发明名称 AMMONIA SYNTHESIS AND A PLANT FOR CARRYING OUT THIS SYNTHESIS
摘要 In an ammonia synthesis process at a pressure under 120 bar bas. ammonia is recovered from incompletely reacted synthesis gas by absorption in water. Unreacted synthesis gas is dried preparatory to further reaction by passing it through a charge of regenerable solid absorbent until that charge is loaded with water and switching its flow to a fresh or regenerated charge. The loaded charge is regenerated by passing ammonia-containing reacted synthesis gas through it, the displaced water being separated in the ammonia absorption step. Alternatively or additionally the water content of the unreacted synthesis gas is decreased by contacting it with liquid aqueous ammonia at below 0 DEG C.
申请公布号 DE2860300(D1) 申请公布日期 1981.02.19
申请号 DE19782860300 申请日期 1978.08.16
申请人 IMPERIAL CHEMICAL INDUSTRIES PLC 发明人 PINTO, ALWYN
分类号 C01C1/04 主分类号 C01C1/04
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