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Determination of an engineering model for exchange kinetics of strong acid cation resin for the ion exchange of sodium chloride sodium bicarbonate solutions

机译:用于离子交换氯化钠和碳酸氢钠溶液的强酸阳离子树脂交换动力学工程模型

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摘要

udud - The BWS kinetic expression was found to be an optimal engineering model for sodium exchange with SAC resin.udud - Anion identity influenced cation exchange kinetics with SAC resins.udud - Sodium ion exchange rates depended upon resin/liquid ratio.udud - Rate limiting step in exchange kinetics changed with time and resin/liquid ratio.ududududThis study identified an appropriate engineering model which described the exchange kinetics of sodium ionsudwith a strong acid cation resin. Synthetic resins have potential application for the demineralization of coal seam (CS) water prior to beneficial reuse. However, there is limited data regarding the kinetic behaviour of strong acid cation (SAC) resin for the removal of sodium ions, the most prevalent ions in the water collected from coal seams (produced water) during natural gas extraction. In particular, exchange kinetics need to be understood inudrelation to estimating how full scale columns of resin may perform. Kinetic analysis revealed that the exchangeudof sodium ions from both sodium chloride and sodium bicarbonate solutions with SAC resin reached equilibriumudwithin minutes at ambient temperature. Optimal simulation of the kinetic data for both chloride and bicarbonateudcontaining solutions was achieved by application of the Brouers, Weron and Sotolongo (BWS) fractal equation;udand this should be used as the basis for development of an engineering model. The model parameters varieduddepending upon the ratio of resin to liquid employed in the tests, with rates showing substantial enhancementudonce an excess of resin exchange sites were present. The exchange process was apparently controlled in part byudintraparticle diffusion, with three phases inferred for sodium chloride solutions and two for sodium bicarbonateudsolutions. Other rate limiting phenomena such as film diffusion appeared to play a role under certain conditions.
机译:UD UD - 发现BWS动力学表达是囊树脂的钠交换的最佳工程模型。 UD UD - 阴离子身份受囊状树脂的阳离子交换动力学。 ud ud - 钠离子交换率取决于树脂/液体比。 ud ud速率限制步骤在交换动力学随时间和树脂/液体比变化。 ud ud ud udthis研究确定了一个适当的工程模型,描述了钠离子的交换动力学 udwith a强酸阳离子树脂。合成树脂在有益再利用之前具有煤层(CS)水的脱矿质的潜在应用。然而,关于用于除去钠离子的强酸阳离子(SAC)树脂的动力学行为的数据有限,在天然气萃取过程中从煤层(产生的水)中的水中最普遍的离子。特别地,需要在 Udrelation中理解交换动力学,以估计树脂的全尺度柱可以执行。动力学分析表明,在环境温度下,氯化钠和碳酸氢钠溶液的交换 Udof钠离子与囊树脂的平衡率达到平衡 udWithin分钟。通过应用令人讨厌,Weron和Sotolongo(BWS)分形方程,实现了对氯化物和碳酸氢盐的动力学数据的最佳模拟; Udand应该用作工程模型的发展的基础。模型参数随着树脂与试验中使用的液体的比例而变化,具有显示出实质性增强的速率。存在过量的树脂交换位点。通过 udintraparticle扩散显然是控制的交换过程,其中氯化钠溶液和两个用于碳酸氢钠 udsolutions的三个阶段。其他速率限制现象,如胶片扩散似乎在某些条件下发挥作用。

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