首页> 外国专利> Process for catalytically NH3 Drive natural gas comprising O2 Rich gas auto Thermal Reformer, cool,Lead to a catalytic conversion of synthesis gas to be converted to separate washing gaseous CO2, co and CH4, contacting the synthesis gas with liquid N2 in a stage of washing gas.

Process for catalytically NH3 Drive natural gas comprising O2 Rich gas auto Thermal Reformer, cool,Lead to a catalytic conversion of synthesis gas to be converted to separate washing gaseous CO2, co and CH4, contacting the synthesis gas with liquid N2 in a stage of washing gas.

机译:催化的NH3驱动天然气的方法,包括富氧气体自动热重整器,冷却,使合成气催化转化为单独的洗涤气态CO2,co和CH4,在洗涤阶段使合成气与液态N2接触加油站。

摘要

The Home is rich in Natural Gas with gas in O2, an autothermal Reformer, which produces a sitesis Gross gas temperatures in the range of 900 to 1200 degrees C.To provide 40 to 100 bar and in the presence of Catalysts of Fission, calculated on dry, present a hydrogen content of 55 to 75% by volume, a co content of 15 to 30% in volume,A CO2 content from 5 to 30% in volume and Volume H2: co ratio of 1.6 to 4.The crude synthesis gas autothermal Reformer Cools,Driving through a catalytic converter for the conversion of co and H2 is a converted synthesis gas containing H2, calculated on DryAt least 55% in volume and a co content of up to 8% by volume.The synthesis gas is subjected to a gas purification of several Stages for the separation of CO2, co and CH4,We obtain a mixture of n2 and H2 which leads a ammonia synthesis Catalyst for production of Ammonia.Ammonia can be obtained in the synthesis of ammonia from urea, at least partially, by reaction with CO2.
机译:该房屋富含天然气和O2中的气体,这是一种自热重整器,可产生定点的总气体温度,范围为900至1200摄氏度。要提供40至100巴并在裂变催化剂存在下,按干燥,氢气含量为55-75%(体积),co含量为15-30%(体积),CO2含量为5-30%(体积),H2:co的体积比为1.6-4。自动热重整器冷却器,经催化转化器转化为Co和H2的是一种经转化的含H2的合成气,按干燥量计算至少为55%的体积,钴含量最高为8%的体积。分离CO2,co和CH4的几个阶段的气体净化,我们获得了n2和H2的混合物,这导致了氨合成催化剂的生产氨。氨可以从尿素合成氨中获得,至少部分是氨与二氧化碳反应。

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