Abstract

In the arid west, the freshwater supply of many communities is limited, leading to increased interest in tapping brackish water resources. Although reverse osmosis is the most common technology to upgrade saline waters, there is also interest in developing and improving alternative technologies. Here we focus on membrane capacitive deionization (MCDI), which has attracted broad attention as a portable and energy-efficient desalination technology. In this study, a fully coupled two-dimensional MCDI process model capable of capturing transient ion transport and adsorption behaviors was developed to explore the function of the ion-exchange membrane (IEM) and detect MCDI influencing factors via sensitivity analysis. The IEM enhanced desalination by improving the counter-ions’ flux and increased adsorption in electrodes by encouraging retention of ions in electrode macropores. An optimized cycle time was proposed with maximal salt removal efficiency. The usage of the IEM, high applied voltage, and low flow rate were discovered to enhance this maximal salt removal efficiency. IEM properties including water uptake volume fraction, membrane thickness, and fixed charge density had a marginal impact on cycle time and salt removal efficiency within certain limits, while increasing cell length and electrode thickness and decreasing channel thickness and dispersivity significantly improved overall performance.

Highlights

  • Freshwater is essential in our daily life with diverse demands for drinking water, agricultural irrigation, and industrial water

  • The novelties of this model lie in that: (1) this model is the first fully coupled two-dimensional process model for membrane capacitive deionization (MCDI) considering non-ideal ion-exchange membrane (IEM); (2) hydraulic dispersion effects caused by fluid flowing through the porous spacer are included; (3) cycle time with maximal salt removal efficiency is proposed as an optimized operating mode

  • The main results are as follows: (1) A near doubling in desalination rate in MCDI compared to capacitive deionization (CDI) was achieved due to the enhanced counter-ions’ flux in the vicinity of the IEM; (2) Electrode macropores exhibited

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Summary

Introduction

Freshwater is essential in our daily life with diverse demands for drinking water, agricultural irrigation, and industrial water. The goals of this study include exploring the function of the IEM on desalination rate and adsorption capability and evaluating the impacts of hydraulic dispersion, IEM properties, and cell configuration on cell performance via a series of sensitivity analyses The novelties of this model lie in that: (1) this model is the first fully coupled two-dimensional process model for MCDI considering non-ideal IEM; (2) hydraulic dispersion effects caused by fluid flowing through the porous spacer are included; (3) cycle time with maximal salt removal efficiency is proposed as an optimized operating mode.

MCDI Parameters and Operating Conditions
Assumptions
Ion Transport in the Spacer-Filled Channel
Ion Transport in the IEM
Ion Transport and Adsorption in the Electrode
Boundary Conditions
Results
Model Validation
Desalination Rate
Adsorption Capacity
Sensitivity Analysis
Discussion
Full Text
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