膜科学与技术
膜科學與技術
막과학여기술
MEMBRANE SCIENCE AND TECHNOLOGY
2010年
2期
93-96
,共4页
余作龙%姜岷%吴昊%陈可泉%韦萍
餘作龍%薑岷%吳昊%陳可泉%韋萍
여작룡%강민%오호%진가천%위평
陶瓷膜%丁二酸发酵液%膜分离%膜清洗
陶瓷膜%丁二痠髮酵液%膜分離%膜清洗
도자막%정이산발효액%막분리%막청세
ceramic membrane%succinic acid fermentation%membrane separation%membrane cleaning
对陶瓷膜过滤丁二酸发酵液的条件进行研究.考察在不同压差下,发酵液的pH以及浓缩倍数对膜通量的影响,并对膜清洗条件进行选择.结果表明在0.3 MPa压差下,发酵液调节pH至4.5,可获得最大膜通量,浓缩到7倍最佳.菌体截留率达到98.37%,蛋白质去除率为89.67%,总有机碳下降约40%.而膜污染后先后用1%次氯酸钠,1%氢氧化钠+0.5%EDTA清洗,可以恢复膜通量.实验表明,可以将陶瓷膜用于分离丁二酸发酵液,有利于简化操作步骤,提高生产效率.
對陶瓷膜過濾丁二痠髮酵液的條件進行研究.攷察在不同壓差下,髮酵液的pH以及濃縮倍數對膜通量的影響,併對膜清洗條件進行選擇.結果錶明在0.3 MPa壓差下,髮酵液調節pH至4.5,可穫得最大膜通量,濃縮到7倍最佳.菌體截留率達到98.37%,蛋白質去除率為89.67%,總有機碳下降約40%.而膜汙染後先後用1%次氯痠鈉,1%氫氧化鈉+0.5%EDTA清洗,可以恢複膜通量.實驗錶明,可以將陶瓷膜用于分離丁二痠髮酵液,有利于簡化操作步驟,提高生產效率.
대도자막과려정이산발효액적조건진행연구.고찰재불동압차하,발효액적pH이급농축배수대막통량적영향,병대막청세조건진행선택.결과표명재0.3 MPa압차하,발효액조절pH지4.5,가획득최대막통량,농축도7배최가.균체절류솔체도98.37%,단백질거제솔위89.67%,총유궤탄하강약40%.이막오염후선후용1%차록산납,1%경양화납+0.5%EDTA청세,가이회복막통량.실험표명,가이장도자막용우분리정이산발효액,유리우간화조작보취,제고생산효솔.
The conditions of ultrafiltrate succinic acid by ceramic membrane was researched.The influences of pressure, pH and concentration ratio of fermentation on the membrane flux were studied.The optimal membrame cleaning methods were chosen.The result showed that under pressure 0.3 MPa and the fermentation broth of pH 4.5, the maximum membrane flux was attained.The cell retention rate of 98.73% retained, the removal of protein was 89.67%, and the contain of the total organic carbon declined about 40%, respectively.For cleaning the contaminated membrane, its flux could be restored by using 1% sodium hypochlorite, 1% sodium hydroxide + 0.5% EDTA washing, in turn.This work shows that ceramic membrane could be used for separating succinic acid fermentation broth, which helps to simplify the operation steps and increase productivity.