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    • 4. 发明申请
    • USE OF LIQUID HYDROGEN CHLORIDE AS REFRIGERANT IN PROCESSES FOR PREPARING CHLORINE
    • 氯化氢作为制冷剂在制备氯化物的工艺中的应用
    • US20120213693A1
    • 2012-08-23
    • US13371910
    • 2012-02-13
    • Hans-Jürgen PALLASCHHeiner SCHELLINGPeter VAN DEN ABEELTill EINIG
    • Hans-Jürgen PALLASCHHeiner SCHELLINGPeter VAN DEN ABEELTill EINIG
    • C01B7/04
    • C01B7/04
    • This invention relates to a process for preparing chlorine from HCl and a method of using liquid HCl to cool and optionally liquefy chlorine in the process. The process involves introducing at least one HCl-containing stream and an oxygen-containing stream into an oxidation zone and catalytically oxidizing the HCl to chlorine, contacting the chlorine with aqueous HCl with partial separation of water and HCl to yield a gas stream, drying the gas stream to yield an essentially water-free gas stream, which is compressed and cooled to give an at least partially liquefied stream, and separating the liquefied stream into a gas stream and a liquid stream which is separated into a chlorine stream, such that cooling and partial liquefaction of the gas stream is effected by indirect heat exchange with a liquid HCl stream, resulting in some of the liquid HCl stream vaporizing to form a gaseous HCl stream.
    • 本发明涉及一种从HCl制备氯的方法,以及使用液体HCl冷却和任选地在该过程中液化氯的方法。 该方法包括将至少一种含HCl流和含氧物流引入氧化区并将HCl催化氧化成氯,将氯与HCl水溶液接触,部分分离出水和HCl,产生气流,干燥 气流以产生基本上无水的气流,其被压缩和冷却以产生至少部分液化的流,并将液化物流分离成气流和液态物流,其被分离成氯气流,使得冷却 并且通过与液体HCl流的间接热交换来实现气流的部分液化,导致一些液体HCl流汽化以形成气态HCl流。
    • 5. 发明申请
    • METHOD FOR THE PRODUCTION OF CHLORINE
    • 氯仿生产方法
    • US20090304572A1
    • 2009-12-10
    • US12162368
    • 2007-01-26
    • Martin SesingKnud JacobsenKlaus-Dieter ReinhardtHans-Juergen PallaschPeter Van Den AbeelHeiner Schelling
    • Martin SesingKnud JacobsenKlaus-Dieter ReinhardtHans-Juergen PallaschPeter Van Den AbeelHeiner Schelling
    • C01B7/04
    • C01B7/04C01B7/0743
    • Process for preparing chlorine from hydrogen chloride, which comprises the steps: a) feeding of a stream a1 comprising hydrogen chloride and of a stream a2 comprising oxygen into an oxidation zone and catalytic oxidation of hydrogen chloride to chlorine, giving a product gas stream a3 comprising chlorine, water, oxygen, carbon dioxide and inert gases; b) contacting of the product gas stream a3 with aqueous hydrochloric acid I in a phase contact apparatus and partial separation of water and of hydrogen chloride from the stream a3, leaving a gas stream b comprising hydrogen chloride, chlorine, water, oxygen, carbon dioxide and possibly inert gases, with at least 5% of the hydrogen chloride comprised in the stream a3 remaining in the gas stream b; c) drying of the gas stream b) to leave a gas stream c which is substantially free of water and comprises hydrogen chloride, chlorine, oxygen, carbon dioxide and possibly inert gases; d) partial liquefaction of the gas stream c by compression and cooling, giving an at least partially liquefied stream d; e) gas/liquid separation of the stream d into a gas stream e1 comprising chlorine, oxygen, carbon dioxide, hydrogen chloride and possibly inert gases and a liquid stream e2 comprising hydrogen chloride, chlorine, oxygen and carbon dioxide and, if appropriate, recirculation of at least part of the gas stream e1 to step a); f) separation of the liquid stream e2 into a chlorine stream f1 and a stream f2 consisting essentially of hydrogen chloride, oxygen and carbon dioxide by distillation in a column, with part of the hydrogen chloride condensing at the top of the column and running back as runback into the column, as a result of which a stream f2 having a chlorine content of
    • 从氯化氢制备氯的方法,其包括以下步骤:a)将包含氯化氢的流a1和包含氧的料流a1进料到氧化区中并将氯化氢催化氧化成氯,得到产物气流a3,其包含 氯,水,氧,二氧化碳和惰性气体; b)在相位接触装置中将产物气流a3与盐酸I水溶液接触,并从流a3中部分分离水和氯化氢,留下包含氯化氢,氯,水,氧气,二氧化碳的气流b 和可能的惰性气体,其中包含在流a3中的至少5%的氯化氢保留在气流b中; c)干燥气流b)以留下基本上不含水的气流c,并包含氯化氢,氯气,氧气,二氧化碳和可能的惰性气体; d)压缩和冷却气流c的部分液化,给出至少部分液化的流d; e)将气流d气体/液体分离成包含氯气,氧气,二氧化碳,氯化氢和可能的惰性气体的气体流e1和包含氯化氢,氯气,氧气和二氧化碳的液体流e2,如果合适的话,再循环 的气流e1至步骤a)的至少一部分; f)通过在柱中蒸馏将液体流e2分离成氯流f1和基本上由氯化氢,氧气和二氧化碳组成的物流f2,其中一部分氯化氢在塔的顶部冷凝并回流为 反应到塔中,结果得到氯含量<1重量%的料流f2。