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化学工业与工程 2009, Vol. 26 Issue (2) :119-123    DOI:
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硝酸银沉淀L-精氨酸的研究
刘凤英;翁连进;杨欣;甘林火;
华侨大学化工与制药工程系;
Investigation on L-Arginine Precipitated by Silver Nitrate
LIU Feng-ying,WENG Lian-jin,YANG Xin,GAN Lin-huo(Department of Chemical and Pharmaceutical Engineering,Huaqiao University,Quanzhou 362021,Fujian Province,China)
(Department of Chemical and Pharmaceutical Engineering,Huaqiao University,Quanzhou 362021,Fujian Province,China

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摘要 以硝酸银为沉淀剂,用稀硝酸和热氢氧化钡调节pH值,沉淀溶液中的L-精氨酸。考察沉淀温度、pH值、硝酸银与L-精氨酸的摩尔比、L-精氨酸的初始质量浓度、和L-赖氨酸对硝酸银沉淀L-精氨酸的影响。结果表明,随着温度升高沉淀率略有下降;pH值在10.0以上时沉淀率明显增大,pH值至11.0时沉淀率达到最大,继续增大pH值沉淀率基本不再变化;硝酸银与L-精氨酸的摩尔比达到2.0时,沉淀率可达90.0%以上;L-精氨酸的初始浓度应大于10.0 g/L,沉淀率才可达90.0%以上;钠离子浓度对沉淀率基本无影响,但是当铵离子浓度或L-赖氨酸与L-精氨酸的质量比增大时,沉淀率迅速下降。最后,用2.0 mol/L盐酸溶解沉淀,过滤,滤液用高效毛细管电泳检测,并与L-精氨酸标准峰比较,结果表明沉淀中的L-精氨酸可初步分离出来。
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刘凤英
翁连进
杨欣
甘林火
关键词L-精氨酸   硝酸银     
Abstract: L-arginine is precipitated when hot barium hydroxide is added to a solution containing arginine together with silver nitrate.Effects of temperature,pH,mole ratio of silver nitrate to L-arginine,initial L-arginine concentration,NH~+_4 and Na~+ concentration and mass ratio of L-lysine to L-arginine on the yield of L-arginine precipitation were investigated.Results show that,temperature has little effect on the precipitation yield,the maximum precipitation yield is reached at pH higher than 11.0.The mole ratio of silver nitrate to L-arginine should be higher than 2.0 and the initial Larginine concentration should be more than 10.0 g/L to keep over 90.0% precipitation yield.The precipitation yield hardly changes with the increase of Na~+ concentration but decreases sharply with the increase of NH~+_4 concentration and the increase of mass ratio of L-lysine to L-arginine.At last,we purified L-Arg from the precipitation using of 2.0 mol/L HCl,L-Arg of the solution was detected by HPCE.
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Received 2009-03-15; published 2009-03-15
引用本文:   
刘凤英;翁连进;杨欣;甘林火;.硝酸银沉淀L-精氨酸的研究[J].  化学工业与工程, 2009,26(2): 119-123
LIU Feng-ying,WENG Lian-jin,YANG Xin,GAN Lin-huo.Investigation on L-Arginine Precipitated by Silver Nitrate[J].  Chemcial Industry and Engineering, 2009,26(2): 119-123
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