摘要
在发酵生产L-精氢酸的提取工艺中,对提取总收率影响较大的离子交换工艺进行了研究。结果表明,用国产强酸性001×7树脂对发酵液中的L-精氨酸进行动态交换吸附,当上柱流速控制在1/50vvm条件下,其交换量为1.135meq/ml湿树脂。用2.5mol/L氨水洗脱,流速控制在1/50vvm时,其洗脱效果最好。用国产201×4树脂进行脱色,每10ml树脂可脱色160ml以上的洗脱液,透光度大于90%,几乎不发生交换吸附L-精氨酸的现象。离子交换工序收率大于95%。
The study showed that the L-argmine-adsorbing capacity of strong-acidic resin 001×7 was 1.135 meq per ml of wet resin by controlling the flow rate of the broth at 1/52 vvm, and the efficiency of the elution was higher by using ammnia water as an eluent at the flow rate of 1/50 vvm. About 160 ml of the above eluant was decolorized with 10 ml of 201×4 resin, the transparance of the decolorized eluant was over 90%, and no adsorption of L-arginine by the 201×4 resin was observed. Under the controlled conditions, the extraction yield of L-arginine reached over 95%.
出处
《微生物学通报》
CAS
CSCD
北大核心
1992年第5期273-277,共5页
Microbiology China
