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Process method for preparing epoxy fatty acid ester based on double liquid phase extraction technology

A technology of epoxy fatty acid ester and extraction technology, which is applied in the field of epoxy plasticizer epoxy fatty acid methyl ester, can solve the problems of discontinuous industrial process and difficult product separation, and achieves reduction of reaction mass transfer resistance and epoxy conversion. High rate, less corrosive effect

Inactive Publication Date: 2016-01-13
NANJING TECH UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] The purpose of the present invention is to provide a kind of processing method that prepares epoxy fatty acid ester based on two-liquid phase extraction technology, to solve the problem that the raw material oil that obtains the better epoxy plasticizer of quality existing in the prior art all uses is refined oil
[0008] Another object of the present invention is to solve the problem of discontinuous industrialization process existing in the prior art
[0009] Another object of the present invention is to solve the difficult problem of product separation in the prior art

Method used

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  • Process method for preparing epoxy fatty acid ester based on double liquid phase extraction technology

Examples

Experimental program
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Effect test

Embodiment 1

[0037] Example 1 : figure 1 For the process flow diagram of preparing epoxy fatty acid ester based on two-liquid phase extraction technology, the specific steps are as follows:

[0038] Step 1 Add 50g of cottonseed powder into a three-necked flask, mix with 225ml of methanol containing 0.1% citric acid and 125ml of petroleum ether, stir at 30°C for 45 minutes, separate the solid from the liquid, and transfer the mixed solution to a separatory funnel for static Set the layers, the methanol phase in the lower layer is recovered by distillation, and the liquid in the upper layer is the petroleum ether phase containing cottonseed oil.

[0039] Step 2 Mix the petroleum ether phase containing cottonseed oil prepared in step 1 with 0.3 g of potassium hydroxide and 10 ml of methanol into the reaction kettle, stir and heat to 60° C. for 2 hours to react. After the reaction is over, let stand to separate layers. The upper layer is fatty acid methyl ester, and the lower layer is glyc...

Embodiment 2

[0041] Example 2 : Step 1: Add 50g of cottonseed powder into a three-necked flask, mix with 250ml of methanol containing 0.1% citric acid and 150ml of n-hexane, stir at 30°C for 45 minutes, separate the solid from the liquid, and move the mixture to a separatory funnel After standing for stratification, the methanol phase in the lower layer is recovered by distillation, and the liquid in the upper layer is the n-hexane phase containing cottonseed oil.

[0042] Step 2 is the same as step 2 of embodiment 1.

[0043]Step 3 is with the fatty acid methyl ester that makes in the step 2 and 5g formic acid and 1.2g acidic ion exchange resin

[0044] Add it into the reaction kettle, slowly add 28g of hydrogen peroxide dropwise, react at 60°C for 3.5h, let it stand for stratification, take the upper layer solution and wash it with water until it is neutral, and recover n-hexane by distillation under reduced pressure to obtain the target product epoxy fatty acid methyl ester . After ...

Embodiment 3

[0045] Example 3 : Step 1: Add 50g of cottonseed powder into a three-necked flask, mix with 300ml of methanol containing 0.1% citric acid and 150ml of isohexane, stir at 40°C for 40 minutes, separate the solid from the liquid, and move the mixture to a separatory funnel After standing for stratification, the methanol phase in the lower layer is recovered by distillation, and the liquid in the upper layer is the isohexane phase containing cottonseed oil.

[0046] Step 2 is the same as step 2 of embodiment 1.

[0047] Step 3 Add the fatty acid methyl ester prepared in step 2, 4g of formic acid and 1.5g of acidic ionic liquid into the reaction kettle, slowly add 16g of hydrogen peroxide dropwise, react at 60°C for 3.5h, let stand to separate layers, and take the upper layer The solution was washed with water until neutral, and the isohexane was recovered by distillation under reduced pressure to obtain the target product epoxy fatty acid methyl ester. After testing, the epoxy ...

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Abstract

The invention provides a process for preparing epoxy fatty acid esters based on two-liquid phase extraction technology, comprising the following steps: using two-liquid phase solvent extraction technology, using low-carbon alkanes as non-polar solvents, low-carbon alcohol-auxiliary -The low-carbon alcohol phase composed of water is a polar solvent to co-process oil-containing plant seeds; the low-carbon alkane phase containing crude vegetable oil is mixed with the basic catalyst-low-carbon alcohol solution and added to the transesterification reaction device for reaction to obtain fatty acids Esters and glycerin, after the reaction, let stand to separate and separate, the upper layer is the low-carbon alkane phase containing fatty acid esters; mix the low-carbon alkane phase containing fatty acid esters with organic acids and catalysts into the epoxy reactor, slowly drop Oxidizing agent, after the reaction is finished, let stand to separate layers, take the upper layer liquid, and reclaim the solvent by distillation under reduced pressure to obtain the target product epoxy fatty acid ester. The production process of the invention is environment-friendly, has low energy consumption, saves process time and reduces product cost.

Description

technical field [0001] The invention relates to a process for epoxy plasticizer epoxy fatty acid methyl ester, in particular to a process based on epoxy fatty acid methyl ester prepared from crude vegetable oil. Background technique [0002] Plastic products are widely used in people's daily life and have become indispensable daily necessities. In order to improve the processing performance and stability of plastic products, it is often necessary to add a certain proportion of plasticizers. Phthalates are currently the most used plasticizers. However, with the increasing awareness of global environmental protection, the toxicity and carcinogenicity of phthalate plasticizers have greatly restricted their application. Epoxy plasticizers have attracted much attention due to their excellent properties of being environmentally friendly, non-toxic and harmless. At present, the industrial production of epoxy plasticizers mainly includes: epoxy soybean oil, epoxy cottonseed oil, ep...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07D303/42C07D301/12
CPCC07D301/12C07D303/42
Inventor 云志丁滢桂霞包宗宏史美仁
Owner NANJING TECH UNIV