A kind of preparation method of 3 chloro-1,2-propanediol
A technology of propylene glycol and chloropropene, which is applied in the field of preparation of 3-chloro-1,2-propanediol, can solve the problems of many by-products, reduced yield, and difficulty in meeting the requirements, and achieves the reduction of waste acid discharge, solid waste discharge, and reduction of The effect of hydrolysis by-products
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
Embodiment 1
[0023] In the 1000ml reactor, add chloropropene 300g, mass concentration is 50% hydrogen peroxide aqueous solution 90g, add 20g reaction control phase-transfer catalyst [π-C 5 h 5 NC 16 h 33 ] 3 (PO 4 ) (WO 3 ) 4 ], the reaction temperature was 45°C, and the reaction pressure was 0.5MPa. After 2.5 hours of reaction, the reaction materials were centrifuged to recover the reaction-controlled phase transfer catalyst.
[0024] Continue to add 90g of aqueous hydrogen peroxide solution with a mass concentration of 50%, 400g of deionized water, and solid acid catalyst B to the material containing epichlorohydrin prepared above. 2 o 3 -Al 2 o 3 5g was reacted at 75°C for 2h, and the reaction pressure was 1.5MPa.
[0025] After the hydrolysis reaction was completed, the solid acid catalyst reaction material was filtered and separated, and the filtrate was washed with 300g of chloropropene and then subjected to vacuum distillation. The vacuum of the vacuum distillation was 40...
Embodiment 2
[0027] In the 1000ml reactor, add chloropropene 300g, mass concentration is 50% hydrogen peroxide aqueous solution 90g, add 20g reaction control phase-transfer catalyst [π-C 5 h 5 NC 16 h 33 ] 3 (PO 4 ) (WO 3 ) 4 ], the reaction temperature was 45°C, and the reaction pressure was 0.5MPa. After 2.5 hours of reaction, the reaction materials were centrifuged to recover the reaction-controlled phase transfer catalyst.
[0028] The above-mentioned prepared material containing epichlorohydrin is continued to add 120 g of 50% hydrogen peroxide aqueous solution, 300 g of deionized water, and solid acid catalyst SiO 2 -Al 2 o 3 5g was reacted at 75°C for 1.5h, and the reaction pressure was 1.0MPa.
[0029] After the hydrolysis reaction was completed, the solid acid catalyst reaction material was filtered and separated, and the filtrate was washed with 350g of chloropropene and then subjected to vacuum distillation. The vacuum of the vacuum distillation was 200KPa, and the vac...
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More