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    • 5. 发明申请
    • Method for the production of chlorine
    • 生产氯的方法
    • US20060263290A1
    • 2006-11-23
    • US10567579
    • 2004-08-06
    • Christian WalsdorffMartin FieneMartin SesingOlga MetelkinaLothar SeidemannEckhard StroeferKlaus Harth
    • Christian WalsdorffMartin FieneMartin SesingOlga MetelkinaLothar SeidemannEckhard StroeferKlaus Harth
    • C01B7/00
    • C01B7/04Y02P20/228
    • The invention relates to a process for preparing chlorine by catalytic gas-phase oxidation of hydrogen chloride, which comprises the steps: a) providing a feed gas stream I comprising hydrogen chloride and a feed gas stream II comprising oxygen; b) in a first oxidation stage, feeding the feed gas stream I, the feed gas stream II, if desired a recycle stream la comprising hydrogen chloride and if desired an oxygen-containing recycle stream IIa into a first oxidation zone and bringing them into contact with a first oxidation catalyst so that a first partial amount of the hydrogen chloride is oxidized to chlorine and a gas stream III comprising chlorine, unreacted oxygen, unreacted hydrogen chloride and water vapor is obtained; c) in a second oxidation stage, feeding the gas stream III into a second oxidation zone and bringing it into contact with at least one further oxidation catalyst so that a second partial amount of the hydrogen chloride is oxidized to chlorine and a product gas stream IV comprising chlorine, unreacted oxygen, unreacted hydrogen chloride and water vapor is obtained; d) isolating chloride, if desired the recycle stream Ia and if desired the recycle stream IIa from the product gas stream IV, wherein the first oxidization catalyst in the first oxidation zone is present in a fluidized bed and the further oxidation catalyst or catalysts in the second oxidation zone is/are present in a fixed bed.
    • 本发明涉及通过氯化氢的催化气相氧化制备氯的方法,其包括以下步骤:a)提供包含氯化氢的进料气流I和包含氧的进料气流II; b)在第一氧化阶段,如果需要,将进料气流I,进料气流II进料到包含氯化氢的再循环流1a,并且如果需要,将含氧循环流IIa进入第一氧化区并使其接触 用第一氧化催化剂使得第一部分氯化氢被氧化成氯,得到包含氯,未反应的氧,未反应的氯化氢和水蒸气的气流III; c)在第二氧化阶段,将气流III进料到第二氧化区并使其与至少一种其它氧化催化剂接触,使得第二部分量的氯化氢被氧化成氯,产物气流IV 包括氯,未反应的氧,未反应的氯化氢和水蒸气; d)如果需要,根据需要从产物气流IV中分离氯化物,如果需要,再循环流Ia,如果需要,再循环流IIa,其中第一氧化区中的第一氧化催化剂存在于流化床中, 第二氧化区存在于固定床中。
    • 6. 发明申请
    • Method For Producing Chlorine
    • 氯生产方法
    • US20080159948A1
    • 2008-07-03
    • US11816045
    • 2006-02-20
    • Martin SesingArmin DiefenbacherHartwig VossOlga SchubertLothar SeidemannMartin KarchesThomas GrasslerEckhard Stroefer
    • Martin SesingArmin DiefenbacherHartwig VossOlga SchubertLothar SeidemannMartin KarchesThomas GrasslerEckhard Stroefer
    • C01B7/04
    • C01B7/075C01B7/04C01B7/0743
    • 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) cooling of the product gas stream a3 and removal of water and hydrogen chloride as aqueous hydrochloric acid, leaving a gas stream b comprising chlorine, water, oxygen, carbon dioxide and inert gases; c) optional drying of the gas stream b) to leave a gas stream c which is substantially free of water and comprises chlorine, oxygen, carbon dioxide and inert gases; d) at least partial liquefaction of the gas stream c and of a chlorine-rich recycle stream f1 comprising chlorine, oxygen and carbon dioxide 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 and inert gases and into a liquid stream e2 comprising chlorine, oxygen and carbon dioxide; f) feeding of at least part of the gas stream e1 into a membrane separation unit and fractionation by membrane separation to give the chlorine-rich recycle stream f1 and a gas stream f2 which is low in chlorine and comprises chlorine, oxygen and carbon dioxide and recirculation of the chlorine-rich recycle stream f1 to step d); g) separation of the liquid stream e2 by distillation into a chlorine stream g1 and a stream g2 comprising essentially oxygen and carbon dioxide.
    • 从氯化氢制备氯的方法,其包括以下步骤:a)将包含氯化氢的物流1和包含氧的物流2加入氧化区并将氯化氢催化氧化成氯,得到产物气流 a 3,包括氯,水,氧,二氧化碳和惰性气体; b)冷却产物气流a 3,除去水和氯化氢作为盐酸水溶液,留下包含氯,水,氧气,二氧化碳和惰性气体的气流b; c)气流的任选干燥b)留下基本上不含水的气流c,包括氯,氧,二氧化碳和惰性气体; d)通过压缩和冷却至少部分液化气流c和包含氯,氧和二氧化碳的富含氯的循环流f 1,产生至少部分液化的流d; e)将气流d气体/液体分离成包含氯气,氧气,二氧化碳和惰性气体的气流e 1并进入包含氯​​气,氧气和二氧化碳的液体流e 2中; f)将至少部分气流e 1进料到膜分离单元中并通过膜分离进行分馏,得到富氯循环流f 1和氯含量低的气流f 2,包括氯,氧和 二氧化碳和富氯循环流f 1再循环到步骤d); g)通过蒸馏将液体流e 2分离成氯流g 1和基本上包含氧和二氧化碳的流g 2。
    • 7. 发明授权
    • Mechanically stable catalyst based on alpha-alumina
    • 基于α-氧化铝的机械稳定催化剂
    • US07910517B2
    • 2011-03-22
    • US12064725
    • 2006-08-22
    • Olga SchubertMartin SesingLothar SeidemannMartin KarchesThomas GrasslerMartin Sohn
    • Olga SchubertMartin SesingLothar SeidemannMartin KarchesThomas GrasslerMartin Sohn
    • B01J23/00B01J21/00B01J20/00B01J29/00B01J37/00
    • C01B7/04B01J21/04B01J23/462B01J23/52B01J23/72B01J23/8926
    • A catalyst for gas-phase reactions which has high mechanical stability and comprises one or more active metals on a support comprising aluminum oxide as support material, wherein the aluminum oxide in the support consists essentially of alpha-aluminum oxide.Ruthenium, copper and/or gold are preferred as active metal.Particularly preferred catalysts according to invention comprise a) from 0.001 to 10% by weight of ruthenium, copper and/or gold, b) from 0 to 5% by weight of one or more alkaline earth metals, c) from 0 to 5% by weight of one or more alkali metals, d) from 0 to 10% by weight of one or more rare earth metals, e) from 0 to 10% by weight of one or more further metals selected from the group consisting of palladium, platinum, osmium, iridium, silver and rhenium, in each case based on the total weight of the catalyst, on the support comprising alpha-Al2O3. The catalysts are preferably used in the oxidation of hydrogen chloride (Deacon reaction).
    • 一种用于气相反应的催化剂,其具有高机械稳定性并且在包含氧化铝作为载体材料的载体上包含一种或多种活性金属,其中载体中的氧化铝基本上由α-氧化铝组成。 作为活性金属,优选钌,铜和/或金。 根据本发明的特别优选的催化剂包含a)0.001至10重量%的钌,铜和/或金,b)0至5重量%的一种或多种碱土金属,c)0至5% 一种或多种碱金属的重量,d)0至10重量%的一种或多种稀土金属,e)0至10重量%的一种或多种另外的金属,其选自钯,铂, 锇,铱,银和铼,在每种情况下,基于催化剂的总重量,在包含α-Al 2 O 3的载体上。 催化剂优选用于氯化氢的氧化(Deacon反应)。
    • 8. 发明申请
    • MECHANICALLY STABLE CATALYST BASED ON ALPHA-ALUMINA
    • 基于ALPHA-ALUMINA的机械稳定催化剂
    • US20110014114A1
    • 2011-01-20
    • US12888082
    • 2010-09-22
    • Olga SCHUBERTMartin SesingLothar SeidemannMartin KarchesThomas GrasslerMartin Sohn
    • Olga SCHUBERTMartin SesingLothar SeidemannMartin KarchesThomas GrasslerMartin Sohn
    • C01B7/04
    • C01B7/04B01J21/04B01J23/462B01J23/52B01J23/72B01J23/8926
    • A catalyst for gas-phase reactions which has high mechanical stability and comprises one or more active metals on a support comprising aluminum oxide as support material, wherein the aluminum oxide in the support consists essentially of alpha-aluminum oxide.Ruthenium, copper and/or gold are preferred as active metal.Particularly preferred catalysts according to invention comprise a) from 0.001 to 10% by weight of ruthenium, copper and/or gold, b) from 0 to 5% by weight of one or more alkaline earth metals, c) from 0 to 5% by weight of one or more alkali metals, d) from 0 to 10% by weight of one or more rare earth metals, e) from 0 to 10% by weight of one or more further metals selected from the group consisting of palladium, platinum, osmium, iridium, silver and rhenium, in each case based on the total weight of the catalyst, on the support comprising alpha-Al2O3. The catalysts are preferably used in the oxidation of hydrogen chloride (Deacon reaction).
    • 一种用于气相反应的催化剂,其具有高机械稳定性并且在包含氧化铝作为载体材料的载体上包含一种或多种活性金属,其中载体中的氧化铝基本上由α-氧化铝组成。 作为活性金属,优选钌,铜和/或金。 根据本发明的特别优选的催化剂包含a)0.001至10重量%的钌,铜和/或金,b)0至5重量%的一种或多种碱土金属,c)0至5% 一种或多种碱金属的重量,d)0至10重量%的一种或多种稀土金属,e)0至10重量%的一种或多种另外的金属,其选自钯,铂, 锇,铱,银和铼,在每种情况下,基于催化剂的总重量,在包含α-Al 2 O 3的载体上。 催化剂优选用于氯化氢的氧化(Deacon反应)。