Continuous esterification production process of trimethyl borate
A technology of trimethyl borate and production process, applied in the field of medicine and chemical industry, can solve the problems of high requirements for equipment material selection, low primary conversion rate and high equipment cost, so as to improve reaction conversion rate and reaction yield, and reduce heat energy. The effect of reducing energy consumption and cooling energy consumption
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Embodiment 1
[0039] Methanol and boric acid are mixed in a molar ratio of 6:1, and enter the esterification tower after pre-reaction in the pre-reactor. 30% to 40% trimethyl borate is produced from the top of the esterification tower, and water is produced from the bottom of the esterification tower. 30%~40% trimethyl borate gaseous phase is extracted from the top of the tower and enters the refining tower, the trimethyl borate product is extracted from the top of the refining tower, the bottom of the tower is methanol, and the methanol is reused, and the specific parameters are as follows:
[0040] 1. The temperature at the top of the esterification tower is 62-64°C, and the temperature at the bottom of the tower is 100-102°C;
[0041] 2. The reflux ratio of the esterification tower is controlled at 3;
[0042] 3. The temperature at the top of the refining tower is 53-55°C, and the temperature at the bottom of the tower is 64-66°C;
[0043] 4. The reflux ratio of the refining tower is cont...
Embodiment 2
[0047] Mix methanol and boric acid in a molar ratio of 5:1, pre-react in the pre-reactor and then enter the esterification tower. 30% to 40% trimethyl borate is produced from the top of the esterification tower, and water is produced from the bottom of the esterification tower. , 30% to 40% of the trimethyl borate gas phase is extracted from the top of the tower and enters the refining tower, and the trimethyl borate product is extracted from the top of the refining tower, and the bottom of the tower is methanol, and the methanol is reused. The specific parameters are as follows:
[0048] 1. The temperature at the top of the esterification tower is 62-64°C, and the temperature at the bottom of the tower is 100-102°C;
[0049] 2. The reflux ratio of the esterification tower is controlled at 4;
[0050] 3. The temperature at the top of the refining tower is 53-55°C, and the temperature at the bottom of the tower is 64-66°C;
[0051] 4. The reflux ratio of the refining tower is ...
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