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Method for removing acetic acid from DMF solution of sucrose-6-ethyl ester

A technology of acetic acid and solution, applied in separation methods, chemical instruments and methods, sugar derivatives, etc., can solve problems such as increased processing difficulty, raw material consumption cost, complicated separation process, and difficult to handle solid reaction products

Pending Publication Date: 2021-06-15
TIANJIN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] Chinese patent CN107459540A discloses a method to remove acetic acid by adding alkali to neutralize the acid-base reaction until the pH is 6-8. This process will generate sodium acetate as a solid by-product, which increases the difficulty of treatment.
[0007] Therefore, comprehensive prior art method, there is the raw material consumption cost that adds the 3rd kind of medium to bring and the complication of corresponding separation process, and the problem such as difficult handling of the reaction solid product that produces, need to invent a kind of not adding the 3rd kind of medium, does not need to invent Generate solid waste, a new energy-saving and environmentally-friendly method to remove acetic acid from sucrose-6-ethyl ester DMF solution, so that the production process can achieve simple, efficient and environmentally friendly goals

Method used

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  • Method for removing acetic acid from DMF solution of sucrose-6-ethyl ester

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0030] (1) The sucrose-6-ethyl ester solution containing DMF, acetic acid and water is sent to the dehydration tower T101 for rectification, and the total feed rate is 1000kg / hr. The operating pressure of the dehydration tower T101 is -0.095Mpa, and the operating temperature is 78°C. The condensate at the top of the tower is withdrawn as waste water. The tower still liquid phase is connected to the tower still reboiler for vaporization, and part of the tower still liquid is sent to the T102 stripping tower.

[0031] (2) The discharge from the T101 tower kettle enters the top of the stripper T102 tower, and the steam of DMF is introduced into the bottom of the stripper tower, and the gas and liquid are countercurrently contacted in the tower. The operating pressure of the stripper T102 is -0.095Mpa, and the operating temperature is 56 ℃. The sucrose-6-ethyl ester solution containing DMF is obtained from the bottom of the stripping tower T102, and the mixture of DMF and acetic...

Embodiment 2

[0035] (1) The sucrose-6-ethyl ester solution containing DMF, acetic acid and water is sent to the dehydration tower T101 for rectification, and the total feed rate is 1000kg / hr. The operating pressure of the dehydration tower T101 is -0.099Mpa, and the operating temperature is 60°C. The condensate at the top of the tower is withdrawn as waste water. The tower still liquid phase is connected to the tower still reboiler for vaporization, and part of the tower still liquid is sent to the T102 stripping tower.

[0036] (2) The discharge from the T101 tower kettle enters the top of the stripper T102 tower, and the steam of DMF is passed into the bottom of the stripper tower, and the gas-liquid contacts in countercurrent in the tower. The operating pressure of the stripper T102 is 0 MPa, and the operating temperature is 90 ° C. The sucrose-6-ethyl ester solution containing DMF is obtained from the bottom of the stripping tower T102, and the mixture of DMF and acetic acid is extrac...

Embodiment 3

[0040] (1) The sucrose-6-ethyl ester solution containing DMF, acetic acid and water is sent to the dehydration tower T101 for rectification, and the total feed rate is 1000kg / hr. The operating pressure of the dehydration tower T101 is -0.09Mpa, and the operating temperature is 80°C. The condensate at the top of the tower is withdrawn as waste water. The tower still liquid phase is connected to the tower still reboiler for vaporization, and part of the tower still liquid is sent to the T102 stripping tower.

[0041] (2) The discharge from the T101 tower kettle enters the top of the stripper T102 tower, and the steam of DMF is passed into the bottom of the stripper tower, and the gas-liquid contacts in countercurrent in the tower. The operating pressure of the stripper T102 is 0 MPa, and the operating temperature is 90 ° C. The sucrose-6-ethyl ester solution containing DMF is obtained from the bottom of the stripping tower T102, and the mixture of DMF and acetic acid is extract...

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Abstract

The invention relates to a method for removing acetic acid from a DMF (Dimethyl Formamide) solution of sucrose-6-ethyl ester. The method comprises the following steps that: firstly, a solution containing DMF, acetic acid, water and sucrose-6-ethyl ester are fed into a dehydrating tower for dehydrating, materials is discharged from a tower kettle and fed into a stripping tower, DMF steam is introduced to enable gas and liquid to be in countercurrent contact in the tower, a DMF-containing sucrose-6-ethyl ester solution is obtained from the tower kettle of the stripping tower, a DMF and acetic acid mixture is obtained from the tower top of the stripping tower, and a pressure swing distillation system is used for separation. DMF with acetic acid removed is obtained at the top of the low-pressure tower, and a part of DMF is heated and vaporized to serve as a steam source of the stripping tower. Tower kettle materials of the low-pressure tower enter a high-pressure tower, a tower top gas phase of the high-pressure tower serves as a dehydrating tower reboiler heat source, heat integration is achieved, and acetic acid is obtained after condensation. The content of acetic acid in the DMF solution at the top of the low-pressure tower can be reduced below 200ppm. The process is simple, does not add a third medium, does not generate solid waste, is energy-saving and environment-friendly, and can realize continuous operation.

Description

technical field [0001] The invention relates to a method for removing acetic acid from sucrose-6-ethyl ester DMF solution, in particular to the removal of acetic acid from sucrose-6-ethyl ester DMF solution involved in the production process of sucralose. Background technique [0002] The industrial synthesis of sucralose is generally based on sucrose as raw material, through transesterification to obtain sucrose-6-ethyl ester, sucrose-6-ethyl ester is chlorinated by Vilsmeier reagent to generate intermediate sucralose-6-acetate, trichloro Sucralose is obtained by deacetylation of sucrose-6-acetate. Among them, sucrose-6-ethyl ester is an important intermediate product in the process of producing sucralose, and a solution of water, acetic acid, dimethylformamide (DMF) and sucrose-6-ethyl ester will be formed during its production. The mixed liquid needs to remove acetic acid and moisture, and then enter the subsequent section of processing with DMF and sucrose-6-ethyl ester...

Claims

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Application Information

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IPC IPC(8): C07H5/02C07H1/00C07H13/04C07H1/06B01D3/14B01D3/38
CPCC07H5/02C07H1/00C07H13/04C07H1/06B01D3/143B01D3/38Y02P20/10
Inventor 何永超许春建李玲郑凯天
Owner TIANJIN UNIV
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