首页> 外国专利> Process and Apparatus for the De-sulphurisation of Sulphurous Substances, and the Treatment of the Spent Substances in the Purification of Gas.

Process and Apparatus for the De-sulphurisation of Sulphurous Substances, and the Treatment of the Spent Substances in the Purification of Gas.

机译:含硫物质脱硫的工艺和设备,以及天然气净化中废物质的处理。

摘要

4646. Maybluh, C. F. Sept. 25, A.D. 1901, [date applied for under Patents Act, A.D. 1901]. Sulphur.-Substances containing sulphur, such as spent gas purifier waste, are treated to obtain the sulphur. If purifier waste is the substance treated, ammonia and ferrocyanide are also obtained, while the residue is suitable for re-use in the purifiers. The substance is charged into a desulphurizing tank 1, which also receives a supply of petroleum or other mineral oil. The temperature is raised to 135‹ to 150‹ C. by means of a steam coil connected to the main 32, and the mixture is agitated by a mixer. The petroleum at this temperature dissolves out the sulphur, and the solution passes through a double filter bottom and a tube 5 to a lower refrigerating vessel 2, wherein the temperature is reduced by cooling coils connected to the tube 45. By this means the sulphur is precipitated. Rotating brushes prevent the deposition of sulphur upon the cooling-coils. The mixture is passed to the lower vessel 3, also having a double filter bottom, frcm which the petroleum runs through the tube 27 to the reservoir 13. The sulphur is next treated in the vessel 3 with benzine to remove all the petroleum. This benzine is drawn up from the vessel 15 by opening the connection to the vacuum main 38. The benzine solution obtained runs into the separating-vessel 4. Any benzine remaining with the residue in vessel 3, is recovered by adding water and heating by means of a steam coil. The benzine vapours are condensed in the coil 23, and collected in the vessel 15. The benzine solution in the vessel 4 is heated by a steam coil connected to the main 32. The benzine is distilled off, and is condensed by the coil 24 and collected in the vessel 15. The petroleum is afterwards run off to the reservoir 13. The petroleum is forced by the pump 57 to the tank 12, from which it may be passed to the vessel 1 by connecting the latter to the vacuum main 38. The vacuum in the latter is produced by a Koerting ejector 60. The residue in the vessel 1 is treated with benzine to extract the whole of the oil, the liquid running through the tube 11 to the separating-vessel 4.
机译:4646年。美国联邦调查局(Maybluh),公元1901年9月25日,[根据美国专利法,1901年申请的日期]。硫-含硫物质(例如废气净化器废料)经过处理后得到硫。如果净化器废物是经过处理的物质,则还会获得氨和亚铁氰化物,而残留物适合在净化器中重复使用。将该物质装入脱硫罐1,该脱硫罐也接收石油或其他矿物油的供应。借助于连接到主管32的蒸汽盘管将温度升高至135℃至150℃,并通过混合器搅拌混合物。在该温度下的石油溶解了硫,溶液通过双重过滤器底部和管子5到达下部制冷容器2,在该容器中,温度通过连接到管子45的冷却盘管降低。沉淀。旋转刷可防止硫沉积在冷却线圈上。混合物被送入下部容器3,下部容器3也具有双重过滤器底部frcm,石油通过管道27流到储罐13。接下来在容器3中用汽油处理硫以除去所有的石油。通过打开与真空总管38的连接,从容器15中抽出该汽油。所获得的汽油溶液进入分离容器4中。任何残留在容器3中的汽油都可以通过加水和加热的方式回收。的蒸汽盘管。汽油蒸气在盘管23中冷凝,并收集在容器15中。容器4中的汽油溶液被连接到主管32的蒸汽盘管加热。蒸馏出汽油,并通过盘管24和30冷凝。然后,将石油收集到容器15中。随后,将石油排到储罐13中。通过泵57将石油推到储罐12,通过将储罐连接到真空主管38,可以将其从储罐输送到容器1。后者中的真空是通过Koerting喷射器60产生的。容器1中的残留物用汽油处理,以提取全部油,液体通过管11到达分离容器4。

著录项

  • 公开/公告号GB190204646A

    专利类型

  • 公开/公告日1902-11-20

    原文格式PDF

  • 申请/专利权人 CHARLES FREDERIC MAYBLUH;

    申请/专利号GBD190204646

  • 发明设计人 CHARLES FREDERIC MAYBLUH;

    申请日1902-02-24

  • 分类号

  • 国家 GB

  • 入库时间 2022-08-24 16:53:48

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