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A single closed loop direct exchange geothermal power production system that utilizes a refrigerant working fluid in at least one of three primary designs to generate electrical power from deep wells: with a first version of a direct exchange geothermal power generating system operating primarily on

A single closed loop direct exchange geothermal power production system that utilizes a refrigerant working fluid in at least one of three primary designs to generate electrical power from deep wells: with a first version of a direct exchange geothermal power generating system operating primarily on refrigerant vapor pressure; with a second version of a direct exchange geothermal power generating system operating primarily on liquid refrigerant gravitational pressure; and with a third version of a direct exchange geothermal power generating system operating primarily on both liquid refrigerant gravitational pressure and refrigerant phase change/expansion from a liquid to a vapor state.

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1. A direct exchange geothermal power production apparatus for use with the single walled casing of a single well extending into and within a subsurface formation below a surface of ground or water, the subsurface formation providing a heat source, the apparatus comprising: a closed loop of refriger

1. A direct exchange geothermal power production apparatus for use with the single walled casing of a single well extending into and within a subsurface formation below a surface of ground or water, the subsurface formation providing a heat source, the apparatus comprising: a closed loop of refrigerant piping including a supply refrigerant transport line/pipe and a return refrigerant transport line, wherein the supply refrigerant transport line/pipe and the return refrigerant transport line are disposed in the single well from the top to the bottom of the single well, and where at least a portion of at least one of the return line and the supply line/pipe define a sub-surface heat exchange segment positioned in thermal conductive relation to the heat source;a working refrigerant fluid disposed in the closed loop of refrigerant piping, the working refrigerant fluid both attaining gravitational energy as it returns within the return line within the well casing and absorbing heat from the heat source as it travels through the sub-surface heat exchanger segment;a turbine assembly including at least one of a vapor drive, a liquid drive, and an expansion drive turbine disposed in fluid communication with the closed loop of refrigerant piping and configured to operate in response to working refrigerant flow through the turbine to generate mechanical power; anda condenser disposed in an upper portion of the closed loop of refrigerant piping and having an inlet in fluid communication with the supply refrigerant transport line for receiving working refrigerant vapor and an outlet in fluid communication with the return refrigerant transport line, wherein the condenser is configured to condense the working refrigerant vapor into working refrigerant liquid; andthe sub-surface geothermal heat exchange segment comprising a lower single well supply line/pipe segment that is one of an expanded portion of the supply line within the well casing and a segment of a lower portion of the single well casing itself, in which the upper top end portion of the lower single well supply line/pipe segment that comprises the heat exchange segment is sealed from the remaining upper portion of the well casing and is fluidly communicating with a bottom end of the supply refrigerant transport line/pipe segment and in which a lower portion of the return line extends one of through and past the seal so that the bottom end of the return refrigerant transport line is fluidly communicating with the lower bottom end portion of the lower single well supply line/pipe segment that comprises the heat exchange segment, wherein the lower supply line/pipe heat exchange segment defines an expanded heat exchange surface area positioned in heat transfer relation to the heat source of the subsurface geologic formation to convert the working refrigerant from a more dense and higher pressure liquid refrigerant state to a less dense and lower pressure refrigerant state, so that the return refrigerant transport line comprises a more dense and higher pressure liquid refrigerant transport line and the supply, refrigerant transport line/pipe comprises a less dense and lower pressure refrigerant transport line/pipe. 2. The apparatus of claim 1, in which the working refrigerant comprises R-134A refrigerant. 3. The apparatus of claim 1, in which the lower portions of the supply refrigerant transport line and the return refrigerant transport line extend below the surface less than approximately 27,000 feet, and in which the working refrigerant comprises R-125. 4. The apparatus of claim 1, in which the lower portions of the supply refrigerant transport line and the return refrigerant transport line extend below the surface more than approximately 30,000 feet, and in which the working refrigerant comprises CO2. 5. The apparatus of claim 1, in which the return refrigerant transport line has a first interior cross-sectional area and the supply refrigerant transport line/pipe has a second interior cross-sectional area, and wherein the first interior cross-sectional area is less than the second interior cross-sectional area. 6. The apparatus of claim 1, in which the sub-surface heat exchange segment is configured to permit the heat source of the subsurface formation to convert the working refrigerant from a higher pressure and denser liquid refrigerant phase to one of a vapor phase and a lower pressure and less dense liquid refrigerant phase, so that the return refrigerant transport line to the heat exchange segment comprises a liquid refrigerant transport line and the supply refrigerant transport line/pipe comprises one of a vapor phase and a lower pressure and less dense liquid refrigerant phase refrigerant transport line. 7. The apparatus of claim 6, in which at least one turbine is disposed in the one of a vapor phase and a lower pressure and less dense liquid refrigerant phase refrigerant transport line that exits the single well casing and is upstream of the condenser and comprises one of a one of a refrigerant vapor driven turbine, a liquid refrigerant driven turbine, and a refrigerant expansion driven turbine. 8. The apparatus of claim 1, in which at least one liquid drive turbine is disposed above the well and in fluid communication with the less dense and lower pressure liquid refrigerant transport supply line and is configured to produce mechanical power hi response to a flow of working refrigerant liquid. 9. The apparatus of claim 1, in which the turbine assembly further comprises at least one second and additional turbine disposed in fluid communication with the less dense and lower pressure liquid refrigerant transport supply line and is positioned above the well and downstream of the first liquid drive turbine, wherein the at least one second turbine is configured to induce a phase change of the refrigerant from the less dense and lower pressure liquid refrigerant state to a vapor refrigerant phase, and in which the at least one second turbine generates mechanical power in response to the expanding refrigerant phase change. 10. The apparatus of claim 1, further comprising the expanded heat exchange surface area segment, which segment is one of a lower well casing segment and an expanded part of the working fluid supply line within the lower well casing segment, providing a means both for geothermal heat transfer to the working fluid and for transporting the working fluid up and out of the expanded heat exchange surface area segment, and which lower segment includes a top wall working fluid containment portion of the said lower segment, which top wall effectively seals an upper portion of the well casing from a lower portion of the well casing, with the liquid working fluid return line extending through the seal all the way to the bottom of the expanded heat exchange surface area segment, all within the lower portion of the casing of a single well, which lower well portion segment extends from a depth that is no greater than from the bottom of the well casing up to where the surrounding geology's temperature is at least one of equal to and greater than that of the refrigerant temperature designed for that of the refrigerant working fluid temperature as it exits the well casing at the surface. 11. The apparatus of claim 10, further comprising a heat conductive fill material, with a heat transfer rate of at least 1.4 BTUs/Ft. Hr. Degrees F. at least one of disposed within any empty space within the lower well casing segment around the expanded refrigerant return line and disposed within any empty space around the exterior of the lower well casing segment to a depth that is no greater than from the bottom of the well casing up to where the surrounding geology's temperature is one of equal to and greater than that of the refrigerant temperature designed for that of the refrigerant working fluid temperature as it exits the well casing at the surface. 12. The apparatus of claim 11, in which the heat conductive fill material comprises a cementitious grout. 13. The apparatus of claim 11, in which the heat conductive fill material comprises a metal. 14. The apparatus of claim 10, further comprising: a first respective thermal insulator surrounding the supply refrigerant transport line from the top wall of the expanded heat exchange surface segment to the top of the well at the surface; anda second respective thermal insulator surrounding the return refrigerant transport line from at least the top wall of the expanded heat exchange surface segment to the top of the well at the surface. 15. The apparatus of claim 14, in which the second respective thermal insulator surrounding the return refrigerant line extends from the lowest elevation of the return line at/near the bottom of the expanded heat exchange surface area segment to the top of the well at the surface. 16. The apparatus of claim 1, in which the supply refrigerant transport line extends from the expanded heat exchange surface segment, which expanded area segment is comprised of at least one of an expanded supply line within a single well casing and a single wall single well casing segment, to the top of the well surface and is surrounded by a first respective thermal insulator above its expanded surface area segment, and in which the return refrigerant transport line extends from the top of the well surface down to and through the lower portion of the expanded surface area segment and is surrounded by a respective second thermal insulator all the way to its lowermost elevation, and in which the first and second respective thermal insulators comprise at least one respective layers of thermal insulation material. 17. The apparatus of claim 16, in which the otherwise empty space within the single well casing surrounding the first and second thermal insulators surrounding the respective supply and return lines above the expanded surface area segment is filled with a thermal insulation comprised of one of a vacuum and a material comprised of at least one of a poorly/non heat conductive fluid, a solid, and a gel. 18. The apparatus of claim 1, in which at least one vapor drive turbine is disposed above the well and is in fluid communication with the less dense and lower pressure vapor refrigerant transport supply line and is configured to produce mechanical power in response to a flow of working refrigerant vapor. 19. The apparatus of claim 1, in which an intermediate portion of the supply refrigerant transport line that extends from the sub-surface heat exchange segment to the surface is surrounded by a first respective insulator, and in which at least an intermediate portion of the return refrigerant transport line that extends from the sub-surface heat exchange segment to the surface is surrounded by a second respective insulator. 20. A direct exchange geothermal power production apparatus for use with the single walled metal casing of a single well extending into and within a subsurface formation below a surface of ground or water, the subsurface formation providing a heat source, the apparatus comprising: a closed loop of refrigerant piping including a supply refrigerant transport line/pipe and a return refrigerant transport line, wherein the supply refrigerant transport line/pipe and the return refrigerant transport line are disposed in the single well from the top to the bottom of the single well, and where at least a portion of at least one of the return line and the supply line/pipe define a sub-surface heat exchanger segment positioned in thermal conductive relation to the heat source;a working refrigerant fluid disposed in the closed loop of refrigerant piping, the working refrigerant fluid both attaining gravitational energy as it returns within the return line within the well casing and absorbing heat from the heat source as it travels through the sub-surface heat exchange segment;a turbine assembly, including at least one of a vapor drive, a liquid drive, and an expansion drive turbine disposed in fluid communication with the closed loop of refrigerant piping and configured to operate in response to working refrigerant flow through the turbine to generate mechanical power; anda condenser disposed in an upper portion of the closed loop of refrigerant piping and having an inlet in fluid communication with the supply refrigerant transport line for receiving working refrigerant vapor and an outlet in fluid communication with the return refrigerant transport line, wherein the condenser is configured to condense the working refrigerant vapor into working refrigerant liquid,a first respective thermal insulator surrounding at least an intermediate portion of the liquid return refrigerant transport line extending from the surface to at least a depth where the surrounding geology's temperature is at least one of equal to and less than that of the refrigerant temperature designed for that of the refrigerant working fluid temperature as it exits the well at the surface;a second respective thermal insulator surrounding an intermediate portion of the vapor refrigerant transport line/pipe extending from the surface to a depth where the surrounding geology's temperature is less than that of the refrigerant temperature designed for that of the refrigerant working fluid temperature as it exits the well at the surface;where the return line is of a smaller interior cross-sectional area size than that of the supply line/pipe;where the return line is at least one of operably coupled to and in fluid communication with the supply line/pipe within the single well near the bottom of the single well;where any otherwise empty space area surrounding the return line and the supply line/pipe within the single well casing is filled with a heat conductive fill material, comprised of one of a solid, a liquid, and a gel, with a heat transfer rate of at least 1.4 BTUs/Ft. Hr. Degrees F, to a depth from the bottom of the well to where the surrounding geology's temperature is one of equal to and greater than that of the refrigerant temperature designated for that of the refrigerant working fluid temperature as it exits the well at the surface;where any otherwise empty space area surrounding the exterior of the well casing is filled with a heat conductive solid and a liquid fill material, with a heat transfer rate of at least 1.4 BTUs/Ft. Hr. Degrees F. to a depth no greater than from the bottom of the well to where the surrounding geology's temperature is at least one of equal to and greater than that of the refrigerant temperature designed for that of the refrigerant working fluid temperature as it exits the well at the surface;where any otherwise empty space area surrounding the return line and the supply line/pipe within the single well casing is filled with one of a vacuum and a non-heat conductive/poor heat conductive fill material comprised of one of a solid, a liquid, and a gel, at least to a depth from the top of the well to where the surrounding geology's temperature is one of equal to and greater than that of the refrigerant temperature designed for that of the refrigerant working fluid temperature as it exits the well at the surface; andthe sub-surface geothermal heat exchange segment comprising a lower single well supply line/pipe segment that is one of an expanded portion of the supply line within the well casing and a segment of a lower portion of the single well casing itself, in which the upper top end portion of the lower single well supply line/pipe segment that comprises the heat exchange segment is sealed from the remaining upper portion of the well casing and is fluidly communicating with a bottom end of the supply refrigerant transport line/pipe segment and in which a lower portion of the return line extends one of through and past the seal so that the bottom end of the return refrigerant transport line is fluidly communicating with the lower bottom end portion of the lower single well supply line/pipe segment that comprises the heat exchange segment, wherein the lower supply line/pipe heat exchange segment defines an expanded heat exchange surface area positioned in heat transfer relation to the heat source of the subsurface geologic formation to convert the working refrigerant from a more dense and higher pressure liquid refrigerant state to a less dense and lower pressure refrigerant state, so that the return refrigerant transport line comprises a more dense and higher pressure liquid refrigerant transport line and the supply, refrigerant transport line/pipe comprises a less dense and lower pressure refrigerant transport line/pipe. 21. The apparatus of claim 1, further comprising a liquid pump disposed in the liquid refrigerant transport line between the surface and the condenser. 22. The apparatus of claim 1, further comprising a generator operably coupled to the turbine assembly and configured to generate electrical power in response to mechanical power from the turbine assembly. 23. The apparatus of claim 1, further comprising a liquid refrigerant holding tank disposed in the liquid refrigerant transport line immediately downstream of the condenser and before liquid phase refrigerant enters the first of a liquid drive turbine and the sub-surface well. 24. The apparatus of claim 1, further comprising a fan disposed in the vapor refrigerant transport line upstream of the condenser and oriented to advance vapor refrigerant out of a turbine and into the condenser. 25. The apparatus of claim 19, in which the otherwise empty space within the single well casing surrounding the respective first and second thermal insulators surrounding the respective supply and return lines above the sub-surface heat exchange segment is comprised of one of a thermal insulating vacuum and one of a non-heat conductive/poor heat conductive solid, gel, and liquid fill material. 26. A direct exchange geothermal power production apparatus for use with the single walled casing of a single well extending into and within a subsurface formation below a surface of ground or water, the subsurface formation providing a heat source, the apparatus comprising: a closed loop of refrigerant piping including a supply refrigerant transport line/pipe and a return refrigerant transport line, wherein the supply refrigerant transport line/pipe and the return refrigerant transport line are disposed in the single well from the top to the bottom of the single well, and where at least a portion of at least one of the return line and the supply line/pipe define a sub-surface heat exchange segment positioned in thermal conductive relation to the heat source;a working refrigerant fluid disposed in the closed loop of refrigerant piping, the working refrigerant fluid both attaining gravitational energy, as it returns within the return line within the well casing and absorbing heat from the heat source as it travels through the sub-surface heat exchange segment;a turbine assembly including at least one of a vapor drive, a liquid drive, and an expansion drive turbine disposed in fluid communication with the closed loop of refrigerant piping and configured to operate in response to working refrigerant flow through the turbine to generate mechanical power; anda condenser disposed in an upper portion of the closed loop of refrigerant piping and having an inlet in fluid communication with the supply refrigerant transport line for receiving working refrigerant vapor and an outlet in fluid communication with the return refrigerant transport line, wherein the condenser is configured to condense the working refrigerant vapor into working refrigerant liquid;a liquid holding tank positioned directly under the condenser; andthe sub-surface geothermal heat exchange segment comprising a lower single well supply line/pipe segment that is one of an expanded portion of the supply line within the well casing and a segment of a lower portion of the single well casing itself, in which the upper top end portion of the lower single well supply line/pipe segment that comprises the heat exchange segment is sealed from the remaining upper portion of the well casing and is fluidly communicating with a bottom end of the supply refrigerant transport line/pipe segment and in which a lower portion of the return line extends one of through and past the seal so that the bottom end of the return refrigerant transport line is fluidly communicating with the lower bottom end portion of the lower single well supply line/pipe segment that comprises the heat exchange segment, wherein the lower supply line/pipe heat exchange segment defines an expanded heat exchange surface area positioned in heat transfer relation to the heat source of the subsurface geologic formation to convert the working refrigerant from a more dense and higher pressure liquid refrigerant state to a less dense and lower pressure refrigerant state, so that the return refrigerant transport line comprises a more dense and higher pressure liquid refrigerant transport line and the supply, refrigerant transport line/pipe comprises a less dense and lower pressure refrigerant transport line/pipe. 27. The apparatus of claim 26, further comprising respective thermal insulation materials surrounding the respective portions of the respective supply and return refrigerant transport lines/pipes within the upper portion of the well least from the top of the well to where the surrounding geology's temperature is less than that of the refrigerant temperature designed for that of the refrigerant working fluid temperature as it exits the well at the surface. 28. The apparatus of claim 27, in which the otherwise empty space within the single well casing the respectively thermally insulated supply and return lines/pipes within the said upper portion of the well casing is filled with a thermal insulation material comprised of at least one of a poorly/non-heat conductive vacuum, a fluid, a solid, and a gel. 29. The apparatus of claim 26, in which the return refrigerant transport line is disposed within the single well casing, and where the thermal insulation surrounding the return refrigerant transport line extends all the way from the top of the well down to the lowest elevation of the return line within the well casing, inclusive of extending through the area where the surrounding geology's temperature is greater than that of the refrigerant temperature designed for that of the refrigerant working fluid temperature as it exits the well at the surface. 30. The apparatus of claim 26, in which the thermal insulation surrounding the supply refrigerant transport line/pipe extends all the way from the top of the well at least down to the elevation where the surrounding geology's temperature is greater than that of the refrigerant temperature designed for that of the refrigerant working fluid temperature as it exits the well at the surface. 31. The apparatus of claim 27, in which the otherwise empty space within the single well casing surrounding the respective thermal insulation around the respective supply and return lines within the upper portion of the well contains a thermal insulation comprised of at least one of a vacuum and at least one of a non-heat conductive/poor heat conductive solid, fluid, and gel. 32. The apparatus of claim 1 where the otherwise empty space area surrounding the exterior of the well casing is filled with a heat conductive fill material, comprised of one of at least one of solid and a liquid, with a heat transfer rate of at least 1.4 BTUs/Ft. Hr. Degrees F, to a depth no greater than from the bottom of the well to where the surrounding geology's temperature is one of equal to and greater than that of the refrigerant temperature designed for that of the refrigerant working fluid temperature as it exits the well at the surface. 33. The apparatus of claim 1 where a liquid holding tank is provided that is positioned directly under the condenser. 34. The apparatus of claim 20 where a liquid holding tank is provided that is positioned directly under the condenser. 35. The apparatus of claim 26 where a liquid holding tank is provided that is positioned directly under the condenser. 36. The apparatus of claim 1, in which the sub-surface heat exchange segment is configured to permit the heat source of the subsurface formation to convert the working refrigerant from a denser and higher pressure liquid refrigerant to a less dense and lower pressure liquid refrigerant, so that the return refrigerant transport line to the heat exchange segment comprises a denser and higher pressure liquid refrigerant transport line and the supply refrigerant transport line/pipe comprises a less dense and lower pressure refrigerant transport line/pipe. 37. The apparatus of claim 36, in which at least one turbine is disposed in the less dense and lower pressure liquid refrigerant transport line that exits the well casing and is upstream of the condenser and comprises a liquid refrigerant driven turbine. 38. The apparatus of claim 36 in which at least one turbine is disposed in the less dense and lower pressure liquid refrigerant transport line that exits one of the well casing and a liquid refrigerant driven turbine, and is downstream of one of the well casing and the liquid refrigerant driven turbine and is upstream of the condenser and comprises an expansion refrigerant driven turbine, within which the liquid phase refrigerant is expanded into a vapor phase refrigerant. 39. The apparatus of claim 20 where the empty space area surrounding the return line and the supply line within the upper portion of the single well casing is filled with a poor/non-heat conductive fill material, comprised of one of a solid, a liquid, a gel, a vapor, and a vacuum to a depth from the top of the well to where the surrounding geology's temperature is at least one of equal to and greater than that of the refrigerant temperature designed for that of the refrigerant working fluid temperature as it exits the well at the surface. 40. The apparatus of claim 1, in which the turbine is positioned below the elevation of a liquid working fluid holding tank, with the liquid working fluid holding tank situated immediately below the condenser. 41. The apparatus of claim 20, in which the turbine is positioned below the elevation of a liquid working fluid holding tank, with the liquid working fluid holding tank situated immediately below the condenser. 42. The apparatus of claim 26, in which the turbine is positioned below the elevation of a liquid working fluid holding tank, with the liquid working fluid holding tank situated immediately below the condenser. 43. The apparatus of claim 1, in which the turbine is positioned above the elevation of the condenser, with a liquid working fluid holding tank situated immediately below the condenser. 44. The apparatus of claim 20, in which the turbine is positioned above the elevation of the condenser, with a liquid working fluid holding tank situated immediately below the condenser. 45. The apparatus of claim 26, in which the turbine is positioned above the elevation of the condenser, with a liquid working fluid holding tank situated immediately below the condenser. 46. The apparatus of claim 1, in which the exterior upper portion of the casing within the well is not provided/surrounded with a heat conductive fill material above an elevation at least from the bottom of the well where the temperature of the surrounding geology is cooler than the design temperature of the working fluid exiting the well. 47. The apparatus of claim 20, in which the exterior upper portion of the casing within the well is not provided/surrounded with a heat conductive fill material above an elevation at least from the bottom of the well where the temperature of the surrounding geology is cooler than the design temperature of the working fluid exiting the well. 48. The apparatus of claim 26, in which the exterior upper portion of the casing within the well is not provided/surrounded with a heat conductive fill material above an elevation at least from the bottom of the well where the temperature of the surrounding geology is cooler than the design temperature of the working fluid exiting the well. 49. The apparatus of claim 1 with the provision of a double inverted U bend at the lower distal end of the liquid return line, in conjunction with a liquid holding tank positioned above the well, with the bottom of the holding tank operably connected to the upper top end of the liquid return line. 50. The apparatus of claim 20 with the provision of a double inverted U bend at the lower distal end of the liquid return line, in conjunction with a liquid holding tank positioned above the well, with the bottom of the holding tank operably connected to the upper top end of the liquid return line. 51. The apparatus of claim 26 with the provision of a double inverted U bend at the lower distal end of the liquid return line, in conjunction with a liquid holding tank positioned above the well, with the bottom of the holding tank operably connected to the upper top end of the liquid return line.