Environment protection type starch-base surfactant and its preparing process
A technology of surfactants and production methods, applied in chemical instruments and methods, dissolution, chemical/physical processes, etc., can solve problems such as low product quality and long production cycle, and achieve good compatibility, fast reaction speed, and color easy effect
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Embodiment 1
[0012] Add 5 kg of starch into a 20 liter reactor, add 10 kg of butanol, 0.05 kg of catalyst (a compound system made of p-toluenesulfonic acid and rare earth chloride according to 8:2), replace the air with nitrogen, and heat up to 150 ℃, the system pressure is 6Kg / cm 2 . As the reaction proceeds, the system pressure drops, and the reaction time is 2 hours, and the pressure drops to 2Kg / cm 2 And stable, the temperature was lowered to 70°C, and 1 / 3 was released for use (hereinafter referred to as intermediate).
[0013] Then add 2.5 kilograms of oleic acid monoethanolamide in the reactor. Vacuumize and react under stirring, the butanol is continuously distilled out, the temperature of the system rises, when the temperature rises to 150 ° C, the constant temperature reaction, the vacuum degree is not less than 0.09 MPa, the reaction is 3 hours, when the butanol no longer flows out, Raise the temperature to 200°C, vacuum degree 0.09987 MPa, remove excess oleic acid monoethanol...
Embodiment 2
[0016] Add 5 kg of starch into a 20 liter reactor, add 10 kg of butanol, 0.05 kg of catalyst (a compound system made of p-toluenesulfonic acid and rare earth chloride according to 8:2), replace the air with nitrogen, and heat up to 150 ℃, the system pressure is 6Kg / cm 2 . As the reaction proceeds, the system pressure drops, and the reaction time is 2 hours, and the pressure drops to 2Kg / cm 2 And stable, the temperature was lowered to 70°C, and 1 / 3 was released for use (hereinafter referred to as intermediate).
[0017] Then add 2.5 kilograms of C12-14 fatty alcohol in the reactor. Vacuumize and react under stirring, the butanol is continuously distilled out, the temperature of the system rises, when the temperature rises to 150 ° C, the constant temperature reaction, the vacuum degree is not less than 0.09 MPa, the reaction is 3 hours, when the butanol no longer flows out, Raise the temperature to 200°C, vacuum 0.09987 MPa, remove excess C12-14 alcohol for 1 hour, cool down...
Embodiment 3
[0020] Add 5 kg of starch into a 20 liter reactor, add 10 kg of butanol, 0.05 kg of catalyst (a compound system made of p-toluenesulfonic acid and rare earth chloride according to 8:2), replace the air with nitrogen, and heat up to 150 ℃, the system pressure is 6Kg / cm 2 . As the reaction proceeds, the system pressure drops, and the reaction time is 2 hours, and the pressure drops to 2Kg / cm 2 And stable, the temperature was lowered to 70°C, and 1 / 3 was released for use (hereinafter referred to as intermediate).
[0021] Then add 2.5 kilograms of coconut oil monoethanolamides in the reactor. Vacuumize and react under stirring, the butanol is continuously distilled out, the temperature of the system rises, when the temperature rises to 150 ° C, the constant temperature reaction, the vacuum degree is not less than 0.09 MPa, the reaction is 3 hours, when the butanol no longer flows out, Raise the temperature to 200°C, vacuum degree 0.09987 MPa, remove excess coconut oil monoetha...
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