Preparation method of hydrodesulfurization catalyst

A hydrodesulfurization and catalyst technology, applied in chemical instruments and methods, physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, etc., can solve the limitation of active metal loading, increase processing costs, Issues such as conditions that cannot be controlled

Active Publication Date: 2016-05-18
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although high-metal W-Mo-Ni hydrogenation catalysts have good hydrogenation performance and can achieve the purpose of ultra-deep desulfurization, in the process of diesel hydrodesulfurization, highly reactive sulfides and unsubstituted bis Part of the benzothiophene sulfides will also be desulfurized through the hydrogenation route, which consumes too much hydrogen and increases the processing cost. At the same time, the excessively high total metal amount also increases the investment cost of the catalyst.
[0011] Most of the currently disclosed bulk catalysts do not impose any restrictions on the size of the particles 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 make them in subsequent steps. The final catalyst has a high specific 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 the metal.
[0012] CN101089132A discloses a hydrodesulfurization catalyst of four active metal components of W-Mo-Ni-Co, although a specific ratio of W-Mo-Ni-Co-P active components is used to make the Co-Mo type The hydrolysis desulfurization performance and the good hydrodesulfurization performance of the W-Ni type have been comprehensively utilized, but the loading of its active components is achieved by saturated co-impregnation technology, and the loading amount of active metals is limited, so it is impossible to provide more The total amount of active metals is more; at the same time, the active component W-Mo-Ni-Co-P cannot control the conditions for the formation of the hydrogenation active phase and the hydrogenolysis active phase precursor during a dry roasting process, so that the catalyst's hydrogenation and Hydrolysis desulfurization activity does not work well together
Adding phosphorus to the impregnation solution can adjust the surface properties of the carrier and improve the interaction between the carrier and the active metal, but during the impregnation process, the interaction between phosphorus and the surface groups of the carrier will weaken the adsorption of active components on the carrier. , so that the active components are prone to agglomeration, reducing the dispersion of the active components in the catalyst, thereby reducing the catalyst activity

Method used

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Examples

Experimental program
Comparison scheme
Effect test

preparation example Construction

[0024] The invention provides the preparation method of catalyst, a kind of specific preparation process is as follows:

[0025] (1) Preparation of W, Ni, Al, Mg composite oxide precursors by co-precipitation method

[0026] Prepare a salt solution containing W, Ni, Al, and Mg 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. , the tungsten-containing salt can be one or more of ammonium metatungstate, sodium tungstate, etc., the aluminum-containing salt can be one or more of aluminum chloride, aluminum nitrate, aluminum sulfate, etc., and the magnesium-containing salt can be It is one or more of soluble magnesium salts such as magnesium chloride, magnesium nitrate, etc., and additives such as Si, P, Ti, B, Zr, etc. can be introduced into the mixed solution according to the catalyst requirements, preferably Si and / or P, silicon source ...

Embodiment 1

[0038] Add 500ml of clean water into a container A, add 47g of ammonium metatungstate, 34g of nickel chloride, 9.5g of magnesium chloride, and 2.5g of ammonium dihydrogen phosphate into it and stir evenly.

[0039] Add 300ml of clean water into a container B, add 47g of aluminum chloride into it and stir to dissolve.

[0040] Prepare the concentration in a container C with SiO 2 (weight) 100ml of 2.2wt% dilute water glass solution.

[0041] 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 , MgO, P 2 o 5 , SiO 2 Precursor saline solution.

[0042] Add 500ml of clean water into the reaction tank, stir and heat up to 50°C with 2g of polyethylene glycol with a molecular weight of 6000.

[0043] Combine the salt solution prepared above and 15wt% ammonia solut...

Embodiment 2

[0047] The entire preparation process of the catalyst is the same as in Example 1, wherein during the preparation of the catalyst precursor strips, 2 g of polyethylene glycol with a molecular weight of 4000 is added to the clean water of the reaction tank, and the salt solution is prepared by adding 40 g of ammonium metatungstate and 28 g of nickel chloride , Aluminum Chloride 85g, Magnesium Chloride 7.3g, do not add ammonium dihydrogen phosphate and dilute water glass solution, impregnating liquid preparation adds basic cobalt carbonate 19g, ammonium molybdate 77g, citric acid 22g, obtains catalyst B of the present invention.

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Abstract

The invention discloses a preparation method of a hydrodesulfurization catalyst. The preparation method of the hydrodesulfurization catalyst is as follows: using a coprecipitation method for preparation of a W, Ni, Al and Mg composite oxide precursor, introducing high molecular polyethylene glycol in the precipitation process, forming, washing, drying and roasting to obtain a catalyst intermediate, using a specific Co and Mo-containing impregnation liquid for impregnation, drying and roasting to obtain the hydrodesulfurization catalyst. The prepared catalyst is smaller in particle and larger in surface area, and enables an active metal to form a hybrid active center with excellently-matched hydrogenation performance and hydrogenolysis performance in the premise of uniform dispersion of the active metal, so that the hydrogenation and hydrogenolysis desulfurization effects of the catalyst active component can be better cooperatively played, ultra-deep desulfurization can be achieved, meanwhile no excess hydrogen consumption is produced, and the processing cost is reduced.

Description

technical field [0001] The invention relates to a method for preparing a hydrodesulfurization catalyst, in particular to a method for preparing a diesel ultra-deep hydrodesulfurization catalyst. Background technique [0002] The trend of high-sulfur crude oil caused by heavy and inferior crude oil is further expanding. According to reports, currently the world's low-sulfur crude oil accounts for only 17wt%, and high-sulfur crude oil with sulfur content > 2wt% is as high as 58wt%. [0003] 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...

Claims

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Application Information

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