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Fatty oil ethoxylate and process for preparing the same

A technology of ethoxylates and oils, applied in chemical instruments and methods, chemical/physical processes, dissolution, etc., can solve the difficulty of potassium hydroxide to achieve the catalytic effect, the difficulty of non-ionic products, the irritation of non-ionic surfactants and Unsatisfactory ecological toxicity and other problems, to achieve the effect of excellent oil solubilization ability, HLB value can be adjusted at will, and superior emulsification performance

Active Publication Date: 2007-06-13
中轻日化科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] This process has a long process route, and the preparation of methyl ester still needs to go through operations such as washing, dehydration, and distillation, and the process is cumbersome.
Due to the collection of by-product methanol, a frozen brine system needs to be configured, and methyl ester hydrogenation requires high temperature and high pressure, so the equipment is complicated, resulting in high product costs. In addition, the irritation and ecotoxicity of alcohol ether nonionic surfactants are not ideal. The foam is too rich, it is not easy to rinse
However, it is difficult to directly synthesize non-ionic products from oils and fats by one-step ethoxylation
Natural oils are mainly triglycerides, not only the raw materials themselves have no active hydrogen connected with heteroatoms, but also contain three long chains in the molecule, with large molecular weight and large steric hindrance. Traditional ethoxylation catalysts such as sodium hydroxide , Potassium hydroxide is difficult to achieve an effective catalytic effect, the catalytic speed is extremely slow, the reaction conversion rate is low, the content of unreacted oil is high, and the content of by-products such as polyethylene glycol is high

Method used

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  • Fatty oil ethoxylate and process for preparing the same
  • Fatty oil ethoxylate and process for preparing the same
  • Fatty oil ethoxylate and process for preparing the same

Examples

Experimental program
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Effect test

Embodiment 1

[0024] Add 2.6g of the catalyst into 90g of soybean oil, put it into a 1L autoclave while stirring, start stirring, N 2 Replace the air, raise the temperature to 180°C, introduce ethylene oxide, and keep the system pressure at 0.4MPa. When the amount of ethylene oxide added is 238g, close the EO feed valve, age for 10min, cool to 70°C, release the material, and weigh 329.5 g to obtain a product with a single-chain average oxyethylene group content of 18.0—soybean oil ethoxylate.

Embodiment 2

[0026] Add catalyst 6.3g to 132gC 8~10 In triglyceride, put it into a 1L autoclave while stirring, start stirring, N 2 Replace the air, raise the temperature to 150°C, introduce ethylene oxide, and keep the system pressure at 0.3MPa. When the amount of ethylene oxide added is 275g, the reaction is completed, aged for 10min, cooled to 70°C and discharged, weighed 345g, and obtained single-chain Products with an average oxyethylene content of 8.0 - C 8~10 Ethoxylates of triglycerides.

Embodiment 3

[0028] Add 1.2g of the catalyst into 147.7g of olive oil, put it into a 1L autoclave while stirring, start stirring, N 2 Replace the air, raise the temperature to 200°C, introduce ethylene oxide, and keep the system pressure at 0.5MPa. When the amount of ethylene oxide added is 396g, close the ethylene oxide feed valve, age for 10min, cool to 70°C and discharge, weigh Weighing 544 g, the product—olive oil ethoxylate—was obtained with a single-chain average oxyethylene content of 15.0.

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PUM

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Abstract

The grease ethoxylate is characterized in that it comprises the following forms: R is C1-30 hydrocarbon radicals or their mixtures; x, y, z are the same or different; x + y + z=1-180. The invention comprising the following steps: mixing grease and catalyst with each other; replacing the air in reactor with nitrogen; Adjusting the mixture to reaction temperature and operating pressure; leading-in ethylene oxide while keeping reaction pressure; aging for 10-20 minutes and cooling to get product. The invention has the advantages of non-toxicity, non-irritating and good compatibility with skin.

Description

technical field [0001] The invention belongs to a kind of nonionic surfactant, in particular to an ethoxylate of oil and a preparation method. Background of the invention [0002] Oleochemicals in the traditional sense generally pre-esterify and transesterify oils and fats to obtain fatty acid methyl esters, hydrogenate methyl esters to obtain fatty alcohols, and then prepare alcohol ether nonionic surfactants through ethoxylation. . [0003] [0004] The process route of this process is long, and the preparation of methyl ester also needs to go through operations such as washing, dehydration, and distillation, and the process is cumbersome. Due to the collection of by-product methanol, a frozen brine system needs to be configured, and methyl ester hydrogenation requires high temperature and high pressure, so the equipment is complicated, resulting in high product costs. In addition, the irritation and ecotoxicity of alcohol ether nonionic surfactants are not ideal. The...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01F17/08C09K23/08
Inventor 孙永强罗毅张高勇田春花刘广宇
Owner 中轻日化科技有限公司
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