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Improvements in a process for recovery of elementary sulphur from gases containing hydrogen sulphide

机译:从含硫化氢的气体中回收单质硫的方法的改进

摘要

Sulphur is recovered from gas containing hydrogen sulphide by mixing the gas with air or other oxygen-containing gas, burning the mixture in a furnace to produce a mixture of sulphur, hydrogen sulphide and sulphur dioxide, cooling the gaseous mixture from e.g. 1500-2200 DEG F. to, e.g. 450 DEG F. in a waste heat boiler, scrubbing it with liquid sulphur to recover sulphur therefrom, heating the scrubbed gas in a separate furnace from, e.g. 270-280 DEG F. to, e.g. 400-450 DEG F., passing the heated gas through a catalyst to produce further sulphur by the interaction of the sulphur dioxide and hydrogen sulphide, cooling the reacted gas by indirect heat exchange with water subsequently fed to the waste heat boiler from, e.g. 550-600 DEG F. to, e.g. 450 DEG F., and scrubbing the cooled gas with liquid sulphur dioxide to recover sulphur therefrom. The catalyst may be disposed in two beds with an intermediate water cooling coil, the gas being cooled from 585 to 500 DEG F. after leaving the first bed and leaving the second bed at 525 DEG F. The catalyst may be activated bauxite.
机译:通过将气体与空气或其他含氧气的气体混合,从该含硫化氢的气体中回收硫,在炉中燃烧该混合物以产生硫,硫化氢和二氧化硫的混合物,从例如氢气中冷却气态混合物。 1500-2200°F至例如在废热锅炉中加热到450°F,用液态硫洗涤它以从中回收硫,然后在与例如270-280°F至例如400-450°F,使加热的气体通过催化剂,通过二氧化硫和硫化氢的相互作用产生更多的硫,通过与水的间接热交换冷却反应后的气体,随后将水从例如水蒸气送入废热锅炉。 550-600°F至例如450°F,并用液态二氧化硫洗涤冷却的气体以从中回收硫。可以将催化剂放置在带有中间水冷却盘管的两个床中,在离开第一床并在525°F离开第二床之后,将气体从585冷却到500°F。催化剂可以是活性铝土矿。

著录项

  • 公开/公告号GB754001A

    专利类型

  • 公开/公告日1956-08-01

    原文格式PDF

  • 申请/专利权人 FOSTER WHEELER LIMITED;

    申请/专利号GB19540006559

  • 发明设计人

    申请日1954-03-05

  • 分类号C01B17/04;

  • 国家 GB

  • 入库时间 2022-08-23 22:47:43

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