Preparation method for natural isostearic acid
A technology of isostearic acid and stearic acid, applied in the field of preparation of natural isostearic acid, can solve the problems of increasing side reactions, affecting product quality and yield, and complicated processes, reducing pollution and achieving high utilization rate of raw materials. , good color effect
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Embodiment 1
[0026] In this example, the raw material monoacid is first subjected to pressurized catalytic hydrogenation to obtain hydrogenated monoacid, and then the hydrogenated monoacid is separated in a solvent by urea envelope to obtain crude isostearic acid and stearic acid, and the isostearic acid The crude product was distilled under reduced pressure to obtain isostearic acid product.
[0027] The raw material monoacid is a by-product monoacid produced during the production of dimer acid by thermal polymerization of oleic acid.
[0028] The step of pressurized catalytic hydrogenation of the single acid is that the single acid is under the action of the nickel-containing composite catalyst R1, the pressure is controlled at 0.05MPa, the temperature is controlled at 100°C, and hydrogen gas is introduced to react for 3 hours. After the reaction is completed, it is cooled and filtered out. Catalyst, the obtained filtrate is hydrogenated monoacid.
[0029] Described hydrogenated monoaci...
Embodiment 2
[0039] In this example, the raw material monoacid is first subjected to pressurized catalytic hydrogenation to obtain hydrogenated monoacid, and then the hydrogenated monoacid is separated in a solvent by urea envelope to obtain crude isostearic acid and stearic acid, and the isostearic acid The crude product was distilled under reduced pressure to obtain isostearic acid product.
[0040] The raw material monoacid is a by-product monoacid produced during the production of dimer acid by linoleic acid clay catalysis.
[0041] The step of pressurized catalytic hydrogenation of the single acid is that the single acid is under the action of the nickel-containing composite catalyst R1, the pressure is controlled at 1.0 MPa, the temperature is controlled at 180°C, and the hydrogen gas is introduced to react for 4 hours. After the reaction is completed, it is cooled and filtered out. Catalyst, the obtained filtrate is hydrogenated monoacid.
[0042] Described hydrogenated monoacid ur...
Embodiment 3
[0053] In this example, the raw material monoacid is first subjected to pressurized catalytic hydrogenation to obtain hydrogenated monoacid, and then the hydrogenated monoacid is separated in a solvent by urea envelope to obtain crude isostearic acid and stearic acid, and the isostearic acid The crude product was distilled under reduced pressure to obtain isostearic acid product.
[0054] The raw material monoacid is a by-product monoacid produced during the production of dimer acid by thermal polymerization of linoleic acid.
[0055] The octadecyl unsaturated fatty acid may be oleic acid, linoleic acid and the like.
[0056] The step of pressurized catalytic hydrogenation of the single acid is that the single acid is under the action of the nickel-containing composite catalyst R2, the pressure is controlled at 1.4 MPa, the temperature is controlled at 200 ° C, and the hydrogen gas is passed into the reaction for 5 hours. After the reaction is completed, it is cooled and filte...
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Abstract
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