A kind of Levextrel resin separation process was developed for separation ofindium (III), gallium (III), and zinc (II) from aqueous sulfate solution with Levextrel resincontaining di(2-ethylhexyl) phosphoric acid (CL-...A kind of Levextrel resin separation process was developed for separation ofindium (III), gallium (III), and zinc (II) from aqueous sulfate solution with Levextrel resincontaining di(2-ethylhexyl) phosphoric acid (CL-P 204). The aim of the research is to collectpreliminary results for a pilot-scale production. Properties of adsorbing indium (III), gallium(III), and zinc (II) from sulfate solution with the Levextrel resin were first studied by batchoperation and column operation. The optimum pH, adsorption capacities and concentrations ofstripping agents for indium (III), gallium (III) were tested. The separation order of indium (III),gallium (III), and zinc (II) from sulfate solution with CL-P 204 Levextrel resin was found thatindium (III) could be first separated by adsorbing at the acidity of 1.0 mol/L whereas gallium (III)and zinc (II) could not, and they were adsorbed together by adsorbing at pH =2.8, then separatedfrom each other by stripping with 0.1 and 0.5 mol/L hydrochloric acid, respectively. The recoveriesof three metal ions were all higher than 99 percent. The cyclic properties of this resin are well.展开更多
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
文摘A kind of Levextrel resin separation process was developed for separation ofindium (III), gallium (III), and zinc (II) from aqueous sulfate solution with Levextrel resincontaining di(2-ethylhexyl) phosphoric acid (CL-P 204). The aim of the research is to collectpreliminary results for a pilot-scale production. Properties of adsorbing indium (III), gallium(III), and zinc (II) from sulfate solution with the Levextrel resin were first studied by batchoperation and column operation. The optimum pH, adsorption capacities and concentrations ofstripping agents for indium (III), gallium (III) were tested. The separation order of indium (III),gallium (III), and zinc (II) from sulfate solution with CL-P 204 Levextrel resin was found thatindium (III) could be first separated by adsorbing at the acidity of 1.0 mol/L whereas gallium (III)and zinc (II) could not, and they were adsorbed together by adsorbing at pH =2.8, then separatedfrom each other by stripping with 0.1 and 0.5 mol/L hydrochloric acid, respectively. The recoveriesof three metal ions were all higher than 99 percent. The cyclic properties of this resin are well.
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.
