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    • 6. 发明授权
    • Process for the purification of a pentafluoroethane azeotrope
    • 纯化五氟乙烷共沸物的方法
    • US5346595A
    • 1994-09-13
    • US23827
    • 1993-02-23
    • Paul G. ClemmerHsueh S. TungAddison M. Smith
    • Paul G. ClemmerHsueh S. TungAddison M. Smith
    • B01D3/14C07B63/00C07C17/383C07C19/08C07C17/38
    • C07C17/383B01D3/14Y10S203/13
    • The invention generally relates to a process for the purification of a component of a binary azeotrope in which the composition of the azeotrope changes by about 10 mole percent with pressure comprising:(a) subjecting a binary azeotrope to a distillation step in which most of one of the binary components is removed as distillate (distillate 1) with the bottoms (bottoms 1) enriched in the other component;(b) subjecting distillate 1 to at least one additional distillation step conducted at a different pressure in which most of the component recovered as bottoms 1 is removed as distillate 2 with the bottoms 2 enriched in the component enriched in distillate 1;(c) optionally repeating step (b) as many times as desired; and(d) recovering the desired purified component.The invention is particularly useful in the purification of pentafluoroethane in a pentafluoroethane/chloropentafluoroethane azeotrope.
    • 本发明一般涉及纯化二元共沸物组分的方法,其中共沸物的组成随压力变化约10摩尔%,包括:(a)使二元共沸物进行蒸馏步骤,其中大部分 的二元组分作为馏出物(馏出物1)除去富含其它组分的塔底物(塔底物1); (b)使馏出物1进行至少一个另外的蒸馏步骤,在不同的压力下进行另外的蒸馏步骤,其中作为塔底馏出物1回收的大部分组分作为馏出物2被除去,富含富含馏分1的组分富含塔底物2; (c)任选地重复步骤(b)多次; 和(d)回收所需的纯化组分。 本发明特别可用于五氟乙烷/氯五氟乙烷共沸物中五氟乙烷的提纯。
    • 8. 发明授权
    • Single stage process for producing hydrofluorocarbons from
perchloroethylene
    • 从全氯乙烯生产氢氟烃的单阶段工艺
    • US5545778A
    • 1996-08-13
    • US248981
    • 1994-05-25
    • Hsueh S. TungAddison M. SmithCharles F. Swain
    • Hsueh S. TungAddison M. SmithCharles F. Swain
    • C07C17/087C07B61/00C07C17/21C07C17/35C07C17/38C07C17/383C07C19/08C07C19/12C07C17/08
    • C07C17/21C07C17/383
    • A process for the preparation of one or more of CHClFCF.sub.3 (HCFC-124), CHF.sub.2 CClF.sub.2 (HCFC-124a) and CHF.sub.2 CF.sub.3 (HFC-125) by reaction of perchloroethylene with hydrogen fluoride in a single stage reaction vessel in the presence of a fluorination catalyst. These compounds are useful in a variety of industrial applications including blowing agents, refrigerants, sterilant gases and solvent applications. Distilling the reaction product produces a distillate comprising HCl, CHClFCF.sub.3, CHF.sub.2 CClF.sub.2 and CHF.sub.2 CF.sub.3 and a minor amount of HF which distillate is scrubbed to remove the acids. The bottoms product comprises perchloroethylene, hydrogen fluoride and organic by-products which is phase separated to sequester the hydrogen fluoride from the mixture of perchloroethylene and organic by-products. The hydrogen fluoride and mixture of perchloroethylene with organic by-products are then preferably re-mixed at a controlled rate and recycled to the reaction vessel.
    • 在氟化催化剂存在下,在单级反应容器中通过全氯乙烯与氟化氢的反应制备CHClFCF3(HCFC-124),CHF2CClF2(HCFC-124a)和CHF2CF3(HFC-125)中的一种或多种的方法 。 这些化合物可用于各种工业应用,包括发泡剂,制冷剂,灭菌气体和溶剂应用。 蒸馏反应产物产生包含HCl,CHClFCF 3,CHF 2 CClF 2和CHF 2 CF 3的馏出物和少量HF,该馏出物被洗涤以除去酸。 底部产物包括全氯乙烯,氟化氢和有机副产物,其相分离以从全氯乙烯和有机副产物的混合物中隔离氟化氢。 然后将氟化氢和全氯乙烯与有机副产物的混合物优选以受控的速率重新混合并再循环至反应容器。