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    • 1. 发明授权
    • Method of operating a dehydrogenation reactor system
    • 操作脱氢反应器系统的方法
    • US07282619B2
    • 2007-10-16
    • US10897248
    • 2004-07-22
    • Ruth Mary KowaleskiRobert Dielman Culp
    • Ruth Mary KowaleskiRobert Dielman Culp
    • C07C5/333
    • C07C5/3332B01J23/745B01J23/76C07C5/321C07C2523/745Y10S585/952C07C11/02C07C15/46C07C11/12
    • Described is a method for operating and shutting down a dehydrogenation reactor that contains a volume of dehydrogenation catalyst. After termination of the introduction of a dehydrogenation feed into the dehydrogenation reactor that is operated under dehydrogenation reaction conditions, a first cooling fluid comprising steam is introduced into the reactor for a first time period sufficient to cool the dehydrogenation catalyst contained in the dehydrogenation reactor to a second temperature. The introduction of the first cooling fluid is terminated followed by the introduction of a second cooling fluid for a second time period sufficient to cool the dehydrogenation catalyst contained in the dehydrogenation reactor to a third temperature that allows for the handling and removal of the dehydrogenation catalyst from the dehydrogenation reactor.
    • 描述了一种用于操作和关闭含有一定体积的脱氢催化剂的脱氢反应器的方法。 在脱氢反应器引入脱氢反应器终止之后,在脱氢反应条件下运行的脱氢反应器中,将包含蒸汽的第一冷却流体引入反应器中第一次足以将脱氢反应器中所含的脱氢催化剂冷却至 第二温度。 第一冷却流体的引入被终止,然后引入第二冷却流体第二时间段,足以将脱氢反应器中所含的脱氢催化剂冷却至允许将脱氢催化剂从 脱氢反应器。
    • 5. 发明授权
    • Process to recover metals from spent catalyst
    • 从废催化剂中回收金属的工艺
    • US06180072B2
    • 2001-01-30
    • US09306134
    • 1999-05-06
    • Jack Thomas VealKevin Arnold AndersenRuth Mary Kowaleski
    • Jack Thomas VealKevin Arnold AndersenRuth Mary Kowaleski
    • C01G3900
    • C22B7/008C22B7/009C22B34/325C22B34/345Y02P10/214Y02P10/23Y02P10/234
    • There is provided a process to reclaim metals from catalysts, said process comprising collecting one or more catalyst containing at least one metal sulfide; leaching the catalyst in an atmospheric leach step; separating the leached slurry into a first liquid stream and a first solid; leaching the first solid in a pressure leach process; separating the second leached slurry into a second liquid stream and a second solid; collecting the first and second liquid streams; oxidizing the combined liquid stream; cooling the oxidized liquid stream; adjusting the pH of the oxidized liquid stream; contacting the cooled oxidized liquid stream with an organic solvent containing an extractant; stripping the soluble metal species from the organic phase; adjusting the pH of the aqueous phase to selectively precipitate at least one metal as a metal salt; and separating the metal salt from the aqueous phase.
    • 提供了从催化剂回收金属的方法,所述方法包括收集一种或多种含有至少一种金属硫化物的催化剂; 在大气浸出步骤中浸出催化剂; 将浸出的浆料分离成第一液体流和第一固体; 在压力浸出过程中浸出第一固体; 将第二浸出浆料分离成第二液体流和第二固体; 收集第一和第二液体流; 氧化组合的液体流; 冷却氧化液流; 调节氧化液流的pH值; 使冷却的氧化液体流与含有萃取剂的有机溶剂接触; 从有机相中剥离可溶性金属物质; 调节水相的pH以选择性沉淀至少一种金属作为金属盐; 并将金属盐与水相分离。