Method for synthesizing trioxymethylene by methanol through condensation, oxidation and polycondensation
A trioxymethylene and methylal technology, which is applied in organic chemistry, chemical industry, climate sustainability, etc., can solve the problems of high equipment material requirements, low trioxymethylene yield, and large recovery volume, and achieves reduction in concentration. The effect of energy consumption, improving one-way conversion rate, and reducing residence time
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Embodiment 1
[0034] As shown in Figure 1, the synthesis method of this embodiment is:
[0035] Step 1, methanol condensation to prepare methylal: according to the molar ratio of methanol and formaldehyde of 2.0:1, methanol and dilute formaldehyde with a mass concentration of 5% are mixed and then sent to reactor 1 filled with a catalyst for condensation reaction. The reaction temperature of the condensation reaction is 90°C, the reaction pressure is 8.0MPa, and then the material after the condensation reaction is sent to the first reactive distillation tower 2, and the number of sieve trays at the top of the first reactive distillation tower 2 is 30 , the number of sieve trays at the bottom of the tower is 30, the number of layers of the packed bed is 8 layers, the pressure at the top of the first reactive distillation tower 2 is controlled to be 50kPa, the temperature at the top of the tower is 47°C, and the temperature at the bottom of the tower is 115°C. Ratio is 3.0, including product ...
Embodiment 2
[0041] As shown in Figure 1, the synthesis method of this embodiment is:
[0042] Step 1, methanol condensation to prepare methylal: according to the molar ratio of methanol and formaldehyde of 3.0:1, methanol and dilute formaldehyde with a mass concentration of 20% are mixed and then sent to reactor 1 filled with a catalyst for condensation reaction. The reaction temperature of the condensation reaction is 70°C, the reaction pressure is 5.0MPa, and then the material after the condensation reaction is sent to the first reactive distillation tower 2, and the number of sieve trays at the top of the first reactive distillation tower 2 is 20 , the number of sieve trays at the bottom of the tower is 20, the number of layers of the packed bed is 5 layers, the top pressure of the first reactive distillation tower 2 is controlled to be 30kPa, the temperature of the top of the tower is 45°C, and the temperature of the bottom of the tower is 108°C. Ratio is 2.0, the product methylal and...
Embodiment 3
[0048] As shown in Figure 1, the synthesis method of this embodiment is:
[0049] Step 1, methanol condensation to prepare methylal: according to the molar ratio of methanol and formaldehyde of 3.5:1, methanol and dilute formaldehyde with a mass concentration of 45% are mixed and then sent to reactor 1 filled with a catalyst for condensation reaction. The reaction temperature of the condensation reaction is 60°C, the reaction pressure is 2.0MPa, and then the material after the condensation reaction is sent to the first reactive distillation tower 2, and the number of sieve trays at the top of the first reactive distillation tower 2 is 5 , the number of sieve trays at the bottom of the tower is 5, the number of layers of the packed bed is 2, the top pressure of the first reactive distillation tower 2 is controlled to be 5kPa, the temperature of the top of the tower is 42.3°C, the temperature of the bottom of the tower is 100°C, the reflux ratio is 1.0, the material after the co...
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