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Method and system for recovering high-purity CO2 from gasification gas

机译:从气化气中回收高纯二氧化碳的方法和系统

摘要

To provide a method and a system for recovering CO 2 from gasification gas, the method and the system being capable of preventing the recovered CO 2 from being contaminated with COS, without repeating cooling and heating operations and without increasing the steam consumption, even when the CO 2 recovery ratio is changed in recovering CO 2 from gasification gas. Gasification gas being produced in a gasifier (10) and containing CO, CO 2 , COS and H 2 S is subjected to dust removal in a scrubber (20). Then, a part of the gas is subjected to a CO shift reaction, in which CO is converted into CO 2 , in a CO shift reactor (30). Another part of the gasification gas is not subjected to the CO shift reaction by means of a bypass (34), and is mixed with the gas after the CO shift reaction. Thereby, the temperature of the mixture gas is set at 180°C to 300°C, and COS in the mixture gas is converted into H 2 S in a COS converter (40). The H 2 S is absorbed and removed by a H 2 S absorption apparatus (50). Then, CO 2 is absorbed and removed by a CO 2 absorb apparatus.
机译:为了提供一种用于从气化气体中回收CO 2的方法和系统,该方法和系统能够防止回收的CO 2被COS污染,而无需重复进行冷却和加热操作并且不会增加蒸汽消耗,即使当在从气化气中回收CO 2时改变了CO 2回收率。在气化器(10)中产生并包含CO,CO 2,COS和H 2 S的气化气体在洗涤器(20)中进行除尘。然后,将一部分气体在CO变换反应器(30)中进行CO变换反应,将CO转化为CO 2。气化气体的另一部分不通过旁路(34)进行CO变换反应,而是与CO变换反应后的气体混合。由此,将混合气体的温度设定为180℃〜300℃,并且在COS转化器(40)中将混合气体中的COS转化为H 2S。通过H 2 S吸收装置(50)吸收和除去H 2S。然后,CO 2被CO 2吸收装置吸收并除去。

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