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Method for industrially preparing medium-chain triglyceride

A medium-carbon chain triglyceride and a technology for carbon-chain triglycerides are applied in the field of industrialized preparation of medium-carbon chain triglycerides, can solve the problems of many side reactions, dehydration, and high investment costs, and reduce production costs, yield and The effect of high esterification rate and time shortening

Pending Publication Date: 2022-04-12
POLYROCKS TECH&RES CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, enzymatic synthesis technology is still immature so far, although it has been widely studied, it is still in the laboratory stage.
[0005] The currently disclosed method for preparing medium-carbon chain triglycerides, the catalyst mainly includes an acidic solid catalyst, which is a macroporous strong acidic cation exchange resin, immobilized phosphotungstic acid, and the lipase is an immobilized lipase, mainly Novozyme435 or LipozymeRMIM , the last is traditional sulfuric acid, etc. Different catalysts have different characteristics. The advantage of lipase is environmental protection, but its disadvantages are also obvious and often cannot be applied due to long reaction time and high investment. Secondly, compared with traditional Although the acid provides convenience for post-processing, it also faces difficulties that are difficult to bypass with traditional acids, such as high reaction temperature, usually around 180°C, and long time, usually 14 hours, which can easily cause fatty acid polymerization, glycerin oxidation and dehydration. It leads to many side reactions and high energy consumption, and the product quality and color are not ideal, so a lot of post-processing work is required, resulting in high production costs

Method used

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  • Method for industrially preparing medium-chain triglyceride
  • Method for industrially preparing medium-chain triglyceride

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0046] The present embodiment has prepared a kind of caprylic acid-capric triglyceride, and specific process is:

[0047](1) Measure 3kg of industrial grade glycerin, 12kg of caprylic acid and 6kg of capric acid respectively through a meter, and transport each raw material into the esterification reactor through a vacuum pump; simultaneously open the heating device, the vacuum device and the stirring device of the esterification reactor, Control the pressure of the reactor to -0.1MPa, and the stirring speed to 100r / min; when the temperature of the material system in the reactor rises to 70°C-90°C, keep stirring for 20 minutes in this state to remove the air carried in the raw material Moisture and other volatile gases are added with a catalyst (the mass of p-toluenesulfonic acid accounts for 45%, and the mass of hypophosphorous acid accounts for 55%). The mass of the catalyst is 0.7% of the total mass of raw materials. Carry out three-stage programmatic temperature rise and de...

Embodiment 2

[0051] The present embodiment has prepared a kind of caprylic acid-capric triglyceride, and specific process is:

[0052] (1) Measure 3kg of industrial grade glycerin, 9kg of caprylic acid and 6kg of capric acid respectively through a meter, and transport each raw material into the esterification reactor through a vacuum pump; simultaneously open the heating device, vacuum device and stirring device of the esterification reactor, Control the pressure of the reactor to -0.1MPa, and the stirring speed to 100r / min; when the temperature of the material system in the reactor rises to 70°C to 80°C, keep stirring for 20 minutes in this state to remove the air carried in the raw materials Moisture and other volatile gases are added with a catalyst (the mass of p-toluenesulfonic acid accounts for 40%, and the mass of hypophosphorous acid accounts for 60%). The mass of the catalyst is 1.0% of the total mass of raw materials. Carry out three-stage programmed temperature rise and depressu...

Embodiment 3

[0056] The present embodiment has prepared a kind of caprylic acid-capric triglyceride, and specific process is:

[0057] (1) Measure 4kg of industrial grade glycerin, 11kg of caprylic acid and 9kg of capric acid respectively through a meter, and transport each raw material into the esterification reactor through a vacuum pump; simultaneously open the heating device, the vacuum device and the stirring device of the esterification reactor, Control the pressure of the reactor to -0.1MPa, and the stirring speed to 90r / min; when the temperature of the material system in the reactor rises to 80°C to 90°C, keep stirring for 20 minutes in this state to remove the air carried in the raw materials Moisture and other volatile gases are added with a catalyst (the mass of p-toluenesulfonic acid accounts for 50%, and the mass of hypophosphorous acid accounts for 50%). The mass of the catalyst is 0.4% of the total mass of raw materials. Carry out three-stage programmed temperature rise and ...

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Abstract

According to the method for industrially preparing the medium-chain triglyceride, the composite catalyst is adopted, caprylic acid, capric acid and glycerol react, the high-purity caprylic / capric triglyceride product is synthesized through three-stage programmed heating and decompression, the efficiency is high, the yield and the esterification rate are high, the energy consumption is reduced, and the production cost is remarkably reduced; the industrial preparation of the high-purity medium-carbon chain triglyceride is realized.

Description

technical field [0001] The invention belongs to the fields of oleochemical technology and fine chemical technology, and in particular relates to a method for industrially preparing medium-carbon chain triglycerides. Background technique [0002] C 8 -C 10 Fatty acid triglycerides, commonly known as medium chain triglycerides (MCT), are widely used in food, medicine and other industries. MCTs are esters derived from the reaction of fatty acids with a carbon chain length of 8 to 10 and glycerol. MCTs consist of a glycerol backbone and three fatty acids attached to the backbone. Typical MCTs refer to saturated caprylic triglycerides or saturated capric triglycerides or saturated caprylic-capric mixed triglycerides. [0003] MCTs are generally considered to be an excellent source of bio-inert energy that is easily metabolized by the body. Due to their rapid absorption by the body, medium chain triglycerides have been used in the treatment of various malabsorption disorders....

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C67/08C07C69/30A61K31/23A61P3/04A61P3/00A61P3/06A61K47/14A23L33/115C07C67/52C07C67/54
Inventor 兰天齐郭欢朱红芳戚良明杨正高陈钢
Owner POLYROCKS TECH&RES CO LTD
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