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Device system and method for continuously producing alkoxy propane

A technology of alkoxypropane and feeding device, which is applied in separation methods, chemical instruments and methods, distillation separation, etc., can solve the problems of inability to directly obtain high-purity products, lower single-pass conversion rate, and high requirements for heat transfer equipment, and achieve Avoid ultra-low temperature or high vacuum operating conditions, high selectivity, low equipment investment and low energy consumption

Pending Publication Date: 2022-03-11
WANHUA CHEM (SICHUAN) CO LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although the product quality and purity of this scheme is relatively high (99%), the total yield is only 70%, and the recycled material contains more products, which inhibits the forward reaction to a certain extent and reduces the conversion rate per pass.
In addition, the resin needs to be regenerated, increasing the complexity of the system
[0009] In summary, at present, the main difficulties in the synthesis of alkoxypropane by the direct method of alcohol and ketone are reflected in the following aspects: 1. The reaction balance is limited, the single-pass conversion rate is low, and the reaction temperature is too low, and the heat transfer equipment requires high requirements. Second, the by-product water in the system will inhibit the positive shift of the equilibrium and reduce the reaction conversion rate. At the same time, the by-product water and the product are azeotropes, and the existing separation scheme cannot directly obtain high-purity products; Third, the raw material alcohol, The ketone and the product are azeotropes. The product refining process requires multiple azeotropic distillation or extractive distillation. The separation process is complicated, the number of equipment is large, and the investment is large.

Method used

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  • Device system and method for continuously producing alkoxy propane

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Embodiment 1

[0094] This embodiment provides a figure 1 The device system for the continuous production of alkoxypropane shown, the device system includes a feed unit connected in sequence, a packing reaction extraction tower 9 and a product refining tower 10;

[0095] The feeding unit includes an extraction agent feeding device and a raw material feeding device;

[0096] The extractant feeding device is connected with the extractant inlet at the bottom of the packing reaction extraction tower 9 towers;

[0097] The raw material feeding device is connected with the raw material inlet at the top of the packed reactive extraction tower 9;

[0098] The material outlet of the packing reactive extraction tower 9 is connected with the material inlet of the product refining tower 10 .

[0099] The extractant feeding device comprises an extractant storage tank 1, an extractant delivery pump 2 and an extractant heat exchanger 3 connected in sequence; the outlet of the extractant heat exchanger 3 ...

Embodiment 2

[0106] This embodiment provides a device system for the continuous production of alkoxypropane. The device system is the same as that of Embodiment 1 except that the number of theoretical plates of the plate distillation column is replaced by 55.

Embodiment 3

[0108] This embodiment provides a device system for the continuous production of alkoxypropane. In the device system, the plate rectification tower is changed to a packed rectification tower, and the number of theoretical plates of the packed rectification tower is changed to 50 , all the other are identical with embodiment 1.

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Abstract

The invention provides a device system and method for continuously producing alkoxy propane, and the method comprises the following steps: carrying out condensation reaction on a raw material solution in a filler reaction extraction tower under the action of a solid acid catalyst, and then carrying out countercurrent contact on the raw material solution and an extraction agent to obtain an extraction phase; and carrying out azeotropic distillation on the extract phase in a product refining tower to obtain a target product. According to the method, modified solid acid is used as a catalyst and is matched with an extracting agent, in-situ separation and removal of byproduct water and promotion of right shift of balance are realized through countercurrent contact, the retention time is short, and the conversion per pass can be improved; besides, in the rectification process, due to the existence of the extraction agent, the product separation process is greatly simplified, the number of equipment and energy consumption are remarkably reduced, and the extraction agent is low in price, easy to obtain, capable of being directly recycled and reused, free of subsequent treatment, green and environmentally friendly and has great market competitive advantages.

Description

technical field [0001] The invention belongs to the field of chemical synthesis, in particular to a device system and method for continuously producing alkoxypropane. Background technique [0002] As an important intermediate in the field of fine chemicals, alkoxypropane has the characteristics of high reactivity and strong water absorption due to its unique chemical structure. It is often used as a dehydrating agent, protective agent, condensation agent, and insecticide etc., playing an important role in fine chemical fields such as medicine, pesticide and spices. [0003] At present, the preparation methods of alkoxypropane mainly include indirect method and direct method. Among them, the direct method using alcohol and ketone as raw materials has obtained more advantages due to its cheap and easy-to-obtain raw materials, simple process flow, and easier realization of industrial production. Much favor. The alcohol-ketone condensation reaction is a reversible exothermic r...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J8/02B01D3/00B01D3/36B01D11/04C07C41/56C07C43/303
CPCB01D11/0488B01D3/009B01D3/36B01J8/0242C07C41/56B01D2011/002C07C43/303
Inventor 于丽君乔小飞隋东武杨颖赵一鸣贾峥瑞宋明焱孙犀璨顾鑫诚
Owner WANHUA CHEM (SICHUAN) CO LTD
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