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Method for preparing methanol from natural gas methanol natural gas
Method for preparing methanol from natural gas methanol natural gas
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机译:由天然气制甲醇制甲醇的方法
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摘要
Abstract: the present invention relates to the production process of natural gas methanol methanol natural gas include: (a) natural gas catalytic reaction with water vapor and oxygen oxygen in the reactor operated in Harar Self autothermic reactor J (I) contains a burning stove burner) injected natural gas Waksjyn oxygen, and one granular catalyst (II) positioned beneath the burner (burner) and (b) removing artificial raw gas in the drawer The temperature of 800.M, hundred of the reactor, cooling, condensation of water vapor and usually formed condensate almtktvh and (c) mixing the crude synthetic gas with a hydrogen rich gas rich gas H2 and circulating gas circulating gas, well Artificial gas cap equal computational stoichiometric number ranges of 1.3-1.9 calculated from the molar concentrations of molecular hydrogen H2) hydrogen), carbon monoxide CO) carbon monoxide) and carbon dioxide (CO2) CO2) carbon dioxide), the gas mixture comprising of synthesis of synthesis gas and (d) feeding Methanol (the) containing mixture to the reactor for methanol synthesis catalyst, copper Cu catalyst works when 10-150 Joe when registered - 350 (L) pull the mixture gas containing vapor of methanol methanol cooled down. The thick of methanol metHanol and (f) to withdraw the remaining gas refrigerant from the methanol methanol and distribution within the gas stream and partially recycled recirculating gas Thanyghaz purge discharge gas) contains 30-80 (% by volume) of hydrogen H2) Hydrogen) and CO2 7-35 CO2) carbon dioxide) and 3-25 Co CO) carbon monoxide) and (g) of gas removal hydrogen rich hydrogen gas discharge by separating the separating device (XV) and mixing it with G Is aTo fabricate increasingly rough.
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机译:【摘要】本发明涉及天然气甲醇甲醇天然气的生产工艺,包括:(a)在哈拉尔自热式反应器J中运行的反应器中,天然气与水蒸气和氧气氧气催化反应。 )注入天然气Waksjyn氧气和一种位于燃烧器(燃烧器)下方的颗粒催化剂(II),以及(b)除去抽屉中的人工原料气体温度为800.M,反应器百个,冷却,水蒸气冷凝通常会形成冷凝水,并且(c)将粗合成气与富氢气体H2和循环气体循环气混合,从分子氢H2的摩尔浓度计算得出的人工气顶的化学计量数范围为1.3-1.9 )氢),一氧化碳CO)一氧化碳和二氧化碳(CO2),二氧化碳(CO2),混合气体包括合成气的合成和(d)进料g。将含甲醇的混合物送至反应器中作甲醇合成催化剂,铜铜催化剂在10-150 Joe时工作-350(L)将含甲醇蒸气的混合物气体甲醇冷却下来。浓甲醇甲醇和(f)从甲醇甲醇中抽出剩余的气体制冷剂并分布在气流中和部分再循环的再循环气体Thanyghaz吹扫排气中)含有30-80(体积%)的氢H2)氢)和二氧化碳(7-35 CO2)二氧化碳)和3-25 Co CO)一氧化碳)和(g)气体去除氢气通过分离装置(XV)分离并与G混合将富氢氢气排出。
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