通过液相离子交换试验研究了Zn2+和Ag+两种抗菌金属离子与NH4+型斜发沸石离子交换的热力学特征,绘制了Zn2+和Ag+的离子交换等温线,计算了不同条件下达到离子交换平衡时,NH4+型斜发沸石对Zn2+和Ag+的选择性校正系数Kc和交换平衡常数Ka,...通过液相离子交换试验研究了Zn2+和Ag+两种抗菌金属离子与NH4+型斜发沸石离子交换的热力学特征,绘制了Zn2+和Ag+的离子交换等温线,计算了不同条件下达到离子交换平衡时,NH4+型斜发沸石对Zn2+和Ag+的选择性校正系数Kc和交换平衡常数Ka,得出了ln Ka值与1/T之间的线性关系,导出了反应标准摩尔焓变(ΔrHθm)、反应标准摩尔Gibbs自由能变(ΔrGθm)和反应标准摩尔熵变(ΔrSθm)。结果表明:达到离子交换平衡时,NH4+型斜发沸石对Zn2+和Ag+的最大交换度分别为0.668和0.856,ΔrHθm分别为7.165 k J/mol和5.276 k J/mol,ΔrGθm<0,ΔrSθm>0,即该过程是吸热和熵增加反应,并且该反应在20℃能自动发生,升高温度有利于NH4+型斜发沸石交换Zn2+和Ag+;在相同条件下,NH4+型斜发沸石对Ag+的离子交换能力大于Zn2+。展开更多
Aim To study the exchange reaction characteristics of anion exchange resin for diclofenac sodium. Methods The drug-resin complexes were prepared by a batch method with diclofenac sodium as the model drug and the stron...Aim To study the exchange reaction characteristics of anion exchange resin for diclofenac sodium. Methods The drug-resin complexes were prepared by a batch method with diclofenac sodium as the model drug and the strong anion exchange resin (201 × 7) as the carrier. The effects of different forms (OH~ - and Cl~ - ) of the strong anion exchange resin, the particle size of the resin, and the reaction temperature on the exchange behavior were described. The exchange kinetic profiles were fitted. The related exc...展开更多
Removal of Cr（VI） from aqueous solution by strong alkaline anion exchange fiber （SAAEF） was achieved using batch adsorption experiments. The effect of contact time, initial Cr（VI） concentration and pH was invest...Removal of Cr（VI） from aqueous solution by strong alkaline anion exchange fiber （SAAEF） was achieved using batch adsorption experiments. The effect of contact time, initial Cr（VI） concentration and pH was investigated. The results showed that the maximum adsorption capacity of SAAEF was 187.7 mg/g at pH=1.0. The adsorption capacity increased with Cr（VI） concentration but decreased with pH value when pH〉1.0. Adsorption isotherms at various temperatures were obtained. Langmuir, Freundlich, Dubinin-Radushkevich and Temkin models were adopted and the equilibrium data fitted best with the Langmuir isotherm. The constants of these models indicated that the adsorption process involved both chemisorption and physisorption. The values of thermodynamic parameters, including DH, DG and DS, suggested that the adsorption of Cr（VI） on SAAEF was a spontaneous, entropy-driven and endothermic process. Q（iso） was not a constant value, which indicated an inhomogenous energy distribution on SAAEF.展开更多
The present study dealt with the mechanism of competitive adsorption of Sb(Ⅲ)and Fe(Ⅱ)ions from a copper-containing aqueous solution on Purolite S957,a commercially available cationic ion-exchange adsorbent.Experime...The present study dealt with the mechanism of competitive adsorption of Sb(Ⅲ)and Fe(Ⅱ)ions from a copper-containing aqueous solution on Purolite S957,a commercially available cationic ion-exchange adsorbent.Experiments were conducted using aqueous copper sulfate solutions containing either single or conjoint ions,using both sedentary and batch adsorption techniques to ascertain the sensitivity of the adsorption process to variation in p H,mass of resin,contact time,and temperature as well as establishing the optimal range of variables for maximum ion removal.The data from single ion adsorption tests were fitted by non-linear regression techniques to Henry,Langmuir,Freundlich,Temkin,and Dubinin–Radushkevich isotherm models.Freundlich isotherm for Sb(Ⅲ)and Freundlich and Henry models for Fe(Ⅱ)solutions best express the adsorption equilibrium data;while for binary ion electrolytes,the extended Freundlich model fitted the data satisfactorily.The kinetic model adequately describing adsorption was shown to be the pseudo-first-order,underscoring the dominant role of physical adsorption playing in the process.Thermodynamic parameters for the adsorption process reveal differences in the Sb(Ⅲ)adsorption mechanism from single ion and Sb(Ⅲ)-Fe(Ⅱ)containing electrolytes.The adsorption of Sb(Ⅲ)alone is endothermic,whereas the process becomes exothermic in the Sb(Ⅲ)-Fe(Ⅱ)system.展开更多
文摘通过液相离子交换试验研究了Zn2+和Ag+两种抗菌金属离子与NH4+型斜发沸石离子交换的热力学特征,绘制了Zn2+和Ag+的离子交换等温线,计算了不同条件下达到离子交换平衡时,NH4+型斜发沸石对Zn2+和Ag+的选择性校正系数Kc和交换平衡常数Ka,得出了ln Ka值与1/T之间的线性关系,导出了反应标准摩尔焓变(ΔrHθm)、反应标准摩尔Gibbs自由能变(ΔrGθm)和反应标准摩尔熵变(ΔrSθm)。结果表明:达到离子交换平衡时,NH4+型斜发沸石对Zn2+和Ag+的最大交换度分别为0.668和0.856,ΔrHθm分别为7.165 k J/mol和5.276 k J/mol,ΔrGθm<0,ΔrSθm>0,即该过程是吸热和熵增加反应,并且该反应在20℃能自动发生,升高温度有利于NH4+型斜发沸石交换Zn2+和Ag+;在相同条件下,NH4+型斜发沸石对Ag+的离子交换能力大于Zn2+。
文摘Aim To study the exchange reaction characteristics of anion exchange resin for diclofenac sodium. Methods The drug-resin complexes were prepared by a batch method with diclofenac sodium as the model drug and the strong anion exchange resin (201 × 7) as the carrier. The effects of different forms (OH~ - and Cl~ - ) of the strong anion exchange resin, the particle size of the resin, and the reaction temperature on the exchange behavior were described. The exchange kinetic profiles were fitted. The related exc...
基金Project (20080242009) supported by Basic Research Foundation of Beijing Institute of Technology, China
文摘Removal of Cr（VI） from aqueous solution by strong alkaline anion exchange fiber （SAAEF） was achieved using batch adsorption experiments. The effect of contact time, initial Cr（VI） concentration and pH was investigated. The results showed that the maximum adsorption capacity of SAAEF was 187.7 mg/g at pH=1.0. The adsorption capacity increased with Cr（VI） concentration but decreased with pH value when pH〉1.0. Adsorption isotherms at various temperatures were obtained. Langmuir, Freundlich, Dubinin-Radushkevich and Temkin models were adopted and the equilibrium data fitted best with the Langmuir isotherm. The constants of these models indicated that the adsorption process involved both chemisorption and physisorption. The values of thermodynamic parameters, including DH, DG and DS, suggested that the adsorption of Cr（VI） on SAAEF was a spontaneous, entropy-driven and endothermic process. Q（iso） was not a constant value, which indicated an inhomogenous energy distribution on SAAEF.
文摘The present study dealt with the mechanism of competitive adsorption of Sb(Ⅲ)and Fe(Ⅱ)ions from a copper-containing aqueous solution on Purolite S957,a commercially available cationic ion-exchange adsorbent.Experiments were conducted using aqueous copper sulfate solutions containing either single or conjoint ions,using both sedentary and batch adsorption techniques to ascertain the sensitivity of the adsorption process to variation in p H,mass of resin,contact time,and temperature as well as establishing the optimal range of variables for maximum ion removal.The data from single ion adsorption tests were fitted by non-linear regression techniques to Henry,Langmuir,Freundlich,Temkin,and Dubinin–Radushkevich isotherm models.Freundlich isotherm for Sb(Ⅲ)and Freundlich and Henry models for Fe(Ⅱ)solutions best express the adsorption equilibrium data;while for binary ion electrolytes,the extended Freundlich model fitted the data satisfactorily.The kinetic model adequately describing adsorption was shown to be the pseudo-first-order,underscoring the dominant role of physical adsorption playing in the process.Thermodynamic parameters for the adsorption process reveal differences in the Sb(Ⅲ)adsorption mechanism from single ion and Sb(Ⅲ)-Fe(Ⅱ)containing electrolytes.The adsorption of Sb(Ⅲ)alone is endothermic,whereas the process becomes exothermic in the Sb(Ⅲ)-Fe(Ⅱ)system.
