A kind of production method of conjugated linoleic acid
A conjugated linoleic acid and a production method technology are applied in the fields of chemical synthesis of oils and fats and production of linoleic acid, and can solve the problems of reduced purity of conjugated linoleic acid, large usage of catalysts, increased production cost, etc. Production time, improve production efficiency and equipment utilization, cost saving effect
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Embodiment 1
[0050] A conjugated linoleic acid production method, the specific process steps are as follows:
[0051] First, an ester exchange reaction
[0052] First, the Mole ratio is called 2: 1, respectively, the methanol and safflower seed oil, and 1 / 3 of the total amount of methanol and safflower oil are added to the continuous filler device (mass accounted for each wheel). 5% of the total mass of methanol and safflower oil in the exchange reaction; adjust the high pressure reaction kettle in supercritical carbon dioxide conditions, that is, 35 ° C, the temperature is 35 ° C, to reach the pressure to 16 MPa; in subsequent 15h The remaining 2 / 3 of methanol was slowly added to the high-pressure reactor by the carbon dioxide jacket; stirring the reaction at 300 r / min at a stirring rate of 300R / min, while the reaction was carried out by carbon dioxide (carbon dioxide from high pressure) while the reaction was reacted while the reaction was stirred. The bottom of the reactor is introduced...
Embodiment 2
[0064] A conjugated linoleic acid production method, the specific process steps are as follows:
[0065] First, an ester exchange reaction
[0066] First, the Mole is 4: 1, respectively, we can weigh ethanol and purple pepsum, and add 1 / 2 of ethanol to the purple filler oil to be added to the immobilized ester exchange enzyme (mass per round). In the exchange reaction, the total mass of the total mass of purple and ethanol is exchanged; the high pressure reactor is adjusted to supercritical carbon dioxide conditions, that is, the temperature is 45 ° C, and the carbon dioxide allows the pressure to reach 12 MPa; in subsequent 20h The remaining 1 / 2 of ethanol was slowly added to the high pressure reactor by the carbon dioxide jacket; stirring the reaction at a stirring rate of 300 r / min, while the reaction was reacted while the product containing fatty acid ethanol ester in the high pressure reactor was carbon dioxide (carbon dioxide from high pressure. The bottom of the reactor i...
Embodiment 3
[0078] The specific process steps of the production method of conjugated linoleic acid are as follows:
[0079] First, an ester exchange reaction
[0080] First, the mole is 3: 1, respectively, the proprinol with sunflower oil, and add 1 / 3 of propanol with sunflower seed oil to be added to the immobilized ester exchange enzyme (mass per round) 8% of the total mass of propanol and sunflower oil in the exchange reaction; adjust the high pressure reaction kettle in supercritical carbon dioxide conditions, that is, 50 ° C, transfer carbon dioxide to reach 10 MPa; in subsequent 18h The remaining 2 / 3 of propanol was slowly added to the high pressure reaction kettle by the carbon dioxide jacket; stirring the reaction at a stirring rate of 300 r / min, while the reaction was carried out by carbon dioxide (carbon dioxide from carbon dioxide while the reaction was stirred at 300 r / min. The bottom of the high pressure reactor is introduced and continuously transferred to the rectification ...
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