ION EXCHANGE ON A FIBROUS ION EXCHANGER IN A FLO-TYPE CAPACITIVE APPARATUS

S. Natareev, D. Zakharov, A. A. Sirotkin, S. Belyaev
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Abstract

The objective of this study is to elaborate the analytical theory of ion exchange in the field of solving the boundary value problems of non steady state mass transfer in solids with a canonical form taking into account a change in the concentration of the solution and the character of movement of the phases in a flow apparatus. The mathematical description of the process of ion-exchange solution purification on ionite particles of cylindrical shape in a batch flow apparatus was developed. At the developing mathematical description the following assumptions were used: the ionite is monodisperse, uniform initial distribution of substances in the ionite, the ion exchange equilibrium is described by Henry equation, the rate of the process is limited by both internal and external diffusion, the flow pattern of the liquid phase in the apparatus is described by the perfect mixing model, the solution with the constant volumetric flow rate and the constant concentration of the substance  is supplied to the apparatus, kinetic and hydrodynamic process parameters are constants. Mathematical description includes the following equations: the diffusion equation of ionite, isotherm equation ion exchange, the equation for average concentration of the substance in the ionite, the material balance equation for a perfect mixing flow apparatus, initial and boundary conditions. To solve boundary value problem, we use the integral Laplace transformations. The obtained equation allows to analyze the effect of the volumetric flow rate of the solution supplied to a flow apparatus, the ratio of the volumes of solid and liquid phases in the apparatus, the diameter of the particle, and other parameters of the process on the concentration distribution of a substance along the internal coordinate of the solid. The developed mathematical model is used to study the desorption of copper ions from the modified polycaproamide fiber with sulfuric acid solution.
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流型电容装置中纤维离子交换器上的离子交换
本研究的目的是在考虑溶液浓度变化和流动装置中相的运动特征的情况下,阐述离子交换的解析理论在解决固体非稳态传质问题方面的典型形式。建立了在间歇流装置中离子交换溶液净化圆柱形离子离子颗粒过程的数学描述。在进行数学描述时,使用了以下假设:离子酸盐是单分散的,离子酸盐中物质的初始分布均匀,离子交换平衡用Henry方程描述,过程的速率受内外扩散的限制,仪器中液相的流动模式用完美混合模型描述,向仪器提供恒定体积流量和恒定物质浓度的溶液。动力学和流体动力学过程参数是常数。数学描述包括:离子离子的扩散方程、离子交换等温线方程、离子离子中物质的平均浓度方程、完美混合流装置的物质平衡方程、初始条件和边界条件。为了解决边值问题,我们使用了积分拉普拉斯变换。所得到的方程允许分析提供给流动装置的溶液的体积流速、装置中固相和液相的体积比、颗粒直径以及该过程的其他参数对物质沿固体内坐标的浓度分布的影响。利用所建立的数学模型,研究了改性聚酰胺纤维在硫酸溶液中对铜离子的解吸。
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来源期刊
CiteScore
1.40
自引率
44.40%
发文量
83
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