Citric Acid Production by Succharomycopsis lipolytica in Air-lift and Membrane Recycle Bioreactors

기포탑 및 막 재순환 생물반응기에서의 Saccharomycopsis lipolytica에 의한 구연산 생산

  • 조대철 (한국과학기술연구원 화학공학부) ;
  • 정봉현 (유전공학센터) ;
  • 장호남 (한국과학기술원 화학공학과)
  • Published : 1989.12.01

Abstract

A study on the citric acid production using Saccharomycopsis lipolytica (NRRL Y7576) was carried out in shake-flasks, air-lift and membrane recycle bioreactors. The cells entrapped in Ca-alginate beads were used in shake-flasks and air-lift reactor. Repeated batch fermentation in shake-flasks was successfully performed for 34 days and resulted in a yield of 54%. Increased yield (63%) was obtained in the air-lift reactor operation using nitrogen deficient medium (NDM). In the membrane recycle bioreactor operation, the maximal dry cell mass concentration was 39 g/1 at a dilution rate of 0.02 h$^{-1}$ and the yield with NDM was higher than that with growth medium. In addition, the yield and volumetric productivity with pure oxygen supply were greatly improved compared with those with air supply.

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