吸着剤とを適切な条件下で接触させること;
h’)細胞片の除去を可能にするため、工程g’)で得られた混合物を適切な条件下で清澄化すること;
i’)オルソポックスウイルスを、一価の塩を含んでなる溶液により溶出すること;
j’)工程i’)で得られた混合物を濃縮すること;
k’)工程j’)で得られたオルソポックスウイルスを含んでなる画分を透析濾過すること。
1.単数または複数のヌクレアーゼの活性を阻害できる1以上の薬剤、および所望により
2.1以上の安定剤の存在下でインキュベートする(工程f’))。
ll Corporation)は、直径約75μmで四級アミンQ官能基を有する、高密度で多孔性のジルコニウムジオキシドビーズである。工程f’)で得られた混合物と陰イオン交換吸着剤とを接触させる工程g’)は、陰イオン交換吸着剤がビーズ型基質にある前記交換吸着剤を用いて、実施例4に記載の条件により好ましく行われ、ここではBioSepra(登録商標)Q hyperZ (Pall Corporation)が用いられる。
1.ゲル濾過工程(すなわち工程l’));および
2.透析濾過工程(すなわち工程m’))をさらに含んでなってよい。
a’’)パッケージング細胞の培養物を用意すること;
b’’)培養パッケージング細胞にオルソポックスウイルスを感染させること;
c’’)感染させたパッケージング細胞を、子孫オルソポックスウイルスが製造されるまで培養すること;
d’’)1以上のヌクレアーゼの存在下でインキュベートすること;
e’’)培養上清および/またはパッケージング細胞からオルソポックスウイルスを回収すること;
f’’)工程e’’)で回収されたオルソポックスウイルスを、
1.単数または複数のヌクレアーゼの活性を阻害できる1以上の薬剤、および所望により
2.1以上の安定剤;
の存在下でインキュベートすること;
g’’)前記オルソポックスウイルスおよび核酸の捕捉を可能にするため、工程f’’)で得られた混合物と陰イオン交換吸着剤とを適切な条件下で接触させること;
h’’)細胞片の除去を可能にするため、工程g’’)で得られた混合物を適切な条件下で清澄化すること;
i’’)オルソポックスウイルスを、一価の塩を含んでなる溶液により溶出すること;
j’’)工程i’’)で溶出されたオルソポックスウイルスが工程k’’)において陰イオン交換吸着剤へ吸着することを避けるために、前記オルソポックスウイルスに一価の塩を添加すること;
k’’)核酸の捕捉を可能にするため、工程j’’)で得られた混合物と陰イオン交換吸着剤とを適切な条件下で接触させること;
l’’)通過画分中に残るオルソポックスウイルスを回収するため、陰イオン交換吸着剤を適切な条件下で一価の塩を含んでなる溶液により洗浄すること;
m’’)工程l’’)で得られた通過画分を濃縮すること;
n’’)工程m’’)で得られたオルソポックスウイルスを含んでなる画分を透析濾過すること。
1.ゲル濾過工程(すなわち工程o’’));および
2.透析濾過工程(すなわち工程p’’))をさらに含んでなってよい。
・MVA−FCU1(国際公開第99/54481号を参照)、TG4023とも称される;
・MVA−FCU1−8(国際公開第05/07857号を参照);および
・VV−FCU1、ここで前記VVは、さらに詳細には、欠陥のあるI4Lおよび/またはF4L遺伝子、および欠陥のあるJ2R遺伝子(PCT/EP2008/009720/国際公開第2009/065546号、およびPCT/EP2008/009721/国際公開第2009/065547号を参照)を含んでなる、である。
・MVA−[MUC1−IL2](国際公開第92/07000号および国際公開第95/09241号を参照)、TG4010とも称される;および
・MVA−[HPV−IL2](国際公開第90/10459号、国際公開第95/09241号、国際公開第98/04705号、国際公開第99/03885号、国際公開第07/121894号、および国際公開第07/121894号を参照)、TG4001とも称される、である。
−受託番号08060502により欧州細胞培養収集機関(ECACC)に寄託されるT3−17490(図2、3、および4を参照)またはその誘導体;
−受託番号08060501により欧州細胞培養収集機関(ECACC)に寄託されるT6−17490(図5、6、および7を参照)またはその誘導体。
・本発明の方法に従って、野生型、弱毒化、および/または組み換えオルソポックスウイルスを製造するための、テロメラーゼ逆転写酵素(telomerase reverse transcriptase:TERT)をコードする核酸配列を含んでなるノバリケン不死化鳥類細胞株の使用
・本発明の方法に従って、野生型、弱毒化、および/または組み換えオルソポックスウイルスを製造するための、受託番号08060502により欧州細胞培養収集機関(ECACC)に寄託されるT3−17490ノバリケン不死化鳥類細胞株(実施例2に記載される)またはその誘導体の使用
・本発明の方法に従って、野生型、弱毒化、および/または組み換えオルソポックスウイルスを製造するための、受託番号08060501により欧州細胞培養収集機関(ECACC)に寄託されるT6−17490ノバリケン不死化鳥類細胞株(実施例3に記載される)またはその誘導体の使用にも関する。
工程a):パッケージング細胞の培養物を用意する
SPF卵66個を、2%ホルモル溶液中で60秒インキュベートした。70%エタノールで洗浄後、卵を開き、胚を抽出および解体した。得られた組織を、次にディスパーゼ(UI/ml)およびトリプルセレクト(UI/ml)によって36.5℃、120分消化した。未消化組織を除去するために混合物を濾過し、CEFを遠心分離(2300rpm、15分)によって回収した。CEFを、55LのVP-SFM (Invitrogen)中で2日間36.5℃にてインキュベートした。
次に細胞用培地を廃棄し、MVA−[MUC1−IL2]、TG4010とも称される(0.05MOI)(寄託番号N○I−721により、Collection Nationale de Cultures de Microorganismes(CNCM)に寄託されたMVA)を、55Lのイーグル基礎培地(Invitrogen)中に加えた。
次に、感染させたCEFを3日間36.5℃にてインキュベートした。
次に、MVA子孫を含んでなる感染させたCEFを、10U/mlまたは50U/mlのBenzonase(登録商標)(Merck;参照1.01653.0001)存在下で、以下の条件:
−攪拌しながら、温度25℃にて2時間;
−Mg2+2mM;
−pH8.0によりインキュベートした。
細胞用培地およびCEFを回収した。次に混合物を15分間、11ml/分にて、Silverson(著作権)L4R高速ホモジナイザー(Silverson)によるか、または75分間、1500ml/分にて、SONITUBE 36 kHz型 SM 35/3WU (Heraeus PSP)によってホモジナイズした。
得られた混合物を次に2時間、攪拌しながら温度25℃、pH8.0にてインキュベートした。
得られた混合物を次にNaCl 250mMの存在下で、pH8.0にてインキュベートした。
得られた混合物を次にUNOsphere(登録商標)Q (BioRad)に加えた。UNOsphere(登録商標)Q (BioRad)ビーズ型基質を、最初に無菌水で洗浄した後、Tris 10mM緩衝液(pH8.0)中でオートクレーブして、次にNaCl、250mMまたは300mM緩衝液(pH8.0)によって平衡化した。
次にUNOsphere(登録商標)Q (BioRad) ビーズ型基質を、蠕動のWatson-Marlowポンプ(参照323ES/4D, 520S; Watson-Marlow)を用いて、Flexboy(登録商標)バッグ(参照FFB101961 ; Sartorius Stedim biotech)内に含まれる、工程f)で得られた混合物に加えた。
UNOsphere(登録商標)Q (BioRad)ビーズ型基質および工程f)で得られた混合物を、1時間ゆっくりと攪拌しながら、室温(20℃ないし22℃)にて接触させた。
得られた混合物を次に、Sartopure(登録商標)PP2、8μm(Sartorius)とSartopure(登録商標)PP2、5μm(Sartorius)を組み合わせた深層濾過により、流速1L/分で清澄化した。
次に、UNOsphere(登録商標)(BioRad)を、SO8緩衝液(10mM Tris−HCl;スクロース 5%(w/v);10mM グルタミン酸ナトリウム;生理的なモル浸透圧濃度(290mOsm/kg)の50mM NaCl;pH8.0)中のNaCl 250mMまたは300mM(v/v)により、蠕動のWatson-Marlowポンプ(参照323ES/4D, 520S; Watson-Marlow)を用いて洗浄した。
次に、工程h)で得られた通過画分と工程i)で得られた通過画分を一晩(すなわち18時間)5℃にて、最終濃度50g/Lのサッカロース存在下でインキュベートした。
工程h)で得られた通過画分と工程i)で得られた通過画分を、次に0.1μm Prostak Microfiltration Module (参照PSVVAG021, Millipore)を通して18倍に濃縮した。
次に濃縮水を同じモジュール、すなわち0.1μm Prostak Microfiltration Module (参照PSVVAG021, Millipore)において透析濾過した。
DNAの定量は、Quant-iT(商標)Picogreen(登録商標)dsDNA Assays Kit (カタログ番号P7589、Invitrogen)を用いて行った。
結果:残存DNAは検出されなかった。
T3−17490細胞(継代39)は、均一な線維芽細胞様の形態を有する(図2)。静的な単層は100%コンフルエンスになるまで安定であり、次に接触阻止が起こる。細胞の検査によると、マイコプラズマ混入および細菌混入は陰性であった。T3−17490細胞株の増殖曲線(継代7から継代75)(図3)により、継代19から継代75までの連続的な指数関数的増殖が示される。集団倍加時間(population doubling time:PDT)の漸進的変化に焦点を当てると、進行的な安定化と減少が観察され、特に最近の10継代の間では、48時間の点におけるPDTの安定化が観察される(図4)。集団倍加に対応する数(集団倍加数(population doubling level, PDL))を、2つの指数関数的増殖段階の累積によって算出した:75継代の間に、細胞は少なくとも147の集団倍加(population doublings:PD)を行った。初代細胞が老化を始める前の集団倍加数は、組織および種に依存する。一般に上限は50ないし60PDであるとされている。従ってT3−17490細胞はヘイフリック限界をはるかに越えており、結果的に不死化細胞株と称される。
注:
・集団倍加数(population doubling level:PDL)は、細胞世代数を指す(現存量の2倍増加)。PDL算出:PDL=Ln(最終の/最初の細胞数)/Ln(2);
・集団倍加時間(population doubling time:PDT)、世代時間とも称される、は、1集団が倍加するために必要とされる時間である。PDT算出:PDT=Δt*Ln(2)/Ln(最終の/最初の細胞数)。
T6−17490細胞(継代45)は、均一な線維芽細胞様の形態を有する(図5)。静的な単層は100%コンフルエンスになるまで安定であり、次に接触阻止が起こる。細胞の検査によると、マイコプラズマ混入および細菌混入は陰性であった。T6−17490細胞株の増殖曲線(継代15から継代51)(図6)により、継代19からの連続的な指数関数的増殖が示される。この期間に測定した集団倍加時間(population doubling time:PDT)は、進行的に減少した。平均PDTは、94時間(継代20から35)から52時間(継代36から51)となった(図7)。51継代に対応する算出した集団倍加の数(PDL)は、少なくとも71集団倍加であった。従ってT6−17490細胞はヘイフリック限界をはるかに越えており、結果的に不死化細胞株と称される。
注:
・集団倍加数(population doubling level:PDL)は、細胞世代数を指す(現存量の2倍増加)。PDL算出:PDL=Ln(最終の/最初の細胞数)/Ln(2);
・集団倍加時間(population doubling time:PDT)、世代時間とも称される、は、1集団が倍加するために必要とされる時間である。PDT算出:PDT=Δt*Ln(2)/Ln(最終の/最初の細胞数)。
工程a’):パッケージング細胞の培養物を用意する
SPF卵66個を、2%ホルモル溶液中で60秒インキュベートした。70%エタノールで洗浄後、卵を開き、胚を抽出および解体した。得られた組織を、次にディスパーゼ(UI/ml)およびトリプルセレクト(UI/ml)によって36.5℃、120分消化した。未消化組織を除去するために混合物を濾過し、CEFを遠心分離(2300rpm、15分)によって回収した。CEFを、55LのVP-SFM (Invitrogen)中で2日間36.5℃にてインキュベートした。
次に細胞用培地を廃棄し、MVA−[MUC1−IL2]、TG4010とも称される(0.05MOI)(寄託番号N○I−721により、Collection Nationale de Cultures de Microorganismes(CNCM)に寄託されたMVA)を、55Lのイーグル基礎培地(Invitrogen)中に加えた。
次に、感染させたCEFを3日間36.5℃にてインキュベートした。
次に、MVA子孫を含んでなる感染させたCEFを、10U/mlのBenzonase(登録商標)(Merck;参照1.01653.0001)存在下で、以下の条件:
−攪拌しながら、温度25℃にて2時間;
−Mg2+2mM;
−pH8.0によりインキュベートした。
細胞用培地およびCEFを回収した。次に混合物を15分間、11ml/分にて、Silverson(著作権)L4R高速ホモジナイザー(Silverson)によるか、または75分間、1500ml/分にて、SONITUBE 36 kHz型 SM 35/3WU (Heraeus PSP)によってホモジナイズした。
得られた混合物を次にNaCl 100mMおよびEDTA 10mMの存在下で、pH8.0にてインキュベートした。
得られた混合物を次にBioSepra(登録商標)Q hyperZ (Pall Corporation)に加えた。BioSepra(登録商標)Q hyperZ (Pall Corporation)ビーズ型基質を、最初に無菌水で洗浄した後、次にNaOH 0.5Nにより消毒して、Tris 10mM緩衝液(pH8.0)で洗浄して、次にTris 10mM、NaCl 10mM、サッカロース5%緩衝液(pH8.0)によって平衡化した。
次にBioSepra(登録商標)Q hyperZ (Pall Corporation)ビーズ型基質を、蠕動のWatson-Marlowポンプ(参照323ES/4D, 520S; Watson-Marlow)を用いて、Flexboy(登録商標)バッグ(参照FFB101961 ; Sartorius Stedim biotech)内に含まれる、工程f’)で得られた混合物に加えた。
BioSepra(登録商標)Q hyperZ (Pall Corporation)ビーズ型基質および工程f’)で得られた混合物を、1時間ゆっくりと攪拌しながら、室温(20℃ないし22℃)にて接触させた。
得られた混合物を次に、Sartopure(登録商標)PP2、8μm(Sartorius)とSartopure(登録商標)PP2、5μm(Sartorius)を組み合わせた深層濾過により、流速1L/分で清澄化した。
オルソポックスウイルスを、SO8緩衝液(10mM Tris−HCl;スクロース 5%(w/v);10mM グルタミン酸ナトリウム;生理的なモル浸透圧濃度(290mOsm/kg)の50mM NaCl;pH8.0)中の増大するNaCl濃度勾配(300mM;400mM;500mM)により、蠕動のWatson-Marlowポンプ(参照323ES/4D, 520S; Watson-Marlow)を用いて溶出した。
工程i’)で得られた溶出液を、次に0.1μm Prostak Microfiltration Module (参照PSVVAG021, Millipore)を通して18倍に濃縮した。
次に濃縮水を同じモジュール、すなわち0.1μm Prostak Microfiltration Module (参照PSVVAG021, Millipore)において透析濾過した。
DNAの定量は、Quant-iT(商標)Picogreen(登録商標)dsDNA Assays Kit (カタログ番号P7589、Invitrogen)を用いて行った。
結果:残存DNAは検出されなかった。
Claims (28)
- 野生型、弱毒化、および/または組み換えオルソポックスウイルスを製造および精製する方法であって、以下の工程:
a)パッケージング細胞の培養物を用意し、
b)培養パッケージング細胞にオルソポックスウイルスを感染させ、
c)感染させたパッケージング細胞を、子孫オルソポックスウイルスが製造されるまで培養し、
d)1以上のヌクレアーゼの存在下でインキュベートし、
e)培養上清および/またはパッケージング細胞からオルソポックスウイルスを回収し、
f)単数または複数のヌクレアーゼの活性を阻害しかつ工程g)においてオルソポックスウイルスが陰イオン交換吸着剤へ吸着することを避けるのに適切な条件下で、工程e)で回収されたオルソポックスウイルスに一価の塩を添加し、
g)核酸の捕捉を可能にするのに適切な条件下で、工程f)で得られた混合物と陰イオン交換吸着剤とを接触させること
を含んでなる、方法。 - 以下の工程:
h)細胞片の除去を可能にするのに適切な条件下で、工程g)で得られた混合物を清澄化し、
j)工程h)で得られた通過画分を濃縮し、
k)工程j)で得られたオルソポックスウイルスを含んでなる画分を透析濾過することを、さらに含んでなる、請求項1に記載の方法。 - 以下の工程:
h)細胞片の除去を可能にするのに適切な条件下で、工程g)で得られた混合物を清澄化し、
i)陰イオン交換吸着剤に残るオルソポックスウイルスを、通過画分中に回収するのに適切な条件下で、陰イオン交換吸着剤を一価の塩を含んでなる溶液により洗浄し、
j)工程h)で得られた通過画分および工程i)で得られた通過画分を濃縮し、
k)工程j)で得られたオルソポックスウイルスを含んでなる画分を透析濾過することを、さらに含んでなる、請求項1に記載の方法。 - パッケージング細胞が、不死化細胞株である、請求項1〜3のいずれか一項に記載の方法。
- パッケージング細胞が、不死化鳥類細胞株である、請求項4に記載の方法。
- 不死化鳥類細胞株が、動物性産物を含まない培地中にて微小担体の非存在下で懸濁液中にて増殖可能である、請求項5に記載の方法。
- 不死化鳥類細胞株が、ノバリケン種に属する鳥類細胞から得られる、請求項5に記載の方法。
- 不死化鳥類細胞株が、テロメラーゼ逆転写酵素(telomerase reverse transcriptase:TERT)をコードする核酸を含んでなる、請求項7に記載の方法。
- 不死化鳥類細胞株が、
・受託番号08060502により欧州細胞培養収集機関(ECACC)に寄託されるT3−17490もしくはその誘導体、または、
・受託番号08060501により欧州細胞培養収集機関(ECACC)に寄託されるT6−17490もしくはその誘導体である、
請求項8に記載の方法。 - 不死化鳥類細胞株が、E1A核酸およびテロメラーゼ逆転写酵素(TERT)をコードする核酸を含んでなる、請求項7に記載の方法。
- パッケージング細胞が、初代または二次的な鳥類細胞である、請求項1〜3のいずれか一項の方法。
- パッケージング細胞が、ニワトリ胚線維芽細胞(CEF)である、請求項11に記載の方法。
- pHが7.0ないし9.0である、請求項1〜3のいずれか一項に記載の方法。
- ヌクレアーゼがBenzonase(登録商標)である、請求項1〜3のいずれか一項に記載の方法。
- 単数または複数のヌクレアーゼの濃度が、5ないし100U/mlの範囲である、請求項1〜3のいずれか一項に記載の方法。
- オルソポックスウイルスを回収する工程の前に、
1)パッケージング細胞膜を破壊し、かつ
2)工程1)で得られる混合物を少なくとも1時間インキュベートし、予め添加された単数または複数のヌクレアーゼにより、パッケージング細胞から放出された核酸を分解する、請求項1〜3のいずれか一項に記載の方法。 - パッケージング細胞膜を破壊する工程が、高速ホモジナイザーを用いてまたは超音波処理によって行われる、請求項16に記載の方法。
- 陰イオン交換吸着剤が、清澄化工程で用いられるフィルターの孔径よりも大きな直径を有するビーズ型基質に存在する、請求項2または請求項3に記載の方法。
- 陰イオン交換吸着剤が、8μmよりも大きな直径を有するビーズ型基質に存在する、請求項18に記載の方法。
- 陰イオン交換吸着剤の官能基が、ジメチルアミノエチル(DMAE)、ジエチルアミノエチル(DEAE)、トリメチルアミノエチル(TMAE)、およびトリエチルアミノエチル(TEAE)からなる群から選択される、請求項1〜3のいずれか一項に記載の方法。
- 清澄化工程が、深層濾過により行われる、請求項2または請求項3に記載の方法。
- 深層濾過が、孔径8μmのフィルターと孔径5μmのフィルターを組み合わせて行われる、請求項21に記載の方法。
- 濃縮工程が、0.09ないし0.15μmの孔径を有するフィルターを用いる精密濾過により行われる、請求項2または請求項3に記載の方法。
- 透析濾過工程が、0.09ないし0.15μmの孔径を有するフィルターを用いて行われる、請求項2または請求項3に記載の方法。
- 1.ゲル濾過工程;および
2.透析濾過工程を
さらに含んでなる、請求項1〜3のいずれか一項に記載の方法。 - 工程f)で用いられる一価の塩がNaClである、請求項1〜3のいずれか一項に記載の方法。
- 工程f)で用いられる一価の塩の濃度が、50ないし150mMの範囲である、請求項1〜3のいずれか一項に記載の方法。
- 前記オルソポックスウイルスがワクシニアウイルスまたは改変ワクシニアウイルスアンカラ(MVA)である、請求項1〜27のいずれか一項に記載の方法。
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