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A kind of preparation method of hydrogenation catalyst composition

A technology of hydrogenation catalyst and composition, applied in the direction of chemical instruments and methods, metal/metal oxide/metal hydroxide catalyst, physical/chemical process catalyst, etc., can solve the problems affecting the appearance, strength and final catalyst High specific surface area, increased catalyst wear and other issues, to achieve the effect of improving hydrogen absorption and dehydrogenation capacity and speed, reducing catalyst wear, and increasing catalyst strength

Active Publication Date: 2016-10-26
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the catalyst does not impose any restrictions on the particle size during the co-precipitation process at the beginning of the formation of the active phase. If large crystal particles are formed at this step, it will be difficult to obtain a high ratio of the final catalyst in subsequent steps. Surface area, even if the metal is evenly distributed, some metals wrapped in large particles will not be able to fully play their role and become ineffective components, reducing the utilization rate of metals
At the same time, due to the high metal content, the material has poor cohesiveness, which will affect the appearance and strength of the extruded product, and increase the wear and tear of the catalyst during use.
In addition, bulk catalysts with high metal content require greater power consumption during the extruding process, causing great wear and tear on machinery.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

preparation example Construction

[0018] The invention provides the preparation method of catalyst composition, a kind of specific preparation process is as follows:

[0019] (1) Preparation of W and Ni composite oxide precursors by co-precipitation method

[0020] Prepare a salt solution containing W and Ni according to the ratio of the catalyst components. The nickel-containing salt can be one or more of nickel sulfate, nickel nitrate, nickel chloride, basic nickel carbonate, nickel oxalate, etc., and the tungsten-containing salt It can be one or more of ammonium metatungstate, sodium tungstate, etc., and additives such as Si, P, Ti, B, Zr, Mg, etc. can be introduced into the mixed solution according to the catalyst requirements, preferably Si and / or P, silicon can be one or more of water glass, silica sol, etc., phosphorus can be one or more of phosphoric acid, phosphorous acid, ammonium phosphate, ammonium hydrogen phosphate, ammonium dihydrogen phosphate, etc.

[0021] Add an appropriate amount of clean ...

Embodiment 1

[0027] Add 500ml of clean water into a container A, add 48g of ammonium metatungstate, 32g of nickel chloride, and 3.5g of ammonium dihydrogen phosphate into it and stir to dissolve;

[0028] Add 300ml of clean water into a container B, add 57g of aluminum chloride into it and stir to dissolve;

[0029] Prepare the concentration in a container C with SiO 2 (weight) 100ml of 2.2% dilute water glass solution;

[0030] Add 500ml of clean water into the reaction tank, add 2g of polyethylene glycol with a molecular weight of 6000, stir and heat up to 50°C;

[0031] Add the aluminum chloride solution in container B to container A under stirring, then drop the dilute water glass solution in container C into container A under stirring, adjust the total volume of the solution to 1000ml with clean water, Get metal W, Ni and Al 2 o 3 ,P 2 o 5 , SiO 2 Saline solutions of precursors;

[0032] Add the above-prepared salt solution and 15wt% ammonia solution into the reaction tank in ...

Embodiment 2

[0037] The whole preparation process of the catalyst was the same as that in Example 1, wherein 2 g of polyethylene glycol with a molecular weight of 6000 was added to the clean water of the reaction tank during the catalyst preparation process, and the gelling temperature was 50°C. The salt solution was prepared by adding 47g of ammonium metatungstate, 29g of nickel chloride, and 80g of aluminum chloride, without adding ammonium dihydrogen phosphate and dilute water glass solution, and adding 16.2g of molybdenum trioxide to obtain the catalyst composition B of the present invention.

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PUM

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Abstract

The invention discloses a preparation method of a hydrogenation catalyst composition. The preparation method is as follows: using a coprecipitation method for preparation of a W and Ni composite oxide precursor, adding high molecular polyethylene glycol before coprecipitation and / or in the precipitation process, then beating and mixing with MoO3, filtering, forming, washing, drying and roasting to obtain the hydrogenation catalyst composition. According to the method, at the beginning of the formation of a particulate matter, the aggregation growth of the W and Ni composite oxide precursor can be controlled, a catalyst precursor with smaller particle and larger superficial area can be obtained, the catalyst hydrogenation performance can be improved, the catalyst strength is increased, abrasion is reduced, and the catalyst use performance is improved.

Description

technical field [0001] The invention relates to a preparation method of a hydrogenation catalyst composition, in particular to a preparation method of a diesel ultra-deep hydrodesulfurization catalyst composition. Background technique [0002] The SOx, NOx, CH and soot emitted during the combustion process of sulfur, nitrogen and aromatics in diesel can lead to the formation of acid rain, photochemical smog, carcinogens, etc., causing serious pollution to the environment and serious harm to the health of residents. Based on this, governments of various countries are paying more and more attention to air cleanliness, and have stricter requirements on vehicle diesel specifications. In the future, clean diesel specifications are developing towards the direction of no sulfur, low aromatics, low density, and high cetane number. [0003] Most of the raw materials for diesel hydrotreating are straight diesel, coke diesel, and catalyzed diesel, or a mixture of two or more of them. ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J27/19B01J23/888C10G45/08
Inventor 刘东香王海涛徐学军王继锋冯小萍
Owner CHINA PETROLEUM & CHEM CORP