食品与发酵工业
食品與髮酵工業
식품여발효공업
FOOD AND FERMENTATION INDUSTRIES
2001年
2期
5-7
,共3页
张峻%何志敏%胡鲲%冯耀宇%张志钢
張峻%何誌敏%鬍鯤%馮耀宇%張誌鋼
장준%하지민%호곤%풍요우%장지강
β-甘露聚糖酶%地衣芽孢杆菌%制备
β-甘露聚糖酶%地衣芽孢桿菌%製備
β-감로취당매%지의아포간균%제비
提出了一种地衣芽孢杆菌β-甘露聚糖酶制备的工艺。结果表明:在设定的操作条件下,6.6L自控罐发酵酶活可达260u/mL。发酵液用AlCl3与壳聚糖絮凝预处理后,絮凝体喷雾干燥可制成900u/g的酶粉,适合饲料和造纸工业使用;絮凝上清液先以平均截留分子质量5万的中空纤维聚砜膜分离,透过液再用平均截留分子质量1万的中空纤维聚砜膜浓缩后,喷雾干燥可制成11000u/g的酶粉,适合食品和医药工业使用。以上工艺酶活总收率88%,并易于工业放大。
提齣瞭一種地衣芽孢桿菌β-甘露聚糖酶製備的工藝。結果錶明:在設定的操作條件下,6.6L自控罐髮酵酶活可達260u/mL。髮酵液用AlCl3與殼聚糖絮凝預處理後,絮凝體噴霧榦燥可製成900u/g的酶粉,適閤飼料和造紙工業使用;絮凝上清液先以平均截留分子質量5萬的中空纖維聚砜膜分離,透過液再用平均截留分子質量1萬的中空纖維聚砜膜濃縮後,噴霧榦燥可製成11000u/g的酶粉,適閤食品和醫藥工業使用。以上工藝酶活總收率88%,併易于工業放大。
제출료일충지의아포간균β-감로취당매제비적공예。결과표명:재설정적조작조건하,6.6L자공관발효매활가체260u/mL。발효액용AlCl3여각취당서응예처리후,서응체분무간조가제성900u/g적매분,괄합사료화조지공업사용;서응상청액선이평균절류분자질량5만적중공섬유취풍막분리,투과액재용평균절류분자질량1만적중공섬유취풍막농축후,분무간조가제성11000u/g적매분,괄합식품화의약공업사용。이상공예매활총수솔88%,병역우공업방대。
A process has been developed for the preparation of β-mannanase from Bacillus licheniformis. The enzyme activity was 260 u/mL when incubated in a 6.6L fermentor under the designed conditions. After pretreatment of culture broth using flocculants of AlCl3 and chitosan,the floc was spray-dried (900 u/g) for use in feed or pulp industries, while the supernatant was fractionated by polysulfone membrane and then concentrated by polysulfone membrane. The final product was spray-dried (11 000u/g) for use in food or pharmaceutical industries. The proposed process resulted in the total yield of β-mannanase activity of 88 % and is easily scale-up.