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Molecular sieve based catalyst for carbonylation and preparation method and application thereof

A technology of carbonylation reaction and molecular sieve, which is applied in the direction of molecular sieve catalyst, carbon monoxide or formate reaction preparation, physical/chemical process catalyst, etc. It can solve the problems of easy collapse of molecular sieve structure, poor selectivity of dealumination, shortening the service life of molecular sieve catalyst, etc. question

Active Publication Date: 2018-01-05
ZHENGZHOU TOBACCO RES INST OF CNTC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

The mordenite with pre-adsorbed pyridine desorbs slowly during use, resulting in a gradual increase in carbon deposits, which deteriorates the selectivity of mordenite and shortens its lifespan, affecting product quality
The method of treating mordenite with acid or steam for dealumination has poor selectivity of dealumination, and the molecular sieve structure is easy to collapse, which shortens the service life of the molecular sieve catalyst.

Method used

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  • Molecular sieve based catalyst for carbonylation and preparation method and application thereof

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Embodiment 1

[0029] The preparation method of the molecular sieve catalyst used for carbonylation reaction of the present embodiment, such as figure 1 shown, including the following steps:

[0030] 1) Roast the original powder of mordenite molecular sieve, then immerse it in 1mol / L ammonium nitrate solution for 2 hours for ammonia exchange, then wash and dry, repeat the steps of ammonia exchange, washing and drying 3 times, and then roast at 550°C for 4 hours, Prepared hydrogen-type mordenite molecular sieve;

[0031] 2) Immerse the hydrogen-type mordenite molecular sieve prepared in step 1) in a mixed solution of lanthanum nitrate and ferric nitrate for 12 hours for ion exchange, then filter, dry, and then roast at 550° C. for 4 hours to obtain a metal oxide loading capacity of 2.0% (mass fraction) metal oxide modified molecular sieve; the amount concentration of lanthanum nitrate in the mixed solution is 1mol / L, and the amount concentration of iron nitrate is 2mol / L; oxidation in metal ...

Embodiment 2

[0036] The preparation method of the molecular sieve catalyst that is used for carbonylation reaction of the present embodiment comprises the following steps:

[0037] 1) Roast the original powder of mordenite molecular sieve, then immerse it in 1mol / L ammonium nitrate solution for 2 hours for ammonia exchange, then wash and dry, repeat the steps of ammonia exchange, washing and drying 3 times, and then roast at 550°C for 4 hours, Prepared hydrogen type mordenite molecular sieve;

[0038] 2) Immerse the hydrogen-type mordenite molecular sieve prepared in step 1) into a solution of 2 mol / L calcium nitrate for 12 hours for ion exchange, then filter, dry, and then roast at 550° C. for 4 hours to obtain a metal oxide Loading capacity is 2.5% (mass fraction) metal oxide modified molecular sieve;

[0039] 3) Take a certain amount of the metal oxide modified molecular sieve prepared in step 2) and place it in a reactor, heat it to 600°C under air purging and keep it warm for 0.5h, t...

Embodiment 3

[0043] The preparation method of the molecular sieve catalyst that is used for carbonylation reaction of the present embodiment comprises the following steps:

[0044] 1) Roast the original powder of mordenite molecular sieve, then immerse it in 1mol / L ammonium nitrate solution for 2 hours for ammonia exchange, then wash and dry, repeat the steps of ammonia exchange, washing and drying 3 times, and then roast at 550°C for 4 hours, Prepared hydrogen-type mordenite molecular sieve;

[0045] 2) Soak the hydrogen-type mordenite molecular sieve prepared in step 1) in a zinc acetate solution with a concentration of 2.5 mol / L for 6 hours for ion exchange, then filter, dry, and then roast at 550° C. for 4 hours to obtain metal oxide The material load is 1.5% (mass fraction) metal oxide modified molecular sieve;

[0046] 3) Take a certain amount of the metal oxide modified molecular sieve prepared in step 2) and place it in the reactor, heat it to 500°C under the purging of oxygen and...

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Abstract

The invention relates to a molecular sieve based catalyst for carbonylation and a preparation method and application thereof, and belongs to the technical field of molecular sieve based catalysts. Thepreparation method of the molecular sieve based catalyst for carbonylation comprises the following steps that a hydrogen molecular sieve is immersed in a metal salt solution to conduct ion exchange,then, calcination is conducted, unsaturated hydrocarbon is catalyzed at the temperature ranging from 400 DEG C to 600 DEG C to conduct a carbonation reaction, carbonation is conducted at 700-1,000 DEGC, pickling is conducted by adopting inoxidable acid, and the molecular sieve based catalyst is obtained, wherein the hydrogen molecular sieve is a hydrogen mordenite or hydrogen ZSM-35 molecular sieve, and the molecular dynamic diameter of unsaturated hydrocarbon ranges from 0.5 nm to 0.75 nm. The molecular sieve based catalyst obtained through the preparation method can eliminate acid sites ina channel of the large size on the condition that acid sites in an octatomic ring channel are not affected, selection of the catalyst in a reaction of preparing methyl acetate through dimethyl ether carbonylation is improved, and the service life of the catalyst is prolonged.

Description

technical field [0001] The invention relates to a molecular sieve catalyst used for carbonylation reaction, its preparation method and application, and belongs to the technical field of molecular sieve catalysts. Background technique [0002] Methyl acetate (methyl acetate) is widely used in textile, perfume and pharmaceutical industries, and is an important intermediate of organic raw materials. The downstream products mainly include acetic acid, acetic anhydride, methyl acrylate, vinyl acetate, acetamide, etc. In China, the production of methyl acetate is mainly the traditional esterification method. This method has the problems of complex separation of product and catalyst, expensive and scarce precious metal rhodium, and iodides cause severe corrosion to equipment. Solid acid catalyzed carbonylation of dimethyl ether to produce methyl acetate is a novel route. The catalyst used in the reaction process is a solid catalyst, which is easy to separate without corrosion and ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/24B01J29/68C07C67/37C07C69/14
Inventor 王金棒程多福高运谦邱纪青邓楠汪志波张仕华刘亚丽郑路冯伟华郑新章
Owner ZHENGZHOU TOBACCO RES INST OF CNTC