首页> 外国专利> Purifying a natural gas by reducing carbon dioxide, hydrogen sulfide and water present in the gas, adsorbing light mercaptans and contacting with an adsorbent material, and mixing a gaseous effluent with a hydrocarbon displacement agent

Purifying a natural gas by reducing carbon dioxide, hydrogen sulfide and water present in the gas, adsorbing light mercaptans and contacting with an adsorbent material, and mixing a gaseous effluent with a hydrocarbon displacement agent

机译:通过减少气体中存在的二氧化碳,硫化氢和水,吸附轻质硫醇并与吸附剂材料接触并将气态流出物与烃置换剂混合来纯化天然气

摘要

The process for the purification of natural gas by reducing carbon dioxide, hydrogen sulfide and water present in the gas, comprises adsorbing light mercaptans and contacting with an adsorbent material at a pressure of 2-10 MPa and at -40[deg] C to 100[deg] C, mixing a gaseous effluent with a hydrocarbon displacement agent constituted of a liquid phase having five carbon atoms to enrich the gaseous effluent, passing a charge of mercaptans and the obtained mixture through the adsorbent material, and carrying out a thermal desorption using a purge gas to desorb the displacement agent. The process for the purification of natural gas by reducing carbon dioxide, hydrogen sulfide and water present in the gas, comprises adsorbing light mercaptans and contacting with an adsorbent material at a pressure of 2-10 MPa and at -40[deg] C to 100[deg] C, mixing a gaseous effluent with a hydrocarbon displacement agent constituted of a liquid phase having five carbon atoms to enrich the gaseous effluent, passing a charge of mercaptans and the obtained mixture through the adsorbent material, carrying out a thermal desorption using a purge gas to desorb the displacement agent at a pressure of 0.5-10 MPa and a temperature of 50-400[deg] C, and cooling the adsorbent material at a pressure of 0.5-10 MPa using another gaseous effluent or directly using a purifier gas. The quantity of displacement agent introduced in the adsorbent material is = 50 mass% of maximum capacity for the adsorption of the displacement agent on the adsorbent material. The gaseous effluent is constituted of a purified natural gas or any other gas, and is mixed with the hydrocarbon displacement agent at a pressure of 0.5-10 MPa and a temperature of 0-150[deg] C. The mercaptan gas is washed with the adsorbent solution, and then it is recycled. The hydrocarbon is a saturated hydrocarbon, aromatic hydrocarbon, paraffin and naphthene.
机译:通过减少气体中存在的二氧化碳,硫化氢和水来纯化天然气的方法包括吸附轻质硫醇并在2-10 MPa的压力下和-40℃至100的压力下与吸附剂材料接触℃下,将气态流出物与由具有五个碳原子的液相构成的烃置换剂混合以富集气态流出物,使一部分硫醇和所得混合物通过吸附剂材料,并进行热解吸。吹扫气体以解吸置换剂。通过减少气体中存在的二氧化碳,硫化氢和水来纯化天然气的方法包括吸附轻质硫醇并在2-10 MPa的压力下和-40℃至100的压力下与吸附剂材料接触℃下,将气态流出物与由具有五个碳原子的液相构成的烃置换剂混合以富集气态流出物,使一定量的硫醇和所得混合物通过吸附剂材料,使用碳氢化合物进行热脱附。在0.5-10 MPa的压力和50-400℃的温度下吹扫气体以解吸置换剂,并使用另一种气体流出物或直接使用净化器气体将吸附剂材料在0.5-10 MPa的压力下冷却。引入到吸附剂材料中的置换剂的量为最大容量的50质量%,以用于将置换剂吸附在吸附剂材料上。气态流出物由纯净的天然气或任何其他气体构成,并在0.5-10 MPa的压力和0-150的温度下与烃置换剂混合。吸附剂溶液,然后将其回收。烃是饱和烃,芳族烃,石蜡和环烷烃。

著录项

  • 公开/公告号FR2923838A1

    专利类型

  • 公开/公告日2009-05-22

    原文格式PDF

  • 申请/专利权人 IFP;CECA;

    申请/专利号FR20070008174

  • 发明设计人 THOMAS MICHEL;MEYER PETER;

    申请日2007-11-21

  • 分类号C10L3/10;B01D53/04;C07C7/13;C10G5/02;

  • 国家 FR

  • 入库时间 2022-08-21 19:07:18

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