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Preparation method of low-abrasion fluidized bed microspherical catalyst

A catalyst, low-wear technology, applied in physical/chemical process catalysts, molecular sieve catalysts, chemical instruments and methods, etc., can solve problems such as difficulty in controlling molecular sieve particle size and crystallinity, unfavorable modification, etc. Sexually wide effect

Active Publication Date: 2014-01-08
SHAANXI COAL & CHEM TECH INST
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] Improving the wear resistance of catalysts by reducing the content of molecular sieves is not suitable for the production process of catalysts that require high activity; while using microspheres to synthesize molecular sieves in situ to improve wear resistance, it is difficult to control the particle size of molecular sieves in the obtained catalysts and crystallinity, and also have adverse effects on subsequent operations such as modification

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0028] Disperse ZSM-5, aluminum sol, kaolin, and turnip powder in water according to the ratio of solid content of 40%, 40%, 20%, and 10% (by molecular sieve weight) to make a slurry with a solid content of 30% , spray until the particle size of the slurry is lower than 6μm, the air inlet temperature is 400°C, and the air outlet temperature is 130°C, control to obtain particles with a particle size of less than 40μm, add water to disperse, and prepare a slurry with a solid content of 30%, shear Afterwards, spray again, the spraying condition is 390°C for the air inlet, 170°C for the air outlet, and control to obtain particles with a particle size distribution of 20-150 μm and an average particle size of 85 μm. After calcining at 550°C for 8 hours, a low-wear fluidized bed catalyst was obtained. The resulting catalyst attrition index was 0.48%.

Embodiment 2

[0030] ZSM-5, colloidal silica, kaolin, and starch are dispersed in water at a ratio of 30%, 20%, 50%, and 10% (by molecular sieve weight) according to the solid content, to make a slurry with a solid content of 35%. Spray after cutting until the particle size of the slurry is less than 6 μm, the air inlet temperature is 380°C, and the air outlet is 140°C, control to obtain particles with a particle size of less than 40 μm, re-add water to disperse, prepare a slurry with a solid content of 30%, and re-shear after cutting For spraying, the spraying conditions are 400°C air inlet and 150°C air outlet, controlled to obtain particles with a particle size distribution of 20-300μm and an average particle size of 70μm. After calcining at 650°C for 12 hours, a low-wear fluidized bed catalyst was obtained. The abrasion index was 0.54%.

Embodiment 3

[0032] SAPO-34, silica sol, pseudo-boehmite, and safflower powder are dispersed in water at a ratio of 40%, 10%, 50%, and 5% (by molecular sieve weight) according to the solid content, and the solid content is 35%. % of the slurry, cut until the particle size of the slurry is less than 6 μm, then spray, the air inlet temperature is 380 ° C, the air outlet temperature is 140 ° C, and the particles with a particle size of less than 40 μm are controlled, and then added to water for dispersion to prepare a slurry with a solid content of 40%. After shearing, re-spray, repeat the above spray-shearing process 3 times, the final slurry spraying conditions are 370°C inlet air, 150°C outlet air, controlled to obtain particles with a particle size distribution of 20-150μm and an average particle size of 75μm. After calcining at 520°C for 10 hours, a low-wear fluidized bed catalyst was obtained. The abrasion index was 0.54%.

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Abstract

The invention discloses a preparation method of a low-abrasion fluidized bed microspherical catalyst. The method comprises the steps of: preparing slurry containing a molecular sieve, an adhesive, a dispersing agent and water according to a ratio, shearing, spray-drying to obtain microspheres, dispersing the microspheres in water again, shearing again, spraying, finally spray-shaping the dispersed slurry to obtain microspheres, and baking to obtain the low-abrasion microspherical fluidized bed catalyst. By adopting the method, the abrasion resistance of the catalyst is significantly improved under the condition that the property of the active ingredient molecular sieve is not influenced. The method has wide practicability, has no special requirement on the traditional catalyst production device, and can be used for the production process of multiple molecular sieve fluidized bed microspherical catalysts.

Description

technical field [0001] The invention belongs to the field of synthesis and preparation of catalytic materials, and relates to a method for preparing a microsphere catalyst, in particular to a method for preparing a low-wear fluidized bed microsphere catalyst. Background technique [0002] In the chemical industry, especially petrochemical industry, the fluid catalytic cracking process has been widely used. The current high oil price has made the conversion of cheap and easy-to-get hydrocarbons and oxygenated compounds more and more important. Fluidized bed technology is also widely used in the conversion of hydrocarbons and oxygenated compounds such as MTO, MTP, and C4 hydrocarbon cracking. process. [0003] In the fluidized bed process, the microsphere catalyst flows continuously between the reactor and the regenerator under the high-speed airflow, so as to realize the continuous progress of the reaction and regeneration process. Due to the severe friction and collision b...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J35/08B01J29/08B01J29/70B01J29/40B01J29/03B01J29/85
Inventor 张世刚张亚秦张小虎张随平沈鹏飞高力丹刘建斌李志鹏张军民罗熙
Owner SHAANXI COAL & CHEM TECH INST