Method and special device for separating trimethyl borate from carbinol mixture
A technology of trimethyl borate and a special device, which is applied in the field of organic matter preparation, can solve the problems of high sulfuric acid concentration, large plate load, and large sulfuric acid consumption, and achieve low equipment investment, convenient recycling and good results.
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Embodiment 1
[0022] The theoretical plate number of the extractive distillation column is 15 (the number of plates is counted from top to bottom), and ethylene glycol containing lithium chloride (the mass fraction of lithium chloride is 15%) is used as the salting solvent. The theoretical plate is added, the flow rate is 20g / min, the mixture of trimethyl borate and methanol is added from the ninth theoretical plate, the mass fraction of trimethyl borate is 75%, the mass fraction of methanol is 25%, and the flow rate is 10g / min. The reflux ratio at the top of the extractive distillation column is 0.2, and the temperature at the top of the column is controlled at 68.5~69.0℃. The product at the top of the column is analyzed. The mass fraction of trimethyl borate is 99.6%, and the mass fraction of methanol is 0.4%. The extractive distillation tower tower kettle discharge is methanol, salt, solvent mixture into the solvent recovery tower, the solvent recovery tower has 10 theoretical trays, th...
Embodiment 2
[0024] The theoretical plate number of the extractive distillation column is 40 (the number of plates is counted from top to bottom), and ethylene glycol containing lithium chloride (the mass fraction of lithium chloride is 8%) is selected as the salting solvent. The theoretical plate is added, the flow rate is 5g / min, the mixture of trimethyl borate and methanol is added from the 24th theoretical plate, the mass fraction of trimethyl borate is 75%, the mass fraction of methanol is 25%, and the flow rate is 10g / min . The reflux ratio at the top of the extractive distillation column is 4, the temperature at the top of the column is controlled at 68.5~69.0℃, and the product at the top of the column is analyzed. The mass fraction of trimethyl borate is 99.5%, and the mass fraction of methanol is 0.5%. The extractive distillation tower reactor discharge is methanol, salt, solvent mixture into the solvent recovery tower, the solvent recovery tower has 30 theoretical trays, the feed...
Embodiment 3
[0026] The theoretical plate number of the extractive distillation column is 25 (the number of plates is counted from top to bottom), and ethylene glycol containing lithium chloride (the mass fraction of lithium chloride is 12%) is selected as the salting solvent. The theoretical plate is added, the flow rate is 10g / min, the mixture of trimethyl borate and methanol is added from the 15th theoretical plate, the mass fraction of trimethyl borate is 75%, the mass fraction of methanol is 25%, and the flow rate is 10g / min . The reflux ratio at the top of the extractive distillation column is 2, the temperature at the top of the column is controlled at 68.5~69.0℃, and the product at the top of the column is analyzed. The mass fraction of trimethyl borate is 99.8%, and the mass fraction of methanol is 0.2%. The extractive distillation tower tower kettle discharge is methanol, salt, solvent mixture into the solvent recovery tower, the solvent recovery tower has 20 theoretical trays, t...
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