Micro-interface preparation system and method of 1, 4-butanediol
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A preparation system, butanediol technology, applied in the field of butanediol production, can solve the problems of catalyst waste, increase of production cost, uniform mixing of hydrogen, etc., to increase the mass transfer area of phase boundary, reduce temperature and pressure, and improve reaction efficiency effect
Pending Publication Date: 2022-05-17
NANJING YANCHANG REACTION TECH RES INST CO LTD
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Problems solved by technology
[0008] 1. In order to promote the reaction in the hydrogenation section, manufacturers will increase the amount of catalyst, which increases the production cost
[0009] 2. Due to the increase in the amount of catalyst in the hydrogenation section, incomplete catalyst reaction often occurs, and the remaining catalyst is wasted, and after entering the follow-up system, it will affect the normal production of the follow-up system
[0010] 3. During the mixing process of hydrogen and slurry, there will still be a dead angle of stirring, and there will still be problems of uneven stirring between hydrogen, catalyst and slurry, resulting in insufficient reaction in the hydrogenation section and affecting the output of 1,4-butanediol
[0011] 4. Stirring cannot break or completely break the hydrogen bubbles, and the hydrogen cannot be mixed evenly with the slurry
Method used
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Embodiment 1
[0059] refer to figure 1 Shown is a schematic structural view of the micro-interface preparation system for 1,4-butanediol provided by the present invention, which includes a mixing tank 10, a heat exchanger 20, a monoesterification reactor 30, a diesterification reactor 40, and a Hydrogen reactor 50 , flash tower 60 , methanol rectification tower 70 , dimethyl maleate rectification tower 80 and 1,4-butanediol rectification tower 90 .
[0060] Methanol is transported to the mixing tank 10 through the feed pump 11 and the methanol feed pipeline 13, and the maleic anhydride is transported to the mixing tank 10 through the maleic anhydride feed pipeline 12. In the mixing tank 10, methanol and maleic anhydride are fully mixed, and then the mixed materials It is sent to the heat exchanger 20, one end of the heat exchanger 20 delivers low-pressure steam, and the other end discharges the process water after heat exchange. The mixed material heated to 75° C. is sent to the monoesteri...
Embodiment 2
[0069] Other operating steps are the same as in Example 1, the only difference is that there is only a pneumatic micro-interface generator inside the hydrogenation reactor.
Embodiment 3
[0071] Other operating steps are the same as in Example 1, the only difference is that there is only a hydraulic micro-interface generator inside the hydrogenation reactor.
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Abstract
The invention provides a micro-interface preparation system of 1, 4-butanediol, which comprises a mixing tank, the mixing tank is connected with a methanol feeding pipeline and a maleic anhydride feeding pipeline, and the mixing tank is sequentially connected with a heat exchanger, a single esterification reactor, a double esterification reactor, a hydrogenation reactor, a flash tower, a methanol rectifying tower, a dimethyl maleate rectifying tower and a 1, 4-butanediol rectifying tower. A product outlet is formed in the 1, 4-butanediol rectifying tower, a gas-liquid linkage type micro-interface generator is arranged in the hydrogenation reactor, and the gas-liquid linkage type micro-interface generator is connected with a hydrogen inlet pipeline and a circulating pump. Hydrogen is dispersed and broken into hydrogen microbubbles through the gas-liquid linkage type micro-interface generator, the gas-liquid two-phase mass transfer area is increased, and due to the fact that the gas-liquid linkage type micro-interface generator has the circulating stirring function, the hydrogen can better react with mixed liquid in the hydrogenation reaction process, and the hydrogenation reaction is more sufficient.
Description
technical field [0001] The invention belongs to the technical field of butanediol production, and in particular relates to a micro-interface preparation system of 1,4-butanediol. Background technique [0002] 1,4-butanediol is one of the methanol series product chains, and is an important basic organic chemical and fine chemical raw material. In the process of producing 1,4-butanediol, manufacturers generally do not use 1,4 - Butanediol is the final product, but focus on the extension of 1,4-butanediol derivatives, 1,4-butanediol derivatives are fine chemical products with high added value, widely used as solvents, medicines, cosmetics , plasticizers, curing agents, pesticides, herbicides, foamed artificial leather, fibers and engineering plastics, etc.; due to the wide range of uses and large amounts of 1,4-butanediol products, the 1,4-butanediol Production technology needs to be continuously improved. [0003] The production methods of 1,4-butanediol mainly include: (1) ...
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