Preparation method of 2, 4-hexadienoic acid polyester
A technology of hexadienoic acid polyester and ketene, applied in 2 fields, can solve the problems of low conversion rate and low yield of beta-methacrolein, and achieve the effects of improving the conversion rate of beta-methacrolein and reducing the amount of waste water
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Embodiment 1
[0035] Embodiment 1: the preparation method of titanium dioxide-silicon dioxide-caprolactam composite catalyst:
[0036] Hydrolyze 8.8083g butyl titanate in 103.6ml0.1mol / L hydrochloric acid to obtain TiO2 sol A; then hydrolyze 21.5544g ethyl orthosilicate in a mixed solution of 12.8ml0.2mol / L hydrochloric acid and 15.4ml ethanol to obtain SiO2 Sol B; mix A and B and stir for 0.5 hours to obtain a colorless, clear and transparent TiO2 / SiO2 sol C; dissolve 11.7099g caprolactam in 780g water to obtain solution D, drop sol C into solution D, wash and dry , to obtain a titanium dioxide-silicon dioxide-caprolactam composite catalyst.
Embodiment 2
[0037] Embodiment 2: the preparation method of 2,4-hexadienoic acid polyester
[0038] Add 550Kg β-methacrolein and 5Kg titanium dioxide-silicon dioxide-caprolactam composite catalyst into a 1500L reactor, start stirring, raise the temperature to 40°C, and control the temperature between 40±1°C and feed 330Kg ketene gas to react After the reaction is completed, the catalyst is filtered, and the reaction liquid is rectified by negative pressure (vacuum degree 0.098MPa) to recover 27Kg of β-methacrolein (one-pass conversion rate 95.1%) and apply it to the next batch to obtain high-viscosity 2,4- Hexadienoic acid polyester 757.3Kg, one-way yield 90.5%.
Embodiment 3
[0039] Embodiment 3: the preparation method of 2,4-hexadienoic acid polyester
[0040]Add 580Kg β-methacrolein and 7Kg titanium dioxide-silicon dioxide-caprolactam composite catalyst into a 1500L reactor, start stirring, raise the temperature to 45°C, and control the temperature between 45±1°C and feed 345Kg ketene gas to react After the reaction is completed, the catalyst is filtered, and the reaction liquid is rectified by negative pressure (vacuum degree 0.099MPa) to recover 24.4Kg of β-methacrolein (one-pass conversion rate 95.8%) and apply it to the next batch to obtain high viscosity 2,4 - 809.8Kg of hexadienoic acid polyester, the yield per pass is 91.1%.
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