System and method for in-line geothermal and hydroelectric generation
원문보기
IPC분류정보
국가/구분
United States(US) Patent
등록
국제특허분류(IPC7판)
F03G-007/00
출원번호
UP-0305832
(2005-12-15)
등록번호
US-7788924
(2010-09-27)
발명자
/ 주소
Hines, Garold Paul
대리인 / 주소
Lewis and Roca LLP
인용정보
피인용 횟수 :
22인용 특허 :
6
초록▼
A stack system and method for in-line geothermal and hydroelectric generation from recovered natural gas-fired water/steam process waste heat. The stack system and method is a new way of reusing natural gas fired water/steam process waste heat to make more electricity from the same Btu inputs. The s
A stack system and method for in-line geothermal and hydroelectric generation from recovered natural gas-fired water/steam process waste heat. The stack system and method is a new way of reusing natural gas fired water/steam process waste heat to make more electricity from the same Btu inputs. The stack system and method uses warm industrial demineralized water from various sources, a micro-managed combined stack flue system and specific terrain to ring out every bit of energy possible from traditional, heretofore, acceptable wastes. The stack uses two marginal waste heat sources to make one significant heat source for additional fossil fuel-free generation. This stack is unique in that it incorporates tandem, geothermal and hydroelectric generators. The stack can be applied to closed-loop (Power Stack) and open-loop (Desalination Stack) processes.
대표청구항▼
What is claimed is: 1. A method for reusing natural gas waste heat to produce electricity without additional BTU inputs, the method comprising: providing a systematic closed loop for circulating demineralized circulating water (DCW) in a consistent direction around said loop, said loop comprising a
What is claimed is: 1. A method for reusing natural gas waste heat to produce electricity without additional BTU inputs, the method comprising: providing a systematic closed loop for circulating demineralized circulating water (DCW) in a consistent direction around said loop, said loop comprising a DCW pump, a natural gas heat exchanger fluidly coupled in-line to said DCW pump, a steam cycle heat exchanger fluidly coupled in-line to said natural gas heat exchanger, a flue gas heat exchanger fluidly coupled in-line to said steam cycle heat exchanger, a geothermal turbine and geothermal heat exchanger fluidly coupled in-line to said flue gas heat exchanger, a hydroelectric unit fluidly coupled in-line in between said geothermal turbine and said DCW pump; said DCW flowing from said DCW pump to said natural gas heat exchanger, wherein said natural gas heat exchanger cools said DCW; said cooled DCW flowing through said steam cycle heat exchanger and to said flue gas heat exchanger, wherein said cooled DCW is heated into DCW saturated steam, contributing heat to said DCW; said DCW saturated steam flowing to said geothermal turbine and heat exchanger, wherein said geothermal heat exchanger condenses said DCW saturated steam and heats a refrigerant, causing said heated refrigerant to flow through said geothermal turbine and generate electricity; said condensed DCW flowing to said hydroelectric unit and generating electricity; and said DCW flowing from said hydroelectric unit back to said DCW pump, wherein the geothermal generation and the hydroelectric generation are powered by waste heat from flue gas and waste heat from said steam cycle heat exchanger into said DCW, and wherein said systematic closed loop is free from additional fossil fuel input. 2. The method of claim 1, wherein said refrigerant is Freon. 3. The method of claim 1, wherein the infrastructure of said systematic closed loop includes pumps and fans powered by supplies having voltages not exceeding 480 volts. 4. The method of claim 1, wherein said systematic closed loop further comprises a DCW-in header fluidly coupled between said natural gas heat exchanger and said steam cycle heat exchanger, said DCW-in header configured to route DCW through said steam cycle heat exchanger to a DCW-out header fluidly coupled between said steam cycle heat exchanger and said flue gas heat exchanger. 5. The method of claim 4, wherein said steam cycle heat exchanger comprises a plurality of steam cycle heat exchangers. 6. The method of claim 4, wherein DCW from said DCW-out header is heated by cumulative flue gas heat at said flue gas heat exchanger, said flue gas heat provided by a thermal flue source fluidly coupled to said flue gas heat exchanger. 7. The method of claim 6, wherein DCW in said flue gas heat exchanger is vaporized by said cumulative flue gas heat. 8. The method of claim 6, wherein the temperature of said flue gas heat is increased by a duct burner fluidly coupled between said thermal flue source and said flue gas heat exchanger. 9. The method of claim 6, wherein said systematic closed loop further comprises a natural gas supply fluidly coupled to said natural gas heat exchanger and said thermal flue source, wherein said natural gas supply provides cooling in said natural gas heat exchanger and combustion BTUs to said thermal flue source. 10. The method of claim 1, wherein said DCW saturated steam from said flue gas heat exchanger flows up a vertical distance to said geothermal turbine. 11. The method of claim 10, wherein said DCW saturated steam from said flue gas heat exchanger flows upwards a vertical distance through a de-aerator to said geothermal turbine. 12. The method of claim 11, wherein said de-aerator removes non-condensables from said DCW saturated through an eductor fluidly coupled to said de-aerator. 13. The method of claim 1, wherein said condensed DCW flows down a vertical distance to said hydroelectric unit. 14. The method of claim 1, wherein said systematic closed loop is retrofitted with a pre-existing natural gas combustion turbine. 15. The method of claim 14, wherein: said DCW is boiled a first time by the thermal desalination process; and said DCW is boiled a second time from the flue gas of said pre-existing natural gas combustion turbine.
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