首页> 外国专利> PROCESS AND COMPOSITION FOR SEPARATION OF OXYGEN FROM AIR USING PR-CE OXIDES AS THE CARRIER

PROCESS AND COMPOSITION FOR SEPARATION OF OXYGEN FROM AIR USING PR-CE OXIDES AS THE CARRIER

机译:以PR-CE氧化物为载体从空气中分离氧气的过程和组成

摘要

1489224 Oxygen separation UNION CARBIDE CORP 24 Oct 1974 [25 Oct 1973] 45984/74 Heading ClA Oxygen is separated from an O 2 containing gas mixture by oxidizing a Pr-Ce oxide mixture present in a "first oxidized state" by reacting with the gas mixture to convert at least a portion of the reaction mass into a relatively more "oxidized state" followed by separation of the O 2 depleted gas mixture from the relatively more oxidized Pr-Ce oxide reaction mass and then dissociating at least a portion of the oxidized mass to a relatively more reduced state of Pr-Ce oxide with liberation of O 2 ; the Pr-Ce oxide mixture and O 2 are then separated. The reaction masses may have the general formula (Pr x Ce y )O z where x and y are the relative molar amounts of cations in the oxide materials and x + y = 1 and z varies from 1À5 to 2À0; at values of z = 2À0 the materials are in their fully oxidized state while at z = 1À5 they are at their lower limit of dissociation. The Pr-Ce oxide mixture may contain a surface dopant, e.g. Ag, which increases the resistance of the oxide material to the effects of CO 2 and H 2 O which may be present in the gas mixture. A Pr-Ce oxide reaction mass of general formula (Pr x Ce y )O z , containing a dopant, preferably silver, is synthesized by contacting an aqueous solution comprising the nitrate salts of Pr, Ce and dopant with excess precipitating agent with respect to the molar amount of Pr and Ce in the aqueous starting solution; the precipitated material is separated from the aqueous solution, dried and then calcined at 600-1000‹ C. to form the mixed oxide; the precipitating agent is selected from the group ammonium oxalate or hydroxide or oxalic acid.
机译:1489224氧气分离UNION CARBIDE CORP 1974年10月24日[1973年10月25日] 45984/74标题CLA通过与以气体“第一氧化态”存在的Pr-Ce氧化物混合物进行氧化,将氧气从含O 2的气体混合物中分离出来混合物以将至少一部分反应物料转化为相对更“氧化的状态”,然后从相对较氧化的Pr-Ce氧化物反应物料中分离出O 2耗尽的气体混合物,然后解离至少一部分氧化的释放出O 2,使Pr-Ce氧化物质量相对还原。然后分离Pr-Ce氧化物混合物和O 2。反应物质的通式为(Pr x Ce y)O z,其中x和y是氧化物材料中阳离子的相对摩尔量,x + y = 1且z在1-5到2-0之间变化。在z = 2‑0时,材料处于完全氧化状态,而在z = 1‑5时,材料处于解离下限。所述Pr-Ce氧化物混合物可包含表面掺杂剂,例如Pr-Ce氧化物混合物。 Ag,增加了氧化物材料对混合气体中可能存在的CO 2和H 2 O的抵抗力。通过使包含Pr,Ce和掺杂剂的硝酸盐的水溶液与过量的沉淀剂接触,合成含有掺杂剂,优选为银的通式(Pr x Ce y)O z的Pr-Ce氧化物反应物料。起始水溶液中Pr和Ce的摩尔量;从水溶液中分离出沉淀物,干燥,然后在600-1000℃下煅烧,形成混合氧化物。沉淀剂选自草酸铵或氢氧化物或草酸。

著录项

  • 公开/公告号GB1489224A

    专利类型

  • 公开/公告日1977-10-19

    原文格式PDF

  • 申请/专利权人 UNION CARBIDE CORP;

    申请/专利号GB19740045984

  • 发明设计人

    申请日1974-10-24

  • 分类号C01F17/00;C01B13/08;

  • 国家 GB

  • 入库时间 2022-08-22 23:38:42

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