Removal of aromatic hydrocarbons from lean acid gas feed for sulfur recovery

    公开(公告)号:US10543452B2

    公开(公告)日:2020-01-28

    申请号:US15570645

    申请日:2016-04-28

    Applicant: PROSERNAT

    Abstract: The present invention is directed to a process for the removal of aromatic hydrocarbons from a lean acid gas containing less than 20 mol. % of H2S, comprising: a) contacting the lean acid gas stream (1) with a H2S-selective liquid absorbent solution (29) in a first absorption zone (2) to produce a gas stream depleted in H2S (3) and an absorbent solution enriched in H2S (4), b) introducing the absorbent solution (4) into a non-thermic stripping zone (8) where it is contacted with a stripping gas stream (7) to obtain an absorbent solution depleted in C4+ aliphatic and aromatic hydrocarbons (9) and a stripping gas stream enriched in aromatic and C4+ aliphatic hydrocarbons (10), c) contacting the stripping gas stream (10) obtained in step b) with a H2S-selective liquid absorbent solution (28) in a second absorption zone (12) to obtain a stripping gas stream depleted in H2S (13), and an absorbent solution enriched in H2S (14) d) introducing the absorbent solution (9) obtained in step b) into a desorption zone (16) wherein the H2S-selective liquid absorbent solution (17) is recovered and a lean acid gas is produced.

    METHOD FOR SEPARATING HYDROGEN SULFIDE AND AMMONIA DISSOLVED IN SOUR WATERS
    7.
    发明申请
    METHOD FOR SEPARATING HYDROGEN SULFIDE AND AMMONIA DISSOLVED IN SOUR WATERS 审中-公开
    在水中分离硫化氢和氨水的方法

    公开(公告)号:US20160347625A1

    公开(公告)日:2016-12-01

    申请号:US14733265

    申请日:2015-06-08

    Applicant: PROSERNAT

    Abstract: In a column provided with internals for liquid/gas contacting, the sour water feedstock is stripped using steam, then cooled by a cold liquid and washed using cold water injection. This method allows to separate an ammonia-poor (5-5000 ppm) H2S gaseous effluent and an H2S-lean (100-1000 ppm for example) purified water. The method is yet improved by adding a second column that receives the purified water from the first column and separates the hydrogen sulfide and the ammonia according to the method operated in the first column. The purified water from the second column is preferably partially injected into the first and/or the second column as wash water. A facility for implementing the method according to the invention.

    Abstract translation: 在具有液体/气体接触的内部的柱中,使用蒸汽汽提酸水原料,然后用冷的液体冷却并用冷水注入进行洗涤。 该方法允许分离贫氨(5-5000ppm)H 2 S气态流出物和贫H2S(100-1000ppm)净化水。 通过添加从第一塔接收净化水的第二塔,根据第一塔中操作的方法分离硫化氢和氨,该方法得到改善。 来自第二塔的净化水优选以洗涤水部分地注入第一和/或第二塔。 一种用于实现根据本发明的方法的设备。

    Removal of hydrogen sulfide and sulfur recovery from a gas stream by catalytic direct oxidation and claus reaction

    公开(公告)号:US10195565B2

    公开(公告)日:2019-02-05

    申请号:US15539257

    申请日:2015-12-23

    Applicant: PROSERNAT

    Abstract: A process for the removal of hydrogen sulfide and sulfur recovery from a H2S-containing gas stream by catalytic direct oxidation and Claus reaction through two or more serially connected catalytic reactors, wherein a specific control of the oxygen supplement is operated. The control and improvement of the process is obtained by complementing, in each major step of the process, the H2S-containing gas stream by a suitable flow of oxygen, namely before the H2S-containing gas stream enters the Claus furnace, in the first reactor of the process and in the last reactor of the process. Especially in application in a SubDewPoint sulfur recovery process the H2S/SO2 ratio is kept constant also during switch-over of the reactors R1 and R by adding the last auxiliary oxygen containing gas directly upstream the last reactor R so that the H2S/SO2 ratio can follow the signal of the ADA within a few seconds.

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