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A kind of preparation method of 2,2,3,3-tetrafluoropropanol

A technology of tetrafluoropropanol and tetrafluoroethylene, which is applied in the field of preparation of 2,2,3,3-tetrafluoropropanol, can solve the problems of strict requirements for large-scale production equipment, high investment and maintenance costs, and avoid Amplify the effect, improve the utilization rate, and avoid the effect of gas leakage

Inactive Publication Date: 2019-08-09
李晖 +2
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0006] In view of this, the purpose of the present invention is to provide a preparation method of 2,2,3,3-tetrafluoropropanol without using high-temperature and high-pressure equipment, so as to solve the problem of using high-pressure and high-temperature equipment and large-scale production equipment in the prior art Strict requirements, high input and maintenance costs, simplified operation process, reduced energy consumption and production costs, expanded scope of application, and improved the conversion rate of methanol and the yield of 2,2,3,3-tetrafluoropropanol

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preparation example Construction

[0027] The invention provides a kind of preparation method of 2,2,3,3-tetrafluoropropanol, described preparation method is carried out in microchannel reactor, comprises the following steps:

[0028] (1) methanol is mixed with a free radical initiator to obtain a mixed solution;

[0029] (2) The mixed solution obtained in the step (1) and the tetrafluoroethylene are respectively preheated and then mixed to carry out a polymerization reaction to obtain 2,2,3,3-tetrafluoropropanol.

[0030] The preparation method provided by the invention is carried out in a microchannel reactor. see Figure 5 , specifically, the microchannel reactor comprises a first feed port (1), a second feed port (2), a first preheating module (3), a second preheating module (4), a mixing module, A reaction module, a heat exchanger, and a discharge port, the first feed port (1) is connected to the first preheating module (3) in sequence, and the second feed port (2) is connected to the first Two preheati...

Embodiment 1

[0046] according to figure 1 Shown 2,2,3, the synthetic process flowchart of 3-tetrafluoropropanol, utilize image 3 The device diagram of the microchannel equipment, the device used is a high-throughput microchannel reactor (straight channel module + heart-shaped channel module), refer to Figure 5 The connection mode of the microchannel reactor is determined, the data flow rate and reaction residence time of the mixed reaction module are determined, and the heat conduction medium is silicone oil.

[0047] Store methanol and diisopropyl peroxydicarbonate as a solution in advance in a storage tank, store tetrafluoroethylene in another storage tank, and set the flow rate ratio of the metering pump to diisopropyl peroxydicarbonate:methanol : Tetrafluoroethylene is 38g: 95g: 370g, the materials are respectively passed into the straight channel preheating module, diisopropyl peroxydicarbonate and methanol are preheated at 20°C for 10s, tetrafluoroethylene is preheated at 70°C Fo...

Embodiment 2

[0049] according to figure 1 Shown 2,2,3, the synthetic process flowchart of 3-tetrafluoropropanol, utilize image 3 The device diagram of the microchannel equipment, the device used is a high-throughput microchannel reactor (straight channel module + heart-shaped channel module), refer to Figure 5 The connection mode of the microchannel reactor is determined, the data flow rate and reaction residence time of the mixed reaction module are determined, and the heat conduction medium is silicone oil.

[0050] Store methanol, tert-butyl hydroperoxide and diisopropyl peroxydicarbonate as a solution in advance in a storage tank, store tetrafluoroethylene in another storage tank, and set the flow rate ratio of the metering pump to tert-butyl peroxide. Hydrogen peroxide, diisopropyl dicarbonate: methanol: tetrafluoroethylene is 86g: 164g: 560.7g: 350g, and the materials are respectively passed into the straight channel preheating module, and the temperature of the heat exchanger is ...

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Abstract

The invention provides a preparation method of 2,2,3,3-tetrafluoropropanol, belonging to the technical field of organic synthesis. In a continuous flow microchannel reactor, a free-radical initiator, methanol and tetrafluoroethylene are mixed, heated and subjected to polymerization reaction to finally obtain the 2,2,3,3-tetrafluoropropanol on the premise of avoiding scale-up effect; the method shortens the reaction time to tens of seconds to several minutes, enhances the reaction efficiency, effectively avoids the severe problems of gas leakage and the like in the additional configuration and transfer demanded by the conventional intermittent reaction, does not use any high-temperature high-pressure apparatus, solves the problems of demands for the high-temperature high-pressure apparatus, strict requirements for large-scale production devices, and high investment and maintenance cost in the prior art, simplifies the operating technique, lowers the energy consumption and production cost, widens the application range, and is suitable for industrialized scale-up recovery; and the yield of the 2,2,3,3-tetrafluoropropanol is up to 96%.

Description

technical field [0001] The invention relates to the technical field of organic synthesis, in particular to a preparation method of 2,2,3,3-tetrafluoropropanol. Background technique [0002] 2,2,3,3-Tetrafluoropropanol, commonly known as tetrafluoropropanol, CAS No. 76-37-9, is an important chemical raw material for the preparation of fluorine-containing acrylic resins and some fluorine-containing resins, and is also an important organic intermediate. [0003] The general reaction principle of 2,2,3,3-tetrafluoropropanol is described in the following formula: [0004] [0005] The conventional preparation process requires the use of high-pressure and high-temperature equipment, strict requirements for large-scale production equipment, high investment and maintenance costs, and the disadvantages of low efficiency and low yield. For example, the document React.Kinet.Catal.Lett., 107-114, 63, 1, (1998) reported a method for synthesizing tetrafluoropropanol by telomerization...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C29/62C07C29/44C07C31/38B01J19/00
CPCB01J19/0093C07C29/44C07C29/62C07C31/38
Inventor 李晖俞浙军丁尊良
Owner 李晖