首页> 外国专利> METHOD FOR REMOVING HYDROCARBONS FROM GAS-VAPOR MIXTURE FORMED ON STORAGE OF PETROLEUM OR PETROLEUM PRODUCTS OR WHEN FILLING TANKS BY THE LATTER, AND PUMP- EJECTOR INSTALLATION FOR IMPLEMENTING THE METHOD

METHOD FOR REMOVING HYDROCARBONS FROM GAS-VAPOR MIXTURE FORMED ON STORAGE OF PETROLEUM OR PETROLEUM PRODUCTS OR WHEN FILLING TANKS BY THE LATTER, AND PUMP- EJECTOR INSTALLATION FOR IMPLEMENTING THE METHOD

机译:从汽油或石油产品存储时或从罐中填充油箱时所形成的气态混合物中去除烃的方法,以及用于实现该方法的泵的安装

摘要

FIELD: fluidics. SUBSTANCE: liquid and gas-vapor mixture are fed into jet device and then formed mixture is fed into separator to be separated into gas and liquid media. Part of the latter is withdrawn from flow circuit and the former is absorbed in column by hydrocarbon-containing liquid with saturated vapor pressure inferior to that of petroleum or petroleum product. Gas phase is removed and hydrocarbon-containing liquid with hydrocarbons dissolved therein is mixed with liquid medium. Part of liquid medium in flow circuit is transferred into system wherein absorbed hydrocarbons are isolated from liquid medium and remaining hydrocarbon-containing liquid is fed into column. Installation has pump, liquid-gas jet device, and separator. Liquid- medium inlet of device is connected to pump discharge side, gas-vapor-mixture inlet of device is connected to petroleum or petroleum product tank, and device outlet is connected to separator. Liquid-phase outlet of separator is connected to inlet side of pump. Installation is provided with absorption column and system foe isolation of absorbed hydrocarbons from liquid medium. Column communicates with gas-phase outlet of separator and top part of column is linked to purified gas phase-discharge pipeline. Above -indicated system includes rectification column provided with liquid phase- supply pipeline and hydrocarbon-containing liquid- and gas medium-discharge pipelines. EFFECT: increased economical efficiency of purification. 9 cl, 1 dwg
机译:领域:流体学。实质:将液体和气体-蒸汽混合物送入喷射装置,然后将形成的混合物送入分离器,以分离成气体和液体介质。后者的一部分从流动回路中抽出,前者在塔中被饱和烃压低于石油或石油产品的含烃液体吸收。除去气相,并将其中溶解有烃的含烃液体与液体介质混合。流动回路中的部分液体介质被转移到系统中,吸收的碳氢化合物与液体介质分离,剩余的含烃液体被送入塔中。装置包括泵,液气喷射装置和分离器。设备的液体介质入口连接到泵的排放侧,设备的气体-蒸汽混合物入口连接到石油或石油产品罐,设备出口连接到分离器。分离器的液相出口连接到泵的入口侧。吸收塔和系统提供安装,可从液体介质中分离吸收的碳氢化合物。塔与分离器的气相出口连通,塔的顶部与纯化的气相排放管线相连。上述系统包括精馏塔,该精馏塔设有液相供应管线和含烃的液体和气体介质排出管线。效果:提纯的经济效益更高。 9厘升,1滴水

著录项

  • 公开/公告号RU2193443C1

    专利类型

  • 公开/公告日2002-11-27

    原文格式PDF

  • 申请/专利权人 TSEGELSKIJ VALERIJ GRIGOREVICH;

    申请/专利号RU20010128896

  • 发明设计人 MALASHKEVICH A.V.;TSEGELSKIJ V.G.;

    申请日2001-10-29

  • 分类号B01D53/72;B65D90/30;

  • 国家 RU

  • 入库时间 2022-08-21 23:44:10

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