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Hydrocracking catalyst containing Y molecular sieve and preparation method thereof

A hydrocracking and molecular sieve technology, applied in molecular sieve catalysts, physical/chemical process catalysts, chemical instruments and methods, etc., can solve problems such as removing non-framework aluminum, affecting the distribution of B acid and L acid, and the cracking performance of difficult molecular sieves. Achieve the effects of increasing specific surface area, promoting hydrogenation performance, improving activity and heavy naphtha selectivity

Active Publication Date: 2011-04-06
FUSHUN RES INST OF PETROLEUM & PETROCHEMICALS SINOPEC CORP
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Using aluminum salt alone can also partially remove the non-framework aluminum formed after hydrothermal treatment, but because the pH value of the aluminum salt solution is generally between 2 and 3, it is not enough to remove a large amount of non-framework aluminum, so that part of the aluminum in the micropores The difficult-to-remove non-skeleton aluminum remains in the molecular sieve, which causes partial acid centers of the molecular sieve to be masked, and also affects the distribution of B acid and L acid, making it difficult to maximize the cracking performance of the molecular sieve

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0041] Take 3000GNA 2 O raw material NH with 2.8WT % (dry base 70.3WT %) NH 4 Nay, put in a bottle with a reflux device and can be closed, use 11700ml to remove the plasma, and quickly hear the temperature under the condition of stirring to 95 ° C.Aquatic sorbate and 4500ml exfoliating water -configured water solution. After adding, the slurry is 2 hours at a constant temperature under 95 ° C.Stop stirring, stir up for 10 minutes, separate the molecular sieve of the upper part of the bottle with an analysis method. After washing 3 times, the filter cake is dried in 120 ° C for 5 hours, and the number is SSY-1.The SSY-1 molecular sieve obtained was analyzed by X-ray diffraction (XRD) and plasma launch spectrum analysis. 2 O content is 0.1WT %.

Embodiment 2

[0043] The 300GSSY-1 molecular sieve is put in the tube-type water heat treatment furnace, the program is warmed to 550 ° C, handles 1.5 hours under the surface pressure 0.1MPa, and then puts in a boring bottle with a return device and can be closed.The mixed aqueous solution of / L and 0.3 mol / L sulfuric acid is 1500ml of aluminum sulfate and 0.3 mol / L sulfuric acid. Stir at a constant temperature at 95 ° C for 2 hours, filter, and wash the filter cake with hot ion water to stop washing with the pH value of the washing fluid.The filter cake is dry 120 ° C for 5 hours in the oven.Number LSY-1, see Table 1 in the nature of molecular sieve.

Embodiment 3

[0045] Called 300GSSY-1 molecular sieve and put it in a tube-type water heat treatment furnace, the program warmed to 570 ° C, treats 2 hours under the surface pressure 0.2MPa, and then put in a bottle with a reflux device and can be closed.The mixed aqueous solution of the / L sulfate and 0.2mol / L citric acid is 6000ml. Stir at a constant temperature at 100 ° C for 1 hour, filter, and wash the cake with hot ion water. Stop washing after the pH value of the polyester fluid close to 7.The filter cake is dry 120 ° C for 5 hours in the oven.Number LSY-2, see Table 1 in the nature of the molecular sieve.

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Abstract

The invention discloses a hydrocracking catalyst for producing heavy naphtha in great abundance and a preparation method thereof. The catalyst contains hydrogenation active metals and a carrier which consists of modified Y molecular sieves and alumina, wherein the Y molecular sieves are obtained by using a mixed aqueous solution of aluminum salts and an acid to perform hydro-thermal treatment. The properties of the modified Y molecular sieves are as follows: the specific surface area is between 750 m<2> / g and 850 m<2> / g; the total pore volume is between 0.35 and 0.48 ml / g; the relative crystallinity is between 90 and 130 percent; the cell parameter is between 2.437 and 2.445 nanometers; the silicon-aluminum mol ratio is between 15 and 70; the infrared acid amount is between 0.5 and 1.0 mmol / g; the B acid / L acid is more than 7.0; and the content of sodium oxide is less than or equal to 0.05 weight percent. The hydrocracking catalyst has the characteristics of good catalytic activity, high heavy naphtha selectivity, high yield, high latent content of heavy naphtha arene, and so on.

Description

Technical field [0001] The invention involves a hydrogen cracking catalyst and its preparation method of hydrogenation catalysts and its preparation methods, especially the multi -produced catalytic reorganization raw materials (heavy stone brain oil). Background technique [0002] With the rapid development of my country's national economy, the demand for the market for various types of chemical raw materials, especially aromatics, raw materials, will continue to grow for a longer period of time. The demand for heavy stone brain oil that can be catalyzed as a catalytic reorganization material has also increased significantly.As one of the main means of heavy oil lightweight, hydrogenation technology is the most suitable oil refining technology for rational use of limited oil resources and increasing high -quality heavy stone brain oil.Hydrogenation catalyst is the core of hydrogenation technology, which requires the development of stronger hydrogenation catalysts to meet the nee...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G47/16B01J29/08
Inventor 王凤来刘昶关明华杜艳泽
Owner FUSHUN RES INST OF PETROLEUM & PETROCHEMICALS SINOPEC CORP
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