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Improvements in or relating to method for separating the components of gaseous mixtures mixtures in fluidized adsorption system

机译:在流化吸附系统中分离气态混合物混合物成分的方法的改进或与之有关的改进

摘要

Gaseous components of a mixture are separated by means of a fluidized solid adsorbent by passing said mixture into the absorption section of a column consisting from top to bottom of sections for (a) disengaging, cooling, absorption, rectifying, desorption and dehydration, or for (b) disengaging, adsorption, rectification desorption, dehydration and cooling, whilst the adsorbent passes downwardly through said sections. Tail gas is passed from the disengaging section to the dehydrating section (in arrangement (b), via the cooling section) to contact the wet adsorbent passing therethrough, and is also used to recirculate by entrainment the adsorbent from the lowest section to the disengaging section; in arrangement (b) part of this gas is withdrawn as the less adsorbed product gas but in arrangement (a) the latter is withdrawn from the upper part of the adsorption section; from the rectifying section an intermediate fraction or fractions, if present, are withdrawn; heat and stripping steam are applied to the desorption section, and steam and the more adsorbable component withdrawn therefrom; from the dehydrating section, a stream of mixed gases and steam is withdrawn, which may be added after drying to the tail gases from the disengaging section; all or a part of said mixed gases may alternatively in arrangement (a) be introduced into an intermediate section of the adsorption section. In one embodiment of arrangement (a), gas in addition to that required as less adsorbed product is withdrawn from the adsorption section and added to the tail gas, and this mixture used to assist fluidization in the cooling zone in addition to its use for dehydration and recirculation. It is stated that the whole of the wet product gases may be removed from the desorption section, dried and returned to the rectification section after removal of heavy fractions, in arrangement (a). Mixtures to which the process can be applied are:- separations between individual hydrocarbons as in residual gases from cracking of all kinds, separation of gases such as hydrogen and nitrogen from hydrocarbons (activated carbon adsorbent may be used), particularly the products of hydroforming; benzene and an inert carrier such as air, hydrogen and nitrogen; nitrogen and methane.
机译:混合物的气态成分通过流化的固体吸附剂分离,方法是使混合物进入塔的吸收段,该塔的吸收段由塔顶到塔底组成,以进行(a)分离,冷却,吸收,精馏,解吸和脱水,或(b)分离,吸附,精馏,解吸,脱水和冷却,同时吸附剂向下通过所述部分。尾气从分离区流到脱水区(在配置(b)中,通过冷却区),以接触通过其中的湿吸附剂,并且还通过将吸附剂从最低区带入分离区而再循环。 ;在布置(b)中,该气体的一部分作为较少吸附的产物气体被排出,但是在布置(a)中,后者从吸附部分的上部排出;从精馏段中抽出一个或多个中间馏分(如果存在);将热量和汽提蒸汽施加至解吸段,并从中抽出蒸汽和更具吸附性的组分。从脱水区抽出混合气体和蒸汽流,在干燥后可将其加入到来自分离区的尾气中。可选择地,在布置(a)中,全部或部分所述混合气体被引入吸附部分的中间部分。在布置(a)的一个实施方案中,除了需要较少吸附产物的气体外,还从吸附部分抽出气体并将其加入尾气中,该混合物除用于脱水外还用于辅助冷却区的流化。和再循环。据指出,在布置(a)中,可以从解吸段除去全部湿产物气体,干燥并在除去重馏分之后返回精馏段。可以应用该方法的混合物是:-各种裂解过程中残留气体中各个烃之间的分离,烃中氢和氮等气体的分离(可以使用活性碳吸附剂),特别是液压成型的产品;苯和惰性载体,例如空气,氢气和氮气;氮气和甲烷。

著录项

  • 公开/公告号GB761305A

    专利类型

  • 公开/公告日1956-11-14

    原文格式PDF

  • 申请/专利权人 ESSO RESEARCH AND ENGINEERING COMPANY;

    申请/专利号GB19540025506

  • 发明设计人

    申请日1954-09-02

  • 分类号B01D53/12;B01J8/18;C07C7/12;

  • 国家 GB

  • 入库时间 2022-08-23 22:13:30

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