Preparation method of propylene catalytic cracking catalyst with yield increased

A catalytic cracking and catalyst technology, applied in catalytic cracking, carbon compound catalysts, physical/chemical process catalysts, etc., can solve the problems of increasing oil slurry yield, decreasing gasoline yield, and low specific surface area, so as to increase the yield of propylene , the effect of reducing hydrogen transfer activity

Active Publication Date: 2016-12-07
QINGDAO HUICHENG PETROCHEM TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] The catalysts for increasing production of propylene disclosed in the prior art, one is to improve the conversion of light olefins through ZSM-5 metal modification, but at the same time, the yield of gasoline is significantly reduced, and the yield of oil slurry will be increased after the addition ratio is too high
In addition, the use of phosphor-aluminum glue and silica sol as a binder only considers its bonding performance, and its specific surface area is relatively low.

Method used

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  • Preparation method of propylene catalytic cracking catalyst with yield increased
  • Preparation method of propylene catalytic cracking catalyst with yield increased
  • Preparation method of propylene catalytic cracking catalyst with yield increased

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0047] (1) 11.41 kg of ZSM-5 molecular sieve (silicon-aluminum ratio 25, dry basis content 92%) was mixed with 37.72 kg of deionized water, 11.53 kg of kaolin, and 11.03 kg of pseudo-boehmite, and stirred for 3 hours.

[0048] (2) Add 1.18 kg of 35 wt% hydrochloric acid to the slurry in (1), and stir for 45 minutes.

[0049] (3) Add 4.44 kg of water glass to the acidified solution and stir for 30 minutes until uniform.

[0050] (4) Add 0.51 kg of phosphoric acid to the slurry in (3), and stir for 25 minutes until uniform.

[0051] (5) Add 7.2 kg of alkaline silica sol to the above acidified slurry, stir for about 30 minutes until uniform, and obtain a catalyst slurry.

[0052] (6) The obtained catalyst slurry is spray-dried, washed with water and dried to obtain the catalyst SL-1.

Embodiment 2

[0054] (1) 13.33 kg of ZSM-5 molecular sieve (silicon-aluminum ratio 38, dry basis content 95%) was mixed with 33.53 kg of deionized water, 9.62 kg of kaolin, and 13.24 kg of pseudo-boehmite for 4 hours.

[0055] (2) Add 1.67 kg of 35 wt% hydrochloric acid to the slurry in (1), and stir for 50 minutes.

[0056] (3) Add 6.67 kg of water glass to the acidified solution and stir for 30 minutes until uniform.

[0057] (4) Add 0.61 kg of phosphoric acid to the slurry in (3), and stir for 20-30 minutes until uniform.

[0058] (5) Add 10.8 kg of alkaline silica sol to the above acidified slurry, stir for about 30 minutes until uniform, and obtain catalyst slurry.

[0059] (6) The obtained catalyst slurry is spray-dried, washed with water and dried to obtain the catalyst SL-2.

Embodiment 3

[0061] (1) 13.33 kg of ZSM-5 molecular sieve (silicon-aluminum ratio of 60, dry basis content of 90 wt%) was mixed with 41.70 kg of deionized water, 12.31 kg of kaolin, and 11.15 kg of pseudo-boehmite for 5 hours.

[0062](2) Add 0.93 kg of 35 wt% hydrochloric acid to the slurry in (1), and stir for 60 minutes.

[0063] (3) Add 2.22 kg of water glass to the acidified solution and stir for 30 minutes until uniform.

[0064] (4) Add 0.80 kg of phosphoric acid to the slurry in (3), and stir for 30 minutes until uniform.

[0065] (5) Add 3.6 kg of alkaline silica sol to the above acidified slurry and stir for about 30 minutes until uniform to obtain a catalyst slurry.

[0066] (6) The obtained catalyst slurry is spray-dried, washed with water and dried to obtain the catalyst SL-3.

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Abstract

The invention discloses a preparation method of a propylene catalytic cracking catalyst with yield increased. The preparation method includes the steps of: 1) mixing and pulping ZSM-5 molecular sieve with water, clay and pseudo-boehmite and stirring the slurry uniformly; 2) performing primary acidification to the slurry in the step 1) and stirring the slurry uniformly; 3) adding a sodium silicate solution to the acidified slurry and stirring the acidified slurry uniformly; 4) performing secondary acidification to the slurry in the step 3), and stirring the slurry uniformly; 5) adding alkaline silicon sol to the acidified slurry in the step 4), and stirring the slurry uniformly; and 6) performing spray granulation to the slurry in the step 5) and water-washing and drying a product. In the preparation method, silicon-aluminum gel is formed from the acidified pseudo-boehmite and the sodium silicate solution, thus forming a Si-Al tetrahedral structure. The catalyst has high hydrothermal-stability and meso- and macro-pore distribution, is suitable for heavy oil catalytic cracking reaction, and is low in or is free of reduction of gasoline and increases octane value of the gasoline. With silicon sol as a binding agent, hydrogen transfer activity of the catalyst is reduced, so that olefin, as a conversion raw material of the propylene, is not over-saturated, thus increasing the yield of the propylene.

Description

technical field [0001] The invention belongs to the technical field of catalysts, and in particular relates to a preparation method of a catalytic cracking catalyst for increasing the production of propylene. Background technique [0002] Propylene is an important chemical raw material, which mainly comes from the co-production of steam cracking to ethylene and the by-product of catalytic cracking process. In China, the catalytic cracking process occupies a dominant position in oil refining. Therefore, the production capacity of its by-product propylene accounts for more than 50% of the total market propylene. Therefore, increasing the propylene yield of catalytic cracking units is an important way to improve the comprehensive benefits of oil refineries. [0003] The addition of catalyst additives to increase the production of propylene in the catalytic cracking process is widely used due to the advantages of simple operation and flexible reaction. [0004] All catalyst man...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/40C10G11/05C07C4/06C07C11/06
CPCY02P20/52B01J29/40B01J2229/37B01J2229/38C07C4/06C07C2529/40C10G11/05C10G2300/70C07C11/06
Inventor 高明军张晓佳王鹏刘惠娟李凤叶红
Owner QINGDAO HUICHENG PETROCHEM TECH
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