首页> 外国专利> Preparation of iron-doped ruthenium-on-carbon catalysts, used for selective liquid hydrogenation of carbonyls to corresponding alcohols, involves reducing in hydrogen stream and forming catalyst in difficultly-flammable liquid

Preparation of iron-doped ruthenium-on-carbon catalysts, used for selective liquid hydrogenation of carbonyls to corresponding alcohols, involves reducing in hydrogen stream and forming catalyst in difficultly-flammable liquid

机译:用于将羰基化合物选择性加氢成相应醇的铁掺杂碳载钌催化剂的制备涉及减少氢气流并在难燃液体中形成催化剂

摘要

Two methods are claimed for the production of ruthenium/iron/carbon carrier catalysts containing 0.1-5 wt.% iron as well as 0.1-10 wt.% ruthenium on a carbon carrier. Two methods are claimed for the production of ruthenium/iron/carbon carrier catalysts containing 0.1-5 wt.% iron as well as 0.1-10 wt.% ruthenium on a carbon carrier. The first method involves: (i) addition of a base to a mixture in water of the carrier and a solution containing the catalytically-active ruthenium and iron components so as to effect simultaneous precipitation onto the carrier; (ii) separating the catalyst from the aqueous phase of the suspension; (iii) drying the catalyst; (iv) reducing in a hydrogen stream at 400-600 degreesC; and (v) forming the catalyst in a difficultly-flammable liquid or passivating it with a diluted air stream. The second method proceeds as per step (i) above but this is followed by: (iia) reduction of the catalyst by addition of an aqueous reductant; (iiia) separating from the aqueous phase of the suspension; and (iva) washing with water. An Independent claim is included for the use of the catalyst is in selective liquid hydrogenation of carbonyl compounds of formula R1C(O)R2 (I) to the corresponding alcohols of formula R1C(OH)HR2 (II). R1 and R2 = H, optionally mono- or poly-unsaturated, optionally substituted 1-20C alkyl, optionally substituted aryl or optionally substituted heterocyclic group.
机译:要求保护两种用于生产钌/铁/碳载体催化剂的方法,所述催化剂在碳载体上包含0.1-5重量%的铁以及0.1-10重量%的钌。要求保护两种用于生产钌/铁/碳载体催化剂的方法,所述催化剂在碳载体上包含0.1-5重量%的铁以及0.1-10重量%的钌。第一种方法包括:(i)将碱加到载体的水和含有催化活性的钌和铁组分的溶液的混合物中,以同时沉淀到载体上; (ii)从悬浮液的水相中分离出催化剂; (iii)干燥催化剂; (iv)在400-600℃的氢气流中还原; (v)在难燃液体中形成催化剂或用稀释的空气流使其钝化。第二种方法按上述步骤(i)进行,但随后是:(i)通过加入含水还原剂还原催化剂; (iiia)从悬浮液的水相中分离; (iva)用水洗涤。包括使用催化剂的独立权利要求是将式R1C(O)R2(I)的羰基化合物选择性地液体氢化为式R1C(OH)HR2(II)的相应醇。 R1和R2 = H,任选地单或多不饱和,任选地取代的1-20C烷基,任选地取代的芳基或任选地取代的杂环基。

著录项

  • 公开/公告号DE10235064A1

    专利类型

  • 公开/公告日2004-02-19

    原文格式PDF

  • 申请/专利权人 BASF AG;

    申请/专利号DE2002135064

  • 发明设计人 ERFINDER WIRD SPÄTER GENANNT WERDEN;

    申请日2002-07-31

  • 分类号B01J37/03;B01J21/18;B01J23/74;B01J23/89;

  • 国家 DE

  • 入库时间 2022-08-21 22:44:04

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