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    • 5. 发明申请
    • SYSTEMS AND METHODS FOR PURIFYING AND RECYCLING LEAD FROM SPENT LEAD-ACID BATTERIES
    • 从铅酸蓄电池中净化和回收铅的系统和方法
    • WO2015195398A1
    • 2015-12-23
    • PCT/US2015/034761
    • 2015-06-08
    • JOHNSON CONTROLS TECHNOLOGY COMPANY
    • SPENCE, MatthewCURRAN, Patrick
    • H01M10/54C22B7/00C22B3/00
    • H01M10/54B01J6/001B01J6/002B01J8/008B01J19/06B01J19/2465B01J2208/00805C22B3/02C22B3/04C22B7/006C22B7/007C22B7/009C22B13/04C22B13/045H01M6/52Y02P10/234Y02W30/84
    • The present disclosure relates to systems and methods by which lead from spent lead-acid batteries may be extracted, purified, and used in the production of new lead-acid batteries. Such a system may include a first phase separation device (76) configured to receive the first mixture from the basic lead stream digestion device (192), isolate a liquid component (196) from one or more insoluble components (78) of the first mixture, and output the liquid component (196). The system also includes a lead salt precipitation device (200) configured to receive and mix the liquid component and a carboxylate source (201) to form a second mixture including a lead salt precipitate and output the second mixture. The system further includes a second phase separation device (92) configured to receive the second mixture from the lead salt precipitation device (200), isolate the liquid component (96) from the lead salt precipitate (94) of the second mixture, and output the lead salt precipitate, which may later be converted into leady oxide particles (100).
    • 本公开涉及可以提取,纯化和用于生产新铅酸电池的废铅酸电池的铅的系统和方法。 这样的系统可以包括被配置为从碱性引导流消解装置(192)接收第一混合物的第一相分离装置(76),将液体组分(196)与第一混合物的一种或多种不溶性组分(78) ,并输出液体组分(196)。 该系统还包括被配置为接收和混合液体组分和羧酸盐源(201)以形成包含铅盐沉淀物的第二混合物并输出第二混合物的铅盐析出装置(200)。 该系统还包括第二相分离装置(92),其配置为从铅盐沉淀装置(200)接收第二混合物,将液体组分(96)与第二混合物的铅盐沉淀物(94)隔离,并输出 铅盐沉淀物,其可以随后转化成铅氧化物颗粒(100)。
    • 8. 发明申请
    • A REACTOR COMPRISING A PACKED BED OF SUPPORTED CATALYST OR SUPPORTED CATALYST PRECURSOR, AND A USE OF THE REACTOR
    • 包含支持的催化剂或支持的催化剂前体的包装床的反应器和反应器的使用
    • WO02007872A1
    • 2002-01-31
    • PCT/EP2001/008019
    • 2001-07-11
    • B01J8/00B01J8/02B01J12/00B01J23/889C10G2/00
    • B01J37/0225B01J8/008B01J8/02B01J12/007B01J23/8892B01J2208/00805C10G2/341
    • A reactor comprising a packed bed of supported catalyst or supported catalyst precursor wherein the supported catalyst or the supported catalyst precursor comprise an external surface comprising a catalytically active metal or a precursor compound thereof, and the packed bed has a void content of more than 50 %v and a specific surface area of more than 10 cm /cm , which is calculated as the total external surface area of the particles relative to the bed volume; the use of the said reactor in a chemical conversion process; a process for preparing hydrocarbons from syngas, which process comprises contacting a mixture of carbon monoxide and hydrogen in the said reactor, on the understanding that the catalytically active metal is a Group VIII metal which is at least in part present in metallic form; a packed bed of catalyst particles or catalyst precursor particles; and a catalyst particle or catalyst precursor particle.
    • 一种反应器,包括负载催化剂或负载催化剂前体的填充床,其中所述负载型催化剂或所述负载催化剂前体包含包含催化活性金属或其前体化合物的外表面,并且所述填充床的空隙含量大于50% v,比表面积大于10cm 2 / cm 3,其计算为颗粒相对于床体积的总外表面积; 在化学转化过程中使用所述反应器; 从合成气制备烃的方法,该方法包括在所述反应器中使一氧化碳和氢气的混合物接触,理解催化活性金属是至少部分以金属形式存在的第Ⅷ族金属; 催化剂颗粒或催化剂前体颗粒的填充床; 和催化剂颗粒或催化剂前体颗粒。