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Process for preparing hydrogenating refining catalyst by waste hydrogenating refining catalyst

A hydrogenation catalyst and hydrogenation refining technology, applied in the direction of catalyst activation/preparation, catalyst regeneration/reactivation, chemical instruments and methods, etc., can solve the problems of metal environmental pollution, excessive interaction, waste of resources, etc., and achieve improvement Pore ​​structure, easy operation, and the effect of improving activity

Inactive Publication Date: 2006-12-20
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Refineries generally choose to discard these spent catalysts or use them as fillers in construction and other industries, but there are two problems: 1. Because the hydrorefining catalyst generally contains molybdenum, tungsten, and cobalt in a total amount of about 20wt% to 40wt%. , nickel and other valuable metal oxides, such treatment will cause waste of resources
2. The discarded catalyst will pollute the environment due to the loss of the above metals, especially water resources
The main reasons for these catalysts being discarded are: 1. The pore structure and acid properties of the catalyst itself are different from those of fresh catalysts
2. Due to the accumulation of metals during long-term operation and regeneration, the migration of surface metals to the interior of the catalyst, and the strong interaction between metals and supports, some metals, especially the metals on the surface of the catalyst, lose their activity or fail to exert their activity.
3. Excessive deposition of impurities on the catalyst
But this only solves the problem of how to improve the pore structure and acid properties of the catalyst, and does not involve how to supplement the active metal components on the catalyst

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0032] Take a waste W-Ni / Al with a particle size of about 250 mesh 2 o 3 Hydrodesulfurization catalyst powder (containing 27.86wt% WO 3 , 2.39wt% NiO, 6.61wt% C, 6.01wt% S, 0.06wt% Fe, the remainder being Al 2 o 3 ) 20.0g, adding 0.9g WO with a particle size of 250 mesh 3 and 1.6g titania-alumina (the specific surface area is 241m 2 / g, the pore volume is 0.60cm 3 / g, the average pore diameter is 9.0nm, containing 5.32wt% of titanium dioxide) and mixed, adding 4.5g of adhesive to shape. Then regenerate the catalyst under the following conditions: put the catalyst into the regeneration device, first replace the device with nitrogen, then adjust the oxygen content to 2.50v%, then start to heat up, keep the temperature at 120°C for 2 hours, and at 200°C 2h, constant temperature at 290°C for 1.5h, constant temperature at 490°C for 3h. The number of the obtained regenerated catalyst is A.

Embodiment 2

[0034] Get the waste W-Ni / Al used in embodiment 1 2 o 3 Hydrodesulfurization catalyst powder 20.0g, soak with 40ml, 2.25wt% cobalt nitrate solution, add 1.8g alumina monohydrate after drying at 120 ℃ (after roasting, the specific surface area can be 282m 2 / g, the pore volume is 0.63cm 3 / g, γ-alumina with an average pore size of 9.0nm) and ground to 250 mesh, adding 4.5g of binder to shape. The catalyst was then regenerated under the same conditions as in Example 1. The obtained catalyst was numbered B.

Embodiment 3

[0036] Get the waste W-Ni / Al used in embodiment 1 2 o 3 Hydrodesulfurization catalyst powder 20.0g, mixed with 0.4gMoO 3 , 0.4gWO 3 And 0.1gCoO and 0.8g silica / alumina (specific surface area is 272m 2 / g, the pore volume is 0.62cm 3 / g, the average pore diameter is 9.1nm, containing silicon dioxide 1.25wt%) and 0.8g diboron trioxide-alumina (specific surface area is 234m 2 / g, the pore volume is 0.63cm 3 / g, with an average pore diameter of 10.8nm, containing 5.05wt% boron trioxide) and mixing, adding 4.5g of adhesive to form. The catalyst was then regenerated under the same conditions as in Example 1. The number of the obtained catalyst is C.

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PUM

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Abstract

The invention relates to a method of preparing hydrofining catalyst by waste hydrofining catalyst. It adds an active metal component and an alumina-containing substance to the waste hydrofining catalyst powder, and then regenerates. It can improve the activity of catalyst to make the catalyst able to be continued using, thus achieving the purpose of saving resources. As the active metal and the alumina-containing substance are added in a metal salt form and in a hydrated alumina form, respectively, it will absorb the heat by the decomposition of the metal salts and the hydrated alumina in the process of catalyst regeneration to control the heat release of the waste catalyst as regenerating, preventing the catalyst from burning to influence the performance of catalyst. In addition, in the regenerating process, the generated gas as these metal salts decomposed is helpful to improve the pore canal structure of catalyst.

Description

technical field [0001] The invention relates to a method for preparing a hydrorefining catalyst, in particular to a method for preparing a hydrorefining catalyst from a waste hydrorefining catalyst whose reaction performance cannot meet the requirements of the reaction process. Background technique [0002] Every year, a large amount of spent hydrorefining catalysts that cannot be regenerated are produced all over the world. Refineries generally choose to discard these spent catalysts or use them as fillers in construction and other industries, but there are two problems: 1. Because the hydrorefining catalyst generally contains molybdenum, tungsten, and cobalt in a total amount of about 20wt% to 40wt%. , nickel and other valuable metal oxides, such treatment will cause waste of resources. 2. The discarded catalyst will pollute the environment, especially water resources, due to the loss of the above metals. In view of this, many countries now prohibit the random discarding...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J38/00B01J37/00C10G45/04
Inventor 张喜文凌凤香孙万富赵长志王少军
Owner CHINA PETROLEUM & CHEM CORP