Preparation method of starch octenyl succiniade under supercritical condition
An octenyl succinic acid and supercritical technology, applied in the production of bulk chemicals, etc., can solve the problems of increasing the complexity of the post-treatment process, improving the esterification efficiency of the esterification reaction, prolonging the production cycle of the product, and achieving esterification reaction High efficiency, guaranteed food safety, fast penetration effect
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Embodiment 1
[0026] Add 100 parts of cornstarch, 0.3 parts of oxidant, 5 parts of esterification agent, 2.0 parts of sodium hydroxide, 15 parts of water in the supercritical reactor, and use supercritical CO 2 As the reaction medium, at the supercritical temperature of 35°C, the supercritical pressure of 7.5MPa, and the rotation speed of 200r / min, the oxidation and esterification reactions are simultaneously carried out under the stirring state. The reaction time is 1 hour. After the reaction is completed, the extraction temperature is 40°C and the pressure is 18MPa. , CO 2 The product was extracted and purified under supercritical conditions with a flow rate of 15 L / h to obtain a powdered starch octenyl succinate product.
[0027] The product obtained in this example has a degree of substitution of 0.0052 and a viscosity of 10 mPa·s (6%, 95°C).
Embodiment 2
[0029]Add 100 parts of cornstarch, 3.8 parts of oxidizing agent, 18 parts of esterification agent, 2.0 parts of sodium carbonate, 30 parts of water in the supercritical reactor, and use supercritical CO 2 As the reaction medium, at the supercritical temperature of 80°C, the supercritical pressure of 28MPa, and the rotation speed of 400r / min, the oxidation and esterification reactions are simultaneously carried out under stirring. The reaction time is 6 hours. After the reaction is completed, the extraction temperature is 60°C and the pressure is 28MPa CO 2 The product was extracted and purified under supercritical conditions with a flow rate of 15 L / h to obtain a powdered starch octenyl succinate product.
[0030] The product obtained in this example has a degree of substitution of 0.105 and a viscosity of 12 mPa·s (6%, 95°C).
Embodiment 3
[0032] Add 100 parts of potato starch, 1.5 parts of oxidant, 10 parts of esterification agent, 22 parts of water, 3.0 parts of sodium hydroxide in the supercritical reactor, and use supercritical CO 2 As the reaction medium, at the supercritical temperature of 65°C, the supercritical pressure of 12MPa, and the rotation speed of 280r / min, the oxidation and esterification reactions are simultaneously carried out under stirring. The reaction time is 4 hours. After the reaction is completed, the extraction temperature is 45°C and the pressure is 22MPa CO 2 The product was extracted and purified under supercritical conditions with a flow rate of 20 L / h to obtain a powdered starch octenyl succinate product.
[0033] The product obtained in this example has a degree of substitution of 0.073 and a viscosity of 18 mPa·s (6%, 95°C).
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