US2016033172A1PendingUtilityA1

Evacuated Tubes For Solar Thermal Energy Collection

Assignee: THERMAL RESOURCE TECHNOLOGIES INCPriority: Feb 16, 2011Filed: Oct 12, 2015Published: Feb 4, 2016
Est. expiryFeb 16, 2031(~4.6 yrs left)· nominal 20-yr term from priority
F24S 10/45F28D 15/02Y02E10/44F24S 2080/03F24S 80/30F24J 2/32F24J 2/055F24S 10/95
29
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Claims

Abstract

An evacuated tube solar thermal collector uses a set of evacuated solar thermal collector tubes in heat exchanging contact with a fluid flowing through a header tube. Two heat pipes are provided in each evacuated thermal collector tube, and the condenser ends of the heat pipes are positioned in the header tube with a spacing that provides improved heat transfer from the heat pipes to the header tube. When 14 mm heat pipes contained in 58 mm collector tubes are used in a header tube having a capacity of about 0.5 gallons with a heat transfer liquid that is flowing at a rate of about 0.3 gpm, the spacing between heat pipes in each collector tube is about 24 mm, center to center, and the spacing between corresponding heat pipes of immediately-adjacent collector tubes is about 80 mm.

Claims

exact text as granted — not AI-modified
1 - 14 . (canceled) 
     
     
         15 . An evacuated tube solar thermal collector, comprising a plurality of evacuated thermal collector tubes and a header tube;
 wherein said evacuated thermal collector tubes each preferably comprise:
 a) an outer wall, 
 b) an inner wall defining an inner tube space, 
 c) an evacuated space between said outer wall and said inner wall, 
   wherein said evacuated space is effective to create a thermal barrier that limits heat loss from the inner tube space to the environment outside the tube, and
 d) a set of two heat pipes including a first heat pipe and a second heat pipe positioned in the inner tube space in a spaced relation to each other to provide space and spacing therebetween; wherein said first and second heat pipes each comprise: 
 e) a pipe wall defining an inner pipe space and having an upper, condenser end and a lower, heating end, and 
 f) a vaporizing/condensing fluid in the inner pipe space; wherein said header tube preferably comprises: 
 g) a heat transfer tube being open at each end to allow a heat transfer fluid to flow therethrough, 
 h) a series of sockets sized to receive the condenser ends of heat pipes, 
   and
 i) a heat transfer liquid in the heat transfer tube, 
   wherein said sockets in the header tube are spaced so that the spacing relation between the first and second heat pipes is great enough to permit a turbulent flow of heat transfer liquid upstream of the second heat pipe, but small enough so as to not permit a substantial laminar flow of heat transfer liquid upstream of the second heat transfer pipe for optimizing the effectiveness of the heat transfer between the first and second pipes and the heat transfer fluid.   
     
     
         16 . The thermal collector of  claim 15  wherein said evacuated thermal collector tubes each additionally comprise a heat-absorbing material on the inner wall of each collector tube. 
     
     
         18 . The thermal collector of  claim 15  wherein said inner space of each heat pipe is at a low pressure effective to allow the vaporizing/condensing fluid in the inner space to boil at a lower temperature than it would boil if the pressure were not low. 
     
     
         19 . The thermal collector of  claim 15  wherein said header tube is covered by an insulated cover substantially surrounding the header tube and effective for limiting heat loss from the header tube to the environment. 
     
     
         20 . The thermal collector of  claim 15  wherein said collector tubes have an outside diameter of about 58 mm; said heat pipes have an outer diameter of about 14 mm at their condenser end; the heat transfer tube portion of said header tube has a volume of about 0.5 gallons; the spacing between the sockets for the two heat pipes of each collector tube is about 24 mm (center-to-center); and the spacing between the lead sockets of immediately-adjacent collector tubes is 80 mm (center-to-center). 
     
     
         21 . The thermal collector of  claim 15  wherein said header tube is configured to permit a turbulent flow of heat transfer liquid upstream of the second heat pipe, and not permit a substantial laminar flow of heat transfer liquid upstream of the second heat transfer pipe when the fluid flow through the header tube is at a rate of between about 0.2 gpm and 0.4 gpm. 
     
     
         22 . The thermal collector of  claim 15  wherein said header tube has a capacity of between about 0.4 and 0.7 gallons. 
     
     
         23 . A method of collecting heat energy, comprising:
 a) providing an evacuated tube solar thermal collector comprising an evacuated tube solar thermal collector having a plurality of evacuated thermal collector tubes and a header tube;   wherein said thermal collector tubes each preferably comprise:
 i) an outer wall; 
 ii) an inner wall defining an inner tube space; 
 iii) an evacuated space between said outer wall and said inner wall, wherein said evacuated space is effective to create a thermal barrier and cause heat absorbed by the inner wall to be retained in the inner tube space and not to be lost to the environment outside the tube; and 
 iv) a set of two heat pipes including a first heat pipe and a second heat pipe positioned in the inner tube space in a spaced relation to each other to provide space and spacing therebetween; wherein said heat pipes preferably each comprise: 
 v) a pipe wall defining an inner pipe space and having an upper, condenser end and a lower, heating end, and 
 vi) a heating fluid in the inner pipe space; 
   wherein said header tube preferably comprises:
 vii) a heat transfer tube capable of holding between about 0.4 gallons and 0.7 gallons of a heat transfer fluid, and being open at each end to allow a heat transfer fluid to flow therethrough; 
 viii) a series of sockets sized to receive the condenser ends of heat pipes including a first and second socket for respectively receiving the first and second heat pipes; and 
 ix) a heat transfer liquid flowable in the heat transfer tube for transferring heat between the first and second heat pipes and the heat transfer fluid; 
   wherein said spacing between the first and second sockets, and thereby the first and second heat pipes is great enough to permit a turbulent flow of heat transfer liquid upstream of the second heat pipe, but small enough so as to not permit a substantial laminar flow of heat transfer liquid upstream of the second heat transfer pipe, so that sockets in the header tube are spaced for optimizing the effectiveness of the heat transfer between the first and second pipes and a heat transfer fluid; and   b) flowing a heat transfer liquid through said heat transfer tube and past said first and second heat pipes at a flow rate of between about 0.2 gpm and 0.4 gpm.   
     
     
         24 . The method of  claim 23  wherein said evacuated thermal collector tubes each additionally comprise a heat-absorbing material on the inner wall of each collector tube. 
     
     
         25 . The method of  claim 23  wherein said inner space of each heat pipe is at a low pressure effective to allow the heating fluid in the inner space to boil at a lower temperature than it would boil if the pressure were not low. 
     
     
         26 . The method of  claim 23  wherein said header tube is covered by an insulated cover substantially surrounding the header tube and effective for limiting heat loss from the header tube to the environment. 
     
     
         27 . The method of  claim 23  wherein said collector tubes have an outside diameter of about 58 mm; said heat pipes have an outer diameter of about 14 mm; the heat transfer tube portion of said header tube has a volume of about 0.5 gallons; the spacing between the sockets for the two heat pipes of each collector tube is about 24 mm (center-to-center); and the spacing between the lead sockets of immediately-adjacent collector tubes is about 80 mm (center-to-center). 
     
     
         28 . A method of improving the heat transfer performance of an evacuated tube solar thermal collector having a series of evacuated solar thermal collector tubes in heat exchanging contact with a fluid flowing through a header tube, the method comprising providing two heat pipes in each evacuated thermal collector tube and spacing the condenser end of the two heat pipes a distance of about 24 mm apart, for optimizing the heat transfer between the two heat pipes and the heat transfer fluid. 
     
     
         29 . The method of  claim 28  wherein said header tube has a capacity of between about 0.4 and 0.7 gallons, and the fluid flow through the header tube at a rate of between about −0.2 gpm and about 0.4 gpm. 
     
     
         30 . A header tube for use in an evacuated tube solar thermal collector, comprising:
 a) a heat transfer tube adapted to allow a heat transfer fluid to flow therethrough;   b) a series of heat pipe sockets sized to receive the condenser ends of heat pipes; and   c) a heat transfer liquid in the heat transfer tube;   
       wherein said heat pipe sockets are provided in pairs, and the spacing between the sockets of each pair is about 24 mm (center-to-center); and the spacing between the corresponding sockets of each immediately-adjacent socket pairs is about 80 mm, center-to-center. 
     
     
         31 . An evacuated tube solar thermal collector tube, comprising:
 a) an outer wall,   b) an inner wall defining an inner tube space,   c) an evacuated space between said outer wall and said inner wall, wherein said evacuated space is effective to create a thermal barrier that limits heat loss from the inner tube space to the environment outside the tube, and   d) a pair of heat pipes positioned in the inner tube space; wherein said heat pipes each comprise:   e) a pipe wall defining an inner pipe space and having an upper, condenser end and a lower, heating end, and   f) a vaporizing/condensing fluid in the inner pipe space;   
       wherein said heat pipes have an outer diameter at their condenser ends of about 14 mm, and wherein the condenser ends of each heat pipe pair are spaced about 24 mm apart, center-to-center.

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