Method for preparing diisobutyl ketone
A technology of diisobutyl ketone and methyl isobutyl ketone, which is applied in the separation/purification of carbonyl compounds, organic chemistry, etc., can solve the problems of inability to be better utilized, low purity, etc., and reduce the steps of operation , Improve distillation efficiency, improve the effect of purity
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Embodiment 1
[0025] The mixture raw material based on the diisobutyl ketone extracted from the tower kettle of the light component tower of methyl isobutyl ketone is transferred to the reaction tank with a flow rate of 500Kg / h; Silica gel desiccant, and stirring, the stirring speed is 100 rpm; the mixture raw material in the reaction tank is filtered through the filter; the filtrate obtained after filtering is transported to the preheater for preheating, and the preheating temperature is up to 76-94°C; transport the preheated filtrate to the rectification tower for rectification, and control the temperature at the top of the tower to 104-126°C, the temperature of the side line to 156-177°C, and the temperature of the bottom of the tower to 167-189°C; The finished diisobutyl ketone is produced from the side line of the rectification tower at 200Kg / h, wherein the finished diisobutyl ketone produced is returned to the reaction tank at 130Kg / h to be mixed with the filtrate, and the rest of the ...
Embodiment 2
[0028] The mixture raw material based on the diisobutyl ketone extracted from the tower kettle of the light component tower of methyl isobutyl ketone is transferred to the reaction tank with a flow rate of 500Kg / h; Silica gel desiccant, and stirring, the stirring speed is 100 rpm; the mixture raw material in the reaction tank is filtered through the filter; the filtrate obtained after filtering is transported to the preheater for preheating, and the preheating temperature is up to 76-94°C; transport the preheated filtrate to the rectification tower for rectification, and control the temperature at the top of the tower to 104-126°C, the temperature of the side line to 156-177°C, and the temperature of the bottom of the tower to 167-189°C; The finished diisobutyl ketone is produced from the side line of the rectification tower at 300Kg / h, among which, the finished diisobutyl ketone produced is returned to the reaction tank at 200Kg / h to be mixed with the filtrate, and the rest of...
Embodiment 3
[0031] The mixture raw material based on the diisobutyl ketone extracted from the tower kettle of the light component tower of methyl isobutyl ketone is transferred to the reaction tank with a flow rate of 500Kg / h; Silica gel desiccant, and stirring, the stirring speed is 100 rpm; the mixture raw material in the reaction tank is filtered through the filter; the filtrate obtained after filtering is transported to the preheater for preheating, and the preheating temperature is up to 76-94°C; transport the preheated filtrate to the rectification tower for rectification, and control the temperature at the top of the tower to 104-126°C, the temperature of the side line to 156-177°C, and the temperature of the bottom of the tower to 167-189°C; The finished diisobutyl ketone is produced from the side line of the rectification tower at 250Kg / h, among which, the finished diisobutyl ketone produced is returned to the reaction tank at 167Kg / h to be mixed with the filtrate, and the rest of...
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