Method for preparing hydrogenation catalyst

A hydrogenation treatment and catalyst technology, applied in the direction of catalyst activation/preparation, physical/chemical process catalysts, chemical instruments and methods, etc., can solve the problems of atomic ratio mismatch, reduced catalyst activity, metal loss, etc., and achieve simple preparation process , Avoid metal loss, low production cost

Active Publication Date: 2006-05-10
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] Co-precipitation catalyst preparation process is complex, both require an independent precipitation process, the pH value of the two solutions needs to be adjusted before the co-precipitation process, the pH value also needs to be adjusted during the co-precipitation process, and mother liquor separation and washing processes are required, which inevitably leads to The loss of metal leads to an increase in catalyst manufacturing cost. In addition, adjusting the co-precipitation process will lead to a serious mismatch in the atomic ratio of molybdenum (and / or tungsten) to nickel (and / or cobalt) (it is generally considered that cobalt or / and nickel in hydrotreating catalysts and cobalt or / and nickel+molybdenum or / tungsten atomic ratio between 0.2 and 0.4), which reduces the activity of the catalyst, and at the same time makes a large amount of metals not well utilized

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0029] The method of the invention prepares the catalyst.

[0030] (1) According to Chinese patent 96109048, a high-concentration molybdenum-nickel solution is prepared, and the solution contains

[0031] MoO 3 70g / 100mL, NiO18g / 100mL, P2.55g / 100mL.

[0032] (2) Take 60mL of the solution obtained in step 1, add 32g of ammonium metatungstate (containing WO 3 85%), fully dissolved.

[0033] (3) 16.5g (dry basis) of SB-alumina powder (produced in Germany) was fully mixed with the solution obtained in step 2, and extruded into a catalyst precursor.

[0034] (4) Dry the catalyst precursor obtained in step 3 at 120° C. in air for 4 hours.

[0035] (5) Treat the catalyst dry strip obtained in step 4 under the catalyst at 350° C. for 1 hour.

[0036]The prepared catalyst is denoted as catA. The catalyst contains 10.8w% NiO, 42.0w% MoO 3 and 27.2w% WO 3 , 3.5w%P 2 o 5 .

Embodiment 2

[0038] The method of the invention prepares the catalyst.

[0039] (1) Prepare high-concentration molybdenum-nickel solution according to Chinese patent 96109048, which contains MoO 3 60g / 100mL, NiO12g / 100mL, P2g / 100mL.

[0040] (2) Fully mix 15g (dry basis) of SB-alumina powder (produced in Germany) with 110mL of the solution obtained in step 2.

[0041] (3) The mixture obtained in step 4 was dried at 80° C. to 40% on a dry basis, and extruded into a catalyst precursor.

[0042] (4) With embodiment 1 step 4.

[0043] (5) With embodiment 1 step 5.

[0044] The prepared catalyst is denoted as catB. The catalyst contains 13.2w% NiO, 66.0w% MoO 3 and 5.0w%P 2 o 5 .

Embodiment 3

[0046] The method of the invention prepares the catalyst.

[0047] (1) Take 100mL of clean water, add ammonium metatungstate (containing WO 3 85%) 44.7g, nickel nitrate 37.5g, fully dissolved, adding molybdenum oxide 30g. The volume of the final suspension was 120 mL.

[0048] (2) Fully mix 20g (dry basis) of SB-alumina powder (produced in Germany) with the suspension obtained in step 2.

[0049] (3) The mixture obtained in step 2 was dried at 80° C. to 40% on a dry basis, and extruded into a catalyst precursor.

[0050] (4) With embodiment 1 step 4.

[0051] (5) with embodiment 1 step 5.

[0052] The prepared catalyst is denoted as catC. The catalyst contains 12.0w% NiO, 30.0w% MoO 3 and 38.0w% WO 3 .

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Abstract

The invention discloses a method for preparing the hydrogenation treatment catalyst, especially for preparing the hydrogenation treatment catalyst with high metal content. First, preparing high-density metallic salt solution or suspending solution; adding prepared metallic salt solution or suspending solution into adhesive agent and other additives, to be mixed uniformly, molded, dried, and sintered to attain the catalyst, whose metallic oxide is in 50-95 wt%. Compared to present technique, said invention has simple processes and lower producing cost without metal leakage. The invention can be used to prepare hydrogenation treatment catalyst with high metal content and excellent property.

Description

technical field [0001] The invention relates to a preparation method of a hydrogenation treatment catalyst, especially a preparation method of a hydrogenation treatment catalyst with high metal content. Background technique [0002] Crude oil and distillates derived from crude oil contain impurities such as sulfur, nitrogen, oxygen and metals. The existence of these impurities not only affects the stability of the oil, but also emits SO during use. x , NO x and other harmful gases pollute the environment. During the secondary processing of oil products, the presence of impurities such as sulfur, nitrogen, oxygen and metals can poison catalysts. Distillate oil hydrotreating refers to the process of contacting raw oil and hydrogen with a catalyst at a certain temperature and pressure to remove impurities and saturate aromatics. [0003] A hydrotreating catalyst with excellent performance must have excellent hydrogenation activity and certain cracking activity. In addition,...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J37/00B01J23/84C10G45/08
Inventor 彭绍忠王刚魏登凌姜虹
Owner CHINA PETROLEUM & CHEM CORP
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