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RECLAIMING DEVICE AND METHOD AND RECOVERY DEVICE FOR CO2, H2S, OR BOTH

机译:CO2,H2S或两者的回收装置和方法以及回收装置

摘要

Provided are a reclaimer 51 that introduces, through a branch line L 11 , and stores a part 17a of an absorbent 17 regenerated in a regenerator of a recovery unit that recovers CO2 or H 2 S in a gas, a first alkaline agent supply section 53A that supplies an alkaline agent 52 to the reclaimer 51, a heating section 54 that heats the absorbent 17 stored in the reclaimer 51 and to which the alkaline agent 52 has been mixed to obtain recovered vapor 61, a first vapor cooler 55A that cools the recovered vapor 61 discharged from the reclaimer 51 through a vapor line L 12 , a first gas-liquid separator 56A that separates a coexisting substance 62 entrained in the cooled recovered vapor 61 into a recovered absorption agent vapor (gas) 17b and the liquid coexisting substance 62 by gas-liquid separation, and an introduction line L 13 that introduces the recovered absorption agent vapor 17b separated in the first gas-liquid separator 56A into a regenerator 20.
机译:提供一种回收器51,其通过分支线L 11引入,并存储在第一单元的碱性试剂供应部53A中回收的吸收剂17的一部分17a,该吸收剂在回收单元的再生器中再生,该回收单元的再生器用于回收气体中的CO 2或H 2S。将碱性试剂52供给至回收器51的加热部54,加热储存在回收器51中的吸收剂17,并混合有碱性试剂52而得到回收蒸气61的加热部54,和冷却回收的蒸气的第一蒸气冷却器55A。从回收器51通过蒸气管线L 12排出的蒸气61,第一气液分离器56A,其将夹带在冷却的回收蒸气61中的共存物质62分离成回收吸收剂蒸气(气体)17b和液体共存物质62通过气液分离和引入管线L 13将在第一气液分离器56A中分离的回收的吸收剂蒸气17b引入到再生器20中。

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