US2012180988A1PendingUtilityA1

Moving thermal bed to time shift liquifaction and vaporization

Individually held — no corporate assignee on recordPriority: Jan 19, 2011Filed: Dec 21, 2011Published: Jul 19, 2012
Est. expiryJan 19, 2031(~4.5 yrs left)· nominal 20-yr term from priority
Inventors:Craig Laforce
F28D 19/02F28D 20/0056F25J 1/0251F17C 2221/031F25J 2205/24F25J 1/0015F17C 2260/046F17C 2221/014F25J 1/0012F17C 2227/0365F25J 1/0221F17C 2227/0327F25J 1/0017F17C 2270/0581Y02E60/14F17C 2221/011
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Claims

Abstract

A method to store and utilize thermal energy is provided. During a first phase, transferring heat from the heat relocation media to the lower temperature reservoir, transferring heat from the higher temperature stream to the heat relocation media, and transferring heat from the heat relocation media to the high temperature reservoir, thereby at least partially liquefying the higher temperature stream. During a second phase, transferring heat from the higher temperature reserve to the heat relocation media, transferring heat from the heat relocation media to the lower temperature stream, and transferring heat from the heat relocation media to the lower temperature reservoir, thereby at least partially vaporizing the lower temperature stream.

Claims

exact text as granted — not AI-modified
1 . A method to store and utilize thermal energy, comprising:
 providing a higher temperature stream, and a lower temperature stream,   providing a higher temperature reservoir,   during a first phase,   transferring heat from said higher temperature stream to said high temperature reservoir, thereby at least partially liquefying said higher temperature stream; and   during a second phase,
 transferring heat to said lower temperature stream from said higher temperature reservoir, thereby at least partially vaporizing said lower temperature stream 
   
     
     
         2 . The method of  claim 1 , wherein said lower temperature stream is selected from the group consisting of essentially pure oxygen, essentially pure nitrogen, air. 
     
     
         3 . The method of  claim 1 , wherein said higher temperature stream is selected from the group consisting of essentially pure oxygen, essentially pure nitrogen, air. 
     
     
         4 . The method of  claim 1 , wherein said first phase and said second phase do not occur concurrently. 
     
     
         5 . The method of  claim 1 , wherein said first phase and said second phase occur concurrently. 
     
     
         6 . A method to store and utilize thermal energy, comprising:
 providing a heat relocation media,   providing a higher temperature stream, and a lower temperature stream,   providing a heat transfer means between said higher temperature stream and said heat relocation media,   providing a heat transfer means between said lower temperature stream and said heat relocation media,   providing a higher temperature reservoir and a lower temperature reservoir,   providing a heat transfer means between said heat relocation media and said higher temperature reservoir,   providing a heat transfer means between said heat relocation media and said lower temperature reservoir,   during a first phase,
 transferring heat from said heat relocation media to said lower temperature reservoir, 
 transferring heat from said higher temperature stream to said heat relocation media, 
 transferring heat from said heat relocation media to said high temperature reservoir, thereby at least partially liquefying said higher temperature stream; and 
   during a second phase,
 transferring heat from said higher temperature reserve to said heat relocation media, 
 transferring heat from said heat relocation media to said lower temperature stream, 
 transferring heat from said heat relocation media to said lower temperature reservoir, thereby at least partially vaporizing said lower temperature stream. 
   
     
     
         7 . The method of  claim 6 , wherein said heat relocation media comprises a solid heat transfer media. 
     
     
         8 . The method of  claim 7 , wherein said solid heat transfer media is selected from the group consisting of metal particles, carbon particles, pebbles, sand, shot, and ceramic particles. 
     
     
         9 . The method of  claim 7 , wherein said solid heat transfer media comprise solid spheres. 
     
     
         10 . The method of  claim 7 , wherein said solid heat transfer media comprise hollow spheres. 
     
     
         11 . The method of  claim 9 , wherein said solid spheres are comprised of a material selected from the group consisting of ceramic, glass, or quartz. 
     
     
         12 . The method of  claim 10 , wherein said hollow spheres are comprised of a material selected from the group consisting of ceramic, glass, or quartz. 
     
     
         13 . The method of  claim 9 , wherein said solid heat transfer media comprises solid metal spheres. 
     
     
         14 . The method of  claim 9 , wherein said metal is selected from the group consisting of steel, bronze, brass, iron, and copper. 
     
     
         15 . The method of  claim 6 , wherein said lower temperature stream is selected from the group consisting of essentially pure oxygen, essentially pure nitrogen, air. 
     
     
         16 . The method of  claim 6 , wherein said higher temperature stream is selected from the group consisting of essentially pure oxygen, essentially pure nitrogen, air. 
     
     
         17 . The method of  claim 6 , wherein said first phase and said second phase do not occur concurrently. 
     
     
         18 . The method of  claim 6 , wherein said first phase and said second phase occur concurrently. 
     
     
         19 . The method of  claim 6 , wherein the amount of heat transferred from said higher temperature stream to said heat relocation media is greater than the amount of heat transferred from said heat relocation media to said lower temperature stream. 
     
     
         20 . The method of  claim 6 , wherein the amount of heat transferred from said higher temperature stream to said heat relocation media is less than the amount of heat transferred from said heat relocation media to said lower temperature stream.

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