A kind of diketene continuous rectification process
A technology for diketene and crude diketene, which is applied in the chemical industry and can solve problems such as high energy consumption and complicated processes
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Embodiment 1
[0028] After adding an appropriate amount of crude diketene (content 90%) into the film evaporator, the crude diketene enters the film evaporator continuously at 200kg / h, controls the vacuum degree -0.1MPa, and continuously discharges the material at a bottom temperature of 65°C and a top temperature of 55°C ; The discharge temperature of the primary condenser is 45°C, the output condensate is 190.8kg / h, the content of diketene is 99.2%, the discharge temperature of the secondary condenser is 10°C, and the condensate is 2kg / h; the secondary condensate is 2kg / h , residue 7kg / h, methanol 9kg / h, triethylenediamine 0.018kg / h continuously enter the esterification tank, maintain the temperature of the esterification tank at 55-60 ° C, and continuously discharge to the fuel storage tank, the distillation yield of diketene is 95.4 %, the primary finished product content is 99.2%.
Embodiment 2
[0030] After adding an appropriate amount of crude diketene (content 95%) into the film evaporator, the crude diketene enters the film evaporator continuously at 200kg / h, controls the vacuum degree -0.15MPa, and continuously discharges the material at a bottom temperature of 55°C and a top temperature of 50°C ; The discharge temperature of the primary condenser is 40°C, the output condensate is 190.4kg / h, the content of diketene is 99.3%, the discharge temperature of the secondary condenser is 0°C, and the condensate is 2kg / h; the secondary condensate is 2kg / h , residue 7.2kg / h, methanol 13.8kg / h, triethylenediamine 0.012kg / h continuously enter the esterification tank, maintain the temperature of the esterification tank at 75-80°C, and continuously discharge to the fuel storage tank, diketene rectification The rate is 95.2%, and the finished product content is 99.3%.
Embodiment 3
[0032] After adding an appropriate amount of crude diketene (content 93%) into the film evaporator, the crude diketene enters the film evaporator continuously at 200kg / h, controls the vacuum degree -0.12MPa, and continuously discharges the material at a bottom temperature of 60°C and a top temperature of 52°C ; The discharge temperature of the primary condenser is 43°C, the output condensate is 191.4kg / h, the content of diketene is 99.1%, the discharge temperature of the secondary condenser is 5°C, and the condensate is 1.8kg / h; the secondary condensate is 1.8kg / h, residue 6.8kg / h, methanol 11kg / h, triethylenediamine 0.015kg / h continuously enter the esterification tank, maintain the temperature of the esterification tank at 65-70 ° C, and continuously discharge to the fuel storage tank, diketene rectification The yield is 95.7%, and the primary product content is 99.1%.
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