Method of using modified molecular sieve catalyst in isobutane catalytic cracking

Inactive Publication Date: 2013-06-05
DALIAN UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

When ZSM-5 is used as a carrier, only supported gold catalysts with gold particles of 40-50nm can be obtained, and Au / ZSM-5 catalysts with smaller particles cannot be obtained

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0136] The preparation method of 0.1%Au / HZSM-5:

[0137] (1). Synthesize ZSM-5 molecular sieve raw powder with reference to the method disclosed in the published patent CN100364890C. Calcined at 540 DEG C for 4 hours to obtain ZSM-5 molecular sieves.

[0138] (2). Ammonium exchange treatment: the calcined molecular sieve is subjected to ion exchange treatment with an ammonium salt solution at a suitable temperature. Then, it is washed with deionized water to neutrality, then dried and calcined to obtain a hydrogen-type catalyst. Said ammonium salt is ammonium nitrate, and ammonium salt solution concentration is 0.6mol / L, and the liquid-solid volume ratio of catalyzer and ammonium salt solution is 5:1, and exchange temperature is 30 ℃, and exchange time is 1 hour, and exchange number of times is 2 Second-rate. 110 DEG C of drying temperature, 12 hours of drying time, 540 DEG C of roasting temperature, 6 hours of roasting time. Na after exchange + The content is not higher ...

Embodiment 2

[0144] Repeat Example 1, but change the amount of chloroauric acid solution into 3.14ml and add water to 10ml, and the roasting temperature is 300°C. A supported gold catalyst 0.3%Au / HZSM-5 was obtained. Labeled: A-2.

Embodiment 3

[0146] Repeat embodiment 1, but change the degree of vacuum into-0.05MPa, and the consumption of chloroauric acid solution is changed into 10.46ml. The supported gold catalyst 1.0%Au / HZSM-5 was obtained. Labeled: A-3.

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PUM

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Abstract

The invention discloses a method of using modified molecular sieve catalyst in isobutane catalytic cracking and belongs to the technical field of catalysts. The method includes the following steps: conducting full negative pressure degassing purification treatment on a molecular sieve, adopting a negative pressure deposition-precipitation method to load a gold precursor to a molecular sieve carrier, and obtaining an even and high-dispersion small particular supported gold catalyst. The molecular sieve is a high-silica zeolite molecular sieve, the supported gold catalyst obtained by the deposition-precipitation method under the condition of negative pressure is beneficial for purifying the inner surface, the outer surface and a duct of the molecular sieve, and Au can easily enter the duct of the molecular sieve to achieve high dissipation. By means of the method, dehydrogenation is conducted on isobutane to produce olefin under double functions of metal and a carrier, the olefin obtains a proton at an acid center to form a carbonium ion, and the carbonium ion conducts polymer lysis to generate a corresponding olefin.

Description

technical field [0001] The invention belongs to the technical field of catalysts, and relates to the application of a modified molecular sieve catalyst in the catalytic cracking reaction of isobutane. Background technique [0002] Ethylene, propylene and isobutylene produced by catalytic cracking and steam cracking units in refining and chemical enterprises are very important polymer monomers. At the same time, isobutene is also used in the synthesis of MTBE. However, due to the increasing depletion of petroleum resources, there are limitations in increasing the production of these useful olefins simply by expanding the amount of petroleum processing. On the other hand, in some places in the world such as China, the relative surplus of isobutene produced by catalytic cracking units needs to be developed and utilized urgently. The efficient conversion of isobutane into important chemical raw materials such as ethylene, propylene and isobutene through cracking reaction is ve...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C4/06B01J29/44B01J29/74B01J29/22B01J29/89B01J29/04B01J29/46B01J29/48
CPCY02P20/52
Inventor 郭洪臣刘家旭艾沙努拉洪
Owner DALIAN UNIV OF TECH
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