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Assessment of the main engineering parameters controlling the electrodialytic recovery of sodium propionate from aqueous solutions

机译:评估控制从水溶液中电渗析回收丙酸钠的主要工程参数

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摘要

The main engineering parameters (i.e. ion transport numbers in solution and electro-membranes; effective solute and water transport numbers; effective membrane surface area, membrane surface resistances, limiting current intensity and mass transfer coefficient) controlling the recovery of sodium propionate from model solutions by electrodialysis were determined in accordance with a sequential experimental procedure. Such parameters allowed a satisfactorily simulation of training and validation tests carried out under constant- or variable-current intensity. The performance of this ED process was characterised in terms of a current efficiency (Ω) of about 98% in constant- and variable-current regions, a water transport number (t_w) of about 15, and a specific energy consumption (ε) increasing from 0.22 to 0.35 kW h kg~(-1) for a solute recovery yield of 95% as the current density (j) was increased from 200 to 400 A m~(-2). The specific resistance of the cationic or anionic membranes were found to be practically coincident or at least four times greater than that provided by the manufacturer in aqueous solutions of sodium chloride, respectively. These parameters are to be used to design and/or optimise ED stacks involved in the downstream processing of propionic acid fermentation broths.
机译:主要工程参数(即溶液和电子膜中的离子迁移数;有效的溶质和水迁移数;有效的膜表面积,膜表面电阻,极限电流强度和传质系数)控制通过以下方式从模型溶液中回收丙酸钠根据顺序实验程序确定电渗析。这样的参数可以令人满意地模拟在恒定或可变电流强度下进行的训练和验证测试。这种ED工艺的性能通过恒流和变流区域的电流效率(Ω)约为98%,水输送数(t_w)约为15以及比能耗(ε)不断增加来表征当电流密度(j)从200 A m〜(-2)增加到0.22到0.35 kW h kg·(-1)时,溶质回收率达到95%。发现阳离子或阴离子膜的比电阻实际上是重合的,或者比制造商在氯化钠水溶液中所提供的比电阻大至少四倍。这些参数将用于设计和/或优化参与丙酸发酵液下游加工的ED烟囱。

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