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

Active Publication Date: 2021-07-06
HANDAN CHENGUANG PRECIOUS OIL
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] Chinese patent CN107216249A discloses a preparation method of conjugated linoleic acid, which is to carry out transesterification reaction between vegetable oil and short-chain alcohol under the action of basic catalyst to prepare fatty acid short-chain alcohol ester, and then add basic catalyst to carry out isomerization Chemical reaction, saponification, acidification, and molecular distillation after low-temperature crystallization. In this preparation method, the transesterification reaction is to add a non-reusable basic catalyst to carry out the catalytic reaction. The catalyst uses a large amount and is not easy to recycle. It is costly and pollutes the environment. Secondly, the final product is obtained by molecular distillation. Due to the high boiling point of fatty acids, the high temperature during purification will increase the trans-isomer of conjugated linoleic acid, resulting in deterioration of product quality; In the production process, other by-products, such as some substances obtained by the reaction of oleic acid or palmitic acid in the starting raw material vegetable oil, will also be incorporated into the final product conjugated linoleic acid, which further leads to the purity of conjugated linoleic acid. reduce
[0007] A method for preparing conjugated linoleic acid disclosed in Chinese patent CN101440030B is to use corn germ or corn germ oil as a raw material, through the enrichment of linoleic acid under certain temperature and pressure conditions, alkali-catalyzed isomerization, ultra- The critical reaction separator and the rectifier are obtained by rectification. The whole process is carried out under the condition of supercritical carbon dioxide. The energy consumption of the reaction is high, and the product is also purified after the conjugation reaction. Consumption of processing aids also increases production costs
[0008] Chinese patent CN107312805A discloses a method for preparing polyunsaturated fatty acids of conjugated linoleic acid, which is to add lipase to the oil for enzymolysis, then enrich the polyunsaturated fatty acids by urea inclusion method, supercritical carbon dioxide extraction, alkali Catalytic isomerization to prepare conjugated linoleic acid, in which lipase is added according to the quality of oil, lipase is free in the reaction raw materials, the enzymolysis effect is poor, the utilization rate of the enzyme is low, and the enzyme recovery is difficult; the urea inclusion method will have the need The problem of a large amount of organic solvents requires more cost to remove organic solvents in the later stage

Method used

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Effect test

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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Abstract

The invention discloses a production method of conjugated linoleic acid, which belongs to the field of chemical synthesis methods of fats and oils. The separated short alcohol ester of linoleic acid is subjected to alkali-catalyzed isomerization, saponification, acid hydrolysis and water washing to obtain conjugated linoleic acid. The production process of the present invention can be carried out continuously and efficiently, and has the advantages of simple preparation process, mild reaction conditions, high utilization rate of raw materials, high product purity, and high product stability; low energy consumption not only reduces production cost, but also reduces Pollution to the environment, suitable for large-scale production.

Description

Technical field [0001] The present invention relates to the preparation of fatty acids, in particular a method of producing a linoleic acid, which is a chemical synthesis method of grease. Background technique [0002] Lyric acid is one of a variety of fatty acids that form fat. Lyric acid is both one of people and animals that are indispensable fatty acids, and a substance that cannot be synthesized by people and animals must be taken from food. The conjugated linoleic acid (CLA) is the isomer of linoleic acid. It is a series of linoleic acid in carbon 9, 11 or 10, 12 bonds and geometric isomers in nature. It mainly exists in ruminant cattle, sheep cream and meat products and some plants, but the content is very small. It has been studied that conjugated linoleic acid has anti-cancer, removes free radicals, enhancing the human antioxidant capacity and immunity, promoting growth development, regulates blood cholesterol and triglyceride levels, prevents atherosclerosis, promotes f...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C51/42C07C51/493C07C51/44C07C51/50C07C57/12
CPCC07C51/42C07C51/44C07C51/493C07C51/50C07C57/12
Inventor 王靖云杨俊旺田章起李晓辉田良红
Owner HANDAN CHENGUANG PRECIOUS OIL
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