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Apparatus for purifying sulphur and obtaining carbon disulphide and sulphur oxides

机译:用于纯化硫并获得二硫化碳和氧化硫的设备

摘要

310,972. Merturi, G. Jakova-. May 4, 1928, [Convention date]. Chemical manufacture, f u r n a c e s for; sulphur burners.-An apparatus for preparing carbon bisulphide, flowers of sulphur or roll sulphur consists of a chamber 1 divided by partitions 21 into compartments 4, 5, 6, and heated by gases of combustion admitted through openings 13, 14, 15 and exhausted through a flue 23. The compartments contain superposed retorts 3 - - 12. In preparing carbon bisulphide, sulphur or sulphur ore is charged into the retorts 9, 10, and the sulphur vapours are led into the retorts 7, 8, which contain brown or other coal which may have been distilled in an atmosphere such as steam which does not support combustion, and which is contained in perforated liners 50, Fig. 2, having a perforated partition near the base below which the sulphur vapour is delivered. Carbon bisulphide is withdrawn by a pipe 49 to a condenser. If roll sulphur is to be obtained, sulphur vapours from the retorts 9, 10 are led into retorts 11, 12 which are maintained at a temperature of 130-140‹ C., and liquid sulphur is discharged from these retorts through openings at the base. If flowers of sulphur are to be obtained, all the retorts may be charged with sulphur or sulphur ores and the vapours are passed by pipe 33 into an upper chamber 34 leading to air or water-cooled cylinders 40, 41, 42. To obtain sulphur oxide air is admitted to the retorts 8 - - 12, and the products pass through the cylinders 40, 41, 42 to a collecting main 46.
机译:310,972。 Merturi,G。Jakova-。 1928年5月4日,[公约]。化学制造,适用于;硫燃烧器。一种用于制备二硫化碳,硫磺花或硫磺卷的设备,该设备由一个腔室1组成,该腔室由隔板2 1分成隔室4、5、6,并由通过开口13、14进入的燃烧气体加热15和15通过烟道23排出。隔室中有重叠的蒸馏瓶3-12。在制备二硫化碳时,将硫或硫矿石装入蒸馏瓶9、10中,并将硫蒸气引入蒸馏瓶7、8中。包含棕色或其他煤炭,这些煤炭可能已经在不支持燃烧的气氛(例如蒸汽)中进行了蒸馏,并包含在图2的多孔衬管50中,该衬管的底部附近有一个多孔隔板,硫蒸气在该隔板下输送。通过管道49将二硫化碳排出到冷凝器中。如果要获得卷装硫,则将来自蒸馏瓶9、10的硫蒸气引入蒸馏瓶11、12,将其保持在130-140°C的温度下,并通过底部的开口从这些蒸馏瓶中排出液态硫。 。如果要获得硫磺花,则所有的all都可以装入硫磺或硫磺矿石,并且蒸气通过管道33进入上腔室34,通向空气或水冷气缸40、41、42。氧化物空气进入脱水缸8-12,产品通过汽缸40、41、42到达收集主管46。

著录项

  • 公开/公告号GB310972A

    专利类型

  • 公开/公告日1930-10-03

    原文格式PDF

  • 申请/专利权人 GASPARD JAKOVA-MERTURI;

    申请/专利号GB19290013885

  • 发明设计人

    申请日1929-05-03

  • 分类号C01B17/02;C01B17/48;C01B17/54;C01B31/26;F02M19/03;

  • 国家 GB

  • 入库时间 2022-08-24 08:55:49

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