首页> 外国专利> Treatment of purge gas from ammonia synthesis - to recover and recycle hydrogen

Treatment of purge gas from ammonia synthesis - to recover and recycle hydrogen

机译:处理氨合成中的吹扫气-回收和再循环氢气

摘要

The treatment of a purge gas from an ammonia synthesis plant, contg. a large proportion of hydrogen and nitrogen and non-negligible amts. of argon, methane, ammonia and helium, involves a preliminary extn. of ammonia. The gas is then fractionated by partial condensn. in an exchanger, with formation at the cold end of a H2-enriched vapour fraction and a liq. fraction enriched in argon and methane. At least a large part of the H2-enriched gaseous fraction is recycled into the synthesis cycle. The liq. fraction is expanded to a vaporisation pressure by heat exchange at counter-current with the purge gas during cooling. The vaporised liq. fraction is, during the heat exchange, expanded to a second low pressure in an expansion turbine with external work, before being reheated by thermal exchange at counter-current with the purge gas.
机译:来自氨合成厂的吹扫气的处理,续氢和氮以及不可忽略的环的比例很大。氩气,甲烷,氨气和氦气涉及到初步的引爆。氨然后通过部分冷凝将气体分馏。在交换器中,在冷端形成富H2的蒸气馏分和液体。馏分富含氩气和甲烷。至少大部分富H 2的气态部分再循环到合成循环中。液体。在冷却期间,通过与吹扫气体逆流进行热交换,使馏分膨胀至汽化压力。蒸发的液体在热交换期间,该馏分在具有外部功的膨胀涡轮机中膨胀至第二低压,然后与吹扫气体逆流通过热交换进行再加热。

著录项

相似文献

  • 专利
  • 外文文献
  • 中文文献
获取专利

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号