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process for the removal of carbon dioxide damiscele and particularly for conversion into fuel cells h2.c2 alkaline
process for the removal of carbon dioxide damiscele and particularly for conversion into fuel cells h2.c2 alkaline
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机译:脱除达姆塞地尔二氧化碳的方法,尤其是转化为h2.c2碱性燃料电池的方法
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摘要
1392082 Fuel cells VARTA AG 20 March 1972 [27 March 1971] 12838/72 Heading H1B A fuel cell 16 is supplied at 3 with hydrogen derived from a hydrogen reformer 14, CO 2 being removed from the gas mixture by an absorber 9. The gas absorber 9 is of the kind having interconnected coarse and fine pores, the gas mixture flowing through the coarse pores and washing liquid flowing through the fine pores. The washing liquid flows through a recirculating path including a desorber 10 and pump 11 and returns to the absorber 9, the CO 2 being discharged to the atmosphere at 8. Air enters the fuel cell through a pump 21, and may leave at 6 and be supplied at 7 to the desorber whereby the nitrogen in the air may serve to remove the CO 2 . The pump 11 may be controlled by a CO 2 concentration detector 20 so that the rate of washing liquid circulated is related to the fuel cell output. To ensure that the gas pores of the hydrogen electrodes in the fuel cell are not flooded by electrolyte and that the coarse gas pores of the absorber 9 are not flooded by the washing liquid, it is necessary to control both the pressure of the washing liquid and the pressure of the hydrogen gas in relation to the pressure of the electrolyte in the fuel cell. This is done by valves 13, 15 controlled, respectively, by pressure comparators 19, 18.
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机译:1392082燃料电池VARTA AG 1972年3月20日[1971年3月27日] 12838/72标题H1B向燃料电池16提供3源自氢重整器14的氢,并通过吸收器9从混合气体中除去CO 2。吸收器9是具有相互连接的粗孔和细孔的类型,气体混合物流过粗孔,洗涤液流过细孔。洗涤液流过包括解吸器10和泵11的循环路径,并返回到吸收器9,CO 2在8处排放到大气中。空气通过泵21进入燃料电池,并在6处离开并进入在7处将其供应至解吸器,由此空气中的氮气可用于去除CO 2。泵11可以由CO 2浓度检测器20控制,使得循环的洗涤液的速率与燃料电池的输出有关。为了确保燃料电池中的氢电极的气孔不被电解质充满,并且吸收器9的粗气孔不被洗涤液充满,需要控制洗涤液的压力和洗涤液的压力。氢气压力与燃料电池中电解质压力的关系。这由分别由压力比较器19、18控制的阀13、15完成。
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