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1-丁烯分离工艺的技术对比 被引量:5
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作者 王海 《当代化工》 CAS 2004年第3期134-135,152,共3页
介绍 1 丁烯分离技术 ,建议在MTBE后建立 1 丁烯分离装置。推荐了MTBE后的炼油厂C4综合利用的技术路线 ,并进行了经济效益估算。
关键词 MTBE后炼油厂C4 1-丁烯 顺-反-2-丁烯 烃化油 甲乙酮 分离技术
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Separation and identification of cis and trans isomers of 2-butene-1,4-diol and lafutidine by HPLC and LC-MS 被引量:1
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作者 潘春秀 徐秀珠 +2 位作者 何红梅 蔡小军 张雪君 《Journal of Zhejiang University-Science B(Biomedicine & Biotechnology)》 SCIE EI CAS CSCD 2005年第1期74-78,共5页
The cis and trans isomers separation of 2-butene-1,4-diol and lafutidine were studied by HPLC on two kinds of chiral columns: (S,S)-Whelk-O 1 and ChiraSpher. The isomers of 2-butene-1,4-diol can be separated on both c... The cis and trans isomers separation of 2-butene-1,4-diol and lafutidine were studied by HPLC on two kinds of chiral columns: (S,S)-Whelk-O 1 and ChiraSpher. The isomers of 2-butene-1,4-diol can be separated on both chiral columns while the isomers of lafutidine can only be resolved on ChiraSpher column. The influence of different type and amount of mobile phase modifier on the isomers separation was extensively studied. The resolution of cis and trans isomers of 2-butene-1,4-diol was 2.61on (S,S)-Whelk-O 1 column with hexane-ethanol (97:3, v/v) as the mobile phase. The resolution of lafutidine was 1.89 on ChiraSpher column with hexane-ethanol-THF-diethylamine (92:3:5:0.1, v/v/v/v) as the mobile phase. LC-MS methods were developed to identify the isomer peaks. 展开更多
关键词 2-butene-1 4-diol LAFUTIDINE Isomers separation (S S)-Whelk-O 1 ChiraSpher LC-MS
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Process Design for Separating C4 Mixtures by Extractive Distillation 被引量:3
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作者 雷志刚 陈标华 李建伟 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2003年第3期297-301,共5页
C4 components are useful in industry and should be separated as individuals. A new process was proposed to separate them by extractive distillation, with the advantages of low equipment investment, energy consumption... C4 components are useful in industry and should be separated as individuals. A new process was proposed to separate them by extractive distillation, with the advantages of low equipment investment, energy consumption and liquid load in the columns. One principle to improve the extractive distillation process was put forward. Moreover, the analysis of operation state of the new process was done. There were eight operation states found for the whole process, but only one operation state was desirable. This work provides a way to effectively separate C4 mixtures and helps the reasonable utilization of C4 resource. 展开更多
关键词 process design extractive distillation C4 mixtures operation state
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