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The synthetic method of fatty acid methyl ester alkoxylation catalyst

A fatty acid methyl ester alkane and synthesis method technology, which is applied in the field of synthesis of fatty acid methyl ester alkoxylation catalysts, can solve problems such as low EO distribution index, narrow EO distribution, and many by-products

Active Publication Date: 2018-04-06
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] One of the technical problems to be solved by the present invention is after the catalyst ethoxylation reaction existing in the prior art, the EO distribution index in the ethoxylation product is low, the problem of many by-products, a kind of new fatty acid methyl ester B is provided A synthesis method of an oxygenation catalyst, the method has the characteristics of narrow distribution of EO in the ethoxylation product and few by-products when the obtained catalyst is used for the ethoxylation reaction of fatty acid methyl ester

Method used

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  • The synthetic method of fatty acid methyl ester alkoxylation catalyst
  • The synthetic method of fatty acid methyl ester alkoxylation catalyst
  • The synthetic method of fatty acid methyl ester alkoxylation catalyst

Examples

Experimental program
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Effect test

Embodiment 1

[0030] Put 2mol of 1-ethyl-3-methylimidazolium bromide and 6mol of isopropanol in a three-necked flask with reflux condensation, stir and heat at 80°C for 30min, and obtain mixture i after cooling; mix 2g of anhydrous magnesium acetate, 0.5g of Aqueous zinc acetate and 100g of mixture i were placed in a three-necked flask with reflux condensation, stirred and heated at 80°C for 30min, and cooled to obtain mixture ii; sulfuric acid with a concentration of 98wt% was added dropwise to mixture ii under vigorous stirring to make the mixture pH is 6.0, the mixture iii is obtained after cooling; the mixture iii is vacuum-dried at 80° C. for 30 min, and the desired catalyst is obtained after cooling.

[0031] Add the above 1.0g catalyst to 100g methyl laurate, and put it into a 1L autoclave while stirring; the autoclave is heated to 80°C, vacuum-dried for 10min, and then replaced with high-purity nitrogen for 3 times, and the temperature is raised to 150°C. Introduce EO, keep the temp...

Embodiment 2

[0034] Put 2mol of 1-ethyl-3-methylimidazolium bromide and 6mol of isopropanol in a three-necked flask with reflux condensation, stir and heat at 80°C for 30min, and obtain mixture i after cooling; mix 2g of anhydrous magnesium acetate, 0.5g of Water cadmium acetate and 100g of mixture i are placed in a three-necked flask with reflux condensation, stirred and heated at 80°C for 30min, and cooled to obtain mixture ii; the sulfuric acid with a concentration of 98wt% is added dropwise to mixture ii under vigorous stirring to make the mixture pH is 6.0, the mixture iii is obtained after cooling; the mixture iii is vacuum-dried at 80° C. for 30 min, and the desired catalyst is obtained after cooling.

[0035]Add the above 1.0g catalyst to 100g methyl laurate, and put it into a 1L autoclave while stirring; the autoclave is heated to 80°C, vacuum-dried for 10min, and then replaced with high-purity nitrogen for 3 times, and the temperature is raised to 150°C. Introduce EO, keep the te...

Embodiment 3

[0038] Put 2mol of 1-ethyl-3-methylimidazolium bromide and 6mol of isopropanol in a three-necked flask with reflux condensation, stir and heat at 80°C for 30min, and obtain mixture i after cooling; mix 2g of anhydrous barium acetate, 0.5g of Aqueous zinc acetate and 100g of mixture i were placed in a three-necked flask with reflux condensation, stirred and heated at 80°C for 30min, and cooled to obtain mixture ii; sulfuric acid with a concentration of 98wt% was added dropwise to mixture ii under vigorous stirring to make the mixture pH is 6.0, the mixture iii is obtained after cooling; the mixture iii is vacuum-dried at 80° C. for 30 min, and the desired catalyst is obtained after cooling.

[0039] Add the above 1.0g catalyst to 100g methyl laurate, and put it into a 1L autoclave while stirring; the autoclave is heated to 80°C, vacuum-dried for 10min, and then replaced with high-purity nitrogen for 3 times, and the temperature is raised to 150°C. Introduce EO, keep the tempera...

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Abstract

The invention relates to a synthesis method of a fatty acid methyl ester alkoxylation catalyst, which solves the problem of low EO distribution index in catalyst reaction products in the prior art. The method comprises the following steps: (1) mixing an ionic liquid with a molar ratio of 1: (1 to 10) and a C1 to C4 alcohol to obtain a mixture i; (2) adding an alkaline earth metal salt and a group II B metal salt to the mixture i and Mix to obtain mixture ii, wherein the mass ratio of the alkaline earth metal salt, II B group metal salt and mixture i is (0.1~0.3):(0.01~0.10):1; (3) adjust the pH of mixture ii to 5~8 to obtain mixture iii (4) vacuum drying mixture iii below 100°C to obtain the catalyst; the ionic liquid is a technical solution of imidazolium salt ionic liquid, which solves this technical problem well and can be used for fatty acid methyl ester alkoxy reaction.

Description

technical field [0001] The invention relates to a method for synthesizing a fatty acid methyl ester alkoxylation catalyst. Background technique [0002] Ethoxylated fatty acid methyl esters (FMEE for short) is a double-capped ester ether nonionic surfactant. Since fatty acid methyl ester ethoxylates have -OCH at one end similar to oil 3 , according to the principle of similar compatibility, compared with traditional fatty acid polyether, fatty alcohol polyether, etc., it has stronger decontamination ability, good water solubility, low melting point, strong emulsifying and dispersing ability, less foam, etc.; in addition The product is easy to degrade and is a real environmentally friendly surfactant. Fatty acid methyl ester compounds are widely used in leather, textile and cosmetic industries. FMEE is close to the TX, NP and OP series containing APEO in various performances. Under the background of strict environmental protection requirements abroad, using FMEE instead of...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J31/04C07C69/28C07C67/26
Inventor 肖忠斌畅延青
Owner CHINA PETROLEUM & CHEM CORP