Sucralose continuous high-temperature reaction method and device thereof

A high-temperature reaction and sucralose technology, applied in series/parallel reactions, chemical instruments and methods, sugar derivatives, etc., can solve the problems of sucralose synthesis difficulties, increased production costs, and difficult control of the reaction, and achieve optimal pressure and warming environment, reducing energy consumption and equipment wear, and saving manpower

Pending Publication Date: 2021-03-30
ANHUI JINGHE IND
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

There are a total of 8 hydroxyl groups in the sucrose molecule. It is of course very difficult to replace 3 hydroxyl groups at specific positions by selective chlorination without changing the hydroxyl groups at other positions, and because the hydroxyl groups at each position The reactivity of sucralose varies, making the synthesis of sucralose more difficult
Most of the existing processes are to put the esterified liquid that has been reacted at low temperature into a high-temperature reactor for three-stage high-temperature reaction, mostly a single-pot reaction, the reaction is discontinuous, the reaction is not easy to control, the reaction is insufficient, time-consuming and labor-intensive, resulting in increase in production costs

Method used

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  • Sucralose continuous high-temperature reaction method and device thereof
  • Sucralose continuous high-temperature reaction method and device thereof
  • Sucralose continuous high-temperature reaction method and device thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0020] (1) Put the low-temperature chlorination liquid from the previous section into the 1# reboiler at an amount of 10m³ / h, and then send it to the 1# high-temperature chlorination reaction tower after being heated by the 1# reboiler to 35°C, and open the cycle. Control the temperature in the 1# high-temperature chlorination reaction tower to be 69°C and the pressure to be -3Mpa, and the gas (trichloroethane gas) from the top of the 1# high-temperature chlorination reaction tower is condensed by the condenser 1# (28°C) and enters 1# reflux tank, then return to 1# high-temperature chlorination reaction tower via 1# reflux tank, and circulate and heat for 30min to obtain solution A;

[0021] (2) Extract solution A from the bottom of 1# high-temperature chlorination reaction tower at an amount of 10m³ / h, heat it to 92°C with 2# reboiler, and then enter 2# high-temperature chlorination reaction tower, open the circulation, and control The temperature inside the 2# high-temperatu...

Embodiment 2

[0024] (1) Put the low-temperature chlorination liquid from the previous section into the 1# reboiler at an amount of 11m³ / h, and then send it to the 1# high-temperature chlorination reaction tower after being heated by the 1# reboiler to 32°C, and open the cycle. Control the temperature in the 1# high-temperature chlorination reaction tower to be 68°C and the pressure to be -4Mpa. The gas (trichloroethane gas) from the top of the 1# high-temperature chlorination reaction tower is condensed by the condenser 1# (22°C) and enters 1# reflux tank, then return to 1# high-temperature chlorination reaction tower via 1# reflux tank, and circulate and heat for 30min to obtain solution A;

[0025] (2) Extract solution A from the bottom of 1# high-temperature chlorination reaction tower at an amount of 11m³ / h, heat it to 90°C with 2# reboiler, and then enter 2# high-temperature chlorination reaction tower, open the circulation, and control The temperature inside the 2# high-temperature c...

Embodiment 3

[0028] (1) Put the low-temperature chlorination liquid from the previous section into the 1# reboiler at an amount of 12m³ / h, and then send it to the 1# high-temperature chlorination reaction tower after being heated by the 1# reboiler to 38°C, and open the cycle. Control the temperature in the 1# high-temperature chlorination reaction tower to be 71°C and the pressure to be -2Mpa. The gas (trichloroethane gas) from the top of the 1# high-temperature chlorination reaction tower is condensed by the condenser 1# (33°C) and enters 1# reflux tank, then return to 1# high-temperature chlorination reaction tower via 1# reflux tank, and circulate and heat for 30min to obtain solution A;

[0029] (2) Take solution A at 12m³ / h from the bottom of 1# high-temperature chlorination reaction tower, heat it to 93°C with 2# reboiler, then enter 2# high-temperature chlorination reaction tower, open the circulation, and control The temperature in the 2# high-temperature chlorination reaction tow...

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Abstract

The invention relates to a sucralose continuous high-temperature reaction method and a device thereof, which are characterized in that (1) low-temperature chlorination liquid is heated by a 1 # reboiler and then is fed into a 1 # high-temperature chlorination reaction tower, the temperature in the tower is controlled to be 68-71 DEG C, the pressure is -4-2Mpa, gas from the tower top returns to thetower after being condensed, and is circularly heated for 30min to obtain a solution A; (2) the solution A is heated by a 2 # reboiler and then enters a 2 # high-temperature chlorination reaction tower, the temperature in the tower is controlled to be 98-101 DEG C, the pressure in the tower is controlled to be -4-2 Mpa, gas coming out of the tower top is condensed and then returns to the tower, cyclic heating is conducted for 60 min, and a solution B is obtained; and (3) the solution B is heated by a 3 # reboiler and then enters a 3 # high-temperature chlorination reaction tower, the temperature in the tower is controlled to be 109-111 DEG C, the pressure in the tower is controlled to be -4-2 Mpa, gas coming out of the tower top is condensed and then returns to the tower, cyclic heating is conducted for 120 min, and a solution C is obtained. The device has the advantages that the three high-temperature chlorination reaction towers are connected in series, so that continuous reaction can be realized, the heating rate is increased, the pressure and the heating environment of a high-temperature chlorination system are optimized, the quality and the yield of a product are improved, and the tail gas emission amount is reduced.

Description

technical field [0001] The invention belongs to the technical field of sucralose production, and relates to a method and device for continuous high-temperature reaction of trichloroethane. Background technique [0002] Sucralose is obtained by replacing the hydroxyl groups at positions 4, 1, and 6 in the sucrose molecule with chlorine atoms. There are a total of 8 hydroxyl groups in the sucrose molecule. It is of course very difficult to replace 3 hydroxyl groups at specific positions by selective chlorination without changing the hydroxyl groups at other positions, and because the hydroxyl groups at each position The reactivity of sucralose varies, making the synthesis of sucralose more difficult. Most of the existing processes are to put the esterified liquid that has been reacted at low temperature into a high-temperature reactor for three-stage high-temperature reaction. Most of them are single-pot reactions, the reaction is discontinuous, the reaction is not easy to co...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07H5/02C07H1/00B01J19/00
CPCB01J19/0013B01J19/0046C07H1/00C07H5/02
Inventor 徐成刚石剑王友义徐国家
Owner ANHUI JINGHE IND
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