Phosphorus-and potassium-containing aluminum oxide carrier and preparation method thereof

A technology of alumina carrier and phospho-alumina, applied in catalyst carrier, chemical instrument and method, catalyst activation/preparation, etc., can solve the problems of underutilized pore function, small pore size, etc. Large, increase the effect of deposition

Active Publication Date: 2010-11-24
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0008] CN1123309A discloses a preparation method of a residual oil demetallization catalyst. The selected alumina carrier has a pore volume of 0.45-0.8ml / g, and the edge of the catalyst is passivated by potassium, but this catalyst does not have fully utilized pore channels
[0009] CN1123196A discloses a preparation method of residual oil demetallization catalyst, which uses potassium dihydrogen phosphate to prevent potassium loss, but this invention also has the disadvantage of too small pores

Method used

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  • Phosphorus-and potassium-containing aluminum oxide carrier and preparation method thereof
  • Phosphorus-and potassium-containing aluminum oxide carrier and preparation method thereof

Examples

Experimental program
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Effect test

Embodiment 1

[0044] Under stirring conditions, 375g of aluminum nitrate nonahydrate and 90g of urea are mixed and heated to 100°C, and added to a mixture of 32g of polyisobutylene maleate triethanolamine and 88g of 150 HVI neutral oil at the same temperature to form a super solubilizing agent Then, react at 100°C for 3 hours to obtain nano aluminum hydroxide gel. Wash three times with 200ml distilled water, and dry at 120°C for 10 hours. Mix 70g of dry nano-aluminum hydroxide gel powder with 30g pseudo-boehmite as a binder; mix 2.6g of dilute nitric acid (mass concentration 17%), 18g of water and 1g of cosolvent ethanol, and mix the two mixtures. Make it uniform, then shape it in the extruder, and control the pressure at 10MPa. The molded product was dried at a temperature of 100°C for 10 hours, calcined at a temperature of 240°C for 3 hours, and calcined at a temperature of 850°C for 4 hours, wherein the temperature increase rate was 5°C / min to obtain an alumina carrier A1. 4ml contains ...

Embodiment 2

[0046] Mix 90g minus three-line dewaxing oil and 70g SP-80, heat at 80°C to dissolve and mix uniformly; heat 620g nonahydrate aluminum nitrate to 80°C to melt, slowly add to the above mixture, and mix for 20 minutes to form a uniform super solubilized body. 220 g of saturated ammonia water at 20°C was added dropwise and aged for 3 hours to obtain nano aluminum hydroxide gel. Wash three times with 200ml distilled water, and dry at 120°C for 10 hours. Mix 70g of dry nano-aluminum hydroxide gel powder with 30g of pseudo-boehmite as a binder; mix 2g of dilute nitric acid (mass concentration 17%), 25g of water and 3g of co-solvent ethanol and add them to the above mixture. Forming in the extruder, the control pressure is 23MPa. The molded product was dried at a temperature of 100°C for 10 hours, calcined at a temperature of 240°C for 3 hours, and calcined at a temperature of 850°C for 4 hours, wherein the temperature increase rate was 5°C / min, to obtain the alumina carrier A2 of th...

Embodiment 3

[0048] Mix 20g minus fourth-line oil, 30g minus first-line oil, 25g minus second-line wax paste, 15g SP-80, heat at 100℃ to dissolve, and mix well; heat 800g aluminum nitrate nonahydrate to 100℃ to melt, slowly add to the above mixture, mix A uniform super solubilizing body is formed in 30 minutes. In a closed reactor, 110 g of liquid ammonia at 50°C was added to the super sol-enhancing body and reacted at 180°C for 2 hours to obtain nano aluminum hydroxide gel. Wash three times with 200ml distilled water, and dry at 120°C for 10 hours. The subsequent steps and conditions were the same as those in Example 3 to obtain alumina carrier A3. A solution of 0.1g phosphoric acid and 0.1g potassium nitrate was sprayed on the above 100g A3 carrier in an atomized manner, dried at 100°C for 3 hours, and calcined at 550°C for 4 hours to obtain the potassium and phosphorus-containing alumina carrier of the present invention KA3.

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Abstract

The invention discloses a phosphorus- and potassium-containing aluminum oxide carrier and a preparation method thereof. The aluminum oxide carrier is prepared by molding an aluminum oxide carrier by using aluminum hydroxide gel, which is prepared by a molten-salt super-solubility micelle method, as a raw material at first and then loading potassium and phosphorus on the aluminum dioxide carrier in a spraying and soaking mode. In a process of preparing the carrier, the aluminum hydroxide gel has a surfactant and hydrocarbon components, so that after the aluminum hydroxide gel is molded and roasted, aluminum oxide nanoparticles formed by dewatering the polymerized aluminum oxide still have a rod-like basic structure; the aluminum oxide nanoparticles are stacked into a framework structure in a disordered way, so that the carrier has a large pore volume, a large aperture, a high porosity, a large outer surface orifice and high duct penetrability; and after the surface acidity of the carrier is reduced by the potassium and the phosphorus, the surface activity of a catalyst is reduced, so that asphaltene micelles tend to disperse into the inner part of the carrier to undergo a reaction. Thus, a hydrocracking reaction is restrained, the generation of carbon deposit is prevented, a residual hydrodemetalization reaction is carried out smoothly, and the capability of dissolving metals is improved.

Description

Technical field [0001] The invention relates to an alumina carrier containing phosphorus and potassium and a preparation method thereof, in particular to an alumina carrier used for a residue demetalization catalyst and a preparation method thereof. Background technique [0002] At present, hydroprocessing is still the most important means of producing high-quality and environmentally friendly petroleum products. The core of the hydroprocessing technology is the catalyst, and the performance of the carrier is the key to preparing a hydroprocessing catalyst with excellent properties. For the heavy components of petroleum (such as VGO, especially residual oil), the pore size and pore volume of the carrier will directly affect the activity of the catalyst. [0003] So far, the catalyst carrier used in the residue fixed bed is still the classic alumina carrier. High-temperature roasting method, pH swing method and water vapor treatment can all obtain macroporous alumina suitable for ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J27/14B01J32/00B01J21/04B01J35/10B01J37/00C10G45/04
Inventor 王鼎聪刘纪端
Owner CHINA PETROLEUM & CHEM CORP
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