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Co-current contacting of liq. and gaseous phases - partic. for economical treatment of gaseous effluent from chemical factories

机译:液体的并流接触。和气相-颗粒状。用于经济处理化工厂的废气

摘要

The gas is passed through a contacting chamber, e.g. a column, at a speed between that corresp. to its value at the transition point of phase inversion and to the multiple, critical point. The speed of liq. flow into the gas is adjusted so that liq. in the emulsion also achieves a speed between that corresp. to the transition point of phase inversion and that corresp. to the multiple, critical point. The gas speed is pref. 5.5-13.5 m/sec. and the rate of introduction of liq. 170-20 kg/cm3. The process is pref. employed for treating a gaseous effluent contg. oxides of nitrogen. The process is also favoured for a carbonation reaction by treating soda with a gas contg. CO2. The liq. phase pref. carries a solid catalyst and the gas is free from dust. Partic. applications include treatment of gaseous effluent from chemical industry operations such as the mfr. of HNO3, H2SO4, HCl, HF, combustion exhaust gases etc. Small proportions of liq. can be employed without mixing into the gas and without entering into underisable chemical reaction with consequent waste of raw material and energy. The danger of vesiculation is avoided.
机译:气体通过例如一根柱子,其间的速度相应。在相转换的过渡点和多个临界点处达到其值。液体的速度。调整流入气体的流量,以使液量降低。乳液中的粘度也达到了相应的速度。到相变的过渡点并相应地到多个关键点。气体速度为首选。 5.5-13.5 m /秒和液体的引入速度。 170-20千克/立方厘米。该过程是优选的。用于处理气态废水。氮的氧化物。通过用气体控制苏打,该方法也有利于碳酸化反应。二氧化碳液体。相位预选携带固体催化剂,气体中不含灰尘。参加应用包括处理化学工业操作(如mfr)中的气态废水。 HNO3,H2SO4,HCl,HF,燃烧废气等。可以不与气体混合使用,也不会进行不充分的化学反应,从而浪费原料和能源。避免了囊泡形成的危险。

著录项

  • 公开/公告号FR2431877B1

    专利类型

  • 公开/公告日1981-01-09

    原文格式PDF

  • 申请/专利权人 RHONE POULENC INDUSTRIES;

    申请/专利号FR19780022094

  • 发明设计人

    申请日1978-07-26

  • 分类号B01J10/00;B01D3/00;B01D47/00;B01D53/14;C01D7/07;

  • 国家 FR

  • 入库时间 2022-08-22 15:05:43

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