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Production method of fatty acid diglyceride and special reactor

The technology of a fatty acid diglyceride and a production method, which is applied in the field of deep processing of oils and fats, can solve the problems of high energy consumption, excessive oil and high production costs in the production process, and achieve the effects of low energy consumption and high quality

Active Publication Date: 2015-01-07
山东巧妻食品科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] Currently published patent application: a preparation method of partial glycerides, application number: CN201110083076.1, which mainly passes through a special reactor - fiber reactor (not every manufacturer can afford this special reactor) ), the main product it wants to obtain is monoglyceride, as can be seen from its claim 1. (2) the mol ratio of raw oil and glycerol is 1: 3-30, in addition, this patent application also has There are two flaws: one is that glycerin and alkaline catalyst are simply mixed, which will saponify and lose more oil, and the reaction effect is not good. As can be seen from its embodiment 1 / 2 / 3, this oil glycerin After the proportioning reaction, the monoglyceride should be 42%--50%, and the diglyceride should be more than 50%. This patent application also has other small problems, such as how to deal with its alkaline catalyst, it can only stay in the glycerol monoglyceride. Ester neutralizes diglycerides to prevent alkaline catalysts from remaining in fatty acid diglycerides, which can damage the product by saponification
[0005] In some other published patent applications, the method for manufacturing diglycerides is all reacted with a reaction tank, which is a batch reaction equipment. Their disadvantages are that they cannot be produced on a large scale, and the production process has high energy consumption, resulting in high production cost

Method used

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  • Production method of fatty acid diglyceride and special reactor

Examples

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Effect test

Embodiment 1

[0032] 80 kg of glycerin, 1 kg of sodium hydroxide, heat the glycerin to 100 degrees to completely dissolve the sodium hydroxide

[0033] Solution in glycerin, stand-by; 1000 kg of cotton oil, after the heater is preheated to 180 degrees, then spray the sodium hydroxide glycerin solution into the cotton oil to react; the reaction temperature is 260 degrees, and the reaction time is 10 minutes; the reaction is over After the fat is cooled to 80 degrees, add 1 kg of neutralizing agent phosphoric acid, stand still for 0.5 hours after neutralization, discharge unreacted glycerol solution and generated phosphate; then carry out distillation to separate diglyceride and monoglyceride.

Embodiment 2

[0035]180 kg of glycerin, 0.5 kg of potassium hydroxide, heat the glycerin to 100 degrees, so that the potassium hydroxide is completely dissolved in the glycerin, and set aside; Spray the glycerin solution into the cotton oil to react; the reaction temperature is 240 degrees, and the reaction time is 30 minutes; after the reaction, the oil is cooled to 80 degrees, and the neutralizing agent phosphoric acid is added. solution and the resulting phosphate; followed by distillation to separate diglycerides and monoglycerides.

Embodiment 3

[0037] 270 kg of glycerin, 1 kg of calcium hydroxide, heat the glycerin to 100 degrees, so that the calcium hydroxide is completely dissolved in the glycerin, and set aside; 1000 kg of cotton oil, after the heater is preheated to 180 degrees, then the Spray the glycerin solution into the cotton oil to react; the reaction temperature is 230 degrees, and the reaction time is 50 minutes; after the reaction, the oil is cooled to 80 degrees, and 1 kg of neutralizing agent phosphoric acid is added, and the unreacted glycerin is discharged after neutralization solution and the resulting phosphate; followed by distillation to separate diglycerides and monoglycerides.

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Abstract

The invention provides a production method of fatty acid diglyceride and a special reactor belongs to the fields of fat deep processing methods and special devices. The production method of the fatty acid diglyceride includes: mixing glycerite heated to a preset temperature with catalysts prior to respectively delivering the catalyst-glycerite mixture and fat heated to a preset temperature to the reactor of a special structure; in the reactor, subjecting catalyst-glycerite mixture and the fat to transesterification and esterification so as to generate a reaction product containing diglyceride and monoglyceride; and finally, separating the fatty acid diglyceride from the reaction product by the aid of multistage molecular distilling devices. The production method of the fatty acid diglyceride is naturally carried out in the reactor, and continuous production can be well achieved without power stirring and with low energy consumption; in high-temperature reaction, the produced fatty acid diglyceride is high-quality under protection of nitrogen; and when adopted, the basic catalyst subjected to weak acid neutralization reaction is prevented from remaining in the fatty acid diglyceride to play a saponated destruction role in the fatty acid diglyceride.

Description

(1) Technical field [0001] The invention relates to a deep processing method and special equipment for oil, in particular to a production method and a special reactor for producing functional oil fatty acid diglycerides from cotton oil. (2) Background technology [0002] Cotton oil is a by-product of the cotton planting industry. Before the reform and opening up, because the refining level of cotton oil was not high, the residue of gossypol, which is harmful to human body, was relatively high in cotton oil. This shadow has been affecting the present for decades. With the current With the advancement of oil refining technology, cottonseed oil adopts advanced degumming, deacidification, dehydration, decolorization, deodorization, dewaxing and other six degassing processes, which can effectively remove gossypol and other harmful substances in cottonseed oil, and the taste is pure and healthy. Cotton oil contains a large amount of essential fatty acids, among which linoleic acid...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C11C3/04C11C3/06C11C3/10
Inventor 饶雨农
Owner 山东巧妻食品科技有限公司