기관회원 [로그인]
소속기관에서 받은 아이디, 비밀번호를 입력해 주세요.
개인회원 [로그인]

비회원 구매시 입력하신 핸드폰번호를 입력해 주세요.
본인 인증 후 구매내역을 확인하실 수 있습니다.

회원가입
서지반출
Two-Stage Depth Filter Perfusion Culture for Recombinant Antibody Production by Recombinant Chinese Hamster Ovary Cell
[STEP1]서지반출 형식 선택
파일형식
@
서지도구
SNS
기타
[STEP2]서지반출 정보 선택
  • 제목
  • URL
돌아가기
확인
취소
  • Two-Stage Depth Filter Perfusion Culture for Recombinant Antibody Production by Recombinant Chinese Hamster Ovary Cell
  • Two-Stage Depth Filter Perfusion Culture for Recombinant Antibody Production by Recombinant Chinese Hamster Ovary Cell
저자명
Lee. Joon-Chul,Kim. Do-Yun,Oh. Duk-Jae,Chang. Ho-Nam
간행물명
Biotechnology and bioprocess engineering
권/호정보
2008년|13권 5호|pp.560-565 (6 pages)
발행정보
한국생물공학회
파일정보
정기간행물|ENG|
PDF텍스트
주제분야
기타
이 논문은 한국과학기술정보연구원과 논문 연계를 통해 무료로 제공되는 원문입니다.
서지반출

기타언어초록

A rCHO cell line of DUKX origin 26*-320, producing recombinant antibody against the human platelet, was cultivated in a two-stage depth filter perfusion system (DFPS) for 20 days in order to attain high recombinant antibody concentration. The productivity of the first stage DFPS bioreactor reached 53 times that of the batch culture in a controlled stirred tank reactor and was showed 12.1 mg/L antibody concentration at a perfusion rate of $6.0;d^{-1}$. Glucose concentration in the first DFPS was maintained at 1.5 g/L to avoid cell damage in the perfusion culture. A second stage DFPS system was attached to the first DFPS, which resulted in a low glucose concentration of 0.02 g/L and a high antibody concentration of 23.9 mg/L. The two-stage depth filter perfusion culture yielded 60% higher product concentration than the batch and 49-fold higher productivity of 69.3 mg/L/d in comparison with that (1.4 mg/L/d) in a batch system. Furthermore, antibody concentration of the second stage was 97% higher than that of the first stage, and the antibody productivities were comparable to that of the first stage. This two-stage DFPS system also showed potential for higher titer production of recombinant antibody and high volumetric productivity for long-term culture of bio-pharmaceutical substances.