Method for preparing polyether polyol for wood-like polyurethane employing illegal cooking oil
A technology of polyether polyol and waste oil, which is applied in the field of preparing polyether polyol for wood-like polyurethane by using waste oil, can solve the problems of difficulty in popularization and application of soap, complicated composition of waste oil, etc., and achieves good performance, low production cost, Product stabilization effect
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Embodiment 1
[0018] 1) Formula: raw material mass ratio: sucrose: water: waste oil: propylene oxide=200:50:450:300.
[0019] 2) Production method: react water, sucrose and gutter oil at a temperature of 90-100°C for 1 hour according to the ratio, and react for 1-5 hours at -0.05-0.08 MPa after vacuum dehydration to obtain the reaction precursor. The first stage of reaction is completed; Then add catalyst, feed propylene oxide to carry out the second-stage polymerization reaction, the temperature is 120-150 ° C, keep the pressure at 0.3 MPa and continue to feed propylene oxide for reaction, after passing the propylene oxide, keep warm at 130-160 ° C to react until the pressure After reaching below -0.05MPa, continue to react for 1 hour, and finally remove water and small molecules to obtain waste oil polyether polyol.
[0020] The product indexes of the obtained polyether polyol: hydroxyl value 398.47, viscosity 4148, water content 0.04.
Embodiment 2
[0022] 1) Formula: raw material mass ratio: sucrose: gutter oil: glycerol: propylene oxide = 200:400:100:300.
[0023] 2) Production method: react glycerol, sucrose and gutter oil at a temperature of 90-100°C for 1 hour according to the ratio, and react for 1-5 hours at -0.05-0.08MPa after vacuum dehydration to obtain the reaction precursor. The first stage of reaction is completed ; Then add the catalyst, pass through propylene oxide to carry out the second stage of polymerization reaction, the temperature is 120-150°C, keep the pressure at 0.3MPa and continue to pass through propylene oxide for reaction, after passing through the propylene oxide, keep warm at 130-160°C until After the pressure is below -0.05MPa, the reaction is continued for 1 hour, and finally the water and small molecules are removed to obtain the waste oil polyether polyol.
[0024] The product index of the obtained polyether polyol: hydroxyl value 451.35, viscosity 2437, water content 0.07.
Embodiment 3
[0026] 1) Formula: raw material mass ratio: sorbitol: waste oil: glycerol: propylene oxide = 150: 450: 100: 300
[0027] 2) Production method: react sorbitol, glycerol and waste oil at a temperature of 90-100°C for 1 hour according to the ratio, and react at -0.05-0.08MPa for 1-5 hours after vacuum dehydration to obtain the first-stage reaction of the reaction precursor End; then add the catalyst, pass through propylene oxide to carry out the second-stage polymerization reaction, the temperature is 120-150°C, keep the pressure at 0.3MPa and continue to pass through propylene oxide for reaction, after passing through the propylene oxide, keep warm at 130-160°C for reaction Continue to react for 1 hour until the pressure is below -0.05MPa, and finally remove water and small molecules to obtain waste oil polyether polyol.
[0028] The product indexes of the obtained polyether polyol: hydroxyl value 377.13, viscosity 3271, water content 0.09.
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