Process for prepn. of dialkyl formanmide
A technology of dialkylformamide and a manufacturing method, which is applied in the preparation of carboxylic acid amides, organic chemistry methods, chemical instruments and methods, etc., can solve the problems of accumulation of crystalline by-products, difficulty in controlling reaction temperature, etc., and can solve the problem of reaction temperature Control becomes difficult, stable continuous production for a long time, and the effect of suppressing accumulation of crystalline by-products
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Embodiment 1
[0029] In FIG. 1 , the mixed gas obtained by gasification of coal is purified and adjusted to 40% by volume of carbon monoxide, 58.9% by volume of hydrogen, 1.0% by volume of nitrogen, and 0.1% by volume of oxygen. Supply the mixed gas 2800Nm from the lower part of the reaction tower 3 / hr(Nm 3 / hr is the gas flow rate based on 0°C and 101.3kPa, and the carbon monoxide flow rate based on mass is 1400kg / hr), and 2600kg / hr of dimethylamine containing 200mg of water relative to 1kg of dimethylamine, 260kg / hr of methanol, and 24 56 kg / hr of a methanol solution of sodium methoxide in mass % was reacted at a pressure of 2.0 MPa and a temperature of 115°C. The molar ratio of oxygen / sodium methoxide at this time was 0.5. The reaction product is extracted from the top of the reaction tower as a liquid, and the inert gas is extracted from the top of the tower. The dimethylformamide in the reaction product was 4010 kg / hr, and the conversion rate of dimethylamine to dimethylformamide w...
Embodiment 2
[0031]In FIG. 1 , the mixed gas obtained by gasification of coal is purified and adjusted to 40% by volume of carbon monoxide, 58.7% by volume of hydrogen, 1.0% by volume of nitrogen, and 0.3% by volume of oxygen. Supply the mixed gas 2800Nm from the lower part of the reaction tower 3 / hr(Nm 3 / hr is the gas flow rate based on 0°C and 101.3kPa, and the carbon monoxide flow rate based on mass is 1400kg / hr), and 2600kg / hr of dimethylamine containing 200mg of water relative to 1kg of dimethylamine, 260kg / hr of methanol, and 24 The mass % methanol solution of sodium methoxide was 84 kg / hr, and the reaction was carried out at a pressure of 2.0 MPa and a temperature of 115°C. The molar ratio of oxygen / sodium methoxide at this time was 1.0. The reaction product is extracted from the top of the reaction tower as a liquid, and the inert gas is extracted from the top of the tower. The dimethylformamide in the reaction product was 4010 kg / hr, and the conversion rate of dimethylamine t...
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