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Process for the liquefaction and rectification of air or other gaseous mixture into its components

机译:将空气或其他气体混合物液化和精馏成其组分的方法

摘要

248,977. Cicali, G. June 16, 1925. Separating gases by liquefaction.- Air &e. is divided into two portions, one of which is slightly compressed and cooled without expansion by the cold nitrogen resulting from the subsequent recti fication; the other portions is compressed to a higher pressure, cooled by the whole of the re sulting nitrogen and hydrogen, and separated intc two portions, one of which is liquefied without expansion, throttled down, and delivered to pans in the rectifying column, while the other is ex. panded into a motor to the same pressure as the slightly compressed portion and introduced with this portion into the bottom of the rectifier. Air &c. is compressed to a few atmospheres in a water-cooled compressor C1 and passes through a water-cooled coil s'; it is then divided into twc parts one of which flows through a cock R1 to a two-pipe heat exchange coil S1 where it is cooled by a, counter current of rectified nitrogen, finally being led into the base of the rectification column through the pipe A. The other portion is compressed further in a water-cooled compressor C2 cooled in a coil and passed into the middle pipe of a triple'heat-exchange coil S2 cooled by oxygen and nitrogen flowing through the inner and outer pipes. Issuing from this coil it is divided, one portion flowing into an expansion chamber e and thence to the pipe A, while the other portion is further cooled and liquefied in a coil S3 traversed by nitrogen which afterwards flows through the coil S2, and is delivered at the inlet C into the column. The gases rise from the base of the column through plates D; the liquefied oxygen is lead through a valved pipe E to the top of the column, containing plates G, from which it falls to vessels H. H' and to the outside of a heatexchange apparatus in which it is vaporized, passing off through an outlet z to the coil S2. The nitrogen rising in the column is liquefied in the lulose esters, natural or synthetic resin, paraffin. of the column. Here it is vaporized, and carried down to a point l where it is divided between the coils S1 and S2.
机译:248,977。 Cicali,G.,1925年6月16日。通过液化分离气体。-Air&e。分为两部分,其中一部分被随后的精馏所产生的冷氮稍微压缩和冷却而不会膨胀。另一部分则被压缩至较高压力,并通过全部氮气和氢气进行冷却,并分离为两部分,其中一部分被液化而没有膨胀,被节流并输送到精馏塔的塔盘中,而其他是前。安装在电动机中,使其压力与稍微压缩的部分相同,并随该部分引入整流器的底部。空气&c。在水冷压缩机C 1中被压缩到几个大气压,并通过水冷线圈s'。然后将其分为两部分,其中一部分通过旋塞R <1>流到两管式热交换盘管S <1>,在此通过整流氮气的逆流进行冷却,最后被导引至第二部分。另一部分在盘管中冷却的水冷压缩机C 2中进一步压缩,并进入由氧气冷却的三重热交换盘管S 2的中间管中。氮气流经内管和外管。从该盘管中将其分开,一部分流入膨胀室e,然后流向管A,而另一部分进一步冷却并在被氮气横穿的盘管S 3中液化,然后流过盘管S < 2>,并在入口C处输送到色谱柱中。气体通过塔板D从塔底升起。液化氧气通过带阀的管道E引导到塔的顶部(包含板G),液化的氧气从其中掉落到容器H. H',并流到热交换设备的外部,在该设备中气化的氧气通过出口排出z到线圈S <2>。塔中上升的氮在果糖醛酸酯,天然或合成树脂,石蜡中液化。列的。在此,它被蒸发,并被运送到点l,在点l中,它在线圈S 1和S 2之间被划分。

著录项

  • 公开/公告号GB248977A

    专利类型

  • 公开/公告日1926-03-18

    原文格式PDF

  • 申请/专利权人 GIOVANNI CICALI;

    申请/专利号GB19250015608

  • 发明设计人

    申请日1925-06-16

  • 分类号F25J3/04;

  • 国家 GB

  • 入库时间 2022-08-24 10:37:53

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