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PROCESS FOR REACTIVATING NOBLE METAL CATALYSTS ON A CARRIER FOR THE SYNTHESIS OF H2O2 BY ANTHRAQUINONE PROCESS

机译:蒽醌法合成H2O2的载体上贵金属催化剂的活化方法

摘要

1312149 Hydrogen peroxide DEUTSCHE GOLDUND SILBER-SCHEIDEANSTALT 10 July 1970 [12 July 1969] 33514/70 Heading C1A In the preparation of hydrogen peroxide by the anthraquinone process the catalyst used is regenerated by an oxidative treatment at a pH below 7 and a reductive treatment, both treatments being carried out at below 200‹ C., the catalyst comprising palladium, if desired mixed with other metals of the platinum group (Ru Rh, Os, Ir, and Pt) precipitated upon carrier materials containing silica. Less than 1% by weight of palladium or mixed metals related to the total weight of the carrier may be used. The silica carrier may have a BET surface area below 50 m.SP2/SP/g. The inactive catalyst may be subjected to a pretreatment to remove traces of working solution or degradation products. Reagents for the oxidation may include gaseous chlorine/hydrogen chloride mixtures, moist chlorine, hydrogen peroxide/hydrochloric acid mixtures or nitric acid/hydrochloric acid mixtures. The reduction may be by a dry process (e.g. using free hydrogen containing gas) or a wet process (e.g. with formic acid, formaldehyde or hydrazine). Pressures in the reactivation may be up to 6 kg./cm.SP2/SP. The pretreatment may comprise such operations as water scrubbing or steam treatment of the carrier catalyst, extraction from catalyst with organic solvent, e.g. acetone, isopropanol, trichloroethylene or xylene or drying of catalyst at temperatures below 250‹ C. In Example 1 a catalyst of 0À2% Pd precpitated on filter gravel was pretreated with 1,1,1-trichloroethane, placed in 1À6 ton charges in a rotary drum 1, sprayed with a 15 weight per cent HCl/50 weight per cent H 2 O 2 mixture and then steam heated at about 100‹ C. under a current of N 2 to form a coating of PdCl 2 . Reduction of PdCl 2 to Pd was then carried out by passing a current of H 2 and N 2 . In Example 2 a HCl/Cl 2 gas mixture was used as the oxidizing agent. Apparatus which may be used for carrying out the process is described in the Specification and drawings.
机译:1312149过氧化氢Deutsches Goldund SILBER-SCHEIDEANSTALT 1970年7月10日[1969年7月12日]标题C1A在蒽醌法制备过氧化氢的过程中,所用催化剂通过在pH值低于7的氧化处理和还原处理进行再生,两种处理均在低于200℃下进行,如果需要的话,包含钯的催化剂与铂族的其他金属(Ru Rh,Os,Ir和Pt)混合,沉淀在含二氧化硅的载体材料上。相对于载体的总重量,可以使用少于1重量%的钯或混合金属。二氧化硅载体的BET表面积可以低于50m。 2 / g。可以对惰性催化剂进行预处理以除去痕量的工作溶液或降解产物。用于氧化的试剂可以包括气态氯/氯化氢混合物,湿氯气,过氧化氢/盐酸混合物或硝酸/盐酸混合物。还原可通过干法(例如使用含游离氢的气体)或湿法(例如用甲酸,甲醛或肼)进行。重新激活过程中的压力可能高达6 kg./cm。 2 。预处理可以包括诸如水洗或载体催化剂的蒸汽处理,用有机溶剂例如有机溶剂从催化剂中萃取的操作。丙酮,异丙醇,三氯乙烯或二甲苯,或在低于250°C的温度下干燥催化剂。在实施例1中,将预先沉淀在滤砾上的0‑2%Pd催化剂用1,1,1-三氯乙烷预处理,并以1‑6吨装料置于旋转装置中。用1重量%的HCl / 50重量%的H 2 O 2混合物喷射鼓1,然后在N 2的电流下在约100℃加热蒸汽,以形成PdCl 2涂层。然后,通过使H 2和N 2电流通过,将PdCl 2还原为Pd。在实施例2中,使用HCl / Cl 2气体混合物作为氧化剂。说明书和附图中描述了可用于进行该方法的设备。

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