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Method and device for synthetizing 4-hydroxy-2-butanone through catalytic reaction rectification

A technology for synthesizing butanone alcohol and catalyzing reaction, which is applied in chemical instruments and methods, preparation of organic compounds, separation/purification of carbonyl compounds, etc., can solve the problem of high energy consumption for separation and purification of fractionation tower, large loss of acetone, and long process flow and other problems, to achieve the effect of high temperature, reducing acetone loss and improving reaction yield

Active Publication Date: 2019-03-26
XIAMEN KINGDOMWAY VI TAMIN INC +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The method adopts first pretreatment followed by catalytic reaction and final rectification separation to synthesize butanone alcohol. This method can realize continuous production, but its process flow is long and the equipment is complicated
At the same time, this method improves the conversion rate of formaldehyde by increasing the molar ratio of acetone to formaldehyde, but excessive acetone will condense to form more diacetone alcohol by-products, and in addition, excessive acetone needs to be recovered and used mechanically, which will lead to separation and purification of subsequent fractionation towers High energy consumption, large loss of acetone, high production cost

Method used

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  • Method and device for synthetizing 4-hydroxy-2-butanone through catalytic reaction rectification
  • Method and device for synthetizing 4-hydroxy-2-butanone through catalytic reaction rectification
  • Method and device for synthetizing 4-hydroxy-2-butanone through catalytic reaction rectification

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Embodiment approach

[0043]According to a preferred embodiment of the present invention, the method for synthesizing butanone alcohol by catalytic reaction rectification also includes condensing the unreacted acetone separated and purified from the rectifying section 11, and then partially returning it to the catalytic reaction The tower top of the rectifying tower 1 can provide cooling capacity for gas-liquid mass transfer and heat transfer in the catalytic reaction rectifying tower 1 tower, so as to ensure the purity of the acetone produced at the tower top. At this time, the reflux ratio of the catalytic reaction distillation column 1 is preferably (0.8-2):1, more preferably (1-1.6):1, and most preferably (1.2-1.4):1. The term "reflux ratio" refers to the ratio of the reflux flow to the production flow.

[0044] According to a preferred embodiment of the present invention, the method for synthesizing butanone alcohol by catalytic reaction rectification also includes returning the part of butano...

Embodiment 1

[0054] The diameter of the catalytic reaction rectification tower 1 is 300mm, wherein, the rectification section 11 is filled with BX500 wire mesh corrugated packing and the filling height is 5000mm, and the calculated theoretical plate number is 12; the catalytic section 12 is filled with packed KF / Al 2 o 3 MULTIPAK catalytic rectification structured packing with solid base catalyst (KF / Al 2 o 3 The weight ratio of the solid base catalyst to the MULTIPAK catalytic rectification structured packing is 1.7:1), the packing height is 3000 mm, and the calculated theoretical plate number is 5; the stripping section 13 is filled with BX500 wire mesh corrugated packing and the packing height is 2400 mm, The calculated theoretical plate number is 6. Formaldehyde enters from the upper part of the catalytic section 12 after being preheated to 80°C by the first preheater 2, and the flow rate is 100kg / h; acetone enters from the lower part of the catalytic section 12 after being preheated...

Embodiment 2

[0056] The diameter of the catalytic reaction rectification tower 1 is 300mm, wherein, the rectification section 11 is filled with BX500 wire mesh corrugated packing and the filling height is 4000mm, and the calculated theoretical plate number is 10; the catalytic section 12 is filled with packed KF / Al 2 o 3 KATAPAK Catalytic Distillation Structured Packing with Solid Base Catalyst (KF / Al 2 o 3 The weight ratio of the solid base catalyst to the KATAPAK catalytic rectification structured packing is 1.6:1), the packing height is 3200mm, and the calculated theoretical plate number is 5; the stripping section 13 is filled with BX500 wire mesh corrugated packing and the packing height is 2800mm, The calculated number of theoretical plates is 7. Formaldehyde enters from the upper part of the catalytic section 12 after being preheated to 80°C by the first preheater 2, and the flow rate is 100kg / h; acetone enters from the lower part of the catalytic section 12 after being preheated ...

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Abstract

The invention belongs to the field of compound preparation, and concretely discloses a method and device for synthetizing 4-hydroxy-2-butanone through catalytic reaction rectification. The method forsynthetizing 4-hydroxy-2-butanone through catalytic reaction rectification is performed in the device for synthetizing 4-hydroxy-2-butanone through catalytic reaction rectification. The device comprises a catalytic reaction rectification tower (1), wherein the catalytic reaction rectification tower (1) comprises a rectification section (11), a catalysis section (12) and a stripping section (13) from top to bottom; formaldehyde and acetone are subjected to catalytic reaction in the catalysis section (12) to generate the 4-hydroxy-2-butanone; light ingredients in catalytic reaction products ascend to the rectification section (11) for separation and purification so as to obtain unreacted acetone; heavy ingredients in the catalytic reaction products sink to the stripping section (13) for separation and rectification so as to obtain the 4-hydroxy-2-butanone. When the method and device provided by the invention are used for synthetizing the 4-hydroxy-2-butanone, the reaction yield can be improved; the acetone loss is reduced; the reaction heat of catalytic reaction can be fully utilized; the subsequent separation energy consumption is low; the technological process is simplified; the production cost is reduced.

Description

technical field [0001] The invention belongs to the field of compound preparation, and in particular relates to a method and a device for synthesizing butanone alcohol by catalytic reaction rectification. Background technique [0002] Butanone alcohol, chemical name 4-hydroxy-2-butanone, has both hydroxyl and carbonyl groups in its molecule. It is an important intermediate for the synthesis of vitamin A. Its structural formula is as follows: [0003] [0004] Butanone alcohol can be obtained by the reaction of formaldehyde and acetone, wherein, because the two raw materials of formaldehyde and acetone are easy to get, the cost of synthesizing butanone alcohol is relatively low, so this method has become the main method for preparing butanone alcohol. The specific reaction equation is as follows: [0005] [0006] CN1120831C discloses the method of using basic anion exchange resin to catalyze the synthesis of butanone alcohol. In the method, butanone alcohol is synthe...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C45/72C07C49/17C07C45/78
CPCC07C45/72C07C45/78C07C49/17Y02P20/10
Inventor 陈世豪高鸿鹏潘必文
Owner XIAMEN KINGDOMWAY VI TAMIN INC
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