A continuous salt difference power generation device and method
A power generation device and salt difference technology, which is applied in the field of continuous salt difference power generation devices, can solve the problems of device operation stability, adverse effects of input costs, increased process complexity and power generation costs, and large amount of salt and fresh water supply, etc., to achieve Eliminate concentration polarization phenomenon, high-efficiency continuous power generation, and high power generation efficiency
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Embodiment 1
[0050] combine figure 1 and figure 2 As shown, the ion exchange membrane resistance of the reverse electrodialyzer 12 is 2 Ω·cm 2 , the membrane surface flow rate is 4.5 cm / s; the forward osmosis membrane of the forward osmosis device 13 is a hollow fiber membrane with a composite functional layer of silicon oxide nanoparticles, and the flow rate of the feed liquid is twice the flow rate of the draw liquid; the salt in the concentrated salt solution tank 14 Liquid is 10% sodium chloride solution, and the salt solution of light salt solution tank 15 is 0.5% sodium chloride solution. The forward osmosis draw solution of the forward osmosis device 13 is 23% ammonium chloride solution. The anode 122 and cathode 121 were tested with a wire connected load with a power density of 7.2 W / m 2 .
Embodiment 2
[0052] combine figure 1 and figure 2 As shown, the ion exchange membrane resistance of the reverse electrodialyzer 12 is 2 Ω·cm 2 , the membrane surface flow rate is 4.5 cm / s; the forward osmosis membrane of the forward osmosis device 13 is a hollow fiber membrane with a composite functional layer of silicon oxide nanoparticles, and the flow rate of the feed liquid is 1.5 times of the flow rate of the draw liquid; the salt of the concentrated salt solution tank 14 Liquid is 5% sodium chloride solution, and the salt solution of light salt solution tank 15 is 0.3% sodium chloride solution. The forward osmosis draw solution of the forward osmosis device 13 is 20% ammonium bicarbonate solution. The anode 122 and cathode 121 were tested with a wire connected load with a power density of 5.6 W / m 2 .
Embodiment 3
[0054] combine figure 1 and figure 2 As shown, the ion exchange membrane resistance of the reverse electrodialyzer 12 is 2 Ω·cm 2 , the membrane surface flow rate is 5 cm / s; the forward osmosis membrane of the forward osmosis device 13 is a hollow fiber membrane with a composite functional layer of titanium oxide nanoparticles, and the flow rate of the feed liquid is twice the flow rate of the draw liquid; the salt of the concentrated salt solution tank 14 Liquid is 12% sodium chloride and sodium sulfate mixed solution, and the salt solution of light salt solution tank 15 is 0.3% sodium chloride and sodium sulfate mixed solution. The forward osmosis draw solution of the forward osmosis device 13 is 23% ammonium chloride solution. The anode 122 and the cathode 121 are tested by connecting the load with a wire, and the power density is 8.7W / m 2 .
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