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This invention provides a method for preparing hydrogenation catalyst containing phosphorus supported by aluminum oxide. The catalyst is composed of nickel oxide 1-10 wt.%, molybdena oxide and tungsten oxide 10-50 wt.

以氧化铝为载体的含磷加氢催化剂及其制备,该催化剂烧后的组成为氧化镍1-10重量%,氧化钼和氧化钨之和大于10至50重量%,氧化磷1-9重量%,余量为氧化铝,其中,以氧化物计,钨和钼的摩尔比大于2.6至30。

Molybdena oxide and tungsten oxide 10-50 wt.%, and carrier. The catalyst is prepared by introducing nickel, molybdena and tungsten into the carrier containing molecular sieve.

该催化剂由包括向一种含分子筛的载体引入钼、镍和钨的方法制备,其中,各组分的用量使催化剂烧后的组成为:氧化镍1-10重量%,氧化钼和氧化钨之和大于10至50重量%,余量为载体。

Phosphorus oxide 1-10 wt.%, and aluminum oxide. The molar ratio of tungsten oxide to molybdena oxide is 2.6-30. The method comprises introducing nickel oxide, molybdena oxide, tungsten oxide and phosphorus oxide into aluminum oxide carrier.

该催化剂由包括向氧化铝载体中引入磷、钼、镍和钨,其中,各组分的用量使催化剂烧后的组成为:氧化镍1-10重量%,氧化钼和氧化钨之和大于10至50重量%,氧化磷1-9重量%,余量为氧化铝,其中,以氧化物计,钨和钼的摩尔比大于2.6至30。

The effective recovery new technologies,such as optimum roasting conditions and molybdic acid preparation,etc.

烧最佳条件、钼酸及七钼酸铵制备等问题进行了详实阐述,新工艺具有显著的技术经济效果。

In order to recover Mo and Cu,the acidic from the production process of molybdic ammonium was disposed by DK macropous cation exchange resin,AH compex resin and general cation exchange resin,respectively.Other heavy metals in wastewater were deposited by adding ammonia liquor in the proess.

钼酸铵[分子式为(NH4)2Mo4O13·2H2O或(NH4)6Mo7O24·4H2O]是石油化学工业和高分子合成工业催化剂、陶瓷彩釉和颜料、特殊分析试剂和药物以及生产金属钼丝、片等的重要原料[1],工业上通常采用将精钼砂烧、硝酸浸洗、氨水浸出、净化和加酸沉淀等一系列工艺流程。

Effects of sonic factors, including dosage of catalyst, calcination temperature of catalyst, nitrated reaction time and recovered catalyst, on the selectivity of toluene in mononitration at the presence of silicotungstic acid catalyst were studied by gas chromatography.

通过气相色谱研究了诸如催化剂用量、催化剂烧温度、硝化反应时间、硝化反应温度及催化剂的重复使用等因素对甲苯硝酸硝化区域选择性的影响。

The catalytic performance of mordenite exchanged by calcium ion is superior to the domestic commercial product. This CaHM was prepared by being roasted with adhesive, and can be directly used in pilot plant.

自制的这种钙离子改性丝光沸石催化剂的催化性能优于目前国内工业化的甲胺生产催化剂,而且CaHM是经添加粘接剂烧成型的样品,可直接供产品的中试放大。

The rules and relationships betweenspectroscopic characters of〓ions inzeolites ZSM-5,Beta,Mordenite and L,and calciningconditions were obtained.

得到了含稀土离子的ZSM-5、Beta、丝光沸石和L型沸石中〓〓等离子的光谱变化规律及与烧处理条件的变化关系。

This result laid a foundation of theory and experiment for the development of mordenite sorbent to separate ethene.NaY was firstly modified using two ion-exchange and two calcinations method which was heated by microwave.

首次采用微波加热二次离子交换二次烧的方法改性NaY分子筛,制得CeY、CeY、CuY、AgY、KY、MgY和SrY,并用于吸附噻吩和苯,其中CeY分子筛对噻吩具有最好的吸附容量和选择性。

The process of selective reduction roasting- ammonia leaching is adopted to extract nickel,cobalt and recover iron from low grade nickeliferous laterite ore.

本研究采用选择性还原烧—氨浸工艺从低品位红土镍矿中综合提取镍、钴、铁,重点介绍了该工艺氨浸的试验研究。

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