IP Library Granted Patent US 9,102,080
Granted Patent B2
US 9,102,080 · App. 13/223,122 · Granted Aug 11, 2015

Low cost process for manufacture of form-stable phase change material

Inventor: Ramin Abhari (Bixby, OK)
Assignee: REG SYNTHETIC FUELS, LLC
B29B9/12C08J3/005B29B9/065C08J2323/06C08J2491/06
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Quick Facts
Patent No.
US 9,102,080
App. No.
13/223,122
Granted
Aug 11, 2015
Kind
B2
Abstract

The present invention generally relates to a method for manufacturing phase change material (PCM) pellets. The method includes providing a melt composition including paraffin and a polymer. The paraffin has a melt point between about 10° C. and about 50° C., and more preferably between about 18° C. and about 28° C. In one embodiment, the melt composition includes various additives, such as a flame retardant. The method further includes forming the melt composition into PCM pellets. The method further may include the step of cooling the melt to increase the melt viscosity before pelletizing.

Claims (41)

1. A method for manufacturing phase change material (PCM) pellets comprising the steps of:

providing a melt composition consisting essentially of

a paraffin,

a polymer, and

optionally a thermal conductivity improver, a nucleating agent, an anti-oxidant, or a combination of any two or more thereof; and

forming the melt into PCM pellets in a pelletizer;

wherein

the paraffin is at least 60 wt % of the melt composition;

the polymer is uncrosslinked high density polyethylene (HDPE); and

the uncrosslinked HDPE has a melt flow index between about 0.1 g/10 min and about 20 g/10 min.

2. The method of claim 1 wherein the paraffin has a melt point between about 10° C. and about 50° C.

3. The method of claim 1 wherein the paraffin has a melt point between about 18° C. and about 28° C.

4. The method of claim 1 wherein the paraffin has a heat of fusion between 100 and 240 J/g.

5. The method of claim 1 wherein the paraffin includes n-octadecane.

6. The method of claim 1 wherein the paraffin is produced by hydrodeoxygenation of lipids.

7. The method of claim 1 wherein the melt is formed into PCM pellets in an underwater pelletizer.

8. The method of claim 7 wherein the pelletizer water temperature is between the melting point of the paraffin and the melting point of the polymer.

9. The method of claim 1 wherein the melt is formed into pellets in a strand pelletizer.

10. The method of claim 9 wherein the strand pelletizer trough water temperature is between the melting point of paraffin and the melting point of the polymer.

11. The method of claim 1 further comprising the step of:

cooling the melt to increase the melt viscosity to 4,000 cP or higher before pelletizing.

12. The method of claim 1 wherein the typical size of the PCM pellets is between about 0.5 mm and about 2 mm.

13. The PCM pellets made by the method of claim 1 .

14. The method of claim 1 , wherein the paraffin is from about 60 wt % to about 90 wt % of the melt composition.

15. The method of claim 1 , wherein the nucleating agent is from about 0 wt % to about 10 wt %, the thermal conductivity improver is from about 0 wt % to about 2 wt %, the anti-oxidant is from about 0 wt % to about 0.1 wt %, or combinations of any two or more thereof.

16. A method comprising the steps of:

providing a melt composition consisting essentially of

a paraffin,

a polymer, and

optionally a thermal conductivity improver, a nucleating agent, an anti-oxidant, or a combination of any two or more thereof; and

forming the melt into phase change material (PCM) pellets in a pelletizer;

wherein

the paraffin is at least 60 wt % of the melt composition;

the paraffin has a melt point between about 18° C. and about 28° C.;

the polymer is uncrosslinked high density polyethylene (HDPE); and

the uncrosslinked HDPE has a melt flow index between about 0.1 g/10 min and about 20 g/10 min.

17. The method of claim 16 wherein the paraffin has a heat of fusion between 100 and 240 J/g.

18. The method of claim 16 wherein the paraffin is produced by hydrodeoxygenation of lipids.

19. The PCM pellets of the method of claim 16 .

20. The method of claim 16 , wherein the paraffin is from about 60 wt % to about 90 wt % of the melt composition.

21. The method of claim 16 , wherein the nucleating agent is from about 0 wt % to about 10 wt %, the thermal conductivity improver is from about 0 wt % to about 2 wt %, the anti-oxidant is from about 0 wt % to about 0.1 wt %, or combinations of any two or more thereof.

Assignments (5)
RELEASE OF SECURITY INTEREST Recorded Jul 1, 2022
From: UMB BANK, N.A., AS COLLATERAL TRUSTEE
To: REG SYNTHETIC FUELS, LLC; RENEWABLE ENERGY GROUP, INC.; REG SENECA, LLC; REG BIOFUELS, LLC
Reel/Frame 060562/0428 →
PATENT SECURITY AGREEMENT Recorded Jun 19, 2021
From: REG SYNTHETIC FUELS, LLC
To: UMB BANK, N.A., AS COLLATERAL TRUSTEE
Reel/Frame 056628/0673 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 29, 2014
From: SYNTROLEUM CORPORATION
To: REG SYNTHETIC FUELS, LLC
Reel/Frame 033430/0470 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 24, 2014
From: SYNTROLEUM CORPORATION
To: REG SYNTHETIC FUELS, LLC
Reel/Frame 033170/0166 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 31, 2011
From: ABHARI, RAMIN
To: SYNTROLEUM CORPORATION
Reel/Frame 026840/0940 →
Continuity (2)
Provisional Application 61379252 · Sep 1, 2010
Related Publication 20120049402A1 · Mar 1, 2012