首页> 外国专利> Removal procedure sulfur compounds H2S, SO2, COS and / or CS2 contained in a residual sulfur factory gas with recovery of such compounds in the form of sulfur.

Removal procedure sulfur compounds H2S, SO2, COS and / or CS2 contained in a residual sulfur factory gas with recovery of such compounds in the form of sulfur.

机译:去除程序残留在残留硫工厂气体中的硫化物H2S,SO2,COS和/或CS2,并以硫的形式回收。

摘要

The waste gas (6) is hydrolyzed catalytically (1) to form a hydrolyzate (15) containing gas H 2 and SO 2 and COS-FREE CS 2. After cooling (17), gas hydrolyzate is introduced into a (2A) of the two zones catalytic CLAUS (2A, 2B) mounted in parallel, the other being catalytic zone (2B) for regeneration, COS and / or CS2 RESIDUAL CONTENT IN A GAS fACTORY AYA CONTINUATION cooling. REGENERATION IS DONE IN OPEN CIRCUIT, with a gaseous stream (19, 36) obtained from the gas (15) before cooling (17), the offgas (24b) REGENERATION reinjected (29, 30) on the GAS, between extraction (19) and cooling (17). THE COOLING REACTOR (2B) is performed, OPEN CIRCUIT, with a gaseous stream (11, 36) obtained from waste gas (6), the offgas (24B) COOLING Reintroduced (29, 13) in the waste gas (6) between extraction (11) and heating.
机译:废气(6)被催化水解(1)以形成包含气体H 2和SO 2以及COS-FREE CS 2的水解产物(15)。冷却(17)之后,气体水解产物被引入到气体(2A)中。并联安装的两个催化区CLAUS(2A,2B),另一个是用于催化再生的催化区(2B),气体工厂AYA持续冷却中的COS和/或CS2残留含量。在开路中完成再生,在冷却(17)之前从气体(15)获得气流(19、36),废气(24b)在提取(19)之间将再生(29、30)重新注入GAS。和冷却(17)。冷却反应器(2B)在开路中进行,从废气(6)获得的气流(11、36)被排出,废气(24B)在萃取(6)中在废气(6)中重新引入(29、13)。 (11)加热。

著录项

  • 公开/公告号ES2157121T3

    专利类型

  • 公开/公告日2001-08-01

    原文格式PDF

  • 申请/专利权人 ELF EXPLORATION PRODUCTION;

    申请/专利号ES19980922854T

  • 发明设计人 NOUGAYREDE JEAN;

    申请日1998-04-23

  • 分类号C01B17/04;

  • 国家 ES

  • 入库时间 2022-08-22 01:22:19

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