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
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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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