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
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
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.
PUM
| Property | Measurement | Unit |
|---|---|---|
| pore size | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
Login to View More - R&D
- Intellectual Property
- Life Sciences
- Materials
- Tech Scout
- Unparalleled Data Quality
- Higher Quality Content
- 60% Fewer Hallucinations
Browse by: Latest US Patents, China's latest patents, Technical Efficacy Thesaurus, Application Domain, Technology Topic, Popular Technical Reports.
© 2025 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap|About US| Contact US: help@patsnap.com



