Hydrofining catalyst

A hydrofining and catalyst technology, applied in the direction of catalyst activation/preparation, physical/chemical process catalyst, metal/metal oxide/metal hydroxide catalyst, etc. High hydrogen loss rate, large catalyst loss and other problems, to achieve the effect of excellent anti-coking performance, good hydrogenation activity and long running time

Active Publication Date: 2011-08-31
PETROCHINA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In the process of preparing catalysts containing cobalt and molybdenum by impregnation, the main problem is that the active components Co and Mo are difficult to dissolve, especially when dissolving two active components in one solvent at the same time.
However, the step-by-step impregnation method to prepare the catalyst will cause an increase in the cost of catalyst preparation.
The catalyst is prepared by a one-step impregnation method. The problem in the prior art is that it is necessary to add an organic acid/base to promote the dissolution of the active component. Controlling, prone to overheating phenomenon, and a large amount of gas will be released, and the loss of catalyst is also large
[0012] (1) The dispersion of the active metal components on the catalyst is not good, and there are too strong active centers, resulting in a high loss rate in the hydrogenation of aromatics, especially the hydrogenation of benzene;
[0013] (2) There are a certain number of B acid sites on the catalyst, and there are more strong L acid sites in the L acid, which makes the catalyst easy to coke at high temperature, increases the pressure drop of the bed, affects the circulation of h

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0051] At 30°C, add 14.21g of cobalt acetate to a mixed solution of 60ml of ammonia water and 5ml of ethylenediamine, stir to dissolve, then add 31.97g of ammonium molybdate and 9.32g of nickel nitrate and stir to dissolve, then add 3.49g of potassium hydroxide , add ammonia to adjust the volume of the solution to 80ml, impregnated in 100g of γ-Al 2 o 3 On the carrier, aged for 12 hours, dried at 120°C for 4 hours, and calcined at 580°C for 4 hours to obtain catalyst A.

Embodiment 2

[0053] At 25°C, add 28.01g of cobalt acetate to a mixed solution of 50ml of ammonia water and 7ml of ethylenediamine, stir to dissolve, then add 14.21g of ammonium molybdate and 18.8g of ammonium metatungstate and stir to dissolve, then add lithium hydroxide 2.38g, add ammonia water to adjust the solution volume to 100ml, impregnate in 100g of α-Al 2 o 3 On the carrier, aged for 12 hours, dried at 100°C for 5 hours, and calcined at 350°C for 5 hours to obtain catalyst B.

Embodiment 3

[0055] At 20°C, add 7.1g of cobalt nitrate to a mixed solution of 55ml of ammonia water and 6ml of EDTA, stir to dissolve, then add 42.67g of ammonium molybdate, 7.8g of nickel acetate, and 6.60g of strontium nitrate, stir and dissolve, then add 6.84g of lithium carbonate , adding ammonia water to adjust the volume of the solution to 110ml, impregnated in 100g of modified γ-Al 2 o 3 on the carrier, aged for 12 hours, dried at 200°C for 4 hours, and calcined at 400°C for 3.5 hours to obtain catalyst C.

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Abstract

The invention relates to a hydrofining catalyst which is obtained by adding a carrier into a dipping liquid for aging and drying after dipping, and then activating. The catalyst, containing the carrier, molybdenum and cobalt, is characterized by containing molybdenum oxide 5-25%, cobalt oxide 1-6%, tungstic oxide 0-15%, nickel oxide 0-4%, and alkali metal oxides 0-4.5%, by the catalyst weight of 100%. Besides, the catalyst pore volume is 0.30-0.85ml/g, and the specific surface area is 110-380 m <2>/g. Compound solvent in the catalyst preparation contains ammonia water and polyamine complexingagent at the same time. The catalyst of the invention while undergoing hydrodesulfurization, saturates monoolefine to the maximum through hydrogenation, to be able to meet the requirements of an oil product with changeable sulfur and diene contents and high air speed running. Catalyst has good hydrogenation activity, high selectivity, long running time and superior anti coking performance.

Description

technical field [0001] The invention relates to a hydrorefining catalyst, which is suitable for hydrorefining of middle and low distillate oil. Background technique [0002] At present, there are many reports on hydrotreating catalysts whose active components are Ni-Mo, Co-Mo, Ni-W, Co-W, Co-Mo-Ni, W-Mo-Ni and their preparation methods. In the process of preparing catalysts containing cobalt and molybdenum by impregnation, the main problem is that the active components Co and Mo are difficult to dissolve, especially the simultaneous dissolution of two active components in one solvent. However, the step-by-step impregnation method to prepare the catalyst will increase the cost of catalyst preparation. The catalyst is prepared by a one-step impregnation method. The problem in the prior art is that it is necessary to add an organic acid / base to promote the dissolution of the active component. Controlling, it is easy to produce overheating phenomenon, and it will release a lar...

Claims

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Application Information

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IPC IPC(8): B01J23/888C10G49/04C10G45/08
CPCB01J23/8885B01J37/0203B01J37/08B01J35/1038B01J35/002B01J37/0201C10G45/08B01J23/8872C07B31/00B01J35/1042B01J35/1019B01J23/883B01J23/882B01J37/20C10G2300/202
Inventor 梁顺琴吴杰吕龙刚秦鹏康宏敏常晓昕钱颖孙利民王宗宝陈跟平蒋彩兰郑云弟马好文
Owner PETROCHINA CO LTD
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