Catalytic reaction, rectification integrated technique and special-purpose equipment

A catalytic reaction and rectification technology, which is applied in the direction of unsaturated compound addition to ether, chemical industry, hydroxyl addition preparation, etc., can solve the problems of increased operating cost, low production efficiency, equipment corrosion, etc., and achieve the reaction conversion rate Improvement, reduction of corrosion of equipment, and improvement of productivity

Inactive Publication Date: 2008-09-03
NANJING UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The disadvantages of these production methods are many: if batch operation is adopted, the production efficiency is low, the sulfuric acid catalyst corrodes the equipment seriously, the catalyst needs to be neutralized with alkali from the product, the catalyst cannot be reused, etc.; if the solid acid catalyst fixed bed reaction process is adopted , then not only the reaction time is long, the conversion rate is low (usually about 50%), and the raw material butanol needs to be excessive, which causes the difficulty of butanol separation after the reaction and increases the operating cost
For these reasons, the one-time investment and maintenance costs of the device are high

Method used

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  • Catalytic reaction, rectification integrated technique and special-purpose equipment
  • Catalytic reaction, rectification integrated technique and special-purpose equipment
  • Catalytic reaction, rectification integrated technique and special-purpose equipment

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0033] Embodiment 1: Esterification produces butyl acetate (three tower system)

[0034] The production device is shown in Figure 1. The catalytic reaction and rectification integrated tower T-01 has a diameter of 0.4 meters and a total height of 12 meters, of which the height of the reaction section 6 is 1.5 meters, the height of the rectification section 4 is 4.5 meters, and the stripping section 9 and The height of the tower kettle is 6 meters, and the catalyst adopts high temperature resistant strong acid ion exchange resin. The height of the dehydration tower T-02 is 9 meters, of which the height of the rectification section is 3 meters, and the height of the stripping section and the tower kettle is 6 meters. The height of T-03 is 26 meters, of which the rectification section is 10 meters high, and the stripping section and tower still are 16 meters high. The operation process is as follows:

[0035] The ratio of the amount of acetic acid and n-butanol is 1:1.1 and ent...

Embodiment 2

[0039] Embodiment 2: hydration reaction produces dihydromyrcenol (three tower system)

[0040] Using dihydromyrcene as a raw material, it reacts with water under the action of an acidic catalyst to produce dihydromyrcenol, a high-grade fragrance raw material. Catalytic reaction and rectification integrated tower T-01 has a diameter of 1.2 meters and a total height of 28 meters, of which the height of reaction section 6 is 2.5 meters, the height of rectification section 4 is 14.5 meters, the height of stripping section 9 and tower still is 11 meters, and the catalyst High temperature resistant strong acid ion exchange resin is used. The height of T-02 is 25 meters, of which the rectification section is 10 meters high, and the stripping section and tower still are 15 meters high. The height of T-03 is 36 meters, of which the rectification section is 16 meters high, and the stripping section and tower still are 20 meters high. The operation process is as follows:

[0041] The ...

Embodiment 3

[0045] Embodiment 3: methanol and isobutylene etherification reaction produces MTBE (two tower system)

[0046] Using methanol and isobutylene as raw materials, using AMBERLYST-15 catalyst (provided by Tianjin Weide International Trade Co., Ltd.), the important chemical methyl tert-butyl ether (MTBE for short) can be obtained through etherification. The catalytic reaction and rectification integrated tower T-01 used in this embodiment has a diameter of 0.3 meters and a total height of 18 meters, wherein the height of the reaction section 6 is 1.2 meters, the height of the rectification section 4 is 8 meters, and the height of the stripping section 9 and the tower still It is 8.8 meters. The height of the dehydration tower T-02 is 35 meters, of which the height of the rectification section is 15 meters, and the height of the stripping section and the tower kettle is 20 meters. Its operation process is as follows:

[0047]After the liquid-phase industrial-grade methanol is hea...

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Abstract

A catalytic reaction / rectification integrated process is provided, which includes: reaction raw materials are pre-heated and then mixed with catalysts; the resulting mixture is fed into a jet mixing reaction section 6 of a catalytic reaction / rectification integrated tower through a feed port, wherein the jet mixing reaction section 6 is a kettle-like reactor in the middle of the catalytic reaction / rectification integrated tower T-01; after the reaction raw materials are pressurized by a centrifugal pump, a subsonic or transonic jet mixer 33 inside the jet mixing reaction section 6 jets the reaction raw materials at a high speed into the jet mixing reaction section 6 and performs high-efficiency mixing of solid and liquid phases inside the jet mixing reaction section 6, thereby enhancing the heat and the mass transfer efficiencies during the process; the reaction mixture is directly separated and purified inside the catalytic reaction / rectification integrated tower. Therefore, the catalytic reaction / rectification integrated process has high conversion rate and production capacity and low energy consumption and production cost. The process is used for esterification, alcohol synthesis from alkenes and water, and the ether synthesis from alkenes and alcohols. A special catalytic reaction / rectification integrated tower is also provided.

Description

field of invention [0001] The invention relates to a novel catalytic reaction rectification integrated process, in particular, it relates to two processes of catalytic reaction and rectification separation. Background technique [0002] Ethyl formate, ethyl acetate, butyl acetate, methyl lactate, methyl tert-butyl ether and other esters and ethers are important chemical raw materials in the chemical industry. Esters such as ethyl acetate and butyl acetate can It can be used as raw materials for coatings, spices, organic synthesis intermediates and as a solvent for various organic compounds; it can also be used as an extractant in various petroleum processing and pharmaceutical processes, and can also be used as a component of flavoring agents, etc. Methyl lactate is also an important organic chemical raw material and an important fine chemical, widely used in food, beverage, pharmaceutical and other industries. Methyl lactate is non-toxic, has good solubility, is not volati...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J8/10B01D3/14
CPCB01J8/085B01D3/009B01J8/125B01J2219/00006C07C29/04C07C41/06C07C67/08Y02P20/10C07C33/025C07C43/04C07C69/14
Inventor 张志炳周政吴有庭邵旻
Owner NANJING UNIV
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