IP Library Granted Patent US 9,150,769
Granted Patent B2
US 9,150,769 · App. 13/442,126 · Granted Oct 6, 2015

Phase-changing material microcapsules by using PMMA prepolymer and organic-solvent free synthesis process

Inventors: Yi-Hsiuan Yu (Taoyuan County, TW); Ping-Szu Tsai (Kaohsiung, TW); Tsung-Hsien Tsai (Kaohsiung, TW); Bao-Yann Lin (Hsinchu County, TW); Ming-Hsiung Wei (Taoyuan County, TW)
Assignee: National Chung-Shan Institute of Science and Technology
C09K5/02C08F220/14C09K5/063C08F22/105
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Quick Facts
Patent No.
US 9,150,769
App. No.
13/442,126
Granted
Oct 6, 2015
Kind
B2
Abstract

Phase change material microcapsules are obtained using a PMMA prepolymer and an organic-solvent free synthesis process. A polymer monomer and an initiator are subject to pre-polymerization in a water bath to form Polymethyl methacrylate (PMMA) prepolymer which is then prepared to be a stabilizer aqueous solution. A phase change material is added to the stabilizer aqueous solution and liquefied in advance, and stirred to form an emulsion by a homogenizing mixer. A starting agent, a cross-linking agent and a Polymethyl methacrylate methyl ester prepolymer are added to the emulsion containing the phase-change material. The emulsion is further stirred by the homogenizing mixer for micro-emulsification which then aggregates in water bath. In this way, the process may use organic-solvent free process to pre-polymerize the polymer monomer into a Polymethyl methacrylate prepolymer and carries out encapsulation and polymerization at an oil-water interface to achieve the preparation of phase change material microcapsules.

Claims (20)

1. A method of synthesizing phase change material microcapsules using polymethyl methacrylate (PMMA) pre-polymer, the method comprising:

pre-polymerizing a polymer monomer and a first initiator of benzoyl peroxide (BPO) in an organic-solvent free water bath so as to form PMMA prepolymers;

preparing a stabilizer aqueous solution;

adding a phase change material to the stabilizer aqueous solution for liquefaction; and

adding a second initiator, a cross-linking agent and the polymethyl methacrylate prepolymer are added to the emulsion containing the phase change material, and the emulsion is further stirred for 3 minutes by a homogenizing mixer for micro-emulsion and followed by subject to polymerization in a water bath to produce phase change material microcapsules,

wherein the cross-linking agent is selected from one of 1,4-butanediol diacrylate, triallyl isocyanurate, butyl acrylate, 2-hydroxyethyl acrylate, hydroxygropvl acrylate, 2-hydroxyethyl methacrylate, and hydrolyzed golymaleic anhydride.

2. The method of claim 1 , wherein the polymer monomer is methyl methacrylate (MMA).

3. The method of claim 1 , wherein the amount of the first initiator based on the polymer monomer is 0.1 wt. %.

4. The method of claim 1 , comprising preparing the polymethyl methacrylate prepolymer at 60° C. to 90° C.

5. The method of claim 1 , comprising preparing the polymethyl methacrylate prepolymer for 5 minutes to 90 minutes.

6. The method of claim 1 , wherein the concentration of the stabilizer in water is between 0.01 to 1%.

7. The method of claim 1 , wherein the stabilizer is selected from one of polyvinyl pyrrolidone (PVP), polyethylene glycol (PEG), TWEEN, and SPAN.

8. The method of claim 1 , wherein the phase change material is organic paraffin having 14-44 carbons.

9. The method of claim 1 , comprising stirring the stabilizer aqueous solution after liquefaction for 1 minute by a homogenizing mixer at 3000-12000 r.p.m. to form the emulsion.

10. The method of claim 1 , wherein the second initiator is benzoyl peroxide (BPO), or 2,2-azobisisobutyronitrile (AIBN).

11. The method of claim 1 , wherein the amount of the second initiator based on the polymer monomer is 0.5-5 wt. %.

12. The method of claim 1 , wherein the amount of the cross-linking agent based on the polymer monomer is between 5 wt. % to 30 wt. %.

13. The method of claim 1 , further comprising stirring the emulsion for 3 minutes by a homogenizing mixer at 3000-12000 r.p.m. for micro-emulsion.

14. The method of claim 1 , wherein the temperature for the polymerization in water bath is carried out at 60° C. to 90° C.

15. The method of claim 1 , wherein the phase change material microcapsules produced have a particle size of 2 to 22 micrometers.

Assignments (2)
CHANGE OF NAME Recorded Apr 17, 2015
From: CHUNG-SHAN INSTITUTE OF SCIENCE AND TECHNOLOGY, ARMAMENTS, BUREAU, MINISTRY OF NATIONAL DEFENSE
To: NATIONAL CHUNG SHAN INSTITUTE OF SCIENCE AND TECHNOLOGY
Reel/Frame 035453/0379 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 9, 2012
From: YU, YI-HSIUAN; TSAI, PING-SZU; TSAI, TSUNG-HSIEN; LIN, BAO-YANN; WEI, MING-HSIUNG
To: CHUNG-SHAN INSTITUTE OF SCIENCE AND TECHNOLOGY, ARMAMENTS, BUREAU, MINISTRY OF NATIONAL DEFENSE
Reel/Frame 028014/0067 →
Continuity (1)
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