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A kind of catalytic material and preparation method thereof

A technology for catalytic materials and oxides, applied in chemical instruments and methods, catalytic cracking, molecular sieve catalysts, etc., can solve problems such as affecting the cracking reaction of macromolecules, alleviate subsequent treatment costs and production costs, and expand recycling methods. The effect of long crystallization time

Active Publication Date: 2021-04-06
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, with the increasing trend of crude oil becoming heavier and inferior, microporous molecular sieves have a more obvious effect of restricting the diffusion of macromolecules such as heavy oil or residual oil due to their smaller pores, thus affecting the cracking reaction of macromolecules to a certain extent.

Method used

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  • A kind of catalytic material and preparation method thereof
  • A kind of catalytic material and preparation method thereof
  • A kind of catalytic material and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0029] This example illustrates the use of the preparation method of the present invention and the resulting catalytic material.

[0030] The mixed solution (concentration 50gSiO2) of the NaY molecular sieve crystallization mother liquor and filtrate containing P-type miscellaneous crystal 2 / L, suspended matter concentration 1200mg / L) into the container, and then quantitative sodium metaaluminate solution (concentration 185gAl 2 o 3 / L, caustic ratio 2.55) is added therein and carries out contact treatment, and the control pH value is 13.8, obtains slurry A; In slurry A, add the AlCl of metering 3 Solution (concentration 60gAl 2 o 3 / L), and adjust the final pH value of the slurry to be 9.2, thus obtaining slurry B; the temperature of slurry B was raised to 60°C and treated at a constant temperature at this temperature for 3 hours, and the resulting solid precipitate was filtered according to the dry basis of the precipitate: Ammonium salt: H 2 The weight ratio of O=1:0....

Embodiment 2

[0034] This example illustrates the use of the preparation method of the present invention and the resulting catalytic material.

[0035] Add an appropriate amount of water into the container, heat up to 45°C, and under vigorous stirring, mix the NaY molecular sieve crystallization mother liquor containing P-type heterocrystals and the filtrate (concentration 42gSiO 2 / L, suspended matter concentration 680mg / L) and sodium metaaluminate solution (concentration 150gAl 2 o 3 / L, caustic ratio 1.65) add in the above-mentioned container and carry out contact treatment simultaneously, control pH value to be 13.6, obtain slurry A; Then add Al in slurry A 2 (SO 4 ) 3 Solution (concentration 90gAl 2 o 3 / L), and adjust the end point pH value of the slurry to be 9.8, thus obtaining slurry B; the slurry B was warmed up to 55°C and treated at a constant temperature at this temperature for 6 hours, and the resulting solid precipitate was filtered according to the dry basis of the prec...

Embodiment 3

[0038] This example illustrates the use of the preparation method of the present invention and the resulting catalytic material.

[0039] The NaY molecular sieve crystallization washing filtrate (concentration 38gSiO2) that the crystallization time is longer and the crystallinity is lower but cannot detect P-type miscellaneous crystals 2 / L, suspended matter concentration 495mg / L) into the container, and then add ammonia water to it for contact treatment at 55°C under vigorous stirring, and control the pH value to 13.1 to obtain slurry A; add metered Al to slurry A 2 (SO 4 ) 3 Solution (concentration 60gAl 2 o 3 / L), and adjust the final pH value of the slurry to be 8.6, thus obtaining slurry B; the slurry B was heated up to 70°C and treated at a constant temperature at this temperature for 4 hours, and the resulting solid precipitate was filtered according to the dry basis of the precipitate: Acid: H 2 The weight ratio of O=1:0.12:12 was contacted with dilute sulfuric ac...

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Abstract

A catalytic material is characterized in that the main structure of the catalytic material is an amorphous structure, and at the same time contains a small amount of FAU crystal phase structure, or contains a small amount of NaP crystal phase structure, and the catalytic material contains 50-80% by weight of oxides. % silicon and 20-50% aluminum, BET total specific surface area≯250m 2 / g, wherein the proportion of the micropore specific surface area in the BET total specific surface area≯28%, the average pore diameter is 20~50nm; a / b=1.1~1.7, wherein, said a represents the material surface Al measured by the XPS method / Si atomic ratio, said b represents the material bulk phase Al / Si atomic ratio measured by XRF method.

Description

technical field [0001] The present invention relates to a catalytic material and a preparation method thereof. More specifically, the present invention relates to a catalytic material with mesopore characteristics and a method for preparing the catalytic material by using molecular sieve mother liquor as a raw material. Background technique [0002] Y-type molecular sieve is a kind of molecular sieve widely used in petroleum refining and processing. With the increasing demand for cracking catalysts in the market, the output of Y-type molecular sieve is also increasing. The annual output of Y-type molecular sieve in my country has reached 5 More than 10,000 tons, with the increase of output, the amount of NaY molecular sieve crystallization mother liquor and water washing filtrate also increases. Since the utilization rate of silicon in the synthesis process of NaY molecular sieve is relatively low, the silicon-aluminum ratio of the feed is much higher than that of the product...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/04C10G11/04B01J23/04B01J35/10
CPCC10G11/04B01J23/002B01J23/04B01J29/04B01J2523/00C10G2400/02B01J35/647B01J35/615B01J2523/12B01J2523/31B01J2523/41
Inventor 郑金玉王成强罗一斌
Owner CHINA PETROLEUM & CHEM CORP