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A kind of preparation method of methanol dehydration preparation dimethyl ether catalyst

A methanol dehydration and catalyst technology, which is applied in the direction of ether preparation, dehydration of hydroxyl-containing compounds to prepare ether, chemical instruments and methods, etc., can solve the problems of many by-products, easy deactivation, easy carbon deposition, etc., and achieve high conversion rate and selectivity performance, avoid excessive cracking, and improve the effect of pore structure

Active Publication Date: 2016-11-02
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] At present, the catalyst used for methanol dehydration is generally Al 2 o 3 Or molecular sieves, among which the commonly used molecular sieves include aluminum phosphate, HZSM-5, HY, SAPO, etc., and they all have their own shortcomings: for example, although alumina has high stability, the reaction temperature is high, and the requirements for reaction equipment are very high, resulting in cost High; molecular sieve catalysts have strong acidity and low initial temperature, but they also have the disadvantages of many by-products, easy carbon deposition, and easy deactivation
The above-mentioned catalysts have high catalytic activity and selectivity in the reaction, and the optimal load of silicotungstic acid is 10wt%~16wt%. Under normal pressure, when used to treat pure methanol raw materials, its selectivity is high, but Its low-temperature activity is not good, and when it is used as a methanol raw material containing water, its stability is not good, and the selectivity and activity also decrease.

Method used

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  • A kind of preparation method of methanol dehydration preparation dimethyl ether catalyst
  • A kind of preparation method of methanol dehydration preparation dimethyl ether catalyst
  • A kind of preparation method of methanol dehydration preparation dimethyl ether catalyst

Examples

Experimental program
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Embodiment 1

[0034] (1) Catalyst preparation:

[0035] Weigh 8.9g of lanthanum nitrate, 13.9g of phosphotungstic acid, 120g of cetyltrimethylammonium bromide and 168.8g of citric acid to form a mixed solution, add 249mL tetraethyl orthosilicate to the mixed solution, and stir for 2 h, then stirred at 70°C until it formed a gel, aged the gel at room temperature for 12 h, dried at 110°C for 8 h, and then calcined at 380°C for 3 h, the resulting solid was added to a C6 alkane solvent and immersed for 10 min, Then filter, dry at room temperature until there is no liquid phase on the surface of the carrier, add it to an aqueous solution containing 6.9g of phosphotungstic acid and 4.4g of lanthanum nitrate, stir at 70°C until the solution is evaporated to dryness, and dry the obtained solid at 110°C for 8.0 h, and then calcined at 450°C for 3.0 h to prepare the catalyst, La 2 o 3 The content is 5wt%, and the content of phosphotungstic acid and ammonium salt is 20%. Wherein the molar ratio of ...

Embodiment 2

[0039]Weigh 13.3g of lanthanum nitrate, 15.6g of phosphotungstic acid, 182.2g of cetyltrimethylammonium bromide and 96g of citric acid to form a mixed solution, add 227mL tetraethyl orthosilicate to the mixed solution, and stir for 2 h, then stirred at 70°C until gelling, aging the gel at room temperature for 12 h, drying at 110°C for 8 h, and then roasting at 400°C for 3 h, adding the obtained solid into a C6 alkane solvent and immersing it for 10 min, Then filter, dry at room temperature until there is no liquid phase on the surface of the carrier, add it to an aqueous solution containing 15.6g of phosphotungstic acid and 13.3g of lanthanum nitrate, stir at 70°C until the solution is evaporated to dryness, and dry the obtained solid at 110°C for 8.0 h, and then calcined at 430°C for 3.0 h to prepare the catalyst, La 2 o 3 The content is 10wt%, and the content of phosphotungstic acid and ammonium salt is 30%. Wherein the molar ratio of cetyltrimethylammonium bromide to sili...

Embodiment 3

[0042] Weigh 13.3g of lanthanum nitrate, 12.1g of phosphotungstic acid, 243g of cetyltrimethylammonium bromide and 48g of citric acid to form a mixed solution, add 189mL tetraethyl orthosilicate into the mixed solution, and stir for 2 h , and then stirred at 70°C until it formed a gel. The gel was aged at room temperature for 12 h, dried at 110°C for 8 h, and then calcined at 420°C for 3 h. The resulting solid was added to a C6 alkane solvent and immersed for 10 min. Then filter, dry at room temperature until there is no liquid phase on the surface of the carrier, add it to an aqueous solution containing 26.6g of phosphotungstic acid and 24.2g of lanthanum nitrate, stir at 70°C until the solution is evaporated to dryness, and dry the obtained solid at 110°C for 8.0 h, and then calcined at 400°C for 3.0 h to prepare the catalyst, La 2 o 3 The content is 15wt%, and the content of phosphotungstic acid and ammonium salt is 35%. Wherein the molar ratio of cetyltrimethylammonium b...

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Abstract

The invention discloses a preparation method for a catalyst used for preparation of dimethyl ether through dehydration of methanol. The method comprises the following steps: adding heteropoly acid and a template agent into an aqueous solution containing organic acid so as to obtain a mixed solution, then adding a silicon source, uniformly mixing the silicon source with the mixed solution, carrying out stirring until a gel is formed and carrying out aging, drying and roasting so as to obtain a catalyst intermediate; and impregnating the catalyst intermediate with an alkane solvent at first and then with a heteropoly acid solution and carrying out drying and roasting so as to obtain the catalyst. According to the invention, the pore structure of the catalyst prepared by using the method can be improved; and surface active components of the catalyst are mainly composed of strongly acidic heteropoly acid and ammonium salts thereof, the dominated active component in the pore channel of the catalyst is an ammonium heteropoly acid salt with weak acidity, and thus, the catalyst has high conversion rate and selectivity, excessive cracking of products is avoided and high stability is obtained.

Description

technical field [0001] The invention relates to a preparation method of a catalyst for methanol dehydration to dimethyl ether, in particular to a preparation method of a loaded heteropolyacid (ammonium) salt catalyst for methanol dehydration to dimethyl ether. Background technique [0002] Dimethyl ether (Dimethy Ether, abbreviated as DME) is a colorless, non-toxic gas at normal temperature and pressure, which can be compressed into a liquid. Dimethyl ether is an important organic chemical raw material and chemical intermediate, which can be used in aerosols, refrigerants, alkylating agents, pharmaceuticals, cosmetics, fuels and other industries. [0003] Dimethyl ether was first produced by rectification of by-products in high-pressure methanol production, and soon developed into two processes of methanol dehydration and direct synthesis of synthesis gas. The liquid-phase method of methanol dehydration to produce dimethyl ether, the reaction is carried out in the liquid ph...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J31/26B01J31/18B01J31/16B01J35/10C07C43/04C07C41/09
Inventor 金浩孙素华朱慧红刘杰杨光
Owner CHINA PETROLEUM & CHEM CORP