Method for reducing supercooling degree of alkane phase change microcapsule by using different shell materials, microcapsule prepared by method and application of microcapsule

A technology of phase change microcapsules and alkanes, which is applied in the field of microcapsules, can solve the problems of uneven distribution of nucleating agents, reduction of enthalpy value of phase change microcapsules, reduction of supercooling degree, etc., to achieve uniform particle size and low cost , the effect of reducing supercooling

Active Publication Date: 2021-11-16
GUANGDONG UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] In order to overcome the shortcomings and deficiencies of the preparation of phase change microcapsule nucleating agents in the prior art, such as the uneven distribution of the number of nucleating agents, complex processes, and the reduction of the enthalpy of the phase change microcapsules, the primary purpose of the present invention is to provide a method that utilizes different shell layers A method for reducing the supercooling degree of alkane phase-change microcapsules; the method uses microfluidic technology and ultraviolet lamp radiation to prepare phase-change microcapsules with different shell materials covering core materials, uniform particle size, and controllable structure, so as to achieve The purpose of reducing supercooling

Method used

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  • Method for reducing supercooling degree of alkane phase change microcapsule by using different shell materials, microcapsule prepared by method and application of microcapsule
  • Method for reducing supercooling degree of alkane phase change microcapsule by using different shell materials, microcapsule prepared by method and application of microcapsule

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0029] (1) Preparation of dispersed phase: 5 g of purchased high-purity octadecane was weighed as the dispersed phase.

[0030] (2) Preparation of intermediate phase: Weigh 0.2g of Span 80, 0.4g of 2-hydroxy-2-methyl-1-phenyl-1-propanone and 19.4g of dipropylene glycol diacrylate (DPGDA) in In a 50ml beaker, under the conditions of 25°C and 500r / min, stir continuously for 30min to ensure uniform stirring, as the intermediate phase.

[0031] (3) Preparation of continuous phase and collection phase: Weigh 10g of polyvinyl alcohol (PVA) and pour it into 490ml of deionized water, and keep stirring for 30min at 70°C and 800r / min to ensure that PVA is evenly dispersed in deionized water. In water, the mixed solution obtained by stirring evenly was used as the continuous phase and the collection phase.

[0032] (4) Using the double-emulsified glass capillary microfluidic chip in the Chinese invention patent application number 201811008829.0 as the microfluidic chip, the octadecane d...

Embodiment 2

[0036] (1) Preparation of dispersed phase: 5 g of purchased high-purity octadecane was weighed as the dispersed phase.

[0037] (2) Preparation of intermediate phase: Weigh 0.2g of Span 80, 0.4g of 2-hydroxy-2-methyl-1-phenyl-1-propanone and 19.4g of dipropylene glycol diacrylate (DPGDA) in In a 50ml beaker, under the conditions of 25°C and 500r / min, stir continuously for 30min to ensure uniform stirring, as the intermediate phase.

[0038] (3) Preparation of continuous phase and collection phase: Weigh 10g of polyvinyl alcohol (PVA) and pour it into 490ml of deionized water, and keep stirring for 30min at 70°C and 800r / min to ensure that PVA is evenly dispersed in deionized water. In water, the mixed solution obtained by stirring evenly was used as the continuous phase and the collection phase.

[0039] (4) Using the double-emulsified glass capillary microfluidic chip in the Chinese invention patent application number 201811008829.0 as the microfluidic chip, the octadecane d...

Embodiment 3

[0043] (1) Preparation of dispersed phase: 5 g of purchased high-purity octadecane was weighed as the dispersed phase.

[0044] (2) Preparation of the intermediate phase: Weigh 0.2g Span 80, 0.4g 2-hydroxy-2-methyl-1-phenyl-1-propanone and 19.4g trimethylolpropane triacrylate (TMPTA ) placed in a 50ml beaker, under the conditions of 25°C and 500r / min, continuously stirred for 30min to ensure uniform stirring, as the intermediate phase.

[0045] (3) Preparation of continuous phase and collection phase: Weigh 10g of polyvinyl alcohol (PVA) and pour it into 490ml of deionized water, and keep stirring for 30min at 70°C and 800r / min to ensure that PVA is evenly dispersed in deionized water. In water, the mixed solution obtained by stirring evenly was used as the continuous phase and the collection phase.

[0046] (4) Using the double-emulsified glass capillary microfluidic chip in the Chinese invention patent application number 201811008829.0 as the microfluidic chip, the octadeca...

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Abstract

The invention belongs to the technical field of functional material preparation, and discloses a method for reducing the supercooling degree of an alkane phase change microcapsule by using different shell materials, the microcapsule prepared by the method and application of the microcapsule. The method comprises the following steps: preparing an intermediate phase, a continuous phase and a collection phase, respectively feeding a dispersed phase, the intermediate phase and the continuous phase into a micro-fluidic chip through an injection pump, and respectively introducing the dispersed phase, the intermediate phase and the continuous phase into the micro-fluidic chip from a small sharp-nose glass capillary tube, a first closed liquid storage tank and a second closed liquid storage tank; enabling the dispersed phase to flow out of the small sharp-nose glass capillary tube, to be wrapped by the intermediate phase and then flow into the small sharp-nose glass capillary tube under the flowing of the continuous phase, radiating an initiator in the intermediate phase by an ultraviolet lamp to initiate a polymerization reaction of a shell material, forming a thin film layer to wrap the phase change material, and obtaining the phase change microcapsule after drying. Precision control over particle size control and supercooling degree reduction of the phase change microcapsules is achieved, and the method is suitable for industrial production of the phase change microcapsules.

Description

technical field [0001] The invention belongs to the technical field of preparation of functional materials, and in particular relates to a method for reducing the supercooling degree of alkane phase-change microcapsules by using different shell materials, and the microcapsules produced therefrom and their application. Background technique [0002] Phase change materials have the characteristics of absorbing and releasing a large amount of latent heat during the liquid-solid phase transition process, and are good heat storage materials. They are widely used in latent heat storage of buildings and thermal control of electronic modules. Paraffin wax is the most widely used organic phase change material, with good economy, high enthalpy and wide application temperature range. However, the fluidity and amorphousness of paraffin often cause leakage during use, which is not conducive to its recycling. The use of microcapsule encapsulation technology can encapsulate paraffin phase ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J13/14
CPCB01J13/14Y02E60/14
Inventor 陈颖王慧昌贾莉斯莫松平钟凯李俊覃光军
Owner GUANGDONG UNIV OF TECH
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