Method for continuously synthesizing 1, 1-diethoxypropane
A technology of diethoxypropane and propionaldehyde, applied in chemical instruments and methods, preparation of organic compounds, organic chemistry, etc., can solve problems such as high operating intensity, non-continuous production, low efficiency, and slow reaction
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Embodiment 1
[0017] Turn on the preheater, mix propionaldehyde and ethanol with a molar ratio of 1:2 in the mixer (that is, the feed tank), then pass through the metering pump, pump into the preheater to preheat the raw material to 70°C, and pass through the solid load The trickle bed reaction of sulfonic acid resin was carried out, and the content of 1,1-diethoxypropane in the reaction solution was 29.7%. The reaction solution is continuously pumped into the rectification tower through the feed pump for separation, and a mixed component of unreacted raw materials propionaldehyde, ethanol and water produced by the reaction is obtained at the top of the tower, and the mixed component is dewatered through a membrane to obtain anhydrous propionaldehyde. Aldehyde and ethanol are applied mechanically to the condensation reaction, and 1,1-diethoxypropane with a content >98% is obtained in the tower reactor.
Embodiment 2
[0019] Turn on the preheater, mix propionaldehyde and ethanol with a molar ratio of 1:3, and then pump it into the preheater through a metering pump to preheat the raw material to 60°C, and then pass through the trickle bed reaction with sulfonic acid resin , the content of 1,1-diethoxypropane in the reaction solution was 38.7%. The reaction solution is continuously pumped into the rectification tower through the feed pump for separation, and a mixed component of unreacted raw materials propionaldehyde, ethanol and water produced by the reaction is obtained at the top of the tower, and the mixed component is dewatered through a membrane to obtain anhydrous propionaldehyde. Aldehyde and ethanol are applied mechanically to the condensation reaction, and 1,1-diethoxypropane with a content >98% is obtained in the tower reactor.
Embodiment 3
[0021] Turn on the preheater, mix propionaldehyde and ethanol with a molar ratio of 1:4, and then pump it into the preheater through the metering pump to preheat the raw material to 50°C, and then pass through the trickle bed reaction of the sulfonic acid resin , the content of 1,1-diethoxypropane in the reaction solution was 41.3%. The reaction solution is continuously pumped into the rectification tower through the feed pump for separation, and a mixed component of unreacted raw materials propionaldehyde, ethanol and water produced by the reaction is obtained at the top of the tower, and the mixed component is dewatered through a membrane to obtain anhydrous propionaldehyde. Aldehyde and ethanol are applied mechanically to the condensation reaction, and 1,1-diethoxypropane with a content >98% is obtained in the tower reactor.
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