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采用超滤和纳滤耦合技术对发酵生产的苄青霉素进行分离与纯化。

Separation and purification of benzylpenicillin produced by fermentation using coupled ultrafiltration and nanofiltration technologies.

作者信息

Tessier L, Bouchard P, Rahni M

机构信息

Collège Shawinigan, Département de Biologie et Biotechnologies, 2263 Avenue du Collège, Shawinigan (Qué.), Canada G9N 6V8.

出版信息

J Biotechnol. 2005 Mar 2;116(1):79-89. doi: 10.1016/j.jbiotec.2004.09.002. Epub 2004 Dec 28.

Abstract

The purpose of this study was to evaluate the capacity of using coupled ultrafiltration-nanofiltration technologies for separation and purification of benzylpenicillin (BP). More specifically, we verified the efficiency of three ultrafiltration (UF) membranes (cut-off of 5000, 30,000 and 100,000 Da) to remove impurities that cause stable emulsion during the chemical extraction of the antibiotic. We also tested the effectiveness of a nanofiltration (NF) membrane (cut-off of 300 Da) to concentrate the benzylpenicillin recovered from permeates and to decrease the osmotic pressure by reducing the ionic charge of the broth. Results have shown that high recovery (89.0-91.0%) can be obtained in permeate generated by the 30,000 and 100,000 UF membranes, but a slight emulsion will be formed during phase separation. With the 5000 UF membrane, lower recovery is obtained (81.0%) but no emulsion is produced, leading to a high solvent extraction yield (94.6%). The nanofiltration of 30,000 and 100,000 UF permeates leads to very high recovery (98.0%), but stable emulsions are formed, reducing the chemical extraction yield (80.0-82.6%). For the nanofiltration of 5000 UF permeate, excellent recovery of the antibiotic is noted (97.4%) leading to high extraction yield (92.4%) with no emulsion formed. Diafiltration step should be applied during UF procedure in order to increase the antibiotic recovery in the generated permeates.

摘要

本研究的目的是评估采用超滤-纳滤耦合技术分离和纯化苄青霉素(BP)的能力。更具体地说,我们验证了三种超滤(UF)膜(截留分子量分别为5000、30000和100000 Da)去除抗生素化学提取过程中导致形成稳定乳液的杂质的效率。我们还测试了一种纳滤(NF)膜(截留分子量为300 Da)浓缩从渗透液中回收的苄青霉素并通过降低发酵液离子电荷来降低渗透压的有效性。结果表明,30000和100000截留分子量的超滤膜产生的渗透液中可获得较高的回收率(89.0 - 91.0%),但在相分离过程中会形成轻微乳液。使用截留分子量为5000的超滤膜时,回收率较低(81.0%),但不会产生乳液,从而获得较高的溶剂萃取产率(94.6%)。对30000和100000截留分子量的超滤渗透液进行纳滤,回收率非常高(98.0%),但会形成稳定乳液,降低化学萃取产率(80.0 - 82.6%)。对于截留分子量为5000的超滤渗透液进行纳滤,抗生素回收率极佳(97.4%),萃取产率较高(92.4%),且未形成乳液。在超滤过程中应应用错流过滤步骤,以提高产生的渗透液中抗生素的回收率。

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