The preparation method of (s)-(-)-1,1,2-triphenyl-1,2-ethanediol

A technology of ethylene glycol and triphenyl glycol, which is applied in the field of preparation of 1,1,2-triphenyl-1,2-ethylene glycol, can solve the limitation of mixing effect of the reactor, incomplete reaction, and recovery. In order to achieve the effect of improving conversion rate and product selectivity, precise temperature control, and improving reaction efficiency

Active Publication Date: 2021-03-02
常州沃腾化工科技有限公司
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Problems solved by technology

[0007] Most of the methods reported in the above literature use conventional reaction devices, most of the reaction time is very long, some even reach 50 hours, and the yield is generally not high. The reason for the analysis may be 1), due to the limitation of the mixing effect of the reactor, It is easy to produce incomplete reaction, resulting in a high proportion of impurity (S)-2-hydroxy-1,2-diphenylethanone in the product, and its structural formula is as follows (II); 2), after the reaction is completed, add When hydrochloric acid is quenched, the local acid concentration is too high, and dehydration side reactions occur, resulting in the generation of impurity 1,2,2-triphenylvinyl alcohol, whose structural formula is as follows ( )

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  • The preparation method of (s)-(-)-1,1,2-triphenyl-1,2-ethanediol

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Embodiment 1

[0018] Embodiment 1, after methyl mandelate and phenylmagnesium bromide are respectively dissolved in 2-methyltetrahydrofuran, the molar concentration is 0.5mol / L methyl mandelate solution and the molar concentration is 0.5mol / L phenyl bromide Magnesium solution; The methyl mandelate solution and the phenylmagnesium bromide solution that are made are imported into the first microchannel reactor by a metering pump and carry out the main reaction respectively, and the reaction solution obtained after the reaction directly flows into the second microchannel reactor, When the reaction solution flows into the second microchannel reactor, the hydrochloric acid aqueous solution is input into the second microchannel reactor through a metering pump to carry out the quenching reaction, and the reaction solution is obtained after the quenching reaction, and the reaction solution flows out in a state of continuous flow of highly dispersed phase To the receiver, separate the reaction liquid...

Embodiment 2

[0019] Embodiment 2, after methyl mandelate and phenylmagnesium bromide are respectively dissolved in 2-methyltetrahydrofuran, the obtained molar concentration is 0.5mol / L methyl mandelate solution and the molar concentration is 0.5mol / L phenyl bromide Magnesium solution; The methyl mandelate solution and the phenylmagnesium bromide solution that are made are imported into the first microchannel reactor by a metering pump and carry out the main reaction respectively, and the reaction solution obtained after the reaction directly flows into the second microchannel reactor, When the reaction solution flows into the second microchannel reactor, the sulfuric acid aqueous solution is input into the second microchannel reactor through a metering pump to carry out the quenching reaction, and the reaction solution is obtained after the quenching reaction is completed, and the reaction solution flows out in the state of continuous flow of highly dispersed phase To the receiver, separate...

Embodiment 3

[0020] Embodiment 3, after methyl mandelate and phenylmagnesium bromide are dissolved in 2-methyltetrahydrofuran respectively, it is 1mol / L methyl mandelate solution and molar concentration that 1mol / L phenylmagnesium bromide solution is obtained The obtained methyl mandelate solution and the phenylmagnesium bromide solution are input into the first microchannel reactor by a metering pump and carry out the main reaction respectively, and the reaction solution obtained after the reaction directly flows into the second microchannel reactor, When the solution flows into the second microchannel reactor, the nitric acid aqueous solution is input into the second microchannel reactor through a metering pump to carry out the quenching reaction. After the quenching reaction is completed, the reaction solution is obtained, and the reaction solution flows out to the receiver in the state of continuous flow of highly dispersed phase. In the container, the reaction liquid in the receiver wa...

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Abstract

The present invention relates to a preparation method of (S)-(-)-1,1,2-triphenyl-1,2-ethylene glycol, which is characterized in that methyl mandelate and phenylmagnesium bromide are respectively dissolved Make methyl mandelate solution and phenylmagnesium bromide solution after solvent; The methyl mandelate solution that makes and phenylmagnesium bromide solution are imported into the first microchannel reactor by a metering pump and carry out main reaction respectively, The reaction solution obtained after the reaction directly flows into the second microchannel reactor, and when the reaction solution flows into the second microchannel reactor, the acidic aqueous solution is input into the second microchannel reactor through a metering pump for quenching reaction, and the quenching reaction ends After obtaining the reaction solution, the reaction solution was separated into layers to take the organic phase, dried and concentrated under reduced pressure, and then recrystallized with toluene to obtain the finished product (S)-(-)-1,1,2-triphenyl-1 ,2‑ethylene glycol. The invention has the advantages of high yield and rapid reaction.

Description

technical field [0001] The invention relates to a preparation method of (S)-(-)-1,1,2-triphenyl-1,2-ethanediol, in particular to the preparation of (S)-(-)- 1,1,2-Triphenyl-1,2-ethanediol method. Background technique [0002] (S)-(-)-1,1,2-triphenyl-1,2-ethylene glycol is an important intermediate for the preparation of optically active medicines, pesticides and functional materials, and its structural formula is as follows ( ): [0003] [0004] Its main synthesis method is: in the solution of Grignard reagent phenylmagnesium bromide, slowly add the solution of methyl mandelate dropwise at a certain temperature, keep warm for reaction, and obtain the product after post-processing, the reaction formula is as follows: [0005] [0006] The main references are 1. Advanced Synthesis and Catalysis; vol. 352; nb. 14-15; (2010); p. 2611-2620: 0-20°C under the protection of inert gas in tetrahydrofuran solvent, reaction for 50h, post-processing to obtain the product ; 2. ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C33/26C07C29/36
CPCC07B2200/07C07C29/36C07C33/26
Inventor 李红功王明锋袁志伟
Owner 常州沃腾化工科技有限公司
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