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Preparation method of high-solid content catalytic cracking catalyst

A catalytic cracking, high solid content technology, applied in physical/chemical process catalysts, molecular sieve catalysts, chemical instruments and methods, etc., can solve the problems of complex process and high preparation cost

Active Publication Date: 2017-10-31
PETROCHINA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

By completely replacing pseudo-boehmite with silica sol, the problem of slurry thickening during acidification of pseudo-boehmite can be avoided, but the preparation cost of this method is high and the process is complicated

Method used

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  • Preparation method of high-solid content catalytic cracking catalyst

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0034] Add 2540 grams of deionized water, 800 grams of aluminum sol, 1656 grams of pseudoboehmite in the reaction kettle, add 187 grams of ammonium chloride reagent after beating for 10 minutes, stir for 15 minutes, let stand for 24 hours, then stir, add 138 60 grams of concentrated phosphoric acid, stirred for 30 minutes, then added 60 grams of concentrated phosphoric acid, stirred for 10 minutes, added 1652 grams of kaolin, stirred for 15 minutes, then added 784 grams of REY molecular sieve, 60 grams of ZSM-5 molecular sieve and 600 grams of USY molecular sieve, and stirred evenly , spray-dried, and the obtained catalyst particles were calcined at 500° C. for 30 minutes, then added 8 times of deionized water, stirred evenly, filtered and dried to obtain the FCC catalyst prepared by the method of the present invention, which was recorded as A1.

[0035] The solid content of the catalyst A1 spray slurry was 48%, the slurry viscosity was 4338 centipoise, the wear index of the ob...

Embodiment 2

[0037] Add 1530 grams of deionized water, 635 grams of aluminum sol, and 882 grams of pseudoboehmite in the reaction kettle, add 3612 grams of lanthanum chloride heptahydrate reagent after beating for 10 minutes, stir for 25 minutes, let stand for 20 hours, then stir, Add 185 grams of boric acid, stir for 20 minutes, add 30 milliliters of rare earth chloride, 30 grams of phosphoric acid, 668 grams of kaolin, stir for 10 minutes, then add 678 grams of REY molecular sieves, 40 grams of ZSM-5 molecular sieves and 369 grams of USY molecular sieves, and stir evenly , spray-dried, and the obtained catalyst particles were calcined at 500° C. for 30 minutes, then added 5 times of deionized water, stirred evenly, filtered and dried to obtain the FCC catalyst prepared by the method of the present invention, and recorded as A2.

[0038] The solid content of the catalyst A2 spray slurry was 51%, the slurry viscosity was 4567 centipoise, the wear index of the obtained catalyst was 1.4%, and...

Embodiment 3

[0040] Add 2530 grams of deionized water, 779 grams of aluminum sol, and 1082 grams of pseudoboehmite in the reaction kettle, add 2307 grams of magnesium nitrate hexahydrate reagent after beating for 10 minutes, stir for 15 minutes, let stand for 13 hours, and then add 1000 grams of Stir silicic acid for 20 minutes, add 78 grams of boric acid, stir for 30 minutes, then add 1240 grams of silicic acid and stir for 20 minutes, add 737 grams of REY molecular sieve, 35 grams of ZSM-5 molecular sieve and 296 grams of USY molecular sieve, stir for 10 minutes, add 752 grams of Kaolin, stirred evenly, spray-dried, the obtained catalyst particles were roasted at 500°C for 30 minutes, then added 8 times deionized water, stirred evenly, filtered and dried to obtain the FCC catalyst prepared by the method of the present invention, which was recorded as A3.

[0041] The solid content of the catalyst A3 spray slurry was 57%, the slurry viscosity was 4039 centipoise, the wear index of the obta...

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Abstract

The invention provides a preparation method of a high-solid content catalytic cracking catalyst. The method comprises the following steps: (1) mixing pseudo-boehmite, a binder and water and stirring evenly; (2) adding a soluble salt of which an anion is selected from Cl<->, NO3<->, ClO4<->, CH3COO<-> or HCOO<->, stirring evenly and standing; (3) adding an acid to the slurry obtained in the step (2), stirring and adding the acid in multiple times; and (4) adding a molecular sieve and the clay to the slurry obtained in the step (3), pulping and mixing evenly to prepare catalyst slurry, carrying out spray drying, solidification roasting, water adding and stirring, filtering and drying to prepare the high-solid content FCC catalyst. In the process of preparing the high-solid content catalyst by adopting the preparation method, the peptization speed is controllable and the mobility of the slurry is good; and heating and warming are not needed in the peptization process and a hydrochloric acid is replaced with other acids in the acidifying peptization process, so that the damage of a hydrochloric acid gas to the molecular sieve in the catalyst roasting process is avoided and the activity of the catalyst is improved.

Description

technical field [0001] The invention relates to a preparation method of a fluid catalytic cracking (FCC) catalyst, in particular to a preparation method of a pseudo-boehmite-containing FCC catalyst with a high solid content. Background technique [0002] Fluid catalytic cracking (FCC) process is the main means of secondary processing of crude oil, and an important means of deep processing of heavy oil into vehicle fuel at home and abroad. The consumption of FCC catalyst required by the process is increasing with the heavy and poor quality of processing raw materials. Semi-synthetic catalytic cracking catalysts are usually prepared by first mixing molecular sieves, clay and binders in a certain proportion to form a slurry with a solid content of 20-25%, and then spray drying and other steps. Obviously, the higher the solid content of the slurry, the higher the drying efficiency and the lower the energy consumption of the drying process. Increasing the solid content of the s...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/80B01J29/08
CPCB01J29/084B01J29/088B01J29/40B01J29/405B01J29/80B01J2029/062B01J2229/20B01J2229/26
Inventor 潘志爽李雪礼袁程远曹庚振黄校亮刘明霞张爱萍高雄厚张海涛谭争国蔡进军段宏昌丁伟郑云锋孙书红
Owner PETROCHINA CO LTD
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