Electrodialysis and Electrodeionization Desalination System
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Solution Overview
Problem
Conventional seawater desalination methods, such as reverse osmosis and thermal processes, face high energy consumption and capital costs, with existing electrodialysis and electrodeionization systems experiencing efficiency declines at lower total dissolved solids (TDS) levels due to concentration polarization and water splitting phenomena.
Innovation Solution
A combined electrodialysis and continuous electrodeionization system utilizing concentration differences to facilitate ion separation, with multiple stages of electrodialysis reducing TDS to 3,500-5,500 ppm followed by ion exchange softening and final desalination to less than 1,000 ppm using continuous electrodeionization, minimizing energy consumption by synergizing existing and novel technologies.
Engineering Contradictions & Design Principles
Engineering Contradiction Analysis
1Use of energy by moving object
If conventional reverse osmosis systems are used for seawater desalination, then desalination can be achieved, but energy consumption is high (at least 2.5 kWh/m3)
Solution Approach 1:
The desalination process is divided into multiple stages: first electrodialysis stage, second electrodialysis stage, and final reverse osmosis stage. Each stage operates at optimized conditions for its specific TDS range, preventing energy waste from attempting single-stage desalination of high-salinity seawater
Solution Approach 2:
The system changes operating parameters (electrical potential, flow rates) based on TDS concentration at each stage. Electrodialysis operates at low electrical potentials when TDS is high, then transitions to reverse osmosis at lower TDS where pressure-driven separation is more efficient
2Use of energy by moving object
If electrodialysis systems are used for desalination, then lower energy consumption can be achieved, but efficiency declines at lower TDS levels due to concentration polarization and water splitting
Solution Approach 1:
The system dynamically transitions between different desalination technologies based on TDS concentration. Electrodialysis is used dynamically at high TDS levels where it is most efficient, then the system switches to reverse osmosis at lower TDS levels to avoid efficiency decline from concentration polarization
Solution Approach 2:
The multi-stage system maintains continuous useful action by ensuring each stage operates within its optimal efficiency range. The transition from electrodialysis to reverse osmosis ensures uninterrupted desalination while maintaining high efficiency throughout the entire process
3Productivity
If thermal processes are used for desalination, then desalination can be achieved, but power consumption is high due to phase change requirements
Solution Approach 1:
The system replaces thermal phase-change processes with electrochemical and pressure-driven separation processes. Electrodialysis uses electrical fields to drive ion migration, and reverse osmosis uses pressure to drive water through membranes, eliminating the need for vaporization and condensation cycles
4Ease of manufacture
If reverse osmosis systems are used, then lower capital and operating costs can be achieved, but energy recovery devices are still required to meet energy targets
Solution Approach 1:
The system performs preliminary desalination through two electrodialysis stages that remove a significant portion of salts before reverse osmosis. This preliminary action reduces the energy burden on the reverse osmosis stage, eliminating or reducing the need for energy recovery devices while maintaining cost-effectiveness
Data Source
AI summary
A low energy water treatment system and method is provided. The system has at least one electrodialysis device that produces partially treated water and a brine byproduct, a softener, and at least one electrodeionization device. The partially treated water stream can be softened by the softener to reduce the likelihood of scale formation and to reduce energy consumption in the electrodeionization device, which produces water having target properties. At least a portion of the energy used by the electrodeionization device can be generated by concentration differences between the brine and seawater streams introduced into compartments thereof. The brine stream can also be used to regenerate the softener.


