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A kind of separation and purification method of by-product of ester bond reaction of oil

A technology of by-products and ester bonds, applied in the field of recycling by-products, can solve the problems of increased acid value of main products, decreased quality of main products, entry of free acid, etc.

Active Publication Date: 2020-10-20
ZHEJIANG MEDICINE CO LTD XINCHANG PHAMACEUTICAL FACTORY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, this process will convert the soap formed in the transesterification process into free acid and mix it into the oil layer after acidification, resulting in an increase in the acid value of the final product and affecting product quality.
[0010] CN203960088U and CN 103013673A disclose two kinds of separation devices for glycerol in biodiesel production. The former separates other components to purify glycerin by adjusting the pH value of the glycerin phase, because free acid will be produced in the acidification process, which will affect the quality of biodiesel; the latter Separation of glycerin by sedimentation method based on the density of oil phase and glycerin phase, it is difficult to effectively separate the components in the by-products
[0011] Generally speaking, the current research does not pay enough attention to the treatment of the by-product phase in the ester bond reaction of oils and fats. There is no detailed analysis of the composition, and there is no targeted recovery method for each component. Some existing recovery processes are also mainly for glycerol. The recovery, the deficiencies that exist in the recovery purification process mainly contain the following aspects:
[0012] 1. After the reaction is completed, the by-product phase is directly layered and separated. Due to the high viscosity, it is easy to stick to the wall, especially when it is difficult to define the boundary liquid level during industrial production layering, and the operation is difficult;
[0013] 2. The separation process is rough, and the by-product phase contains unreacted glycerides, short-chain alcohol esters, soaps, glycerin, alkalis, solvents and other components, which are not separated and purified separately, resulting in a decrease in product yield, Purification is difficult;
[0014] 3. Improper separation and purification methods lead to a decline in the quality of the main product. For example, acidification before stratification in the alcoholysis process will cause free acid to enter the upper main product, resulting in an increase in the acid value of the main product;

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0048] 500g of sunflower oil and 200mL of ethanol are carried out alcoholysis reaction under KOH catalysis to prepare sunflower oil ethyl ester, reclaim ethanol after reaction is completed, add 50mL of acetonitrile aqueous solution, wherein acetonitrile: water=2:1, after mixing uniformly, let stand and separate, The upper layer is subjected to degassing, decolorization, distillation and other purification operations to obtain the main product sunflower oil ethyl ester.

[0049] Phosphoric acid is added dropwise to the by-product phase of the lower layer to adjust the pH to 6, and the layers are left to stand:

[0050] After the upper layer is degassed, 5g of ethyl ester is obtained through primary molecular distillation, which has the same composition as the main product sunflower oil ethyl ester, and is added to the main product; after the second molecular distillation, 7g of free fatty acid is obtained, which can be used to prepare ethyl ester or It is used; the remaining 4g...

Embodiment 2

[0053] 200g of soybean oil and 100mL of methanol were subjected to alcoholysis reaction under the catalysis of sodium methoxide to prepare biodiesel. After the reaction was completed, the methanol was recovered, and 60mL of acetone aqueous solution was added, wherein acetone:water=3:1. Then get the main product of biodiesel.

[0054] Add hydrochloric acid dropwise to the by-product phase of the lower layer to adjust the pH to 2, and let the layers stand:

[0055] After the upper layer is degassed, 3g of methyl ester is obtained through primary molecular distillation, which has the same composition as the main product methyl ester, and is added to the main product as biodiesel; after the second molecular distillation, 3g of free fatty acid is obtained, which can be prepared after esterification Ethyl esters or other uses; the remaining 2g is incompletely reacted glycerides, mainly monoglycerides and diglycerides, which can be used as raw materials for the next batch of producti...

Embodiment 3

[0058] 1000g algae oil and 400mL NaOH aqueous solution, heat and stir, saponification and hydrolysis reaction to prepare algae oil free fatty acid, recover part of the solvent after the reaction is completed, add 700mL methanol, mix evenly, let stand and separate, and the upper layer is purified to obtain algae oil free fatty acid product.

[0059] Add sulfuric acid dropwise to the by-product phase of the lower layer to adjust the pH to 4, and let stand to separate layers:

[0060] After the upper layer is degassed, 30g of oil fatty acid is obtained by primary molecular distillation. The composition is the same as that of algal oil free acid prepared from the main product. As the main product of fatty acid, the remaining 5g is incompletely reacted glyceride, which can be used as the next batch of production raw materials or other uses.

[0061] The lower layer was cooled to -10°C to crystallize for 1 hour, filtered, and the filter cake was sodium sulfate; methanol was recovere...

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PUM

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Abstract

The invention discloses a separation and purification method of oil transesterification reaction by-products. At present, after transesterification reactions of oil are completed, by-product phases are directly layered and separated; the by-product phases are large in stickiness and easy to stick to walls, particularly, during industrial production layering, liquid surfaces are difficult to delimit and separate, the operation difficulty is large, the separation process is crude, so that the product yield is reduced, and the purifying difficulty is large. In accordance with the by-product phases after an alcoholysis reaction or a saponification reaction in which glyceride ester bonds participate, a polarity solvent is firstly used for adjusting the polarity and the stickiness of the system, and complete separation of the by-product phases from main products is realized; then, regulating the pH value of the by-product phases is combined with rectification or multistage molecular distillation so as to separate glyceride, and short chain alcohol ester or / and free fatty acids; through crystallization filtering, inorganic salts are separated; finally, the polarity solvent is recovered, and then rectification is preformed, so that high-purity glycerine is obtained. The separation and purification method disclosed by the invention realizes recovering and purifying of components, so that the utilization value of the by-product phases is greatly increased, and besides, the yield and the competitiveness of the main products are also increased.

Description

technical field [0001] The invention relates to a method for recycling reaction by-products, in particular to a method for separating and purifying by-products produced in alcoholysis reactions or saponification reactions in which glyceride bonds participate. Background technique [0002] Natural oils exist in the form of triacylglycerols. In practical applications, due to the complex composition and high boiling point of glycerolipids, it is difficult to purify, which restricts its application. The reaction of glyceride ester bonds is the basis for the realization of transesterification and hydrolysis of oils. It is very important and common in oil industry production. According to production needs, free acids or other fatty acids with simple structure and easy purification can be prepared from glycerides through the reaction of ester bonds. Short-chain alcohol esters, and subsequent purification or reaction can greatly expand the application space of oils. For example, fa...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C31/22C07C29/74C07C29/88
CPCC07C29/74C07C29/88C07C31/225
Inventor 彭永健许新德张莉华代志凯邵斌
Owner ZHEJIANG MEDICINE CO LTD XINCHANG PHAMACEUTICAL FACTORY
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