The extraction of cerium(IV) from sulphuric acid medium with Di(2-ethylhexyl) phosphoric acid(DEHPA) was studied. The influence of sulphate ion, acidity, extractant concentration as well as the presence of fluoride io...The extraction of cerium(IV) from sulphuric acid medium with Di(2-ethylhexyl) phosphoric acid(DEHPA) was studied. The influence of sulphate ion, acidity, extractant concentration as well as the presence of fluoride ion on the extraction of Ce(IV) was investigated, and the extraction mechanism was also discussed. The results show that sulphate ion can inhibit the extraction of Ce(IV) significantly due to its complexation with Ce(IV). Fluoride ion can enhance Ce(IV) extraction dramatically by the formation of CeF_2^(2+) and less amount of CeF^(3+) which can almost be extracted completely. Nevertheless, in the case as F/Ce(mole ratio) in the initial aqueous phase is approximately more than 1.5, the precipitate will be formed and the extraction can not be progressed smoothly.展开更多
文章采用恒界面法对乳化液膜分离Cr(Ⅲ)的液膜内相反萃步骤进行了研究,考察了搅拌速度、温度、界面面积、水相p H值、DEHPA[二(2-乙基己基)磷酸]浓度和络合物浓度对反萃速率的影响,得到反萃反应的动力学与热力学数据,并推导出反萃的反...文章采用恒界面法对乳化液膜分离Cr(Ⅲ)的液膜内相反萃步骤进行了研究,考察了搅拌速度、温度、界面面积、水相p H值、DEHPA[二(2-乙基己基)磷酸]浓度和络合物浓度对反萃速率的影响,得到反萃反应的动力学与热力学数据,并推导出反萃的反应机理。实验结果表明:搅拌速度大于0.45 m/s时出现与搅拌强度无关的化学反应控制"坪区",且反萃速率与界面面积成正比,此时反应属于扩散和化学反应共同控制,并且反应主要发生在相界面上;由温度与反萃速率的关系得知,该反萃反应是一个放热反应,反应的活化能Ea=24.25 k J/mol,焓变ΔH=-55.85 k J/mol,熵变ΔS=-566.37 J/mol,在T=308 K时ΔG=118.59 k J/mol;在控制步骤反应式中,DEHPA反应级数为0,络合物浓度和水相氢离子的反应级数为1,并推导出反萃反应的控制步骤的方程式为r=k0[Cr(OH)2HL2(o)][H+(w)]。展开更多
The process for removal of samarium from NdCl_3 solution containing a little samarium by solvent extrac-tion with unsaponated Di (2-ethyl hexyl) orthosphoric acid (DEHPA) at acidic range is reported. The in-dustri...The process for removal of samarium from NdCl_3 solution containing a little samarium by solvent extrac-tion with unsaponated Di (2-ethyl hexyl) orthosphoric acid (DEHPA) at acidic range is reported. The in-dustrial experiments have been completed on a production line of 150 t Nd_2O_3 per annum in the Baotou ThirdRare Earth Factory. As a result of 9 step counter current extraction , Sm_2 O_3 content in Nd_2 O_3 drops down to0. 08 % from 0. 5% , the purity of neodymium oxide is over 99. 5% and the direct recovery of Nd_2O_3 is 92%～ 93% .展开更多
This work focuses on the preparation and characterization of flat sheet membrane based on modified polyether ether keetone (PEEK-WC). Additives, such as dibutyl phatalate (DBP) and diethyl hexyl phosphoric acid (DEHPA...This work focuses on the preparation and characterization of flat sheet membrane based on modified polyether ether keetone (PEEK-WC). Additives, such as dibutyl phatalate (DBP) and diethyl hexyl phosphoric acid (DEHPA), were used to investigate their effect on membranes properties which are prepared by immersion precipitation. For that, several techniques were used to characterize membranes like thermal analyses, scanning electron microscopy and microanalyses. SEM pictures show versatile structures of the membranes from dense to porous membranes characterized by a sponge and finger like structure. Moreover, microanalyses of both surfaces, bottom and top surfaces show an aggregation of DEHPA at the top surface of the membrane. However, by adding dibutylphtalate, a well dispersion of the extractant was observed. Initially, micro-porous membranes were used in supported liquid membranes experiments for Ni(II) metal ions transports using diethyl hexyl phosphoric acid (DEHPA) as carrier. The extraction efficiency was very low about 28%, but enhanced by adding xylene to the organic phase. However, the modified membranes (with additives) by DBP and DEHPA were used on solid liquid extraction of Ni(II). The results show that by adding the plasticizer and the extractant, the efficiency of the system reached 63%.展开更多
A novel extractant mixture, di-2-ethylhexyl phosphate (DEHPA) plusHX, was proposed and tested for recovering gallium from sulfatesolution. It was found that the extraction capacity of DEPHA forgallium from sulfate sol...A novel extractant mixture, di-2-ethylhexyl phosphate (DEHPA) plusHX, was proposed and tested for recovering gallium from sulfatesolution. It was found that the extraction capacity of DEPHA forgallium from sulfate solution could be enhanced significantly due tothe synergistic effect of acidic extractant HX. Gallium extraction isnegligible below pH 0 and highly sensitive to pH of aqueous phase inthe range from 0 to 1, and satisfactory extraction can be gained atpH＞1. More than 96/100 Ga Extraction was obtained using 15/100 DEHPAplus 2/100 HX.展开更多
Solvent extraction equilibria of four main alkaline earth metals(magnesium, calcium, strontium and barium) with di (2-ethylhexyl)phosphoric acid (DEHPA), 2-ethylhexyl phosphonic acidmono-(2-ethylhexyl) esters, di (2, ...Solvent extraction equilibria of four main alkaline earth metals(magnesium, calcium, strontium and barium) with di (2-ethylhexyl)phosphoric acid (DEHPA), 2-ethylhexyl phosphonic acidmono-(2-ethylhexyl) esters, di (2, 4, 4-tri-methylpentyl) phosphinicacid and IR spectra of the extracts have been studied. Theselectivity order is dependent on the e/r value and hydration energyof the metal ions. The minor shift of the P→O in IR absorption ofthe alkaline earth metal extracts indicates that the interactionbetween the metal ions and P→O is much weaker for alkaline earthmetals than for transitional metals.展开更多
RE sulfate solution containing fluorine is obtained from bastnasite which is roasted in air and then leached with sulfuric acid. Solvent extraction of Ce4+ with DEHPA in sulphonating kerosene from the solution is inv...RE sulfate solution containing fluorine is obtained from bastnasite which is roasted in air and then leached with sulfuric acid. Solvent extraction of Ce4+ with DEHPA in sulphonating kerosene from the solution is investigated. It is found that fluorine ion is extracted into organic phase with Ce4+. The extraction mechanism is proposed by slope analysis and studying the influence of aqueous acidity, fluorine concentration and DEHPA concentration on CF- /cC4+ in equilibrium organic phase.展开更多
文摘The extraction of cerium(IV) from sulphuric acid medium with Di(2-ethylhexyl) phosphoric acid(DEHPA) was studied. The influence of sulphate ion, acidity, extractant concentration as well as the presence of fluoride ion on the extraction of Ce(IV) was investigated, and the extraction mechanism was also discussed. The results show that sulphate ion can inhibit the extraction of Ce(IV) significantly due to its complexation with Ce(IV). Fluoride ion can enhance Ce(IV) extraction dramatically by the formation of CeF_2^(2+) and less amount of CeF^(3+) which can almost be extracted completely. Nevertheless, in the case as F/Ce(mole ratio) in the initial aqueous phase is approximately more than 1.5, the precipitate will be formed and the extraction can not be progressed smoothly.
文摘文章采用恒界面法对乳化液膜分离Cr(Ⅲ)的液膜内相反萃步骤进行了研究,考察了搅拌速度、温度、界面面积、水相p H值、DEHPA[二(2-乙基己基)磷酸]浓度和络合物浓度对反萃速率的影响,得到反萃反应的动力学与热力学数据,并推导出反萃的反应机理。实验结果表明:搅拌速度大于0.45 m/s时出现与搅拌强度无关的化学反应控制"坪区",且反萃速率与界面面积成正比,此时反应属于扩散和化学反应共同控制,并且反应主要发生在相界面上;由温度与反萃速率的关系得知,该反萃反应是一个放热反应,反应的活化能Ea=24.25 k J/mol,焓变ΔH=-55.85 k J/mol,熵变ΔS=-566.37 J/mol,在T=308 K时ΔG=118.59 k J/mol;在控制步骤反应式中,DEHPA反应级数为0,络合物浓度和水相氢离子的反应级数为1,并推导出反萃反应的控制步骤的方程式为r=k0[Cr(OH)2HL2(o)][H+(w)]。
文摘The process for removal of samarium from NdCl_3 solution containing a little samarium by solvent extrac-tion with unsaponated Di (2-ethyl hexyl) orthosphoric acid (DEHPA) at acidic range is reported. The in-dustrial experiments have been completed on a production line of 150 t Nd_2O_3 per annum in the Baotou ThirdRare Earth Factory. As a result of 9 step counter current extraction , Sm_2 O_3 content in Nd_2 O_3 drops down to0. 08 % from 0. 5% , the purity of neodymium oxide is over 99. 5% and the direct recovery of Nd_2O_3 is 92%～ 93% .
文摘This work focuses on the preparation and characterization of flat sheet membrane based on modified polyether ether keetone (PEEK-WC). Additives, such as dibutyl phatalate (DBP) and diethyl hexyl phosphoric acid (DEHPA), were used to investigate their effect on membranes properties which are prepared by immersion precipitation. For that, several techniques were used to characterize membranes like thermal analyses, scanning electron microscopy and microanalyses. SEM pictures show versatile structures of the membranes from dense to porous membranes characterized by a sponge and finger like structure. Moreover, microanalyses of both surfaces, bottom and top surfaces show an aggregation of DEHPA at the top surface of the membrane. However, by adding dibutylphtalate, a well dispersion of the extractant was observed. Initially, micro-porous membranes were used in supported liquid membranes experiments for Ni(II) metal ions transports using diethyl hexyl phosphoric acid (DEHPA) as carrier. The extraction efficiency was very low about 28%, but enhanced by adding xylene to the organic phase. However, the modified membranes (with additives) by DBP and DEHPA were used on solid liquid extraction of Ni(II). The results show that by adding the plasticizer and the extractant, the efficiency of the system reached 63%.
文摘A novel extractant mixture, di-2-ethylhexyl phosphate (DEHPA) plusHX, was proposed and tested for recovering gallium from sulfatesolution. It was found that the extraction capacity of DEPHA forgallium from sulfate solution could be enhanced significantly due tothe synergistic effect of acidic extractant HX. Gallium extraction isnegligible below pH 0 and highly sensitive to pH of aqueous phase inthe range from 0 to 1, and satisfactory extraction can be gained atpH＞1. More than 96/100 Ga Extraction was obtained using 15/100 DEHPAplus 2/100 HX.
基金the National Natural Science Foundation of China (No. 50074028).
文摘Solvent extraction equilibria of four main alkaline earth metals(magnesium, calcium, strontium and barium) with di (2-ethylhexyl)phosphoric acid (DEHPA), 2-ethylhexyl phosphonic acidmono-(2-ethylhexyl) esters, di (2, 4, 4-tri-methylpentyl) phosphinicacid and IR spectra of the extracts have been studied. Theselectivity order is dependent on the e/r value and hydration energyof the metal ions. The minor shift of the P→O in IR absorption ofthe alkaline earth metal extracts indicates that the interactionbetween the metal ions and P→O is much weaker for alkaline earthmetals than for transitional metals.
文摘RE sulfate solution containing fluorine is obtained from bastnasite which is roasted in air and then leached with sulfuric acid. Solvent extraction of Ce4+ with DEHPA in sulphonating kerosene from the solution is investigated. It is found that fluorine ion is extracted into organic phase with Ce4+. The extraction mechanism is proposed by slope analysis and studying the influence of aqueous acidity, fluorine concentration and DEHPA concentration on CF- /cC4+ in equilibrium organic phase.
