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Characterization of a Membrane-Based, Electrochemically Driven Pumping System Using Aqueous Electrolyte Solutions

机译:使用电解质水溶液的基于膜的电化学驱动泵系统的表征

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Electrokinetic flow provides a mechanism for a variety of fluid pumping schemes. The design and characterization of an electrochemically driven pump that utilizes porous carbon electrodes, iodide/triiodide redox electrolytes, and Nafion membranes is described. Fluid pumping by the cell is reversible and controlled by the cell current. Chronopotentiometry experiments indicate that the total available fluid that can be pumped in a single electrolysis without gas evolution is determined solely by the initial concentration of electrolyte and the applied current. The magnitude of the fluid flow at a given current is determined by the nature of the cation in the electrolyte and by the water absorption properties of the Nafion membrane. For 1 M aqueous electrolytes, pumping rates ranging from 1 to 14 (mu)L/min were obtained for current densities of 10-30 mA/cm~(2) of membrane area. Molar volume changes for the I_(3~(-))/I~(-) redox couple and for the alkali cation migration contribute little to the observed volumetric flow rates; the magnitude of the flow is dominated by the migration-induced flow of water.
机译:电动流动为各种流体泵送方案提供了一种机制。描述了使用多孔碳电极,碘化物/三碘化物氧化还原电解质和Nafion膜的电化学驱动泵的设计和特性。单元的流体泵送是可逆的,并由单元电流控制。计时电位法实验表明,可以在单次电解中泵入而不会产生气体的总可用流体仅由电解质的初始浓度和施加的电流确定。在给定电流下的流体流量大小取决于电解质中阳离子的性质以及Nafion膜的吸水特性。对于1M的水性电解质,对于膜面积为10-30mA / cm 2的电流密度,获得的抽气速率为1-14μL/ min。 I_(3〜(-))/ I〜(-)氧化还原对的摩尔体积变化以及碱金属离子迁移的摩尔变化对观察到的体积流量的贡献很小;流量的大小主要由迁移引起的水流控制。

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