Preparation method of boron-containing hydrogenation and demetalization catalyst

A technology for hydrodemetallization and catalyst, which can be used in metal/metal oxide/metal hydroxide catalysts, chemical instruments and methods, physical/chemical process catalysts, etc., and can solve the problems of low utilization rate of macropores

Active Publication Date: 2016-11-23
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] The active metal components of the residual oil hydrodemetallization catalyst prepared by the above method are relatively uniformly distributed in the macropores and small pores of the carrier, resulting in a low utilization rate of the macropores

Method used

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  • Preparation method of boron-containing hydrogenation and demetalization catalyst
  • Preparation method of boron-containing hydrogenation and demetalization catalyst
  • Preparation method of boron-containing hydrogenation and demetalization catalyst

Examples

Experimental program
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Effect test

Embodiment 1

[0034]Take 55g of industrial ammonium heptamolybdate, put it in ammonia water, stir until there is no insoluble matter, then add 25g of industrial basic nickel carbonate, stir until there is no insoluble matter, and make MoO 3 10 g / 100 ml, NiO1.2 g / 100 ml molybdenum-nickel-ammonia active metal salt solution. The immersion solution with different concentrations can be prepared by adjusting the addition amount of ammonium heptamolybdate and basic nickel carbonate according to the needs.

[0035] Weigh the carbon black powder I11.4 with a particle size of 800 mesh (the particles can pass through the 800 mesh sieve but not the 1000 mesh sieve) and put it in the spray rolling pot. The carbon black powder in the spray dipping contains molybdenum oxide 0.6 gram, the active metal impregnating solution 3.4ml of nickel oxide 0.4 gram, then continue to spray distilled water and make carbon black powder adsorption saturation, the carbon black powder after impregnating is dried 3 hours in ...

Embodiment 2

[0041] With embodiment 1, just carbon black powder I weight is 14.3 grams, and particle diameter is 600 orders (particle can pass through 600 mesh sieves but cannot pass through 800 mesh sieves), contains molybdenum oxide 0.8 gram, nickel oxide in the active component I 0.5 grams, the active ingredient impregnating liquid dosage is 7.2ml. Boron-containing solution I contains 0.6 grams of boron oxide, the amount of boric acid solution is 7.2 ml, the weight of carbon black powder II is 5.7 grams, and the particle size is 400 mesh (the particles can pass through the 400-mesh sieve but not the 500-mesh sieve), Active component II contains 0.6 g of molybdenum oxide and 0.2 g of nickel oxide, and the amount of active component impregnating solution is 1.2 ml. The boron-containing solution II contains 0.2 grams of boron oxide, the amount of boric acid solution is 1.7 ml, and the content of urea in the solution is 7.5 grams. The add-on of polyethylene glycol solution is 43 grams, and...

Embodiment 3

[0043] With embodiment 1, just carbon black powder I weight is 7.2 grams, and particle diameter is 1000 orders (particle can pass through 1000 mesh sieve holes but cannot pass through 1340 mesh sieve holes), contains molybdenum oxide 0.7 gram, nickel oxide in the active component I 0.3 grams, the active ingredient impregnating liquid dosage is 2.9ml. Boron-containing solution I contains 0.4 grams of boron oxide, the amount of boric acid solution is 2.9 ml, the weight of carbon black powder II is 7.2 grams, and the particle size is 500 mesh (the particles can pass through the 500-mesh sieve but not the 600-mesh sieve), The active component II contains 0.4 grams of molybdenum oxide and 0.3 grams of nickel oxide, and the amount of active component impregnation solution is 2.9 ml. Boron-containing solution II contains 0.3 grams of boron oxide, the amount of boric acid solution is 2.9 ml, and the content of urea in the solution is 11.5 grams. The addition amount of polyethylene gl...

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Abstract

The invention discloses a preparation method of a boron-containing hydrogenation and demetalization catalyst. The preparation method comprises steps as follows: (1) hydrogenation active components, namely, an impregnation liquid I and a boron-containing solution I are used for impregnating a physical pore expanding agent I respectively, hydrogenation active components, namely, an impregnation liquid II and a boron-containing solution II are used for impregnating a physical pore expanding agent II respectively, and the impregnated physical pore expanding agent I and the impregnated physical pore expanding agent II are dried and soaked with a urea solution respectively for standby use; (2) the physical pore expanding agent I and the physical pore expanding agent I obtained in the step (1) are mixed with pseudo-boehmite dry gelatine powder, a chemical pore expanding agent, an extrusion aid and a peptizing agent, the mixture is kneaded to form a plastic body, the plastic body is extruded to form strips, formed products are put in a sealing device for heat treatment, a treated material is dried and calcined, and a modified alumina support is prepared; (3) a hydrogenation active component, namely, an impregnation liquid III is used for impregnating the modified alumina support, the catalyst is dried and calcined after impregnation, and the boron-containing hydrogenation and demetalization catalyst is prepared. According to the catalyst prepared with the method, the content of active metal is relatively high at large pores and relatively low at small pores, the utilization rate of the large pores is remarkably increased, and the hydrogenation and demetalization catalyst has high activity and long-period operation stability.

Description

technical field [0001] The invention relates to a preparation method of a boron-containing hydrogenation demetallization catalyst. Background technique [0002] With the increasing requirements for deep processing of raw materials worldwide, the main energy structure is gradually developing in the direction of macromolecules and high carbon, especially for my country where crude oil is generally heavy. In order to effectively solve the problems of excessive diffusion resistance of heavy oil components in the catalyst pores, heavy metal impurity deposition and coking caused by catalyst activity decline or deactivation, it is urgently required that the alumina carrier widely used in the petrochemical industry has a large pore volume and The characteristic of large aperture. The large pore size is conducive to the diffusion of macromolecular compounds into the catalyst particles, and the large pore volume is conducive to improving the ability to accommodate metals or coke. ...

Claims

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Application Information

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IPC IPC(8): B01J21/04B01J23/88B01J23/883C10G45/08
Inventor 季洪海王少军凌凤香沈智奇杨卫亚郭长友王丽华
Owner CHINA PETROLEUM & CHEM CORP
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