Preparation method of 2, 2, 4-trimethyl-1, 3-pentanediol monoisobutyrate
A technology of pentanediol monoisobutyrate and trimethyl, applied in the field of preparation of 2,2,4-trimethyl-1,3-pentanediol monoisobutyrate, can solve the problem of no industrial scale-up , isobutyraldehyde instant heat release and other problems, to achieve the best catalytic effect, the best water absorption effect
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[0027] The invention provides a preparation method of 2,2,4-trimethyl-1,3-pentanediol monoisobutyrate, comprising:
[0028] (1) Alkali metal hydroxide, alkaline earth metal oxide and alcohol ester twelve are added to reaction vessel, stir evenly;
[0029] (2) adding isobutyraldehyde and controlling the feed rate of isobutyraldehyde, controlling the temperature to be 20-70° C., carrying out the first-stage isobutyraldehyde condensation reaction to obtain an intermediate product;
[0030] (3) After the addition of isobutyraldehyde is completed, the control temperature is 40~70° C., and it is incubated for 1~5 hours to carry out the Cannizzaro reaction of the second stage to obtain the alcohol ester twelve crude product;
[0031] (4) Purifying the crude product of the alcohol ester twelve to obtain the finished product of the alcohol ester twelve.
[0032] The preparation method of 2,2,4-trimethyl-1,3-pentanediol monoisobutyrate provided by the present invention mainly involves ...
Embodiment 1
[0048] Pump 2000kg of alcohol ester twelve finished products into 20m through the delivery pump 3 In the first reactor, 75kg of barium oxide and 75kg of potassium hydroxide are added at one time through the star feeder on the first reactor. Stirring was started, and the inner and outer coils of the first reaction kettle were fed with -5°C ethylene glycol-water solution to cool the materials.
[0049] Cool the material in the first reaction kettle to about 20°C, pump isobutyraldehyde into the first reaction kettle at a speed of 1 to 5 tons / hour through the isobutyraldehyde delivery pump, and control the isobutyraldehyde pump The input speed and the ethylene glycol-water solution inside and outside the first reaction kettle are coiled, and the temperature of the reaction materials is controlled at 20-70°C. The amount of adding isobutyraldehyde is 15 tons.
[0050] After the addition of isobutyraldehyde is completed, the first stage of isobutyraldehyde condensation reaction is ...
Embodiment 2
[0063] 3000kg alcohol ester twelve finished products are pumped into the 20m 3 In the first reaction kettle, 250kg of barium oxide and 400kg of sodium hydroxide were added at one time through the star feeder on the first reaction kettle. Stirring was started, and the inner and outer coils of the reaction kettle were fed with ethylene glycol-water solution at -5°C to cool the materials.
[0064] Cool the material in the first reaction kettle to about 20°C, pump isobutyraldehyde into the first reaction kettle at a speed of 1 to 5 tons / hour through the isobutyraldehyde delivery pump, and control the isobutyraldehyde pump The input speed and the ethylene glycol-water solution inside and outside the first reaction kettle are coiled, and the temperature of the reaction materials is controlled at 20-70°C. The amount of isobutyraldehyde added is 13 tons.
[0065] After the addition of isobutyraldehyde is completed, the first stage of isobutyraldehyde condensation reaction is complet...
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