Separation of xylo-oligosaccharides from enzymatic hydrolytes using membrane reactor

被引:9
|
作者
Yang, FG [1 ]
Fang, Z
Xu, Y
Yao, CC
Yu, SY
Zhu, QX
机构
[1] Cent S Univ, Coll Chem & Chem Engn, Changsha 410083, Peoples R China
[2] Nanjing Forestry Univ, Coll Chem Engn, Nanjing 210037, Peoples R China
[3] Anhui Normal Univ, Coll Chem & Mat Sci, Wuhu 241000, Peoples R China
来源
关键词
xylo-oligosaccharides; enzymatic hydrolystes; membrane reactor; separation;
D O I
10.1007/s11771-003-0052-4
中图分类号
TF [冶金工业];
学科分类号
0806 ;
摘要
The time course of xylo-oligosaccharides concentration and xylo-oligosaccharides yield in the separation xylo-oligosaccharides from enzymatic hydrolytes was studied using a membrane reactor with constant permeate flux of 4 L . m(-2) . h(-1). The results show that xylanases retain 90%, of its activity in the reactor. The concentration xylo-oligosaccharides achieves the maximum, about 5. 48 g/L in. 30 min. The difference of xylo-oligosaccharides in the retentate and permeate stream is low, <0. 62 g/L, therefore it can permeate through membrane. Under the operating conditions that xylan concentration is 30. 0 g/L, pH 5.0, operating pressure 16 kPa, temperature 48 degreesC, feed velocity 400 mL/min, reaction volume 400 mL, enzyme dosage 10%(volume fraction), dilution rate 1-h(-1), and enzymatic hydrolysis time 195 min, the yield of xylo-oligosaccharides reaches 31. 69%.
引用
收藏
页码:122 / 125
页数:4
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