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    • 6. 发明专利
    • DE502007001903D1
    • 2009-12-17
    • DE502007001903
    • 2007-01-26
    • BASF SE
    • SESING MARTINJACOBSEN KNUDREINHARDT KLAUS-DIETERPALLASCH HANS-JUERGENVAN DEN ABEEL PETERSCHELLING HEINER
    • C01B7/04C01B7/07
    • 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
    • 7. 发明专利
    • AT447539T
    • 2009-11-15
    • AT07722774
    • 2007-01-26
    • BASF SE
    • SESING MARTINJACOBSEN KNUDREINHARDT KLAUS-DIETERPALLASCH HANS-JUERGENVAN DEN ABEEL PETERSCHELLING HEINER
    • C01B7/04C01B7/07
    • 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
    • 8. 发明专利
    • PROCEDIMIENTO PARA LA OBTENCION DEL CLORO.
    • ES2334523T3
    • 2010-03-11
    • ES07722774
    • 2007-01-26
    • BASF SE
    • SESING MARTINJACOBSEN KNUDREINHARDT KLAUS-DIETERPALLASCH HANS-JURGENVAN DEN ABEEL PETERSCHELLING HEINER
    • C01B7/04C01B7/07
    • Procedimiento para la obtención de cloro a partir de cloruro de hidrógeno, con los siguientes pasos: a) Introducción de un flujo a1 que contiene cloruro de hidrógeno y un flujo a2 que contiene oxígeno en una zona de oxidación y oxidación catalítica de cloruro de hidrógeno a cloro, obteniendo un flujo de gas de producto a3 que contiene cloro, agua, oxígeno, dióxido de carbono y gases inertes; b) Puesta en contacto, en un aparato de puesta en contacto de fases, del flujo de gas de producto a3 con ácido clorhídrico acuoso I y una separación parcial de agua y de cloruro de hidrógeno del flujo a3, obteniendo un flujo de gas b que contiene cloruro de hidrógeno, cloro, agua, oxígeno, dióxido de carbono y, eventualmente, gases inertes, asimismo, al menos 5% del cloruro de hidrógeno contenido en el flujo a3 permanece en el flujo de gas b; c) Secado del flujo de gas b, obteniendo un flujo de gas c esencialmente libre de agua, que contiene cloruro de hidrógeno, cloro, oxígeno, dióxido de carbono y, eventualmente, gases inertes; d) Licuefacción parcial del flujo de gas c mediante compresión y refrigeración, obteniendo un flujo d al menos parcialmente líquido; e) Separación de gas y líquido del flujo d, en un flujo de gas e1 que contiene cloro, oxígeno, dióxido de carbono, cloruro de hidrógeno y, eventualmente, gases inertes y un flujo líquido e2 que contiene cloruro de hidrógeno, cloro, oxígeno y dióxido de carbono y, eventualmente, un retorno de, al menos, una parte del flujo de gas e1 al paso a); f) Separación del flujo líquido e2 por destilación, en una columna, en un flujo de cloro f1 y un flujo f2 que consiste, esencialmente, en cloruro de hidrógeno, oxígeno y dióxido de carbono, asimismo, una parte del cloruro de hidrógeno es condensado en la cabeza de la columna y es reconducida a la columna, por lo que se obtiene un flujo f2 con una proporción de cloro