A fuel cell anode drainage device and drainage system
A fuel cell and drainage device technology, which is applied to fuel cell additives, battery electrodes, electrolyte treatment of solid electrolyte batteries, etc., can solve the problems of no condensation effect, insufficient water separation effect, insufficient hydrogen transfer, etc., and achieve drainage effect. Good, compact structure, timely drainage effect
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Embodiment 1
[0025] like figure 1 As shown, the present invention provides a fuel cell anode drainage device. The drainage device includes a drainer and a return pump sequentially arranged between the hydrogen outlet 2 and the hydrogen inlet 13 of the fuel cell; the drainer is sequentially provided with a hydrogen chamber I3, a sealant I, a water chamber 5, a sealant II, and a hydrogen chamber along the hydrogen flow direction. II6, the hydrogen chamber I3 and the hydrogen chamber II6 are connected by the hollow fiber bundle 7, the hollow fiber bundle 7 has the function of water permeability and gas resistance when there is a pressure difference in the wet state, and the two ends of the hollow fiber bundle 7 pass through the sealant and are open The sealant I isolates the hydrogen chamber I3 and the water chamber 5; the sealant II isolates the hydrogen chamber II6 and the water chamber 5; the hydrogen chamber I3 is provided with a hydrogen inlet 3, which is connected with the hydrogen outl...
Embodiment 2
[0028] The same drainage device as in Example 1 was used. When the system is working, the operating temperature of the alkaline anion exchange membrane fuel cell is 90 °C, the anode hydrogen pressure is 0.2 MPa gauge pressure, and the operating current density is 400 mA / cm 2 , the return pump is a hydrogen circulation pump, and the rotation speed of the circulation pump is 3500 rpm. The outlet of the stack is hydrogen with saturated steam and liquid product water at a temperature of 70°C. After passing through the drain, the hydrogen is pressurized by the return pump, and enters the fuel cell stack together with the hydrogen from the hydrogen source. The cooling water temperature is 40°C and the pressure is normal pressure. The condensed water in the circulating hydrogen of the stack anode and the liquid water together penetrate the wall of the hollow fiber tube and enter the circulating water under the pressure difference of 0.2 MPa to realize the anode drainage. Before dra...
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Abstract
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