探讨了氧化铝对水体中硅酸的吸附去除潜力、影响因素及机理。结果表明,pH 4~8时吸附量随pH、吸附剂投加量的增大而增加,说明氧化铝具有吸附去除硅酸的能力。吸附过程符合Langmuir吸附等温模式,最大吸附量达39.82 mg/g。结合27Al MAS NMR...探讨了氧化铝对水体中硅酸的吸附去除潜力、影响因素及机理。结果表明,pH 4~8时吸附量随pH、吸附剂投加量的增大而增加,说明氧化铝具有吸附去除硅酸的能力。吸附过程符合Langmuir吸附等温模式,最大吸附量达39.82 mg/g。结合27Al MAS NMR与SEM-EDX分析,氧化铝吸附硅酸的机理是通过硅酸分子与氧化铝中4配位的铝发生化学反应,硅原子取代原来Al—O—Al键上的铝原子形成Al—O—Si键而被固定在氧化铝表面。展开更多
The adsorption of methyl orange onto ultrafine coal powder （UCP） and modified ultrafine coal powder （MUCP） from aqueous solutions were studied, in which the influence of contact time, dosage, temperature, pH, and ...The adsorption of methyl orange onto ultrafine coal powder （UCP） and modified ultrafine coal powder （MUCP） from aqueous solutions were studied, in which the influence of contact time, dosage, temperature, pH, and methyl orange concentration in the solution were investigated. The adsorption kinetics of methyl orange by UCP and MUCP can be described by the Lagergren first-order and pseudo second-order kinetic models, respectively. The adsorption isotherms of methyl orange onto MUCP at 303, 313 and 323 K follow the Freundlich and Langmuir isotherm equation. Values of △G^0 for methyl orange adsorption onto MUCP are -22.55, -23.10 and -23.79 kJ·mol^-1 at 303, 313, and 323 K, respectively. The values of △H^0 and △S^0 are -3.74 kJ· mol^-1 and 61.99 J·mol^-1, respectively. The adsorption process is spontaneous and exothermic.展开更多
Understanding the interaction between a fluid and a solid phase is of fundamental importance to the design of an adsorption process.Because the heat effects associated with adsorption are comparatively large,the as-su...Understanding the interaction between a fluid and a solid phase is of fundamental importance to the design of an adsorption process.Because the heat effects associated with adsorption are comparatively large,the as-sumption of isothermal behavior is a valid approximation only when uptake rates are relatively slow.In this article,we propose to determine when it is needed to choose the isothermal or non-isothermal assumption according to two physical parametersα（ratio convection/capacity） andβ（quantity of energy/capacity） .The proposed problem is solved by a mathematical method in the Laplace domain.Whenα→∞（infinitely high heat transfer coefficient） or β→0（infinitely large heat capacity） ,the limiting case is isothermal.When the diffusion is rapid（α10） the kinetics of sorption is controlled entirely by heat transfer.If the adsorption process is to be used as a heat pump,it shall be represented by an isotherm model withαandβas high as possible.展开更多
文摘探讨了氧化铝对水体中硅酸的吸附去除潜力、影响因素及机理。结果表明,pH 4~8时吸附量随pH、吸附剂投加量的增大而增加,说明氧化铝具有吸附去除硅酸的能力。吸附过程符合Langmuir吸附等温模式,最大吸附量达39.82 mg/g。结合27Al MAS NMR与SEM-EDX分析,氧化铝吸附硅酸的机理是通过硅酸分子与氧化铝中4配位的铝发生化学反应,硅原子取代原来Al—O—Al键上的铝原子形成Al—O—Si键而被固定在氧化铝表面。
基金Supported by the National Science Foundation for Post Doctoral Scientists of China （20070411124）, Scientific and Technological Key Project of Shaanxi Province （2006k07-G19）, and Industrialization Project of Shaanxi Provincial Department of Education （06JC 11）.
文摘The adsorption of methyl orange onto ultrafine coal powder （UCP） and modified ultrafine coal powder （MUCP） from aqueous solutions were studied, in which the influence of contact time, dosage, temperature, pH, and methyl orange concentration in the solution were investigated. The adsorption kinetics of methyl orange by UCP and MUCP can be described by the Lagergren first-order and pseudo second-order kinetic models, respectively. The adsorption isotherms of methyl orange onto MUCP at 303, 313 and 323 K follow the Freundlich and Langmuir isotherm equation. Values of △G^0 for methyl orange adsorption onto MUCP are -22.55, -23.10 and -23.79 kJ·mol^-1 at 303, 313, and 323 K, respectively. The values of △H^0 and △S^0 are -3.74 kJ· mol^-1 and 61.99 J·mol^-1, respectively. The adsorption process is spontaneous and exothermic.
文摘Understanding the interaction between a fluid and a solid phase is of fundamental importance to the design of an adsorption process.Because the heat effects associated with adsorption are comparatively large,the as-sumption of isothermal behavior is a valid approximation only when uptake rates are relatively slow.In this article,we propose to determine when it is needed to choose the isothermal or non-isothermal assumption according to two physical parametersα（ratio convection/capacity） andβ（quantity of energy/capacity） .The proposed problem is solved by a mathematical method in the Laplace domain.Whenα→∞（infinitely high heat transfer coefficient） or β→0（infinitely large heat capacity） ,the limiting case is isothermal.When the diffusion is rapid（α10） the kinetics of sorption is controlled entirely by heat transfer.If the adsorption process is to be used as a heat pump,it shall be represented by an isotherm model withαandβas high as possible.
