Method and apparatus for producing formic esters by comprehensively utilizing metronidazole hydroxylation synthesis wastewater
A technology for the hydroxylation and chemical synthesis of metronidazole is applied in the field of comprehensive recycling and utilization of chemical synthesis pharmaceutical production wastewater, which can solve the problems of formic acid consumption and waste, difficult treatment of hydroxylation synthesis production wastewater, etc. Excellent quality of by-products and the effect of eliminating formic acid waste gas
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[0036] Example 1:
[0037] After the hydroxylation synthesis reaction is completed, the materials are transferred to the esterification reactor 4 to prepare for the esterification reaction. Assuming that the mass of formic acid added during the hydroxylation synthesis reaction is Q (Kg), calculate the amount of methanol to be added as follows: W Methanol =1.05×Q / 46×32, and then slowly added to the esterification reactor 4, after the addition is completed, control the temperature to be greater than or equal to 60℃, reflux for 2 hours, after the reaction is completed, then transfer the materials to the No. 1 distillation kettle 7 Distillation, the mixed gas that is distilled is directly sent to rectification tower 8 (the rectification tower is a single-tower process) for rectification separation, and the distillation operation temperature is controlled at 88±2°C until all methyl formate and methanol are distilled out, and then sent Into the rectifying tower for rectification and ...
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[0041] Example 2:
[0042] The process of Example 2 is the same as that of Example 1.
[0043] The difference is that:
[0044] (1) The alcohol added to the esterification reactor 4 is ethanol, and the obtained esterification product is ethyl formate.
[0045] (2) Ethyl formate and water have an azeotropic point (54.23℃). The rectification process must adopt a double-tower (or three-tower) process. The double-tower process uses rectification tower 8 to distill ethyl formate and ethanol first, and then use The desiccant dehydration skips the azeotropic point, and then continues rectification and separation in the rectification tower 8. The fraction at 54±0.5°C is intercepted at the top of the tower to obtain more than 99% ethyl formate product; ethanol is obtained at the bottom of the tower And the entrained components of the distillate during evaporation in the previous process are discharged to the ethanol aqueous solution storage tank 14, and then sent to the sewage treatment stati...
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