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室温离子液体对氨基苯磺酸的萃取性能 被引量:15
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作者 樊静 范云场 +1 位作者 王键吉 崔凤灵 《化学学报》 SCIE CAS CSCD 北大核心 2006年第14期1495-1499,共5页
系统研究了[C4mim][PF6],[C6mim][PF6],[C6mim][BF4]和[C8mim][BF4]室温离子液体对间氨基苯磺酸、对氨基苯磺酸稀水溶液的萃取平衡.实验结果表明:萃取温度和相体积比的变化对分配比影响不大;水相pH值对萃取平衡有较大的影响,氨基苯磺酸... 系统研究了[C4mim][PF6],[C6mim][PF6],[C6mim][BF4]和[C8mim][BF4]室温离子液体对间氨基苯磺酸、对氨基苯磺酸稀水溶液的萃取平衡.实验结果表明:萃取温度和相体积比的变化对分配比影响不大;水相pH值对萃取平衡有较大的影响,氨基苯磺酸在离子液体/水体系中的分配比在pH=4.2时达到最大值;水相中CaCl2或Na2SO4的存在能较大幅度地提高氨基苯磺酸的分配比;离子液体的阴离子的性质对分配比有显著的影响,阴离子为[BF4]-的离子液体对氨基苯磺酸的萃取能力大于阴离子为[PF6]-的离子液体;咪唑环上烷基链的长度也对萃取效果有一定的影响.在所研究的离子液体中,[C6mim][BF4]和[C8mim][BF4]对氨基苯磺酸有较好的萃取性能,且萃取相中的氨基苯磺酸可回收利用,离子液体也可循环使用. 展开更多
关键词 室温离子液体 氨基苯磺酸 水溶液萃取
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离子液体萃取阿魏酸和咖啡酸的性能研究 被引量:13
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作者 余燕影 张玮 曹树稳 《分析化学》 SCIE EI CAS CSCD 北大核心 2007年第12期1726-1730,共5页
以1-甲基-3-丁基咪唑六氟磷酸盐([C4mim][PF6])和1-甲基-3-己基咪唑六氟磷酸盐([C6mim][PF6])离子液体为萃取剂,采用紫外分光光度法研究了溶液pH值、温度、相比率及盐的种类和浓度对其萃取阿魏酸和咖啡酸效率的影响,考察了被萃取物的回... 以1-甲基-3-丁基咪唑六氟磷酸盐([C4mim][PF6])和1-甲基-3-己基咪唑六氟磷酸盐([C6mim][PF6])离子液体为萃取剂,采用紫外分光光度法研究了溶液pH值、温度、相比率及盐的种类和浓度对其萃取阿魏酸和咖啡酸效率的影响,考察了被萃取物的回收及离子液体的循环使用,探讨了两种离子液体替代传统有机溶剂阿魏酸和咖啡酸的可能性。实验结果表明:萃取温度和无机盐的种类及浓度对FA和CA萃取效率的影响较小;水相pH值对萃取效率有较大的影响,萃取FA适宜pH应小于3.67,萃取CA适宜pH应小于3.71;被萃取物浓度增大,萃取效率降低,而相体积比增大其萃取效率升高;两种离子液体对FA和CA的萃取效率[C4mim][PF6]大于[C6mim][PF6],同种离子液体对FA的萃取效率大于CA;在萃取相中的FA和CA可定量回收,且被萃取物中离子液体的残留[C6mim][PF6]小于[C4mim][PF6],离子液体可循环使用。 展开更多
关键词 离子液体 阿魏酸 咖啡酸 水溶液萃取
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Enzymatic Aqueous Extraction of Soybean Oil 被引量:1
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作者 钱俊青 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2001年第2期212-216,共5页
The procedure of enzymatic aqueous extraction of soybean oil was assessed when two-step controlled enzymatic hydrolysis was applied. With aqueous extraction of soybean oil-containing protein, the highest yield of oil ... The procedure of enzymatic aqueous extraction of soybean oil was assessed when two-step controlled enzymatic hydrolysis was applied. With aqueous extraction of soybean oil-containing protein, the highest yield of oil was 96.1% at the optimized conditions studied. Soybean oil-containing protein was hydrolyzed and resulted in releasing part of oil. The separated protein that contained 40% oil was enriched due to its adsorption capacity of released oil, the average oil extraction yeild reached 93.5%. Then the high oil content protein was hydrolyzed again to release oil by enzyme, the oil extraction yeild was 80.4%. As a result, high quality of soybean oil was obtained and the content of total oil yield was 74.4%. 展开更多
关键词 soybean oil aqueous extraction enzymatic methods
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Removal of mercaptans from light oils using ionic liquid–NaOH aqueous solution as extractants 被引量:1
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作者 Jianwei Li Xiang Li +1 位作者 Yan Liu Jie Zhang 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2017年第2期171-174,共4页
The application of ionic liquids as alternatives to conventional organic solvents in the extraction process has been investigated. In the present study, fourteen species of imidazolium-based ionic liquids were added i... The application of ionic liquids as alternatives to conventional organic solvents in the extraction process has been investigated. In the present study, fourteen species of imidazolium-based ionic liquids were added into the NaOH (aq) to remove the mercaptans. The influences of anion species and cation alkyl chain length of the imidazolium-based ionic liquids on the performance of mercaptan removal from light oils have been discussed. The efficiency of extraction for mercaptans exhibited the order of [Ac]- 〉 [OH]- [Br]- 〉 [BF4]-. The longer alkyl chain imidazolium-based ionic liquids contributed to enhance desulfurization rate of l-butyl mercaptan. 100% desulfurization rate of l-butyl mercaptan was achieved by the anion of Ac- ionic liquids and NaOH (aq) at a volume ratio of 40:1 (V(oil]:Vfionic liouid)) and a short eouilibrium time within 10 min. 展开更多
关键词 ExtractionIonic liquidsNaOHLight oilMercaptan removal
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Phenol Removal from Aqueous Solution Through Hollow Fiber Membrane Extraction 被引量:1
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作者 李云峰 骆广生 戴猷元 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 1999年第2期104-109,共6页
In this work, mass transfer mechanism was studied for 50%TBP (in kerosene)-phenol-water as the working system in different hydrophobic microporous hollow fiber modules. The effect of different operating conditions on ... In this work, mass transfer mechanism was studied for 50%TBP (in kerosene)-phenol-water as the working system in different hydrophobic microporous hollow fiber modules. The effect of different operating conditions on the removal of phenol was analyzed. Solvent entrainment in this process was detected with MALVERN-2600 laser pellet diameter analytical equipment. Experimental results indicate the mass transfer coefficient is increased while the two phase flow rates are increased. With increases in the flow rate of the water phase, the removal ratio of phenol will be decreased. Highly effective removal of phenol could be reached by changing the experimental conditions and the module configuration. The solvent entrainment in the water phase in the membrane extraction process was found to be 5%—8% of that in conventional liquid-liquid extraction process. Thus, solvent pollution could be better controlled. 展开更多
关键词 hollow fiber EXTRACTION PHENOL
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Solvent extraction of lanthanum and cerium ions from hydrochloric acidic aqueous solutions using partly saponified 2-ethylhexyl phosphonic acid mono-2-ethylhexyl ester 被引量:2
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作者 Hailong Hou Jianhong Xu +1 位作者 Yundong Wang Jinnan Chen 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2016年第1期79-85,共7页
In order to clarify the extraction process with saponified extractant, the solvent extraction experiments of rare earth elements(REEs), lanthanum and cerium, by using partly saponified 2-ethylhexyl phosphoric acid mon... In order to clarify the extraction process with saponified extractant, the solvent extraction experiments of rare earth elements(REEs), lanthanum and cerium, by using partly saponified 2-ethylhexyl phosphoric acid mono-2-ethylhexyl ester(EHEHPA, HL) from hydrochloric acidic solutions have been performed. The concentration of initial aqueous rare earth ion was in a range of 0.0010–0.1000 mol·L^(-1); EHEHPA in a range of 0.2877–0.8631 mol·L^(-1) with saponification rate of 0.3(mole fraction), and the initial aqueous p H in a range of 1.00–4.00. Firstly, the extracted species were determined by the saturation extraction capacity method. Secondly, according to the equilibrium aqueous pH values, the extraction processes were divided into three different categories: extraction with saponified EHEHPA, extraction with un-saponified EHEHPA, and hydrolysis process. Finally, for the first two processes, in order to predict the distribution ratio, two semi-empirical calculation models were developed with.The calculation results are in good agreement well with the experimental data. 展开更多
关键词 Partly saponified EHEHPA Lanthanum Cerium Solvent extraction Semi-empirical models Equilibrium distribution
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