C18 series fatty acid and C20-C22 series fatty acid fine separation method

A technology of fine separation and fatty acid, applied in the direction of fatty acid esterification, fat oil/fat refining, and fat production. The effect of separation efficiency

Active Publication Date: 2015-11-18
天津领碳能源环保科技有限责任公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

For the separation of long-chain fatty acid methyl esters, common methods include traditional rectification, urea inclusion, supercritical extraction, and low-temperature cryocrystallization, etc., but the separation purity of the above methods is generally not high, and usually only relatively high-purity saturated fatty acids can be obtained Methyl esters and unsaturated fatty acid methyl ester products, but it is almost impossible to obtain a single high-purity fatty acid methyl ester, especially for methyl stearate, methyl oleate and methyl linoleate, few people do it
figure 1 (a) is methyl palmitate (C16:0); (b) is methyl stearate (C18:0); (c) is methyl oleate (C18:1); (d) is linseed oil Acid methyl ester (C18:2), through figure 1 It can be seen that the difference in the structure of the latter three is only one to two double bonds, which results in very little difference in physical and chemical properties between the latter three, and conventional separation methods are rarely able to completely separate the three substances. separated; figure 2 (a) is eicosapentaenoic acid methyl ester (C20:5); (b) is docosahexaenoic acid (C22:6), through figure 2 It can be seen that methyl eicosapentaenoate and methyl docosahexaenoate belong to fatty acid methyl esters with long carbon chains and polyunsaturated bonds. Separation methods such as distillation and supercritical extraction are easy to cause deterioration of raw materials, and it is almost impossible to effectively separate the two through urea inclusion and low temperature freezing crystallization.
In summary, methyl stearate, methyl oleate and methyl linoleate or methyl eicosapentaenoate and methyl docosahexaenoate are completely separated to obtain a single The technology of fatty acid methyl ester is rarely reported, which seriously hinders the further research and application of high-purity and high value-added fatty acid methyl ester

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0036] The raw material used in this example is a vegetable oil with high acid value, and the acid value is 27.9 mgKOH / g as measured by the national standard GB-T5530-2005 method.

[0037] (1) Pretreatment of raw oil and fat, the specific steps are:

[0038] (a) Take the ionic liquid with a mass ratio of 1:6:48 [HO 3 S-(CH 2 ) 3 -NEt 3 ]Cl-FeCl 3 1. A certain high-acid value vegetable oil and methanol are added to the reaction vessel together; the reaction vessel is placed in a 50°C water bath, and the mixed solution in the container is stirred until a certain high-acid value vegetable oil and methanol fully react under the esterification catalysis of the ionic liquid Generate a pretreatment product with an acid value of less than 1 - a mixture of various fatty acid methyl esters;

[0039] (b) After the reaction is over, separate the ionic liquid by decantation and a variety of fatty acid methyl ester mixtures with an acid value of less than 1, and the various fatty acid ...

Embodiment 2

[0045] The raw material used in this example is industrial waste palm oil, and the acid value measured by the national standard GB-T5530-2005 method is 9.53mgKOH / g.

[0046] (1) Pretreatment of raw oil and fat, the specific steps are:

[0047] (a) Take the ionic liquid [BTBD]OH with a mass ratio of 1:2:20, industrial waste palm oil and methanol and add them to the reaction vessel; place the reaction vessel in a water bath at 60°C, and stir the mixed solution in the vessel until Industrial waste palm oil and methanol fully react under the esterification catalysis of ionic liquids to form a pretreatment product with an acid value of less than 1 - a mixture of various fatty acid methyl esters;

[0048] (b) After the reaction is over, separate the ionic liquid by decantation and a variety of fatty acid methyl ester mixtures with an acid value of less than 1, and the various fatty acid methyl ester mixtures are biodiesel;

[0049] (c) Rotate the separated [BTBD]OH ionic liquid at ...

Embodiment 3

[0054] The raw material used in this example is a waste fish oil with high acid value, and the acid value is 16.9 mgKOH / g as measured by the national standard GB-T5530-2005 method.

[0055] (1) Pretreatment of raw oil and fat, the specific steps are:

[0056] (a) Take the ionic liquid [MIMPS]PW with a mass ratio of 1:3:30, waste fish oil with high acid value and methanol and add them to the reaction container; place the reaction container in a water bath at 65°C, and stir the mixture in the container Until the waste fish oil with high acid value and methanol fully react under the esterification catalysis of ionic liquid to form a pretreatment product with an acid value less than 1-a mixture of various fatty acid methyl esters;

[0057] (b) After the reaction is over, separate the ionic liquid by decantation and a variety of fatty acid methyl ester mixtures with an acid value of less than 1, and the various fatty acid methyl ester mixtures are biodiesel;

[0058] (c) Rotate th...

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Abstract

The invention discloses a C18 series fatty acid and C20-C22 series fatty acid fine separation method. The method includes: pretreating the raw material animal and vegetable oil by a ionic liquid to obtain high-yield and low-acid value biodiesel, i.e. a mixture of a variety of fatty acid methyl esters, with the process being simple, green and environment-friendly; then placing the obtained biodiesel in a pressured reduced rectification tower kettle, taking the ionic liquid as an extraction agent to conduct extraction pressured reduced rectification, and collecting methyl stearate, methyl oleate and methyl linoleate or eicosapentaenoic acid methyl ester and docosahexaenoic acid methyl ester with mass percentage purity of over 98% at the tower top. The method provided by the invention makes up the blank of the prior art, has a convenient operation process, provides the operation process for separation of long-chain fatty-acid methyl esters with a same carbon number, different double-bond numbers and poor heat sensitivity, and lays the foundation for fine separation of fatty acid methyl ester.

Description

technical field [0001] The invention relates to a method for the fine separation of C18 series fatty acids and C20-C22 series fatty acids, in particular, extracting, depressurizing, rectifying, separating and purifying pretreated animal and vegetable oils by using ionic liquid as an extractant and obtaining stearic acid therefrom Methyl ester, methyl oleate and methyl linoleate or methyl eicosapentaenoate and methyl docosahexaenoate. Background technique [0002] my country has a vast territory and abundant natural resources, among which there are a large number of fatty acid resources of great value to people's production and life, such as C18 series fatty acids, and omega-3 and omega-6 unsaturated fatty acids. C18 series fatty acids mainly include stearic acid (octadecanoic acid), oleic acid (9-octadecenoic acid) and linoleic acid (9,12-octadecadienoic acid), which are mainly found in vegetable oils , widely used in many fields such as additives, oil additives, surfactant...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C11C3/04C10L1/02C11B3/12
Inventor 丁辉齐金龙
Owner 天津领碳能源环保科技有限责任公司
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