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    • 3. 发明授权
    • Heat recovery in production of vinyl chloride by pyrolysis of
dichloroethane
    • 通过二氯乙烷热解生产氯乙烯时的热回收
    • US4822932A
    • 1989-04-18
    • US178477
    • 1988-04-07
    • Gerhard DummerKlaus HaselwarterHermann KlausLudwig SchmidhammerRudolf Strasser
    • Gerhard DummerKlaus HaselwarterHermann KlausLudwig SchmidhammerRudolf Strasser
    • C07C17/00C07C17/25C07C17/38C07C17/383C07C21/06C07C67/00C07C17/24C07C17/34
    • C07C17/25C07C17/38B01J2219/00006Y02P20/51
    • In a method of treating the reaction product of pyrolysis of 1,2-dichloroethane to form vinyl chloride and hydrogen chloride with multiple stage cooling and distillation separation of the reaction product and recycle of unreacted 1,2-dichloroethane to the pyrolysis step, the improvement comprising direct cooling of the reaction product immediately after leaving the pyrolysis step, within 1 sec from a temperature range of 480.degree. to 540.degree. C. down to 150.degree. to 250.degree. C., charging the cooled product into a quench column, recovering the vapors from the head of the quench column and indirectly cooling the same by heat exchange to at least its condensation point, the heat exchange media being at least one member of the group consisting of (a) 1,2-dichloroethane to be fed in heated condition to the pyrolysis unit, (b) air used as combustion air to fire the pyrolysis zone, (c) the sump of the hydrogen chloride column as defined above, (d) liquid hydrogene chloride to be evaporated and, (e) water, to dissipate heat not used within the measures according to the present invention.
    • 在处理1,2-二氯乙烷热解反应产物形成氯乙烯和氯化氢的方法中,多级冷却和蒸馏分离反应产物并将未反应的1,2-二氯乙烷再循环到热解步骤中,改进 包括在离开热解步骤后立即直接冷却反应产物,在480℃至540℃的温度至150℃至250℃的1秒内,将冷却的产物装入骤冷塔中,回收 来自骤冷塔头部的蒸气并通过热交换间接地冷却至至少其冷凝点,所述热交换介质是由(a)1,2-二氯乙烷组成的组中的至少一个组分,所述组分由待加热的 (b)用作燃烧空气来燃烧热解区的空气,(c)如上所述的氯化氢柱的贮槽,(d)待蒸发的液体氯化烯,(e) 水,以消散根据本发明的措施中不使用的热量。