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2단계 고정화 효소반응기를 활용한 Cyclodextrin의 연속생산
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  • 2단계 고정화 효소반응기를 활용한 Cyclodextrin의 연속생산
  • Continuous Production of Cyclodextrin in Two-Stage Immobilized Enzyme Reactor Coupled with Ultrafiltration Recycle System
저자명
이용현,이상호,한일근,Lee. Yong-Hyun,Lee. Sang-Ho,Han. Il-Keun
간행물명
산업미생물학회지
권/호정보
1991년|19권 2호|pp.171-178 (8 pages)
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한국미생물생명공학회
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이 논문은 한국과학기술정보연구원과 논문 연계를 통해 무료로 제공되는 원문입니다.
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기타언어초록

The two-stage enzyme reactor, packed with cyclodextrin glucanotransferase (CGTase) immobilized on Amberite IRA 900, coupled with ultrafiltration membrane was investigated for continuous production of cyclodextrin (CD). 5% (w/v) of soluble starch was partially cyclized, in the 0.1 l first-stage immobilized enzyme reactor, up to CD conversion yield of 10% (w/w) at retention time of 0.56hr and 1.5 units of immobilized CGTase/1g of carrier. In the second stage main immobilized enzyme reactor capacity of 1.5 l, the maximum CD conversion yield of 39% (w/v) was achieved at retention time of 2.8hr and 0.47 unit of CGTase/1 g of carrier. Unreacted residual dextrin was fractionated with ultrafiltration membrane, and then, recycled into the second-stage main bioreactor to increase the CD conversion yield. The most suitable membrane size and the volume concentration ratio (concentrate: filterate) for recycling of unreacted residual dextrin were found to be 5K dalton and 4:6, respectively. CD conversion yield was increased about 3~4% upon co-immobilization of pulluanase along with CGTase. Spent Amberite IRA 900 can be reutilized consecutively more than 3 times for immobilization of CGTase after regeneration.