IN SITU GEOTHERMAL POWER

Abstract

A method of generating electricity from geothermal energy utilizing an in situ closed loop heat exchanger deep within the earth using a recirculating heat transfer fluid to power an in situ modular turbine and generator system within a vertical, large bore, deep, tunnel shaft. The shaft length and diameter are dependent on the shaft temperature and sustaining heat flux. The method further includes methods of deep shaft boring and excavating, liner placement and sealing, shaft transport systems, shaft Heating, Ventilation, and Air Conditioning, and operations and maintenance provisions. The method has few global location restrictions, maximizes thermal efficiency as to make power generation practical, has a small site surface footprint, does not interact with the environment, is sustainable, uses renewable energy, and is a zero release carbon and hazardous substance emitter.

Claims

1. A method of geothermal electric power production, comprising: an excavated deep tunnel shaft of sufficient diameter, temperature and sustaining heat flux to contain one or more in situ closed loop heat exchangers contained within a high conductivity fixative using a recirculating heat transfer fluid to power a plurality of in situ modular power system components, wherein the modular turbine and electric generator system components that may be routinely decoupled and moved to the surface for maintenance are located near the heat exchangers within the shaft.

2. The method of claim 1, wherein the shaft is not a small diameter well with conventional metal casing, but rather a tunnel shaft of substantial diameter based on the shaft temperature and heat flux with a structurally reinforced, sealed, concrete liner to provide a chemical boundary from the earth to accommodate system components that support the desired electric output.

3. The method of claim 2, wherein the shaft depth and width design parameters are dependent on the earth's data collected during the drilling of test wells.

4. The method of claim 3, wherein the earth's main test data are temperature and sustaining heat flux.

5. (canceled)

6. The method of claim 2, wherein the shaft may be vertical, at an angle, or helical.

7. (canceled)

8. The method of claim 2, wherein the liner supports a transfer system for the purpose of shaft transportation for excavated material, equipment, modular components, and work crews.

9. The method of claim 8, wherein the transport system may use a modular engine to move said objects.

10. The method of claim 1, wherein the heat exchanger(s) further comprising a plurality of tubes, where the configuration, quantity, tube diameter and adequate heat transfer length are dependent on shaft diameter, temperature and sustaining heat flux.

11. (canceled)

12. (canceled)

13. The method of claim 10, wherein the heat exchanger heat transfer fluid is water or other fluid or gas with sufficient boiling point dependent on the shaft design parameters.

14. The method of claim 1, wherein a plurality of modular system components including turbine(s), electric generator, pumps, and support systems are located within the shaft above and relatively close to the heat exchanger(s) to increase thermal efficiency within a desired ambient condition.

15. (canceled)

16. The method of claim 14, wherein the shaft contains a Heating, Ventilation, and Air Conditioning system to provide a desired ambient atmosphere and chemistry conditions within the shaft.

17. The method of claim 14, wherein the systems control room(s) are above ground and/or at varying elevations along the shaft.

18. The method of claim 14, wherein the plant systems are remotely controlled, where practical.

Description

DESCRIPTION OF THE DRAWINGS

[0024] The drawings are for illustrative purposes. The drawings shown are not restrictive to the design and are not to scale.

[0025] The foregoing aspects and many of the attendant advantages of this disclosure will become more readily appreciated as the same become better understood by reference to the following detailed description, when taken in conjunction with the accompanying drawings, wherein:

[0026] FIG. 1 is a cross-sectional illustrative view of a typical IGP plant where all major system components are modular in design and contained within the deep shaft in accordance with the embodiment of the present disclosure;

[0027] FIG. 2 is a cross-sectional illustrative view of example in situ heat exchanger configurations where the location specific design is dependent on the shaft's sustaining heat flux and temperature.

DETAILED DESCRIPTION

[0028] The detailed description set forth below in connection with the appended drawings, where like numerals reference like elements, is intended as a description of various embodiments of the disclosed subject matter and is not intended to represent the only embodiments. Each embodiment described in this disclosure is provided merely as an example or illustration and should not be construed as preferred or advantageous over other embodiments. The illustrative examples provided herein are not intended to be exhaustive or to limit the disclosure to the precise forms disclosed. Similarly, any steps described herein may be interchangeable with other steps, or combinations of steps, in order to achieve the same or substantially similar result.

[0029] In the following description, numerous specific details are set forth in order to provide a thorough understanding of exemplary embodiments of the present disclosure. It will be apparent to one skilled in the art, however, that many embodiments of the present disclosure may be practiced without some or all of the specific details. In some instances, well-known process steps have not been described in detail in order not to unnecessarily obscure various aspects of the present disclosure. Further, it will be appreciated that embodiments of the present disclosure may employ any combination of the features described herein.

[0030] Embodiments of the present disclosure relate to methods for the design of an In Situ Geothermal Power (IGP) plant. An IGP plant may be sited anywhere on the planet. Certain locations are less or more desirable. A less desirable location, dissimilar to an Enhanced Geothermal Systems plant, is an area that exhibits elevated seismic and near surface geothermal activity. A more desirable location is an area that may benefit from a low cost electricity supply, for example, an impoverished area that is isolated from an electric grid, that has an average to low seismic activity, as well as an average to high geothermal gradient.

[0031] Referring to FIG. 1, a deep tunnel shaft 1 is first excavated. The shaft is not a small diameter well, but rather a vertical tunnel of substantial diameter to accommodate some or all power plant system components. The shaft may be vertical, at an angle, or helical. The major regions of the shaft include a near surface region 9, a geothermal heat exchanger region 7, and a region in between the surface and heat exchanger region 8. These regions 7, 8, 9 are defined by transitions, which are shown as lines 12, 13. The surface of the earth is above the shaft 11. Current Tunnel Boring Machines (TBM) and similar vertical boring technology may be utilized to bore the shaft, excavate the earth, and seal the shaft with a structural liner 10. The liner provides a boundary that inhibits shaft collapse and any of earth's corrosive or other hazardous substances from interacting with the closed loop IGP system. The liner may support an integral transport system such as a rail(s) or conveyor. This integral transport system may negate the use of cranes and rigging that could fail or be inefficient under such long distances. The integral transport system may utilize a modular engine to transport equipment, excavated material, crews, and modular components down and up the shaft. The TBM or similar may be left at the bottom of the shaft upon completion of the excavation.

[0032] Completion of the shaft is based on several design parameters. For example, a shaft depth may typically reach 4 to 12 miles dependent on the site location's geothermal properties. The main design parameters are rock temperature and sustaining heat flux. The temperature is simply the temperature of the surrounding shaft rock. Ideal temperatures may be in the hundreds of degrees Celsius. The heat flux is considered as the rate at which heat is replenished by the earth when removed. Referring to FIG. 1, these ideal design parameters are located in region 8. The heat flux rate will be a design parameter in determining the overall heat exchanger(s) dimensions and type. These design parameters will vary based on the shaft site location.

[0033] Referring to FIG. 1 for a typical heat exchanger location 8, the deep shaft may reach a rock temperature well above the boiling point of water. However, some shafts may need to stop excavation for local geological reasons and attain a lower temperature. At lower temperatures, a secondary heat transfer system or an alternate fluid or gas with a lower boiling point than water may be utilized in the IGP design. This maintains design flexibility while still being a closed loop system. For a typical location, the heat flux required may be based on the desired design of the plant electricity output. The heat flux minimum value will replace the heat loss removed from the heat exchanger(s).

[0034] Referring to FIG. 2, a heat exchanger may have different designs. The heat exchanger type, size and shape are based on the heat flux attained and the desired output of the plant. This maintains design flexibility between the heat flux, heat exchanger design, and output desired. For example, in a location where heat flux is very low, multiple shafts may be bored for the placement of multiple heat exchangers 2 to attain the desired output. Heat exchanger design types are not limited, such as u-tube or once-through types.

[0035] Referring to FIG. 2, the heat exchanger 1 is at the shaft bottom and is affixed to the shaft via high conductivity grout 4 or similar. Grout conductivity may be increased with additives such as graphite, aluminum, iron, or similar. Setup inhibitors and/or non-water based grouts may be used due to the high temperature application where water flashing to steam may impede proper setup. Alternatively, coolant may be applied to the heat exchanger during setup to control temperature. Typically, thousands of heat exchange tubes 5 line the shaft supplied by a common header 3 at shaft centerline. U-tube style and other heat exchanger types are also within the scope of design. The individual tube diameter design is also a function dependent on the shaft temperature parameters. Based on the temperature parameters, the total tube length may typically range between feet and miles.

[0036] For an example using water as the fluid heat transfer medium; feed water is pumped downward into the top of the heat exchanger header, circulates upward through the grouted tubes, absorbs geothermal energy, and exists as steam to supply the steam turbines(s). Referring to FIG. 1, steam dryers, pumps, Heating, Ventilation, and Air Conditioning (HVAC), and other support systems are not shown.

[0037] As shown in FIG. 1, typically, the modular high pressure turbine 3, low pressure turbine(s) 4, and generator 5 share the same rotor, and are placed relatively close to the heat exchanger within the shaft to minimize thermal energy dissipation. The modular components may be located in a region 7 away from the heat exchanger region 8 where harsh ambient conditions exits. The typical electric generator 5 is modular and sized for the design parameters and desired plant output. When the shaft is many miles deep, the energy in the fluid will dissipate while traveling to a surface turbine. Thermal efficiency is increased when placing modular plant system components as close to the heat exchanger(s) as the shaft ambient conditions allow. These in situ modular components are designed to remotely couple and decouple for transport to and from the surface 11 for maintenance.

[0038] The shaft may or may not be pressurized dependent on the local site design parameters. A typical shaft is not pressurized or sealed. The shaft is structurally lined and sealed from the earth. The ambient air within the shaft, therefore, is not naturally pressurized and may only be a few atmospheres at depth. Shaft ambient air temperatures and chemistry may be maintained as designed with the use of an HVAC or similar system. The HVAC system may make use of the above ground atmosphere to maintain cooling and chemistry.

[0039] FIG. 1 shows a condenser 6. The condenser may be placed in the shaft region 9 where the shaft temperature and shaft length provide enough cooling to make it possible to return the spent fluid back to the heat exchanger. Based on the design parameters and the availability of conventional surface cooling options specific to the site location, an above ground or enhanced shaft condenser cooling system may be utilized.

[0040] A typical IGP plant may have the electric generator connected to an insulated, high voltage, output line that conveys electricity to a standard surface transformer(s) prior to connecting to a standard switchyard and grid. Depending on the length of the shaft and other design parameters, a modular transformer may also be placed in the shaft prior to the output line exiting the shaft.

[0041] The modular component design used in a typical IGP plant allows for periodic decoupling and conveyance to the surface for maintenance or replacement.

[0042] Multiple IGP shafts at one plant location may serve to smooth power transmission outages from both planned maintenance and unscheduled maintenance. Plant output is dependent on location and associated site parameters, but may be designed at the typical fossil fuel plant MWe range per IGP shaft. This output is significantly higher than other renewable power plants like solar and wind farms. The typical IGP plant surface footprint is considered small as compared to fossil, nuclear, solar, or wind power plants of similar MWe output.

[0043] The IGP fuel source is the geothermal energy from the earth and is considered renewable and sustainable. The carbon emissions from an IGP plant are near zero. The IGP plant system is a closed loop system that does not directly interact with the earth itself, therefore, once the grouted heat exchanger(s) is in place, there are no generating sources of manmade seismic activity as with fracturing, or conditions where toxins and fluids are released into the environment.

[0044] IGP is unlike any current geothermal process in that it requires the excavation of a deep vertical shaft of sufficient diameter to place a closed loop, grouted, in situ heat exchanger that supplies a power system of in situ modular components to maximize the plant's thermal efficiency.

[0045] The principles, representative embodiments, and modes of operation of the present disclosure have been described in the foregoing description. However, aspects of the present disclosure which are intended to be protected are not to be construed as limited to the particular embodiments disclosed. Further, the embodiments described herein are to be regarded as illustrative rather than restrictive. It will be appreciated that variations and changes may be made by others, and equivalents employed, without departing from the spirit of the present disclosure. Accordingly, it is expressly intended that all such variations, changes, and equivalents fall within the spirit and scope of the present disclosure, as claimed.