Gas Capture System with Combined Temperature and Pressure Swings Using Moving Adsorbent

    公开(公告)号:US20230330589A1

    公开(公告)日:2023-10-19

    申请号:US18042838

    申请日:2021-08-10

    申请人: SINTEF TTO AS

    IPC分类号: B01D53/12

    摘要: Disclosed herein is a gas capture system comprising: a first reactor system arranged so that, in the first reactor system, at least some gas in a gas stream that is received by the gas capture system is captured by a sorbent that is arranged to flow through the first reactor system; a second reactor system arranged to regenerate the sorbent so that the sorbent releases at least some of the gas captured in the first reactor system, wherein the sorbent is arranged to flow through the second reactor system and the second reactor system is arranged to output a flow of the released gas; a first sorbent transfer system arranged between a sorbent outlet of the first reactor system and a sorbent inlet of the second reactor system, wherein the first sorbent transfer system comprises a lock hopper; and a second sorbent transfer system arranged between a sorbent outlet of the second reactor system and a sorbent inlet of the first reactor system, wherein the second sorbent transfer system comprises a lock hopper; wherein: the sorbent is a solid; the second reactor system comprises a pump arranged so that the second reactor system may have a lower operational pressure when regenerating sorbent than the operational pressure of the first reactor system during gas capture by the sorbent; and the first reactor system, first sorbent transfer system, second reactor system and second sorbent transfer system are all arranged so that they provide a sorbent flow path that recirculates the sorbent between the first reactor system and the second reactor system.

    Wet desulfurization process using a suspension bed

    公开(公告)号:US10744451B2

    公开(公告)日:2020-08-18

    申请号:US15861126

    申请日:2018-01-03

    摘要: Provided is a wet desulfurization process using a suspension bed. The process comprises mixing desulfurization slurry with a hydrogen sulfide containing gas to obtain a first mixture, and passing the first mixture into a suspension bed reactor from bottom to top, with controlling the first mixture to have a dwell time of 5-60 minutes in the reactor to allow they contact and react sufficiently with each other; and subjecting a second mixture obtained from the reaction to gas liquid separation to produce a purified gas. The process of the present invention may reduce the hydrogen sulfide content in the hydrogen sulfide containing gas from 2.4-140 g/Nm3 to 50 ppm or less, so that the desulfurization efficiency is 98% or more. The process of the present invention is simple and reasonable, with high desulfurization and regeneration efficiency, simple equipment, little occupation of land and low investment, which is very suitable for industrial promotion.