Continuous integrated antibody precipitation with two-stage tangential flow microfiltration enables constant mass flow

被引:47
作者
Burgstaller, Daniel [1 ]
Jungbauer, Alois [1 ,2 ]
Satzer, Peter [1 ]
机构
[1] Univ Nat Resources & Life Sci, Dept Biotechnol, Muthgasse 18, A-1190 Vienna, Austria
[2] ACIB, Vienna, Austria
基金
欧盟地平线“2020”;
关键词
diafiltration; IgG; membrane; polyethylene glycol; tubular reactor; CELL-CULTURE SUPERNATANT; RECOMBINANT ANTIBODIES; PROTEIN PRECIPITATION; POLYETHYLENE-GLYCOL; PURIFICATION; CAPTURE; REACTOR;
D O I
10.1002/bit.26922
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
Continuous precipitation is a new unit operation for the continuous capture of antibodies. The capture step is based on continuous precipitation with PEG6000 and Zn++ in a tubular reactor integrated with a two-stage continuous tangential flow filtration unit. The precipitate cannot be separated with centrifugation, because a highly compressed sediment results in poor resolubilization. We developed a new two-stage tangential flow microfiltration method, where part of the concentrated retentate of the first stage was directly fed to the second stage, together with the wash buffer. Thus, the precipitate was concentrated and washed in a continuous process. We obtained 97% antibody purity, a 95% process yield during continuous operation, and a fivefold reduction in pre-existing high-molecular-weight impurities. For other unit operations, surge tanks are often required, due to interruptions in the product mass flow out of the unit operation (e.g., the bind/elute mode in periodic counter-current chromatography). Our setup required no surge tanks; thus, it provided a truly continuous antibody capture operation with uninterrupted product mass flow. Continuous virus inactivation and other flow-through unit operations can be readily integrated downstream of the capture step to create truly continuous, integrated, downstream antibody processing without the need for hold tanks.
引用
收藏
页码:1053 / 1065
页数:13
相关论文
共 26 条
[11]   Opportunities and challenges of real-time release testing in biopharmaceutical manufacturing [J].
Jiang, Mo ;
Severson, Kristen A. ;
Love, John Christopher ;
Madden, Helena ;
Swann, Patrick ;
Zang, Li ;
Braatz, Richard D. .
BIOTECHNOLOGY AND BIOENGINEERING, 2017, 114 (11) :2445-2456
[12]   Continuous downstream processing of biopharmaceuticals [J].
Jungbauer, Alois .
TRENDS IN BIOTECHNOLOGY, 2013, 31 (08) :479-492
[13]   Continuous precipitation of process related impurities from clarified cell culture supernatant using a novel coiled flow inversion reactor (CFIR) [J].
Kateja, Nikhil ;
Agarwal, Harshit ;
Saraswat, Aditya ;
Bhat, Manish ;
Rathore, Anurag S. .
BIOTECHNOLOGY JOURNAL, 2016, 11 (10) :1320-1331
[14]   Continuous viral inactivation at low pH value in antibody manufacturing [J].
Klutz, Stephan ;
Lobedann, Martin ;
Bramsiepe, Christian ;
Schembecker, Gerhard .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2016, 102 :88-101
[15]   Countercurrent staged diafiltration for formulation of high value proteins [J].
Nambiar, Anirudh M. K. ;
Li, Ying ;
Zydney, Andrew L. .
BIOTECHNOLOGY AND BIOENGINEERING, 2018, 115 (01) :139-144
[16]  
Przybycien T. M, 2016, BIOPROCESS INT EUR S
[17]   Sunflower protein precipitation in a tubular precipitator [J].
Raphael, M ;
Rohani, S .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1999, 77 (03) :540-554
[18]  
Rathore A, 2016, BIOPHARM INT, V29, P14
[19]   Single pass diafiltration integrated into a fully continuous mAb purification process [J].
Rucker-Pezzini, Joanna ;
Arnold, Lindsay ;
Hill-Byrne, Kevin ;
Sharp, Tom ;
Avazhanskiy, Maksim ;
Forespring, Chris .
BIOTECHNOLOGY AND BIOENGINEERING, 2018, 115 (08) :1949-1957
[20]   Capture and intermediate purification of recombinant antibodies with combined precipitation methods [J].
Sommer, Ralf ;
Tscheliessnig, Anne ;
Satzer, Peter ;
Schulz, Henk ;
Helk, Bernhard ;
Jungbauer, Alois .
BIOCHEMICAL ENGINEERING JOURNAL, 2015, 93 :200-211