Method for improving stability of inverse emulsion system

An inverse emulsion and stability technology, applied in the field of emulsion polymerization, can solve the problems of many components, charge distribution, difficult operability, etc., and achieve the effects of increasing interaction, application promotion, and improving stability

Active Publication Date: 2017-05-31
ZHEJIANG UNIV
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  • Abstract
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  • Claims
  • Application Information

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Problems solved by technology

For example, in the Chinese patent literature whose publication number is CN103131398A, organic acid ester surfactants are used as the main emulsifier to reduce the tension of the oil-water two-phase interface, and organic acid amides are used as co-emulsifiers to strengthen the emulsification and wetting ability of the system. Calcium increases the reserve alkalinity, and the fatty alcohol polyoxyethylene ether surfactant is used as a wetting reversal agent, thereby improving the stability of the W / O emulsion, but this method is costly, and there are too many components in the system and it is difficult to control Proportion
In European patent EP904773A, a high-concentration inorganic electrolyte is added to the water phase to form a more stable W / O emulsion, but the introduction of high-concentration inorganic electrolyte makes industrial production difficult
In the Chinese patent document whose publication number is CN1437645A, a polymer that can be functionalized is added to the oil phase before emulsification, and then the polymer is functionalized with a sulfonating agent, thereby providing additional stability for the emulsion. This method Use concentrated sulfuric acid as the sulfonating agent, and then use ammonia water to adjust the pH value, which makes it difficult to achieve the effect of sulfonation and pH adjustment at the same time, and the operation failure rate is high
U.S. Patent US5927404A uses a new type of solid to stabilize the W / O emulsion, but this new type of solid needs to meet the characteristics of being insoluble in oil-water two-phase, having lipophilic groups, having charge distribution, and extremely small size, and the cost of use is high.
[0005] The above methods are all improvements to the stability of W / O emulsions, but most of the current methods are complicated, difficult to operate, and high in cost, so they cannot be well applied.

Method used

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Examples

Experimental program
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Effect test

Embodiment 1

[0036] 300g of liquid paraffin and 45g of a mixed emulsifier system (composed of 37.8g of Span 80 and 7.2g of Tween 80) with an HLB value of 6.0 were mixed uniformly to obtain an oil phase. Mix 300g of deionized water, 57.8g of acrylamide, 42.2g of methacryloxyethyl trimethylammonium chloride, 0.5g of polyacryloxyethyl dimethylbenzyl ammonium chloride with a molecular weight of 50,000. Get the water phase. Put the oil phase in a 1L three-neck jacketed reactor, stir at 1500 rpm, and add the water phase dropwise while stirring. The time is controlled within 30 minutes. Then add 0.15g VA044 initiator and continue to stir for 15 minutes. A W / O pre-emulsion is obtained. Reduce the stirring rate to 300 revolutions per minute, keep the temperature up to 50°C, and react for 8 hours to obtain a stable W / O emulsion polymer. Put 25mL of the W / O emulsion after the reaction in a 25mL graduated glass test tube with a stopper, and place it at room temperature for one month. Observe that the...

Embodiment 2

[0040] 100g of liquid paraffin, 100g of raffinate oil, 100g of cyclohexane, 45g of a mixed emulsifier system (composed of 35.8g of Span 60 and 9.2g of OP-10) with an HLB value of 6.5 are uniformly mixed to obtain an oil phase. Combine 300g of deionized water, 50g of acrylamide, 25g of methacryloxyethyltrimethylammonium chloride, 25g of acryloxyethyltrimethylammonium chloride, 0.25g of polymethacrylamide with a molecular weight of 50,000 Oxyethyl dimethyl benzyl ammonium chloride and 0.25 g of polyacryloxyethyl dimethyl benzyl ammonium chloride with a molecular weight of 50,000 are mixed uniformly to obtain an aqueous phase. Place the oil phase in a 1L three-neck jacketed reactor, stir at 3000 rpm at high speed, add the water phase dropwise while stirring, the time is controlled within 30 minutes, and then add 5.5g potassium persulfate and 2.5g sodium nitrite. After stirring for 15 minutes, the W / O pre-emulsion is obtained. Reduce the stirring rate to 300 revolutions per minute...

Embodiment 3

[0042] 67.5g hexane, 67.5g heptane, 16.7g mixed emulsifier system (composed of 12.57g Span 85, 2.065g Tween 80 and 2.065g OP-10) with an HLB value of 5.0 were mixed uniformly to obtain an oil phase. 270g deionized water, 24g methacrylamide, 3g methacryloxyethyl dimethylbenzyl ammonium chloride, 3g acryloxyethyl dimethylbenzyl ammonium chloride, 0.015g cation degree is 90 % And a molecular weight of 200,000 methacryloxyethyl trimethylammonium chloride-octadecyl methacrylate copolymer is mixed uniformly to obtain an aqueous phase. Put the oil phase in a 1L three-neck jacketed reactor, stir at 1500 rpm at high speed, add the water phase dropwise while stirring, the time is controlled within 30 minutes, and then add 0.315g ammonium persulfate and 0.135g sodium bisulfite The composition of the redox initiator is continuously stirred for 15 minutes to obtain the W / O pre-emulsion. Reduce the stirring rate to 300 revolutions per minute, keep the temperature up to 30°C, and react for 8...

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Abstract

The invention discloses a method for improving the stability of an inverse emulsion system. The method comprises the following steps: (1) uniformly mixing oily liquid with an emulsifier to obtain an oil phase; (2) mixing a monomer and two amphiphilic cationic polymers with water to obtain an aqueous phase; and (3) mixing the aqueous phase with an initiator and the oil phase to form pre-emulsion, and performing inverse emulsion polymerization. According to the method disclosed by the invention, the two amphiphilic cationic polymers with hydrophobic and hydrophilic groups are introduced in the inverse emulsion system to increase the interaction of the two phases of the system so as to improve the stability of the W / O emulsion, and meanwhile the two amphiphilic cationic polymers introduced in the system also have the functions of cationic water-soluble polymers, which also have a positive effect on the application of the product.

Description

Technical field [0001] The invention relates to the field of emulsion polymerization, in particular to a method for improving the stability of an inverse emulsion system. Background technique [0002] Since Vanderhoff et al. (Vanderhoff J W. ACS, 1962, 34:32) used organic solvents as the medium in 1962 to first carry out inverse emulsion polymerization of water-soluble monomers, inverse emulsion polymerization has caused great interest. Inverse emulsion polymerization is to dissolve water-soluble monomers in water and disperse them in a non-polar liquid with the help of low HLB emulsifiers to form a "water-in-oil" (W / O) type emulsion. . This reaction can obtain high-molecular-weight products while obtaining a high reaction rate; the reaction system is a dispersed system, which is easy to transfer heat, and is convenient to realize continuous operation. [0003] The key to inverse emulsion polymerization is to obtain a stable inverse emulsion. The stability of the inverse emulsio...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08F220/56C08F220/34C08F2/32C08F226/02
CPCC08F2/32C08F220/56C08F220/34C08F226/02
Inventor 单国荣陈勇
Owner ZHEJIANG UNIV
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