首页> 外国专利> Inorganic cpd. or mixt. prodn. e.g. for catalyst, alloy, prepn. - includes mechanically pulverising solid starting material mixt. to fine particles

Inorganic cpd. or mixt. prodn. e.g. for catalyst, alloy, prepn. - includes mechanically pulverising solid starting material mixt. to fine particles

机译:无机cpd。或混音。产品例如用于催化剂,合金,制备-包括机械粉碎固体原料混合物。细颗粒

摘要

Prodn. of inorganic cpd(s). (I) or their mixts., esp. catalysts, alloys, intermetallic cpds., adducts of metals and/or oxides or superconductors, involves mixing the solid starting materials (II) and mechanical pulverisation to a particle size finer than 10 microns. Pref. (II) are oxides and/or metals, esp. Ti, Cu, Ni, Co, V, Mo, Fe, Sn, Ag, Cr, Si, Al, Y, Ba, La, Sr, Bi and/or Zn and opt. also Pd, V and/or Re, as metal or oxide. Pref. (II) are pulverised to particles finer than 4 microns, pref. 0.1-4 microns and with a narrow granulation with d50 = 0.1-1 micron. Pulverisation of (II) is carried out for 1 s to 60 min, pref. 5-15 min, and with heating, pref. to 300-400 deg. C, esp. in a reactor operating at an energy desnity of 0.5-500, pref. 5-200 kw/1 reactor vol. (II) pref. are pulverised (mechanically) to 30-300, esp. 60-120 microns before mixing , opt. in the presence of additive(s) (III), pref. in amts. of 0.1-3 (wt.)% w.r.t. (II). (III) pref. prevent reagglomeration of pulverised (II). Mixing and/or pulverisation is carried out by impact with a fluid, pref. a liquid, esp. water or an oxidising or reducing liquid. Oxides may be reduced (with H2) or metals oxidised during and/or after pulverisation. Pref. water is added during pulverisation and (I) are sepd. from the suspension or dispersion by flotation, coagulation and/or pptn. adsorption. ADVANTAGE - High (I) yields and rapid reaction rates are attained with much less environmental pollution than usual.
机译:产品无机cpd。 (I)或它们的混合。催化剂,合金,金属间化合物,金属和/或氧化物或超导体的加合物涉及混合固体原料(II)并进行机械粉碎,使其粒径小于10微米。首选(II)是氧化物和/或金属,尤其是。 Ti,Cu,Ni,Co,V,Mo,Fe,Sn,Ag,Cr,Si,Al,Y,Ba,La,Sr,Bi和/或Zn并选择以及Pd,V和/或Re,作为金属或氧化物。首选(II)粉碎成细于4微米的颗粒。 0.1-4微米,d50 = 0.1-1微米的窄颗粒。优选将(II)粉碎1 s至60分钟。 5-15分钟,并加热预煮。到300-400度C,特别是在能量密度为0.5-500(优选)的反应堆中运行。 5-200千瓦/ 1反应堆体积(II)偏好(机械地)粉碎至30-300,尤其是混合前60-120微米,可选。在添加剂(III)存在下,优选。在地上。重量的0.1-3(wt。)% (II)。 (III)优先防止粉状(II)团聚。混合和/或粉碎是通过与一种液体的预冲击进行的。液体,尤其是水或氧化性或还原性液体。在粉碎过程中和/或之后,氧化物可能会还原(用H2还原)或金属被氧化。首选在粉碎过程中加入水,并分离(I)。通过浮选,凝结和/或pptn从悬浮液或分散体中分离得到。吸附。优势-获得高(I)的收率和快速的反应速率,并且对环境的污染要比平时少得多。

著录项

  • 公开/公告号DE4308114A1

    专利类型

  • 公开/公告日1993-11-04

    原文格式PDF

  • 申请/专利权人 OSER ERWIN DR. 50670 KOELN DE;

    申请/专利号DE19934308114

  • 发明设计人 OSER ERWIN DR. 50670 KOELN DE;

    申请日1993-03-15

  • 分类号C01G1/00;B01F3/18;B01J37/12;B02C23/00;B01J23/72;B01J37/16;B01J37/04;B01J37/08;

  • 国家 DE

  • 入库时间 2022-08-22 05:01:13

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