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Method for depositing catalyst metals into zeolite to produce hydrocarbon processing catalyst

A catalyst carrier and zeolite technology, which is applied in the field of preparing non-acidic hydrocarbon processing catalysts and non-acidic monofunctional reforming catalysts, can solve the problems of damaging the catalyst's operating performance, and achieve the effect of eliminating or minimizing debris deposition

Inactive Publication Date: 2000-03-22
EXXON CHEM PAT INC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Since some debris is deposited in the pores of the zeolite when the zeolite forms aggregates, it will further impair the performance of the catalyst

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0087] According to the process disclosed in US Pat. No. 5,348,924, a 28% (weight) alumina binder is used to bond the zeolite L extrudate. Through the process of the present invention, a certain amount of the above zeolite L extrudate (A=800g) Loading W = 0.64 wt% platinum concentration.

[0088] By combining 9.7055g of tetraaminoplatinum dichloride monohydrate (Platinum assay: 55.53% by weight, 0.02756mol), 4.3211g of potassium hydroxide particles (86% purity, 0.06623mol) and 7.2717g of potassium chloride (0.09754 mol) was dissolved in sufficient water, and the solution with a total weight of 1440 g was prepared to prepare a platinum loading solution with an initial pH value of 12.5.

[0089] The above loading solution was placed in the tank and circulated at a rate of 600 ml / min. 800 g of extrudate were added to the circulating solution. After 15 hours, the platinum loading solution was drained to yield 1048 g of mother liquor. The pH of the mother liquor was determined t...

Embodiment 2

[0091] The catalysts in the following table were prepared using the procedure of Example 1.

[0092] Only one factor varied in catalysts A to E, and that was the endpoint pH of the loading solution. All five catalysts were tested under the same reforming conditions. Thus, this example shows how the endpoint pH of the loading solution affects the performance of the catalyst under reforming conditions.

[0093] The platinum is loaded on the catalyst using the full immersion method, which involves placing the extrudate in a mesh basket and immersing it in a tank. The loading solution was stored in a container at room temperature, pumped through a mesh basket containing catalyst, and returned to the loading solution storage container. The cycle is maintained for 90 minutes. Maintain good contact between the loading solution and the catalyst.

[0094] The endpoint pH varies with the ratio of KOH (base) to KCl (salt) added to the loading solution to achieve the desired potassium...

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PUM

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Abstract

An ion exchange method is provided for loading and uniformly distributing noble metals into a catalyst substrate comprising a zeolite to make a monofunctional, non-acidic reforming catalyst. The catalyst substrate is contacted with an aqueous loading solution comprising noble metal cations and non-noble metal cations. The loading solution is formulated such that the equivalents of non-noble metal cations remaining in the catalyst not ionically bonded to the zeolite when loading is complete is 1.2 to 6.0 times the equivalents of non-noble metal cations displaced from the zeolite when the noble metal cations ion exchange into the zeolite, and simultaneously the endpoint pH of the loading solution is between 10.0 and 11.5. The required 1.2 to 6.0 ratio is achieved when the ratio of moles of non-noble metal cations added to the loading solution to moles of noble metal added to the loading solution is between 1 and 10. The zeolite catalysts obtained by the ion exchange method can reduce the amounts of detrital material in the micropores of the zeolite.

Description

Field of Invention [0001] The present invention relates to the deposition of catalytic metals in a zeolite matrix to produce non-acidic zeolite-based hydrocarbon processing catalysts. More specifically, the present invention relates to a method for preparing a non-acid hydrocarbon processing catalyst by supporting and uniformly distributing Group VIII catalytic metals in large / medium pore zeolites by means of ion exchange with exchangeable cations in the zeolite. More specifically, the present invention is a method for preparing non-acidic monofunctional reforming catalysts by supporting platinum on zeolite L, X, Y and ZSM-5 catalysts. Background of the Invention [0002] Reforming is a major petroleum refining process used to increase the octane number of naphtha blended into engine gasoline and to produce light aromatics from the paraffins and naphthenes in the naphtha, after extraction For the preparation of chemical product intermediates. [0003...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/068B01J29/62B01J37/30C10G35/095
CPCB01J37/30B01J29/62B01J2229/186C10G35/095B01J29/068B01J2229/20
Inventor J-L·考K·R·克莱穆T·H·范德斯普特S·C·方
Owner EXXON CHEM PAT INC