Method for manufacturing dimethyl ether with solid acid catalysis methanol dehydration reaction

A technology of solid acid catalysis and solid acid catalyst, which is applied in the dehydration of hydroxyl-containing compounds to prepare ethers, chemical instruments and methods, molecular sieve catalysts, etc. It can solve uneven temperature distribution, difficult large-scale chemical industrial production, and difficult catalyst bed temperature, etc. question

Active Publication Date: 2008-01-23
YANCHANG ZHONGKE (DALIAN) ENERGY TECH CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Dimethyl ether was first produced by methanol dehydration, and the reaction was carried out in the liquid phase. The main disadvantages are severe equipment corrosion, harsh operating conditions, and serious environmental pollution.
In industrial production, there are problems such as difficult control of catalyst bed temperature or uneven temperature distribution, so it is difficult for large-scale chemical industrial production

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0028] Embodiment 1: Dehydration of fixed-bed methanol to produce dimethyl ether

[0029] Catalyst is the same as Comparative Example 1. 2500 milliliters of catalyst was loaded into a fixed-bed reactor with an inner diameter of 37 mm, and there were four injection points of chilled materials along the axial direction of the catalyst bed section of the reactor. Temperature is 125 ℃ of liquid methanol (purity is 97.5% (weight)) at space velocity 0.102 hours -1 Evenly injected into the reactor.

[0030] At a reactor inlet temperature of 210°C, a reaction pressure (gauge pressure) of 1.1MPa, and a methanol feed space velocity of 3 hours -1 Under the above conditions, the conversion rate of methanol is 75.1%, the selectivity of dimethyl ether is ~100%, the outlet temperature of the bed is 220°C, the highest temperature point of the bed is 225.1°C, and the average temperature of the bed is 215.6.

Embodiment 2

[0031] Embodiment 2: Dehydration of fixed-bed methanol to produce dimethyl ether

[0032] Catalyst, reactor, methanol raw material, quenching material are the same as embodiment 1.

[0033] At a reactor inlet temperature of 225°C, a reaction pressure (gauge pressure) of 1.1MPa, and a methanol feed space velocity of 3 hours -1Under the above conditions, the conversion rate of methanol is 86.2%, the selectivity of dimethyl ether is 99.99%, the outlet temperature of the bed is 237°C, the highest temperature point of the bed is 241.0°C, and the average temperature of the bed is 232.2°C.

Embodiment 3

[0037] Embodiment 3: Dehydration of fixed-bed methanol to produce dimethyl ether

[0038] Catalyst, reactor and methanol raw material are the same as Comparative Example 3.

[0039] At a reactor inlet temperature of 140°C, a reaction pressure (gauge pressure) of 1.0 MPa, and a methanol feed space velocity of 2.0 hours -1 Under the above conditions, the conversion rate of methanol is 66.1%, the selectivity of dimethyl ether is ~100%, the outlet temperature of the bed is 145.0°C, the highest temperature point of the bed is 150.2°C, and the average temperature of the bed is 142.1°C.

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PUM

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Abstract

A method that the solid acid catalyzes the methanol to dehydrate and react to produce the dimethyl ether is provided. Under the condition that the solid acid catalyst exists, the liquid state materials are adopted as the chill materials to control the catalyst bed temperature distribution. The reaction conditions are that the reaction pressure is 0.2MPa to 4.0 MPa, the reaction temperature is 120 DEG C. to 400 DEG C. and the feeding air speed is 0.5 to 20.0. The solid acid catalysts are the cation exchange resin, the ZSM-5 molecular sieve, the ZSM-35 molecular sieve, the MCM-22 molecular sieve, Gamma-alumina or the mixture of the above. The invention can make the bed temperature rapidly lower in the range set by the process via filling the cold-shocking materials. Because the catalyst bed temperature is distributed evenly, the invention greatly reduces the occurrence of the side-effects and the carbon deposit on the catalysts and prolongs the service life of the catalysts.

Description

technical field [0001] The invention relates to a method for producing dimethyl ether from methanol, in particular to a method for continuously producing dimethyl ether by using a solid acid catalyst and dehydrating methanol in gas phase. Background technique [0002] Dimethyl ether is a widely used chemical product and fuel substitute. Dimethyl ether was first produced by methanol dehydration, and the reaction was carried out in the liquid phase. The main disadvantages were severe equipment corrosion, harsh operating conditions, and serious environmental pollution. At present, the production of dimethyl ether by dehydration of methanol with solid acid catalyst is the main method and future development trend in industry. [0003] USP6740783 discloses a molecular sieve catalyst for the production of dimethyl ether from methanol. The protons on the molecular sieve catalyst are replaced by metals or amines, and methanol vapor is dehydrated on the molecular sieve catalyst. [...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C41/09C07C43/04B01J29/04B01J31/08
Inventor 刘中民朱书魁孙新德许磊吕志辉杨虹熠杨越
Owner YANCHANG ZHONGKE (DALIAN) ENERGY TECH CO LTD
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