The mechanism of adsorbing indium(Ⅲ) from sulfate solutions with CL-P204Levextrel resin containing di(-2-ethylhexyl) phosphoric acid was examined by batch operation andinfrared spectra. The results showed that the P2...The mechanism of adsorbing indium(Ⅲ) from sulfate solutions with CL-P204Levextrel resin containing di(-2-ethylhexyl) phosphoric acid was examined by batch operation andinfrared spectra. The results showed that the P204 adsorbed on the resin behaved in the similar wayto solvent extraction except that it was as a monomer in resin adsorbing but in dimeric form insolvent extraction. Three factors including temperature, indium(Ⅲ) concentration of solution, andthe size of resin particles which influence the In^(3+)/H^+ exchange on CL-P204 Levextrel resin wereinvestigated by the modified limited batch technique in order to determine the kinetics ofIn^(3+)/H^+ exchange. It was found that the rate of ion exchange increased with the temperature andthe concentration of solution increasing and with the size of the resin particles decreasing.According to the expression developed by Boyd et al., the controlling factor of In^(3+)/H^+ exchangeon CL-P204 Levextrel resin was the diffusion through the resin particles. The effective diffusioncoefficient, activation energy, and entropy of activation in the particle-diffusion were determinedas 1.57 x 10^(-10) m^2/s, 11.9 kJ/mol, -84.1 J/(mol·K), respectively.展开更多
研究了D418螯合树脂在NaOAc-HOAc缓冲溶液中对In^(3+)的吸附性能与机理,结果表明,D418树脂在不同温度下吸附In^(3+)的表观吸附速率常数分别为k_(293K)=2.07×10^(-4)s^(-1),k_(313K)=3.49×10^(-4)s^(-1),k_(393K)=1.42×10...研究了D418螯合树脂在NaOAc-HOAc缓冲溶液中对In^(3+)的吸附性能与机理,结果表明,D418树脂在不同温度下吸附In^(3+)的表观吸附速率常数分别为k_(293K)=2.07×10^(-4)s^(-1),k_(313K)=3.49×10^(-4)s^(-1),k_(393K)=1.42×10^(-3)s^(-1),表观吸附活化能Ea=38.84 k J·mol^(-1);树脂吸附In^(3+)热力参数△H=96.27 k J·mol^(-1),△S=349.19 J·(mol·K)^(-1),△G_(298K)=-6.04 k J·mol^(-1);吸附过程能较好地遵循Langmuir等温吸附规律。采用红外光谱方法探讨了吸附机理,结果表明,D418树脂功能基氨基和磷酸根与In^(3+)形成了配位键。展开更多
A new extractant,[N,N-di(2-ethylhexyl)amino]methylphenylphosphinic acid(DEAPP),was synthesized to develop the mutual separation techniques of In(III),Ga(III) and Zn(II).The extraction selectivity for In(III),Ga(III)an...A new extractant,[N,N-di(2-ethylhexyl)amino]methylphenylphosphinic acid(DEAPP),was synthesized to develop the mutual separation techniques of In(III),Ga(III) and Zn(II).The extraction selectivity for In(III),Ga(III)and Zn(II) with DEAPP was higher than that of the commercial phosphorus acid extractants such as D2 EHPA and PC-88 A.The extraction selectivity for metal ions in 1 mol·L-1aqueous ammonium nitrate solution with DEAPP was in the following order:In(III) N Ga(III) N Zn(II).These selective extraction behaviors indicate that the amino moiety of DEAPP plays an important role in the mutual separation of In(III),Ga(III) and Zn(II).The extraction equilibria of In(III),Ga(III) and Zn(II) with DEAPP(=HR) were expressed by the following reactions:In3++ 2HRT2In R3HRT + 3H+,Ga3++ 1.5HRT-2+ NO3 GaR 2eHRT N O3T + 2H+,and Zn2++ 2HRT2 Zn R2HRT2+ 2H+.The extraction equilibrium constants of In(III),Ga(III) and Zn(II) with DEAPP were determined to be Kex,M= 1.7 × 104[dm3·mol-1],4.17 [(dm3·mol-1)0.5],and 1.55 x 10-2[–],respectively.展开更多
A selective method has been developed for the extraction chromatography of aluminium(Ⅲ) and its separation from several metal ions with a chromatographic column containing N-n-octylaniline ( a liquid anion exchanger)...A selective method has been developed for the extraction chromatography of aluminium(Ⅲ) and its separation from several metal ions with a chromatographic column containing N-n-octylaniline ( a liquid anion exchanger) coated on silanized silica gel as a stationary phase. The aluminium(Ⅲ) was quantitatively extracted with the 0. 065 mol / L N-n-octylaniline in 0. 013 to 0. 05 mol / L sodium succinate at a flow rate of 1. 0 mL / min. The extracted metal ion has been recovered by eluting with 25. 0 mL of 0. 05 mol / L hydrochloric acid and estimated spectrophotometrically with aurintricarboxylic acid. The effects of the acid concentration,the reagent concentration,the flow rate and the eluting agents have been investigated. The log-log plots of distribution coefficient ( K d ( Al(Ⅲ) ) ) versus N-n-octylaniline concentration in 0. 005 and 0. 007 mol / L sodium succinate gave the slopes of 0. 5 and 0. 7 respectively and showed the probable composition of the extracted species was 1∶ 1 ( metal to amine ratio ) and the nature of extracted species was [RR' NH + 2 Al succinate 2 ] org. . The extraction of aluminium(Ⅲ) was carried out in the presence of various ions to ascertain the tolerance limit of individual ions. Aluminium(Ⅲ) has been separated from multicomponent mixtures,pharmaceutical samples and synthetic mixtures corresponding to alloys. A scheme for mutual separation of aluminium(Ⅲ) ,indium(Ⅲ) ,gallium(Ⅲ) and thallium(Ⅲ) has been developed by using suitable masking agents. The method is fast,accurate and precise.展开更多
文摘The mechanism of adsorbing indium(Ⅲ) from sulfate solutions with CL-P204Levextrel resin containing di(-2-ethylhexyl) phosphoric acid was examined by batch operation andinfrared spectra. The results showed that the P204 adsorbed on the resin behaved in the similar wayto solvent extraction except that it was as a monomer in resin adsorbing but in dimeric form insolvent extraction. Three factors including temperature, indium(Ⅲ) concentration of solution, andthe size of resin particles which influence the In^(3+)/H^+ exchange on CL-P204 Levextrel resin wereinvestigated by the modified limited batch technique in order to determine the kinetics ofIn^(3+)/H^+ exchange. It was found that the rate of ion exchange increased with the temperature andthe concentration of solution increasing and with the size of the resin particles decreasing.According to the expression developed by Boyd et al., the controlling factor of In^(3+)/H^+ exchangeon CL-P204 Levextrel resin was the diffusion through the resin particles. The effective diffusioncoefficient, activation energy, and entropy of activation in the particle-diffusion were determinedas 1.57 x 10^(-10) m^2/s, 11.9 kJ/mol, -84.1 J/(mol·K), respectively.
文摘研究了D418螯合树脂在NaOAc-HOAc缓冲溶液中对In^(3+)的吸附性能与机理,结果表明,D418树脂在不同温度下吸附In^(3+)的表观吸附速率常数分别为k_(293K)=2.07×10^(-4)s^(-1),k_(313K)=3.49×10^(-4)s^(-1),k_(393K)=1.42×10^(-3)s^(-1),表观吸附活化能Ea=38.84 k J·mol^(-1);树脂吸附In^(3+)热力参数△H=96.27 k J·mol^(-1),△S=349.19 J·(mol·K)^(-1),△G_(298K)=-6.04 k J·mol^(-1);吸附过程能较好地遵循Langmuir等温吸附规律。采用红外光谱方法探讨了吸附机理,结果表明,D418树脂功能基氨基和磷酸根与In^(3+)形成了配位键。
基金supported by The Environment Research and Technology Development Fund (3K133005)
文摘A new extractant,[N,N-di(2-ethylhexyl)amino]methylphenylphosphinic acid(DEAPP),was synthesized to develop the mutual separation techniques of In(III),Ga(III) and Zn(II).The extraction selectivity for In(III),Ga(III)and Zn(II) with DEAPP was higher than that of the commercial phosphorus acid extractants such as D2 EHPA and PC-88 A.The extraction selectivity for metal ions in 1 mol·L-1aqueous ammonium nitrate solution with DEAPP was in the following order:In(III) N Ga(III) N Zn(II).These selective extraction behaviors indicate that the amino moiety of DEAPP plays an important role in the mutual separation of In(III),Ga(III) and Zn(II).The extraction equilibria of In(III),Ga(III) and Zn(II) with DEAPP(=HR) were expressed by the following reactions:In3++ 2HRT2In R3HRT + 3H+,Ga3++ 1.5HRT-2+ NO3 GaR 2eHRT N O3T + 2H+,and Zn2++ 2HRT2 Zn R2HRT2+ 2H+.The extraction equilibrium constants of In(III),Ga(III) and Zn(II) with DEAPP were determined to be Kex,M= 1.7 × 104[dm3·mol-1],4.17 [(dm3·mol-1)0.5],and 1.55 x 10-2[–],respectively.
基金supported by BCUD,Pune University for providing financial assistance in form of a research project
文摘A selective method has been developed for the extraction chromatography of aluminium(Ⅲ) and its separation from several metal ions with a chromatographic column containing N-n-octylaniline ( a liquid anion exchanger) coated on silanized silica gel as a stationary phase. The aluminium(Ⅲ) was quantitatively extracted with the 0. 065 mol / L N-n-octylaniline in 0. 013 to 0. 05 mol / L sodium succinate at a flow rate of 1. 0 mL / min. The extracted metal ion has been recovered by eluting with 25. 0 mL of 0. 05 mol / L hydrochloric acid and estimated spectrophotometrically with aurintricarboxylic acid. The effects of the acid concentration,the reagent concentration,the flow rate and the eluting agents have been investigated. The log-log plots of distribution coefficient ( K d ( Al(Ⅲ) ) ) versus N-n-octylaniline concentration in 0. 005 and 0. 007 mol / L sodium succinate gave the slopes of 0. 5 and 0. 7 respectively and showed the probable composition of the extracted species was 1∶ 1 ( metal to amine ratio ) and the nature of extracted species was [RR' NH + 2 Al succinate 2 ] org. . The extraction of aluminium(Ⅲ) was carried out in the presence of various ions to ascertain the tolerance limit of individual ions. Aluminium(Ⅲ) has been separated from multicomponent mixtures,pharmaceutical samples and synthetic mixtures corresponding to alloys. A scheme for mutual separation of aluminium(Ⅲ) ,indium(Ⅲ) ,gallium(Ⅲ) and thallium(Ⅲ) has been developed by using suitable masking agents. The method is fast,accurate and precise.
