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Method for improving solid content of catalytic cracking catalyst slurry

A catalyst slurry and catalytic cracking technology, which is applied in catalytic cracking, physical/chemical process catalysts, chemical instruments and methods, etc. It can solve the problems of destroying molecular sieves, deterioration of catalyst anti-wear strength, and difficulty in pseudo-boehmite

Active Publication Date: 2008-03-05
PETROCHINA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0010] When the existing Pseudo-boehmite acid-adding process is used to prepare the FCC catalyst of the aluminum sol composite aluminum-based binder, the production process reported by domestic and foreign patents all adopts the process step of adding acid after the pseudo-boehmite (such as USP4476239, CN1081218C, CN1098130A etc.), the solid content of the catalyst slurry prepared according to the existing acid addition process or improved process can be controlled at 25-50%. One of the outstanding problems at present is that the inorganic acid is added after the pseudo-boehmite. The reaction with pseudo-boehmite is difficult to occur uniformly, and there is always a local over-reaction phenomenon, resulting in a rapid increase in the viscosity of the slurry; the second outstanding problem is that when the molecular sieve slurry is added before, the addition of inorganic acid will inevitably cause local Destroy the molecular sieve phenomenon, and because the acidity of the system cannot be controlled too low (generally, the pH is greater than 2.8), it is difficult to fully refine the pseudo-boehmite, especially when the molecular sieve content is high (such as greater than 40%), the wear resistance of the catalyst become worse, the performance will be greatly affected

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0042] Add deionized water, 2174 grams of aluminum sol and 2078 grams of kaolin in the reaction kettle, add 200 grams of concentration after beating and be 35% hydrochloric acid, mix well and add 1656 grams of 1 hour under stirring # Pseudo-boehmite, after stirring for 30 minutes, add 1937 grams of REUSY molecular sieves, 123 grams of Fudan ZSM-5 molecular sieves and deionized water mixed molecular sieve slurry, spray dry after beating, and roast the obtained catalyst microspheres at 500 ° C for 0.5 hours, Then add deionized water, stir evenly, wash at 80° C. for 15 minutes, and filter and dry to obtain the FCC catalyst prepared by the method of the present invention, which is recorded as A1.

[0043] The solid content of the spray slurry of catalyst A1 is 39.2w%, the viscosity of the slurry is 4058 centipoise, the wear index of the obtained catalyst is 1.5, and the pore volume is 0.40mL·g -1 , Microreaction Activity 79 .

Embodiment 2

[0052] Add deionized water in the reaction kettle, 2634 grams of aluminum sol and 195 grams of concentration are 35% hydrochloric acid, add 1524 grams of 1# pseudo-boehmite under stirring after mixing, add 1896 grams of kaolin after stirring for 0.5 hours, After beating evenly, add a mixed slurry composed of 2060 grams of REUSY molecular sieves and deionized water, spray dry after beating, and roast the obtained catalyst microspheres at 500°C for 0.5 hours, then add deionized water, stir evenly, and wash at 80°C for 15 minutes, filter and dry to obtain the FCC catalyst prepared by the method of the present invention, which is recorded as A2.

[0053] The solid content of the spray slurry of catalyst A2 is 39.6w%, the viscosity of the slurry is 4856 centipoise, the wear index of the obtained catalyst is 1.7, and the pore volume is 0.41mL·g -1 , micro-reaction activity 80.

Embodiment 3

[0059] Adding 2174 grams of aluminum sol and 200 grams of concentration in the reactor is 35% hydrochloric acid, mix well, then add deionized water and 2078 grams of kaolin, mix well and add 1656 grams of 1 hour under stirring # Pseudo-boehmite, after stirring for 30 minutes, add 1937 grams of REUSY molecular sieves, 123 grams of Fudan ZSM-5 molecular sieves and deionized water mixed molecular sieve slurry, spray dry after beating, and roast the obtained catalyst microspheres at 500 ° C for 0.5 hours, Then add deionized water, stir evenly, wash at 80° C. for 15 minutes, and filter and dry to obtain the FCC catalyst prepared by the method of the present invention, which is recorded as A3.

[0060] The solid content of the spray slurry of catalyst A3 is 39.2w%, the viscosity of the slurry is 4097 centipoise, the wear index of the obtained catalyst is 1.6, and the pore volume is 0.40mL·g -1 , Microreaction Activity 79 .

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PUM

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Abstract

The present invention is method of raising solid content in catalytic cracking catalyst slurry. The method includes mixing clay, molecular sieve slurry, aluminum-containing binder, pseudo boehmite and inorganic acid to form catalyst slurry and the subsequent spray drying. It features that the addition of inorganic acid before adding pseudo boehmite and the molecular sieve, and the addition of inorganic acid after adding kaolin and aluminum-containing binder or into the aluminum-containing binder. The present invention can raise the solid content in catalyst slurry to over 40 % to short the colloid forming time greatly, raise the catalyst producing efficiency and lower catalyst producing cost while ensuring the wear strength of catalyst. At the same time, the catalyst has great pore volume, high micro reaction activity and improved comprehensive reaction performance.

Description

technical field [0001] The invention relates to a method for increasing the solid content of catalytic cracking catalyst slurry, which is suitable for the preparation of catalytic cracking catalyst used in petroleum processing and can greatly increase the solid content of slurry for preparing the catalyst. technical background [0002] Fluid Catalytic Cracking (FCC for short) process is the main process of secondary processing of crude oil, and an important means of deep processing of heavy oil at home and abroad to produce vehicle fuel. With the increasing quality and inferiority of processing raw materials and the increasing demand for vehicle fuel, the consumption of FCC catalyst required by this process is increasing; at the same time, due to the demand for processing heavy oil and the development of FCC process technology, molecular sieve active components are in The proportion in FCC catalysts also shows an increasing trend. Generally speaking, the process of preparin...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G11/05B01J37/00
Inventor 刘从华谭争国高雄厚郑淑琴滕秋霞丁伟陆通汪毅刘涛
Owner PETROCHINA CO LTD
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