[특허]Rotary high density heat exchanger

Bastian, John Carl

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Rotary high density heat exchanger

특허상세정보
국가/구분	United States(US) Patent 등록
국제특허분류(IPC7판)	F28D-011/02 F28F-003/02 F28F-003/12 F28F-009/02 F28F-013/12 F28F-017/00 F28D-011/04
출원번호	US-0962643 (2015-12-08)
등록번호	US-9970712 (2018-05-15)
발명자 / 주소	Bastian, John Carl Jude, John David
출원인 / 주소	Bastian, John Carl
대리인 / 주소	McDonald Hopkins LLC
인용정보	피인용 횟수 : 0 인용 특허 : 8

초록

The present invention relates generally to the rotary high density heat exchangers. In one embodiment, the present invention relates to rotary high density heat exchangers that contain one or more fan blades where each fan blade contains heat exchanging surfaces on the surface thereof.

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1. A rotary high density heat exchanger comprising: a center shaft, wherein the center shaft is designed to permit the transfer of a heat transfer media;at least two heat exchanger blades, wherein each of the at least two further comprises at least one heat transfer passageway within the internal structure of the blade that are fluidically connected to the center shaft so as to permit the flow of heat transfer media from the center shaft to an outer edge of a respective heat exchanger blade;a heat transfer media collector, wherein the heat transfer media collector is fluidically connected to at least one outer portion of a respective heat transfer passageway in order to collect cooled heat transfer media; anda double hollow shaft, wherein one portion of the double hollow shaft is designed to be fluidically connected to the center shaft in order to supply hot, or heated, heat transfer media to the center shaft and wherein the other portion of the double hollow shaft is designed to be fluidically connected to the heat transfer media collector in order to supply cooled heat transfer media for a cooling application,wherein the heat transfer passageway in each of the at least two heat exchanger blades is serpentine in shape, andwherein the heat transfer media collector is formed so as to have an outer wheel-shaped portion that is fluidically connected to a plurality of fluid conveying spokes so as to convey heat transfer media to a portion of the double hollow shaft. 2. The rotary high density heat exchanger of claim 1, wherein the heat exchanger has at least three heat exchanger blades. 3. The rotary high density heat exchanger of claim 1, wherein the heat exchanger has at least four heat exchanger blades. 4. The rotary high density heat exchanger of claim 1, wherein the heat exchanger has at least five heat exchanger blades. 5. The rotary high density heat exchanger of claim 1, wherein the heat exchanger achieves highly turbulent air flow across the exchanger elements at speeds of about 500 feet per minute. 6. The rotary high density heat exchanger of claim 1, wherein the heat exchanger achieves highly turbulent air flow across the exchanger elements at speeds of about 5,000 feet per minute. 7. The rotary high density heat exchanger of claim 1, wherein the heat exchanger achieves highly turbulent air flow across the exchanger elements at speeds of about 10,000 feet per minute. 8. The rotary high density heat exchanger of claim 1, wherein the heat exchanger achieves highly turbulent air flow across the exchanger elements at speeds of about 15,000 feet per minute. 9. The rotary high density heat exchanger of claim 1, wherein the heat exchanger achieves highly turbulent air flow across the exchanger elements at speeds of about 20,000 feet per minute or greater. 10. The rotary high density heat exchanger of claim 1, wherein the passageway in each of the at least two heat exchanger blades further comprises at least one conductive material, powder or particles within at least a portion of the passageway. 11. The rotary high density heat exchanger of claim 1, wherein at least 25 percent or more of the surface area of each individual heat exchanger blade has at least one heat transfer passageway thereunder. 12. The rotary high density heat exchanger of claim 11, wherein at least 50 percent or more of the surface area of each individual heat exchanger blade has at least one heat transfer passageway thereunder. 13. The rotary high density heat exchanger of claim 11, wherein at least 60 percent or more of the surface area of each individual heat exchanger blade has at least one heat transfer passageway thereunder. 14. The rotary high density heat exchanger of claim 11, wherein at least 75 percent or more of the surface area of each individual heat exchanger blade has at least one heat transfer passageway thereunder. 15. The rotary high density heat exchanger of claim 11, wherein at least 90 percent or more of the surface area of each individual heat exchanger blade has at least one heat transfer passageway thereunder. 16. The rotary high density heat exchanger of claim 1, wherein at least 25 percent or more of at least one of the surfaces of an individual heat exchanger blade is covered with heat sink fins. 17. The rotary high density heat exchanger of claim 16, wherein at least 50 percent or more of at least one of the surfaces of an individual heat exchanger blade is covered with heat sink fins. 18. The rotary high density heat exchanger of claim 16, wherein at least 60 percent or more of at least one of the surfaces of an individual heat exchanger blade is covered with heat sink fins. 19. The rotary high density heat exchanger of claim 16, wherein at least 75 percent or more of at least one of the surfaces of an individual heat exchanger blade is covered with heat sink fins. 20. The rotary high density heat exchanger of claim 16, wherein at least 90 percent or more of at least one of the surfaces of an individual heat exchanger blade is covered with heat sink fins. 21. A rotary high density heat exchanger comprising: a center shaft, wherein the center shaft is designed to permit the transfer of a heat transfer media;at least two heat exchanger blades, wherein each of the at least two further comprises at least one heat transfer passageway within the internal structure of the blade that are fluidically connected to the center shaft so as to permit the flow of heat transfer media from the center shaft to an outer edge of a respective heat exchanger blade;a heat transfer media collector, wherein the heat transfer media collector is fluidically connected to at least one outer portion of a respective heat transfer passageway in order to collect cooled heat transfer media; anda double hollow shaft, wherein one portion of the double hollow shaft is designed to be fluidically connected to the center shaft in order to supply hot, or heated, heat transfer media to the center shaft and wherein the other portion of the double hollow shaft is designed to be fluidically connected to the heat transfer media collector in order to supply cooled heat transfer media for a cooling application,wherein the heat transfer passageway in each of the at least two heat exchanger blades is serpentine in shape, and wherein each heat exchanger blade contains a plurality of heat exchange fins one at least one external surface thereof,wherein the heat transfer media collector has an outer diameter defining an outer edge of the heat exchanger blades located distal from the double hollow shaft, andwherein the heat transfer media collector is formed so as to have an outer wheel-shaped portion that is fluidically connected to a plurality of fluid conveying spokes so as to convey heat transfer media to a portion of the double hollow shaft. 22. The rotary high density heat exchanger of claim 21, wherein the heat exchanger has at least three heat exchanger blades. 23. The rotary high density heat exchanger of claim 21, wherein the heat exchanger has at least four heat exchanger blades. 24. The rotary high density heat exchanger of claim 21, wherein the heat exchanger has at least five heat exchanger blades. 25. The rotary high density heat exchanger of claim 21, wherein the heat exchanger achieves highly turbulent air flow across the exchanger elements at speeds of about 500 feet per minute. 26. The rotary high density heat exchanger of claim 21, wherein the heat exchanger achieves highly turbulent air flow across the exchanger elements at speeds of about 5,000 feet per minute. 27. The rotary high density heat exchanger of claim 21, wherein the heat exchanger achieves highly turbulent air flow across the exchanger elements at speeds of about 10,000 feet per minute. 28. The rotary high density heat exchanger of claim 21, wherein the heat exchanger achieves highly turbulent air flow across the exchanger elements at speeds of about 15,000 feet per minute. 29. The rotary high density heat exchanger of claim 21, wherein the heat exchanger achieves highly turbulent air flow across the exchanger elements at speeds of about 20,000 feet per minute or greater. 30. The rotary high density heat exchanger of claim 21, wherein the passageway in each of the at least two heat exchanger blades further comprises at least one conductive material, powder or particles within at least a portion of the passageway. 31. The rotary high density heat exchanger of claim 21, wherein at least 25 percent or more of the surface area of each individual heat exchanger blade has at least one heat transfer passageway thereunder. 32. The rotary high density heat exchanger of claim 31, wherein at least 50 percent or more of the surface area of each individual heat exchanger blade has at least one heat transfer passageway thereunder. 33. The rotary high density heat exchanger of claim 31, wherein at least 60 percent or more of the surface area of each individual heat exchanger blade has at least one heat transfer passageway thereunder. 34. The rotary high density heat exchanger of claim 31, wherein at least 75 percent or more of the surface area of each individual heat exchanger blade has at least one heat transfer passageway thereunder. 35. The rotary high density heat exchanger of claim 31, wherein at least 90 percent or more of the surface area of each individual heat exchanger blade has at least one heat transfer passageway thereunder. 36. The rotary high density heat exchanger of claim 21, wherein at least 25 percent or more of at least one of the surfaces of an individual heat exchanger blade is covered with heat sink fins. 37. The rotary high density heat exchanger of claim 36, wherein at least 50 percent or more of at least one of the surfaces of an individual heat exchanger blade is covered with heat sink fins. 38. The rotary high density heat exchanger of claim 36, wherein at least 60 percent or more of at least one of the surfaces of an individual heat exchanger blade is covered with heat sink fins. 39. The rotary high density heat exchanger of claim 36, wherein at least 75 percent or more of at least one of the surfaces of an individual heat exchanger blade is covered with heat sink fins. 40. The rotary high density heat exchanger of claim 36, wherein at least 90 percent or more of at least one of the surfaces of an individual heat exchanger blade is covered with heat sink fins.

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