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Process for synthesis of polyoxymethylene dimethyl ether from methyl

A technology of polyoxymethylene dimethyl ether and process method, which is applied in the technical field of synthesizing polyoxymethylene dimethyl ether from methanol, can solve the problems of high cost and low yield of synthetic process products, achieve high yield and selectivity, and convenient operation , the effect of low production cost

Active Publication Date: 2014-12-24
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0013] The technical problem to be solved by the present invention is the problem of high product cost and low yield of polyoxymethylene dimethyl ether synthesis process, and a new process for synthesizing polyoxymethylene dimethyl ether is provided, which has the characteristics of low product cost and high yield

Method used

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  • Process for synthesis of polyoxymethylene dimethyl ether from methyl
  • Process for synthesis of polyoxymethylene dimethyl ether from methyl
  • Process for synthesis of polyoxymethylene dimethyl ether from methyl

Examples

Experimental program
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Effect test

Embodiment 1

[0029] Fill 150g in fixed-bed reactor 5, silver-silica-alumina catalyst (composed of silver, silicon oxide and aluminum oxide in mass fraction ratio 18:75:7), fill 150g HZSM-5 molecular sieve (Si / Al=15), purging the device with nitrogen, the liquid phase methanol is heated, vaporized and mixed with air to feed the fixed bed reactor, the air volume space velocity is 4500h -1 , the feed rate of methanol is 93.75g / h, the operating temperature of the fixed-bed reactor is 600°C, and the pressure is 1MPa; at the same time, recycle anhydrous methanol and polyoxymethylene dimethyl ether (n= 1, 2, 5, 6) for the mixed solution, the feed rate is 62.5g / h and 109g / h respectively. The operating conditions of the bubble reactor 7 are a reaction temperature of 150° C. and a reaction pressure of 3.0 MPa. The reaction output enters the anion exchange resin bed layer.

[0030] The discharge material 9 of the bubbling reactor 7 passes through the anion exchange resin bed 10 to remove acid, and...

Embodiment 2

[0032] Fill 150g in the fixed-bed reactor 5, molybdenum-iron catalyst (composed of molybdenum oxide and iron oxide molar ratio 2.00:1), fill 300g strongly acidic styrene-based cation exchange resin in the bubble reactor 7, blow with nitrogen Sweeping device, the liquid phase methanol is heated, vaporized and mixed with air, and then fed to the fixed bed reactor, the air volume space velocity is 4500h -1 , the feed rate of methanol is 93.75g / h, the operating temperature of the fixed-bed reactor is 380°C, and the pressure is 1MPa; at the same time, recycle anhydrous methanol and polyoxymethylene dimethyl ether (n= 1, 2, 5, 6) for the mixed solution, the feed rate is 93.75g / h and 85.5g / h respectively. The operating conditions of the bubble reactor 7 were a reaction temperature of 110°C and a reaction pressure of 1.0 MPa. The reaction output enters the anion exchange resin bed layer.

[0033] Other operations are the same as in Example 1, continuous reaction for 80h, online samp...

Embodiment 3

[0035] Fill 150g in fixed-bed reactor 5, ferromolybdenum catalyst (composed of molybdenum oxide and iron oxide molar ratio 1.90:1), fill 300g dinitrobenzoic acid in bubble reactor 7, purging device with nitrogen, The liquid phase methanol is heated, vaporized and mixed with air, and then fed to the fixed bed reactor, the air volume space velocity is 4500h -1 , the feed rate of methanol is 93.75g / h, the operating temperature of the fixed-bed reactor is 380°C, and the pressure is 1MPa; at the same time, recycle anhydrous methanol and polyoxymethylene dimethyl ether (n= 1, 2, 5, 6) for the mixed solution, the feed rate is 93.75g / h and 106.1g / h respectively. The operating conditions of the bubble reactor 7 are a reaction temperature of 110° C. and a reaction pressure of 1.0 MPa. The reaction output enters the anion exchange resin bed layer.

[0036] Other operations are the same as in Example 1, continuous reaction for 80h, online sampling of the product, analysis by gas chromat...

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Abstract

The invention relates to a process for the synthesis of polyoxymethylene dimethyl ether from methyl, solves the problems of low cost and high yield in the synthesis of polyoxymethylene dimethyl ether. The process for the synthesis of polyoxymethylene dimethyl ether from methyl is divided into a reaction zone and a separation zone; the reaction zones includes a methanol storage tank, a preheater, a fixed bed reactor and a bubbling reactor; the process is the reaction zone is as below: methanol by is preheated, vaporized, mixed with air and sent into the fixed bed reactor, the methanol is subjected to catalytic oxidation under the action of a formaldehyde synthesis catalyst to generate formaldehyde; the formaldehyde enters into the bubbling reactor and reacts with methanol and a recycled mixture under the catalysis of a solid acid catalyst to form polyoxymethylene dimethyl ether. The separation zone includes an anion exchange resin bed, a rectification module and a product storage tank; and the process steps in separation zone are as below: the material discharged from the bubbling reactor passes through the anion exchange resin to remove acid and enters into the distillation separation module, trimer and tetramer of polyoxymethylene dimethyl ether enter into the product storage tank, and other components are recycled to the reactor. The technical scheme can be used in polyoxymethylene dimethyl ether production.

Description

technical field [0001] The invention relates to a process for synthesizing polyoxymethylene dimethyl ether from methanol. Background technique [0002] In recent years, low-carbon has become a major social theme and has gained increasing attention. For example, how to reduce the highly polluting exhaust emissions brought about by the booming automobile manufacturing industry and how to improve the efficiency of fuel oil use has become a research topic of many institutions. [0003] It is generally accepted that oxygenates are very suitable as diesel blending components. At present, many companies and research institutes are investing in finding and screening suitable oxygen-containing compounds, and the screening objects include: acetals, alcohols, carbonates, lipids, ethers, glycol derivatives, etc. For diesel, oxygenated compounds need to have high cetane number, low self-ignition point, and fast ignition. In addition, it should have good miscibility with ordinary diese...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C43/30C07C41/56
CPCY02P20/584C07C41/56C07C41/36C07C41/42C07C45/38C07C43/30C07C47/04
Inventor 高晓晨杨为民刘奕高焕新
Owner CHINA PETROLEUM & CHEM CORP
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