Process for producing methyl carbamate by low pressure solvation homogeneous phase reaction
A technology of methyl carbamate and homogeneous reaction, which is applied in the industrial production of methyl carbamate as a pesticide intermediate, the production of fine chemicals, medicine and medicine, and can solve the problems of short service life of catalysts, difficulty in refining products, high reaction temperature, etc. , to achieve the effects of short reaction time, low production cost, high reaction conversion rate and selectivity
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Embodiment 1
[0013] 1T urea and 3m 3 Methanol was added to 5m 3 In the reaction kettle, the heating reaction temperature is 140°C, and when the pressure reaches 1.2Mpa, the rectification tower starts to work, and at the same time, it is 3 / h rate to supplement 1mol / L urea methanol solution, the reaction time is 4h. The methyl carbamate yield was 86%. Simultaneously by-product 30% ammonia water 0.85T.
Embodiment 2
[0015] Combine 0.8T urea and 3.2m 3 Methanol was added to 5m 3 In the reaction kettle, the heating reaction temperature is 150°C, and when the pressure reaches 1.5Mpa, the rectification tower starts to work, and at the same time, the 0.2m 3 Add 1.5mol / L urea methanol solution at a rate of / h, and the reaction time is 4h. The yield of methyl carbamate is 88%, and 0.86T of 30% ammonia water is by-produced simultaneously.
Embodiment 4
[0017] Combine 1T urea and 3.5m 3 Methanol was added to 5m 3 In the reaction kettle, the heating reaction temperature is 160°C, and the rectification tower starts to work when the pressure reaches 1.4Mpa. 3 Add 1.2mol / L urea methanol solution at a rate of / h, and the reaction time is 3h. The methyl carbamate yield was 91%. Simultaneously by-product 30% ammonia water 0.88T.
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