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Catalyst prepared by impregnation with an aqueous solution containing oxy(hydroxy)de particles of a cation in interaction with a molecular species of a group VIII metal

机译:通过用含阳离子的氧(羟基)de颗粒的水溶液浸渍与第VIII族金属的分子种类相互作用制备的催化剂

摘要

Preparation of catalyst precursors (I) comprises preparing a colloidal solution (A), having oxide/hydroxide particles of a cation (D), by dissolving precursor salts of the cation at 5-100[deg] C, where the concentration of (D) is 0.01-1 mol/l in a volume of sodium hydroxide solution (X) or in a volume of water or in a volume of water added with (X); or using a commercial solution of the aqueous colloidal solution (A) and pouring an aqueous solution (B1) containing a group VIII metal precursor salt (Z) i.e. soluble under the used pH conditions, having a concentration of 0.001-1 mol/l. Preparation of catalyst precursors (I) comprises preparing a colloidal solution (A), of defined pH, having oxide/hydroxide particles of a cation M(z+) (D) including the cations of columns IIA, IIIA, IIIB, IVB or IVA of the periodic table, by dissolving precursor salts of the cation i.e. soluble in aqueous solution, at 5-100[deg] C, where the concentration of (D) is 0.01-1 mol/l in a volume of sodium hydroxide solution (X) having a concentration of 0.01-1 mol/l or in a volume of water or in a volume of water added with (X), or using a commercial solution of the aqueous colloidal solution (A) and pouring an aqueous solution (B1) containing a precursor salt (Z) of a metal of having a concentration of 0.001-1 mol/l, where (Z) is soluble under the used pH conditions. Independent claims are included for: (1) the catalyst precursor obtained by the process; (2) preparation of a catalyst from (I) comprising impregnation of the solution obtained at the end of pouring (B1) on a support having a BET (Brunauer, Emmett and Teller) surface of 300 m 2/g and drying at = 120[deg] C then calcining at 100-600[deg] C; (3) the catalyst obtained by the process; and (4) selective hydrogenation of an olefin cut comprising the implementation of the obtained catalyst.
机译:催化剂前体(I)的制备包括通过在5-100℃下溶解阳离子的前体盐来制备具有阳离子(D)的氧化物/氢氧化物颗粒的胶体溶液(A),其中(D )在一定体积的氢氧化钠溶液(X)或一定体积的水或一定体积的水中添加(X)的0.01-1 mol / l;或使用市售的胶体水溶液(A)溶液,倒入含有VIII族金属前体盐(Z)的水溶液(B1),即在使用的pH条件下可溶,其浓度为0.001-1 mol / l。催化剂前体(I)的制备包括制备具有规定pH的胶体溶液(A),该胶体溶液具有阳离子M(z +)(D)的氧化物/氢氧化物颗粒,该阳离子包括列IIA,IIIA,IIIB,IVB或IVA的阳离子通过在5-100℃下溶解阳离子(即可溶于水溶液)的阳离子前体盐的周期表,其中(D)的浓度为一定体积的氢氧化钠溶液(X)的0.01-1 mol / l浓度为0.01-1 mol / l或在一定体积的水或一定体积的水中添加(X)或使用市售的胶体水溶液(A)的溶液并倒入含有(X1)的水溶液(B1)浓度为0.001-1 mol / l的金属的前体盐(Z),其中(Z)在使用的pH条件下可溶。包括以下独立权利要求:(1)通过该方法获得的催化剂前体; (2)由(I)制备催化剂,该方法包括将在浇注(B1)结束时获得的溶液浸渍在BET表面(Brunauer,Emmett和Teller)为300m 2> / g的载体上,并在200℃下干燥。 120℃然后在100-600℃下煅烧; (3)通过该方法获得的催化剂; (4)烯烃馏分的选择性氢化,包括实施所得催化剂。

著录项

  • 公开/公告号EP1935488A1

    专利类型

  • 公开/公告日2008-06-25

    原文格式PDF

  • 申请/专利权人 IFP;

    申请/专利号EP20070291388

  • 申请日2007-11-22

  • 分类号B01J23/54;B01J23/76;B01J35/00;B01J37/00;B01J37/02;B01J23/58;B01J23/63;B01J23/83;

  • 国家 EP

  • 入库时间 2022-08-21 19:55:45

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