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Hydrocarbon cracking catalyst containing phosphorus and its prepn

A cracking catalyst and catalyst technology, applied in cracking, catalytic cracking, petroleum industry, etc., can solve the problems of catalyst wear rate reduction, chlorine content reduction rate, complicated preparation methods, etc., to achieve gas and coke production rate reduction, diesel production The effect of increased rate and improved product selectivity

Inactive Publication Date: 2004-12-15
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] Report in CN86104860A, add phosphoric acid solution in the pseudo-boehmite of aging, then mix with zeolite and clay, spray dry, roast, the catalyst wear rate that obtains declines to some extent
However, there are also many shortcomings in using this phosphorus-containing aluminum sol as a binder.
One is that the preparation process of this binder requires steps such as high-temperature depolymerization and concentration, and the preparation method is relatively complicated; the other is that in order to ensure the stability and fluidity of the phosphorus-containing aluminum sol, the phosphorus content in the sol is limited. The P / Al (weight) ratio is lower than 0.25; the third is that compared with the aluminum sol, the chlorine content of this phosphorus-containing aluminum sol is reduced very little, and mainly relies on the use of chlorine-containing aluminum with a high Al / Cl (weight) ratio. Sol raw materials to improve its Al / Cl (weight) ratio, which is difficult to achieve industrially
As far as the inventors know, there is no report on the preparation of hydrocarbon cracking catalysts by using chlorine-free phosphorus-containing aluminum sol binders

Method used

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Examples

Experimental program
Comparison scheme
Effect test

preparation example Construction

[0032] The preparation method of said phosphorus-containing hydrocarbon cracking catalyst provided by the invention comprises:

[0033] The clay is beaten and mixed evenly with water, and the amount of water used is to make the solid content of the obtained slurry = 10% to 50% by weight; or:

[0034] Beat the clay with water and mix it evenly; add aluminum oxide or aluminum hydroxide, and hydrochloric acid, continue beating and mixing evenly, then heat the slurry to 55-65°C and age it for 0.5-1.5 hours, so that the pH value of the slurry is higher than 2.8; the amount of hydrochloric acid HCl / Al 2 o 3 Weight ratio=0.02~0.25; The consumption of water is to make the solid content of gained slurry=10~50% by weight; Then:

[0035] Add the mixed sol of chlorine-containing aluminum sol and phosphorus-containing aluminum sol to the slurry obtained above, or add chlorine-containing aluminum sol and phosphorus-containing aluminum sol respectively, and add molecular sieve slurry, and ...

Embodiment 1

[0064] This example illustrates the preparation of a phosphorus-containing aluminum sol and mixed binder for use in the catalyst according to the invention.

[0065] 5.8 kg of pseudoboehmite (containing Al 2 o 3 1.8 kg) and 4.0 kg of decationized water for beating for 30 minutes, add 9.6 kg of concentrated phosphoric acid to the slurry under stirring, heat up to 70°C, and then react at this temperature for 45 minutes to obtain a colorless and transparent phosphorous-containing aluminum sol. Its pH is 1.7. After analysis, the phosphorus-containing aluminum sol contains 14.7% by weight of P, 4.7% by weight of Al, and P / Al (weight)=3.1.

[0066] Preparation of mixed binder: mix the above-prepared phosphorus-aluminum glue and aluminum sol uniformly in different proportions to prepare mixed binders with different P / Al ratios and Al / Cl ratios.

Embodiment 2

[0068] This example illustrates the preparation of a phosphorus-containing aluminum sol and mixed binder for use in the catalyst according to the invention.

[0069] 2.13 kg of SB powder (containing Al 2 o 3 1.6 kg) and 7.6 kg of decationized water for beating for 30 minutes, add 6.0 kg of concentrated phosphoric acid to the slurry under stirring, heat up to 80°C, and then react at this temperature for 45 minutes to obtain a colorless and transparent phosphorus-containing aluminum sol. Its pH is 1.9. After analysis, the phosphorus-containing aluminum sol contains 10.5% by weight of P, 5.0% by weight of Al, and P / Al (weight)=2.1.

[0070] Preparation of mixed binder: mix the above-prepared phosphorus-aluminum glue and aluminum sol uniformly in different proportions to prepare mixed binders with different P / Al ratios and Al / Cl ratios.

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PUM

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Abstract

The hydrocarbon cracking catalyst contains molecular sieve, binder and clay and its features are the mixed sol of chlorine-containing aluminum sol and phosphorus-containing aluminium sol used as binder. The binder raises the antiwear strength of the catalyst, and decreases the chlorine content in the spray drying slurry and the catalyst. The hydrocarbon cracking catalyst results in lower gas and coke yield and higher diesel oil yield and diesel oil / gasoline ratio.

Description

technical field [0001] The invention relates to a petroleum hydrocarbon cracking catalyst and a preparation method thereof, in particular to a molecular sieve-containing hydrocarbon cracking catalyst using aluminum sol and phosphorus-containing aluminum sol mixed sol as a binder and a preparation method thereof. Background technique [0002] Phosphorus-containing hydrocarbon cracking catalysts mainly include the following three types: one is that the molecular sieve component of the catalyst is a phosphorus-containing zeolite molecular sieve, as described in U.S.P.5,312,792, U.S.P.5,472,594, EP 667185, etc.; Aluminum or alumina-aluminum phosphate is used as a substrate or a part of the substrate. This type of catalyst substrate has good thermal stability, good activity and selectivity, and is suitable for heavy oil cracking, such as U.S.P. , described in EP 488427, EP 4962267, etc.; the other is to use phosphoric acid, phosphorous acid and its ammonium salts to treat molecul...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G11/02
Inventor 蒋文斌郑曼英陈蓓艳达志坚桂跃强黄轶唐立文杨青
Owner CHINA PETROLEUM & CHEM CORP
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