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Hydrogenation catalyst taking transition metal phosphide as aid

A kind of hydrogenation catalyst, transition metal technology

Inactive Publication Date: 2015-01-07
CHINA UNIV OF PETROLEUM (EAST CHINA)
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

The transition metal phosphides disclosed in Chinese patent application 200610134020.3 are prepared by reducing metal oxides and phosphorus oxides with hydrogen at a high temperature of 600-950°C. Since the transition metal sulfides will be oxidized when they meet water, the hydrogenation reduction reaction products There is water in the medium, and the preparation of phosphides must adopt high hydrogen flow rate and low heating rate, so the preparation of transition metal phosphides takes a long time and consumes a lot of hydrogen. From the perspective of saving energy and hydrogen resources, it is difficult to realize large-scale industrialization. production; and the transition metal phosphide catalyst itself cannot meet the requirements of economically and effectively removing heteroatoms in petroleum distillates and coal tar

Method used

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  • Hydrogenation catalyst taking transition metal phosphide as aid

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Embodiment 1

[0022] Take by weighing 200g of alumina (Pseudoboehmite of Yantai Henghui Chemical Co., Ltd. Co., Ltd. Yantai Henghui Chemical Co., Ltd.) with a water content of 30.5%, 6 g of scallop powder, add 180 ml of 3% nitric acid aqueous solution after fully mixing, and extrude on the extruder after fully kneading. Form cylindrical strips with a diameter of 1.6 mm, and bake in an oven at 120° C. for 12 hours to obtain a dry carrier. Then it was placed in a muffle furnace and calcined in air at a temperature of 500° C. for 4 hours to obtain a catalyst carrier A. Weigh 39.8 g of ammonium tetrathiomolybdate, add 25 ml of ethanolamine and 15 ml of distilled water, stir to dissolve, and obtain a blood-red clear solution. An equal volume of this solution was impregnated into 74 g of carrier A, left at room temperature for 2 hours, and then placed in an oven at 60° C. for 12 hours. It was placed in a tube furnace and treated with nitrogen gas at 200° C. for 3 hours to obtain molybdenum-loade...

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Abstract

The invention relates to a hydrogenation catalyst taking a transition metal phosphide as an aid. In the hydrogenation catalyst, a porous material is taken as a carrier, a sulfide of molybdenum and / or tungsten is taken as an active component, and the transition metal phosphide is taken as the aid. A preparation method of the catalyst comprises the following steps: introducing precursors of molybdenum and tungsten into the channel of the carrier through soluble sulfo-molybdate and / or soluble sulfo-tungstate, and heating the precursors in a protective atmosphere to obtain the sulfide of the molybdenum and / or the tungsten; and introducing transition metal hypophosphite, and thermally decomposing the transition metal hypophosphite into the phosphide in the protective atmosphere to obtain the hydrogenation catalyst taking the transition metal phosphide as the aid. The hydrogenation catalyst disclosed by the invention has high reaction activity in the hydrogen desulfurization and denitrification reactions of dibenzothiophene and nitrogen heterocyclic ring compounds, and can meet the requirements of low sulfuration and desulphurization of fuel oil.

Description

technical field [0001] The invention relates to the technical field of catalysts, more specifically, the invention relates to a hydrogenation catalyst using transition metal phosphides as auxiliary agents. Background technique [0002] In recent years, the trend of heavy and inferior crude oil has become increasingly obvious worldwide, and the content of sulfur, nitrogen and aromatics in petroleum products is increasing day by day, and the contradiction between increasingly stringent environmental protection requirements and this reality has become more and more acute. More than one-third of my country's petroleum products, especially diesel products, are produced by catalytic cracking technology. With the widespread application of heavy oil catalytic cracking technology, catalytic cracking raw materials are gradually becoming heavier and worse, making the properties of catalytic cracking diesel oil increasingly worse. , The content of sulfur, nitrogen and aromatics in diesel...

Claims

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Application Information

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IPC IPC(8): B01J29/00B01J29/80C10G45/12
Inventor 柴永明刘晨光刘宾刘理华柳云骐殷长龙邢金仙
Owner CHINA UNIV OF PETROLEUM (EAST CHINA)