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Production method of tetrahydrofuran

A technology for tetrahydrofuran and a production method, applied in the chemical industry, can solve the problems of low dehydration efficiency, shorten the service life of catalysts, corrode equipment and the like, and achieve the effects of high separation and dehydration efficiency, improvement of dehydration efficiency, and reduction of production energy consumption

Pending Publication Date: 2022-07-15
CHINA CHEM TECH RES INST
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Among them, the use of inorganic acid as a catalyst has the risk of corroding equipment, and there are many side reactions and complicated processes; the use of solid acid as a catalyst has a high reaction temperature, and the polymerization of product tetrahydrofuran at high temperature and high concentration will increase the amount of tar; using strong acid As a catalyst, cation exchange resin has low reaction temperature and few side reactions, but the conversion rate of 1,4-butanediol is low. If the reaction temperature is increased to increase the conversion rate of raw materials, the service life of the catalyst will be reduced
A large amount of 1,4-butanediol, tetrahydrofuran and the by-products generated during the reaction process are discharged in the form of tar and incinerated, which will cause waste of materials and poor atom economy.
In the separation process of tetrahydrofuran, the combination of high and low pressure rectification towers is commonly used for dehydration, and this method requires a large amount of THF to circulate between the two rectification towers, resulting in high energy consumption for refining and low dehydration efficiency.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0070] In the production system of tetrahydrofuran provided in the embodiment of the present invention, the equipment conditions of the dividing wall reactor are: the catalyst loading height is equivalent to 10 theoretical trays, the number of trays in the first stripping section D1 is 25, and the second stripping section D1 has 25 trays. The number of trays in section D2 is 15, the number of trays in the third stripping section D3 is 5, and the distance between the position of the catalytic reaction section R1 close to the gas-phase product outlet and the position of the partition structure 101 close to the gas-phase product outlet is equivalent to 1 ~ There are 3 trays, so that the 1,4-butanediol will not be brought into the first stripping section D1 by the gas phase, thereby achieving the effect of separating the 1,4-butanediol and the water phase containing tetrahydrofuran. Wherein, the distance between the part of the catalytic reaction section R1 close to the gas phase p...

Embodiment 2

[0078] The equipment conditions of the above-mentioned dividing wall reaction tower are the same as those in Example 1.

[0079] The equipment conditions of the dividing wall reactor are: the pressure at the top of the tower is 0.2Mpa, the feed temperature of 1,4-butanediol is 120°C, and the liquid hourly space velocity of the dehydration cyclization reaction is 3h -1 , the average temperature of the reaction is 120 ℃, the reflux ratio is 0.3, the temperature of the water outlet on the lower side of the auxiliary tower space is 134 ℃, and the temperature of the tower still is 165 ℃.

[0080] The operating conditions of the fixed bed reactor are as follows: the reaction pressure for dehydration cyclization is 3Mpa, the reaction temperature is 300°C, and the liquid hourly space velocity is 4h -1 .

[0081] The operating conditions of the flash tank are: the pressure is 0.2Mpa.

[0082] The operating conditions of the separation device 200 are: the absolute pressure controlled ...

Embodiment 3

[0086] The same equipment conditions and operating conditions are set as in Example 1, except that the separator in the dividing wall reaction tower is provided with a TOY30-21 selective permeable membrane.

[0087] The ratio of the waste water volume of the first waste water pipe P1 of the dividing wall reactor to the waste water volume of the second waste water pipe P2 of the separation device 200 is 1:1. In the dividing wall type reactor, the conversion rate of 1,4-butanediol is 99%. , the conversion rate of 1,4-butanediol in the fixed bed reactor is 100%, the total tetrahydrofuran selectivity is 99.6%, the purity of tetrahydrofuran recovered by the refining tower 500 is 99.9%, and the water content is less than 100ppm. The overhead heat load of the dividing wall reactor is 310KW.

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Abstract

The invention discloses a production method of tetrahydrofuran, relates to the field of chemical engineering, and aims to solve the problems of high refining energy consumption and low dehydration efficiency during tetrahydrofuran production. The production method of tetrahydrofuran comprises the following steps: under the blocking of a dividing wall structure, feeding a raw material at least containing 1, 4-butanediol into a catalytic reaction section, and then carrying out a first dehydration cyclization reaction on 1, 4-butanediol in the catalytic reaction section by adopting a solid acid catalysis mode, a first gas-phase product and a first liquid-phase product at least comprising a first water phase containing tetrahydrofuran are obtained. Wherein the first water phase enters the first stripping section through the dividing wall structure, and a second gas phase product is separated from the first water phase by utilizing the first stripping section. And finally, feeding the first gas-phase product and the second gas-phase product into a separation device from a gas-phase product outlet of the dividing wall type reactor, and separating tetrahydrofuran from the first gas-phase product and the second gas-phase product by using the separation device. The tetrahydrofuran production method provided by the invention is used for producing tetrahydrofuran.

Description

technical field [0001] The invention relates to the chemical field, in particular to a production method of tetrahydrofuran. Background technique [0002] Tetrahydrofuran is an important organic chemical raw material with high polarity, low boiling point, low toxicity and other excellent properties, so it is called a universal solvent. Among them, 1,4-butanediol dehydration cyclization is the most important method for preparing tetrahydrofuran. [0003] At present, the commonly used catalysts for the preparation of tetrahydrofuran by dehydration of 1,4-butanediol are inorganic acids, strongly acidic cation exchange resins or solid acids. Among them, the use of inorganic acid as a catalyst has the risk of corroding equipment, and has many side reactions and complicated processes; using solid acid as a catalyst has a high reaction temperature, and the polymerization of the product tetrahydrofuran at high temperature and high concentration will lead to an increase in the amoun...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07D307/08B01D3/00
CPCC07D307/08B01D3/009
Inventor 冷炳文梁武洋张小明李向阳
Owner CHINA CHEM TECH RES INST
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