Method for on demand power production utilizing geologic thermal recovery

Abstract

Methods for providing on demand power to an end user in a variety of embodiments are disclosed. Closed loop thermal recovery arrangements are disposed within a geologic formation having a predetermined potential thermal output capacity. A power generation device is incorporated in the loop to recover energy. A working fluid is circulated within the loop at varying flow rates to oscillate thermal output about the predetermined potential thermal output capacity, to produce on demand power where the average thermal output may equal the predetermined potential thermal output capacity. Integrations with intermittent renewable energy sources are provided which optimize performance and distribution.

Claims

1. A method for regulating a thermal output capacity of a well system, the well system including a working fluid capable of thermal charging from a geologic formation, and having an inlet well and an outlet well and disposed within the geologic formation, comprising: modulating circulation of said working fluid within said well system to oscillate thermal output from thermally charged working fluid about a characteristic predetermined potential thermal output capacity of said geologic formation, where an averaged oscillated thermal output equals or is less than said characteristic predetermined potential thermal output capacity of said geologic formation and where said characteristic predetermined potential thermal output capacity is determined based on a baseload thermal output of said working fluid flowing at a constant flow rate.

2. The method as set forth in claim 1, wherein said thermal output is inconstant.

3. The method as set forth in claim 1, wherein said thermal output is cycled between a charging operation where said working fluid is thermally charged through conductive heat transfer from said geologic formation and a discharging operation where thermal energy is removed for processing.

4. The method as set forth in claim 3, wherein the processing comprises conversion to at least one of electrical energy, heat energy and combinations thereof.

5. The method as set forth in claim 3, wherein the modulating includes at least one of variation in flow rate of said working fluid, residency time in said system, oscillation duration, thermal charging duration, thermal discharging and combinations thereof.

6. The method as set forth in claim 5, wherein an interaction between said charged working fluid and a power generator includes minimizing said residency time by increasing the flow rate of said charged working fluid.

7. The method as set forth in claim 1, further including a step of generating on demand energy to an end user through interaction between said working fluid and a power generation device.

8. The method as set forth in claim 1, wherein said thermally charged working fluid is circulated above said characteristic predetermined potential thermal output capacity in a discharging cycle to produce on demand power.

9. The method as set forth in claim 1, wherein said geologic formation is selected from a group comprising: a geothermal formation, a low permeability formation, a sedimentary formation, a volcanic formation, a high temperature formation, a variable permeability formation and combinations thereof.

10. The method as set forth in claim 1, wherein cracks, fissures, voids, and/or fractures of said geologic formation are small enough to not allow fluid communication between to spaced-apart inlet and outlet wells.

11. The method as set forth in claim 1, wherein cracks, fissures, voids and or fractures are induced in said geologic formation.

12. The method as set forth in claim 11, further including a step of sealing said cracks, fissures, voids and or fractures is coincident with drilling said inlet and outlet wells.

13. The method as set forth in claim 11, further including a step of sealing said cracks, fissures, voids and or fractures occurring subsequent to drilling said wells.

14. The method as set forth in claim 1, wherein said working fluid includes at least one of a drag reducing additive, a surfactant, a polymeric compound, a suspension, a biological additive, a stabilizing agent, anti-scaling agents, anti-corrosion agents, friction reducers, anti-freezing chemicals, biocides, hydrocarbons, alcohols, refrigerants, phase change materials, organic fluids and combinations thereof.

15. The method as set forth in claim 1, further including a step of storing thermal energy from said charged working fluid in said geologic formation.

16. The method as set forth in claim 1, further including a step of supplementing said working fluid with energy charged working fluid from adjacent wells in said geologic formation.

17. The method as set forth in claim 16, wherein supplementing includes rerouting working fluid from adjacent wells to a well and a power generation device under user demand.

18. The method as set forth in claim 1, wherein the circulation of said working fluid is effected by an induced thermosiphon.

19. The method as set forth in claim 18, wherein hydraulic pressure loss in operation is less than 1.5 times a quantity of a thermosiphon pressure.

20. The method as set forth in claim 18, wherein hydraulic pressure loss in operation is less than 1.0 times a quantity of a thermosiphon pressure.

21. The method as set forth in claim 1, further including a step of amalgamating intermittent renewable energy generating methods with the method of claim 1.

22. The method as set forth in claim 21, wherein said intermittent renewable energy generating methods include wind, solar and electrochemical methods.

23. The method of claim 1, wherein a capacity factor based on an averaged oscillated thermal output divided by said characteristic predetermined potential thermal output capacity of said geologic formation is greater than eighty percent.

24. A method for providing on demand power to an end user with a well system having an inlet well, an outlet well in a thermally productive geologic formation, comprising: forming a closed loop with a power generation device operatively connecting said inlet well and said outlet well; circulating a working fluid in said closed loop with a predetermined residency time to thermally load the circulating working fluid through conduction from said geologic formation; modulating a flow rate of the thermally loaded working fluid within said closed loop for power generation based on user demand; interconnecting said inlet well and said outlet well with a plurality of interconnecting sections in a predetermined pattern within said formation; and selectively modulating circulation of said working fluid within predetermined sections of said plurality of interconnecting sections of said well system to oscillate a thermal output from the thermally charged working fluid about a characteristic predetermined potential thermal output capacity of said formation, where an averaged oscillated thermal output equals or is less than said characteristic predetermined potential thermal output capacity of said formation and where said characteristic predetermined potential thermal output capacity is determined based on a baseload thermal output of said working fluid flowing at a constant flow rate.

25. The method as set forth in claim 24, further including interconnecting said inlet well and said outlet well with an interconnecting section in fluid communication, at least part of said interconnecting section being disposed for conduction in said thermally productive geologic formation.

26. The method as set forth in claim 25, wherein said interconnecting section is at least one of cased, uncased, lined, chemically treated, chemically sealed, thermally sealed, includes single pipe, coaxial pipe and combinations thereof in a continuous or discontinuous configuration.

27. The method as set forth in claim 24, wherein said geologic formation is selected from a group comprising: a geothermal formation, a low permeability formation, a sedimentary formation, a volcanic formation, a high temperature formation, a variable permeability formation and combinations thereof.

28. The method as set forth in claim 24, wherein said well system includes pre-existing wells.

29. The method as set forth in claim 28, wherein said geologic formation includes at least one of hot dry impermeable rock, naturally fissured, fractured or cracked rock, synthetically fissured, fractured or cracked rock and combinations thereof.

30. The method as set forth in claim 24, wherein said inlet well and said outlet well are co-located.

31. The method as set forth in claim 24, wherein said interconnecting sections are arranged at least one of: symmetrically relative to adjacent interconnecting sections; asymmetrically relative to adjacent interconnecting sections; in interdigital relation to adjacent interconnecting sections; in coplanar relation to adjacent interconnecting sections; in parallel planar relation to adjacent interconnecting sections; in isolated or grouped networks; and combinations thereof.

32. The method as set forth in claim 24, further including a step of providing at least one of a plurality of closed loops with the outlet wells of adjacent loops selectively connected to the inlet wells of additional wells, the inlet wells of adjacent wells commonly connected, the outlet wells of adjacent wells commonly connected and combinations thereof.

33. The method as set forth in claim 32, further including a step selectively modulating circulation of said working fluid within predetermined loops of said plurality of closed loops of said well system to oscillate thermal output from thermally charged working fluid about the characteristic predetermined potential thermal output capacity, where the averaged oscillated thermal output substantially equates with said predetermined potential thermal output capacity.

34. The method as set forth in claim 32, wherein the selective connection comprises valved connection with temperature monitoring.

35. The method as set forth in claim 32, wherein the selective connection comprises a daisy chain connection.

36. The method as set forth in claim 35, wherein said daisy chain connection is at least one of continuous, intermittent and combinations thereof.

37. The method as set forth in claim 24, further including a step of amalgamating said method with intermittent renewable energy generating methods.

38. The method as set forth in claim 37, wherein said intermittent renewable energy generating methods include wind, solar and electrochemical methods.

39. The method of claim 24, wherein a capacity factor based on an averaged oscillated thermal output divided by said characteristic predetermined potential thermal output capacity of said formation is greater than eighty percent.

40. A method for providing on demand power to an end user, comprising: providing a well arrangement comprising an inlet well, an outlet well and an interconnecting section between said inlet well and said outlet well and being disposed within a geologic formation having a characteristic predetermined potential thermal output capacity, said geologic formation having a temperature of at least 90° C.; connecting said outlet well to a power generation device to recover energy from the well arrangement in a closed loop between the inlet and outlet wells and the power generation device; and circulating a working fluid within said closed loop at varying flow rates to oscillate thermal output about the characteristic predetermined potential thermal output capacity, to produce on demand power where an average thermal output equals or is less than the predetermined potential thermal output capacity, and where said characteristic predetermined potential thermal output capacity is determined based on a baseload thermal output of said working fluid flowing at a constant flow rate.

41. The method of claim 40, wherein a capacity factor based on an averaged oscillated thermal output divided by said characteristic predetermined potential thermal output capacity of said geologic formation is greater than eighty percent.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) FIG. 1 is a schematic illustration of an energy recovery arrangement disposed in a thermal bearing geologic formation;

(2) FIGS. 2A through 2D are schematic illustrations of alternative interconnecting sections or multilateral sections for use in the recovery arrangement;

(3) FIG. 3 is an alternative for the recovery arrangement;

(4) FIG. 4 is a graphical representation of a series of operating scenarios depicting temperature (thermal output) as a function of time for each scenario;

(5) FIG. 5 is a graph, similar to that in FIG. 4, with the data presented over several days;

(6) FIG. 6 is a schematic illustration of the thermal output over 30 years of specific scenarios referenced in FIGS. 4 and 5;

(7) FIG. 7 is a schematic illustration of a dispatchable geothermal system integrated with other non-dispatchable renewables;

(8) FIG. 8 is a schematic illustration of multiple dispatchable geothermal loops in a network;

(9) FIG. 9 is a flow diagram illustrating the process to plan, control, and optimize the integration of non-dispatchable renewables with a dispatchable geothermal system;

(10) FIG. 10 is a schematic illustration of the combined power output capacity of a network of power generators;

(11) FIG. 11 is a schematic illustration to mitigate electrical grid saturation with intermittent sources of power; and

(12) FIG. 12 is a schematic illustration of an alternate embodiment of the present invention.

(13) Similar numerals used in the Figures denote similar elements.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS

(14) Referring now to the drawings, FIG. 1 illustrates an example of the overall arrangement used to practice embodiments of the methods to be delineated herein. Numeral 10 globally references the overall arrangement. A geologic formation 12 having thermal energy having a temperature of at least 90° C. and which may be and typically above 150° C., or even 600° C. or greater, includes a subterranean loop arrangement having an inlet well 14 and an outlet well 16, which may be co-located, interconnected with at least one interconnecting section 18. In the example, several sections 18 are depicted. The thermal gradient will depend on the formation characteristics.

(15) At the surface 20, inlet 14 and outlet 16 are connected to a power generation device 22. Device 22 completes the loop arrangement as a closed loop which will be referenced for simplicity as L. As will be evident, the sections 18 are disposed within the geologic formation for the purpose of recovering thermal energy from the surrounding formation 12. For clarity, the closed loop, L, and particularly, sections 18 may include fissures, fractures, cracks within which fluid may be transported, however, this will not detract from the point of the closed loop concept; despite the fact that there may be localized multidirectional flow anomalies, the flow pattern remains closed in the inlet, interconnect, outlet, power generation device 22 combination of elements.

(16) The geologic formation may be any formation that provides a temperature as noted above. In this regard, examples include a geothermal formation, a low permeability formation, hot dry rock, a sedimentary formation, a volcanic formation, a high temperature formation, a variable permeability formation and combinations thereof. These are examples only; any number of others are within the purview of the invention.

(17) The formation, depending on its nature will have a predetermined potential thermal output capacity which can be analyzed in advance by suitable techniques known to those skilled in the art. Each formation will, of course, have a different output capacity.

(18) In consideration of this, each loop, L, will have a predetermined potential thermal output capacity which is reflective of its design parameters, such as number of sections 18, geometric arrangement thereof, depth, length, formation temperature, formation rock properties, inter alia. All of these parameters will be apparent to those skilled.

(19) For recovery, a working fluid is circulated through the loop, L, and exits the outlet well 16 flows through power generation device 22 which converts thermal and/or kinetic energy into electricity for use by an end user globally referenced with numeral 24 and/or is redistributed at 26 for alternate uses to be discussed herein after. Once circulated as indicated, the working fluid is reintroduced to the inlet 14.

(20) The working fluid is thermally “charged” or loaded by circulating the working fluid through the closed-loop, L, at a relatively low flow rate during the charging period. The residence time of the working fluid within the subsurface flow path is increased, and hence the fluid is heated up to a high temperature via conductive heat transfer with the surrounding formation 12.

(21) The system is “discharged” by increasing the flow rate significantly and flushing out the volume of heated working fluid within the hot subsurface portion of the closed circuit, L.

(22) The working fluid may comprise water, super critical carbon dioxide, etc., and include a drag reducing additive such as a surfactant, a polymeric compound, a suspension, a biological additive, a stabilizing agent, anti-scaling agents, anti-corrosion agents, friction reducers, anti-freezing chemicals, biocides, hydrocarbons, alcohols, organic fluids and combinations thereof. Other suitable examples will be appreciated by those skilled. It is contemplated that the working fluid may be compositionally modified dynamically where changing subsurface thermal characteristics dictate.

(23) Referring now to FIGS. 2A, 2B, 2C and 2D, shown are schematic illustrations of the possible dispositions and combinations of the interconnecting sections 18. The illustration generally shows that the adjacent interconnecting sections may be symmetrical, asymmetrically relative to adjacent interconnecting sections, in interdigital relation to adjacent interconnecting sections, in coplanar relation to adjacent interconnecting sections, in parallel planar relation to adjacent interconnecting sections, in isolated or grouped networks and combinations thereof. Specific geometric disposition will vary on the temperature gradient characteristics. The Figures are exemplary only; suitable variations will be appreciated by the designer.

(24) FIG. 3 illustrates an example where the loop, L, includes a plurality of interconnecting sections 18 with the output 16 of one section 18 serves as the input 14 of an adjacent section 18 with common collection at power generation device 22. In this manner the loop, L, is subdivided into a daisy chain configuration for operation of the method.

(25) The potential thermal output capacity is the maximum sustainable thermal energy output of the system. Thermal output may be varied temporarily with the methodology disclosed herein, but the long-term average output (i.e. averaged over months or years) cannot exceed the potential thermal output capacity.

(26) The overall geothermal efficiency of a system is equal to the average thermal output divided by the potential thermal output capacity, what is typically referred to as geothermal “capacity factor”. It is advantageous to have a high capacity factor, or high utilization of the available potential thermal output capacity. Conventionally this is achieved by constant thermal output at or near the potential thermal output capacity. Many geothermal systems operate at >90% capacity factor in this manner, sometimes referred to as “baseload” operations. The disclosed methodology enables a high geothermal capacity factor while also providing flexible on-demand energy output rather than a constant output.

(27) FIG. 4 illustrates an example based on transient thermodynamic modelling of a closed-loop multilateral system described in Applicant's co-pending Application No. PCT/CA2019000076, among others. The inputs for the thermodynamic model are tabulated below.

FIG. 4 Example Data

(28) TABLE-US-00001 Vertical In Vertical Out Laterals Total Length 4810 4810 5648 Casing ID (mm) 215.9 215.9 215.9 Casing OD (mm) 244.5 244.5 NA Cement OD (mm) 298.5 298.5 NA Rock Thermal Conductivity 3.2 3.2 3.2 (W/m. K) Roughness (mm) 0.05 0.05 0.15 Elevation In 0 −4415 −4415 Elevation Out −4415 0 −4415 Number of lateral legs 12 Surface Temperature (° C.) 10 Temperature Gradient (° C.) per km 34.3 Bottom Hole Temperature (° C.) 161.3 Rock Density (kg/m3) 2663 Rock Specific Heat (J/kgK) 1112

(29) The figure shows three operating scenarios for the same geothermal loop: operating in a baseload manner with a constant flow rate (Base Case), in which case the thermal output equals the potential thermal output capacity; operating with a charging cycle for 16 hours at 33 kg/s and then discharging for 8 hours at 130 kg/s; and operating with a charging cycle for 12 hours at 30 kg/s and then discharging for 12 hours at 100 kg/s.

(30) Typically, the charging cycle would be done when the energy price is low or there is an excess of variable renewable supply. This allows the interconnecting sections 18, referenced herein previously to recover the thermal energy from the formation.

(31) FIG. 5 illustrates focused details over the timeframe of 3 days. The average flow rate over the combined charge/discharge periods is approximately equal to the optimum fixed flow rate if the system was operated in a baseload manner. In this example, the same subsurface well arrangement as noted in the earlier Figures, if it were operated in a baseload manner, would equal the potential thermal output capacity at all times when the flow rate is equal to 60 L/s. In the vernacular, the system would operate at the full subsurface geothermal capacity. This is a critical differentiator from some prior art (Ormat at Puna) where the average geothermal output over combined “charging” and “discharging” cycles is significantly below long-term capacity.

(32) The charging cycle establishes a strong thermosiphon, driven by the density difference of the cold fluid in the inlet well 14 compared to the hot fluid in the outlet well 16. During the charging cycle, the thermosiphon pressure drive is higher than required to maintain the desired flow rate. Flow rate is therefore controlled by choking flow downstream of the outlet well 16, using a flow-control valve or other apparatus (not shown) to apply a pressure-drop. The flow-control valve is automated and may be controlled with software that uses a thermodynamic model to calculate the required position of the valve. The control valve also helps manage the pressure in the subsurface loop, to keep it within desirable bounds based on the density of the working fluid and pump discharge pressure.

(33) When discharging, flow rate can be immediately increased by releasing the choke (opening the control valve). This near-instantaneous increase in flow rate enables a fast-ramping capability. Flow rate can be increased to until the hydraulic pressure losses through the closed circuit loop equal the thermosiphon pressure drive.

(34) Flow can be increased beyond this level using a pump, which would require a parasitic power load. However, as long as the majority of the pressure drive is generated by the thermosiphon effect, the parasitic load is practically acceptable.

(35) Using these methodologies, flow rate can be controlled to match power output to the end-user demand, through both the charging and discharging cycles and residency time of the working fluid in the loop.

(36) In the prior art traditional open geothermal systems or flow in porous media, the pumping pressure required to reach the high flow rates while discharging cause an unacceptably high parasitic pump load and drastically reduce or eliminate any gains in net power output. It has been found that the practical limit is achieved when the ratio of the pressure losses in the circuit to the thermosiphon pressure drive is approximately 1.5. The system must be designed to have a hydraulic pressure loss less than 1.5 times the thermosiphon pressure drive. Ideally, pressure losses are less than 1 times the thermosiphon drive and the entire flow is driven by the thermosiphon. Accordingly, there is no parasitic pump load.

(37) Energy is stored within the working fluid itself. During the charging cycle, sufficient residence time is required to heat the working fluid enough to accommodate the discharge cycle. For example, if the discharge cycle is typically 8 hours long, the fluid circuit transit time must be at least 8 hours (averaged over both discharge and charge cycles).

(38) During the charging cycle, energy can also be stored temporarily in rock adjacent to the subsurface flow path and outlet well 16. At low flow rates, heat is transferred conductively from hotter rock in the formation 12 into the working fluid and as the fluid progresses through the system, it encounters cooler rock (typically shallower, for example in the outlet well 16), where energy is transferred from the fluid to the cooler rock and stored temporarily. During the discharging cycle, the average fluid temperature drops, and the stored heat is transferred back into the working fluid.

(39) A closed loop avoids the operational problems with traditional geothermal systems, which are exacerbated when varying the flow drastically as discussed herein. For example, common operational issues are caused by brine, solids, scaling, plugging, and dissolved gases.

(40) The dispatchability disclosed herein integrates well with cryogenic air storage (CES), hydrogen production, or other systems that use stored electrical energy. An example of the process flow is shown below. The CES charging cycle can use cheap excess power from the grid or co-located renewables (for example, solar during the peak daytime hours). The CES can also use produced geothermal power to charge but is not necessary. In one embodiment, the geothermal system would generate a fixed amount electricity throughout the charge and discharge cycle. The increase in thermal energy produced during the discharge cycle is directed to heat the air stream from the CES process, prior to expansion in a turbine.

(41) There are several advantages when using CES with dispatchable geothermal:

(42) The heat engine (which converts thermal energy to electricity) is only sized for the charge cycle, not the peak output of the discharge cycle, dramatically reducing equipment and capital costs.

(43) Minor additional facilities are required to supply heat to the CES facility.

(44) CES is discharging only over several peak hours in the day. The dispatchable geothermal system discharging cycle can match the CES discharging cycle.

(45) FIG. 6 illustrates the thermal output over 30 years of the “Base Case” and “8 Hour Dispatchable Case” referred to in previous Figures. The base case is operated in baseload manner and equal to the available thermal output capacity, while the “8 Hour Dispatchable Case” obtains an effective capacity factor of ˜97% despite operated in a dispatchable output and thus substantially equates with the predetermined potential thermal output capacity of the formation.

(46) This illustrates the primary invention, that the output can be made dispatchable while still retaining a high geothermal capacity factor, typically over 80% and approaching 100%.

(47) The transient thermodynamic simulations described above were tested in a prototype geothermal system in central Alberta, Canada. The system includes a multilateral U-tube heat exchanger 2.4 km deep and 2.5 from surface site to site. The results validate the modelling and demonstrate dispatchability can be predicted and controlled by modulating the flow rate using, in this embodiment, an automated control valve at the outlet well. The empirical results confirm that the system is very fast ramping and when combined with a power generation system such as an Organic Rankine Cycle (ORC), can meet the fast-ramping requirements of integrating with Solar systems.

(48) FIG. 7 demonstrates how the dispatchable geothermal system is used when integrated with other non-dispatchable renewables. The system is turned down during peak hours for Solar and ramped-up as Solar declines. The dispatchable geothermal fills the gap between the energy demand and the non-dispatchable renewables. This is only an example and the output can be modified to match any combination of charging/discharging cycles and the flow rate can be varied to meet any shaped output within physical limits.

(49) Solar electricity is used as an example, however, the same dispatchable mechanisms can be used to integrate into direct heat use applications such as district heating systems or in district cooling systems.

(50) FIG. 8 illustrates multiple dispatchable geothermal loops in a network. The charge/discharge cycles may be scheduled for each loop so that the aggregate output meets the required shaped output profile. The flow rate, thermosiphon, and temperatures are controlled in each loop using an automated control system coupled to a thermodynamic model. The charge discharge cycles may be sequenced or simultaneous depending on the situation and the parameters of each loop.

(51) FIG. 9 is a process flow diagram to plan, control, and optimize the integration of non-dispatchable renewables with dispatchable geothermal. Providing an electrical grid system that has a demand profile over time, existing supply profiles from varying non-dispatchable renewable sources like PV, Wind, Baseload Nuclear, etc, the control technology optimizes a network of dispatchable renewable geothermal generators to fill the gap between the existing non-dispatchable supply profile and the demand profile. The optimization parameter can be to meet net demand, or it can be to maximize the price or revenue (price multiplied by volume) received, or any other combination of factors. These may form only a part of the optimization/scheduling algorithm.

(52) In a network of dispatchable geothermal loops, a network of power generation modules (not shown) would be utilized which convert potential and thermal energy into electricity. These power generation systems may be ORCs, flash plants, pressure drive systems, direct turbines, or any other conversion means. The power generation modules may be arranged in series or parallel or a combination. The control system directs flow from each geothermal loop to the appropriate conversion module(s) based on proximity, scheduling, temperature, and other relevant factors.

(53) FIG. 10 illustrates the combined power output capacity of a network of power generators which is necessarily higher than the potential thermal output capacity of the geothermal loop network. The power generation capacity is designed to meet the peak output of the geothermal network when dispatching, which may be set to meet the peak demand from the end-user. This figure illustrates that while the subsurface system has a high geothermal capacity factor, over 80% and typically over 90%, (where the denominator is the potential thermal output capacity), the surface power conversion modules have a relatively lower capacity factor to enable dispatching.

(54) FIG. 11 illustrates an embodiment of the invention designed to mitigate electrical grid saturation with intermittent sources of power. In the example, a solar recovery arrangement 30 is operatively connected to a loop, L, (loop arrangement or solution) and more specifically to the array 30 at 32. The power generation device 22 is in electrical communication with the grid (not shown) with a specific capacity. This is generally denoted by reference numeral 34.

(55) For the following example, loop arrangement or loop solution is intended to embrace the arrangement discussed herein previously, namely the wells, 14, 16 and interconnection 18 in a thermal bearing geologic formation which may include the power generation device 22.

(56) Solar has a leading place in today's shift to newer cleaner forms of power. Success can, however, bring its own complications. Many electrical grids are now saturated with wind and solar, to the point that it is getting difficult to absorb more intermittent sources of power. Scalable green dispatchable power is required in this scenario. The technology herein can complement new or even existing solar plants.

(57) A typical 10 MW loop, L, unit combines a 5 MW subsurface baseload solution with an ORC and surface facilities scaled to 10 MW. This is to facilitate the inherent dispatchability of the energy produced by the loop, L. This may then be further scaled by the simple addition of more loop arrangements, L. By way of example, a 200 MW loop, L, arrangement has the following operational data.

Example—Grid Saturation Mitigation

(58) TABLE-US-00002 Peak Capacity Average Utilization Load (MW) (MW) Factor (%) LOOP ARRANGEMENT Solar Capacity 200 40 20% Loop Capacity 200 100 50% Transmission Capacity 200 140 70% SOLAR ONLY Solar Capacity 700 140 20% Loop Capacity 0 0 N/A Transmission Capacity 700 140 20% SOLAR + BATTERY Solar Capacity 700 140 20% Battery Capacity (8 h) 200 N/A N/A Transmission Capacity 200 140 70%
Solar Only Solution

(59) For a 200 MW solar farm, because of its intermittent nature, would produce on average only 40 MW. In the event that it is desired to increase the average power production 3.5 times or an additional 100 MW on average, one would have to add an additional 500 MW solar farm and an additional 500 MW in transmission capacity for the simple reason that the solar load factor is going to range between 10% and 25%. Unfortunately, not only does this involve increasing the surface footprint 3.5 times, it also requires upgrading the transmission network 3.5 times (or more undesirably, building new transmission lines to a new solar farm). This is further worsened since most of the increased capacity would be produced at times of the day where considerably below average prices would be achievable.

(60) The Loop Solution

(61) In contrast, one could achieve the same results by incorporating a 200 MW loop solution directly under the existing surface footprint of the current or planned solar farm. Advantageously, no new land acquisition would be required. Furthermore, because the loop arrangement would use its inherent dispatchability to produce power around the 20% load factor of the solar farm, there will be no need for any additional transmission capacity—saving both time and money. Finally, while the loop would not have the transmission capacity to produce much during the period of peak solar production around midday, midday production (which is often of little value) could be shifted to attractive monetization because of the pricing premium to be achieved for dispatchable, rather than intermittent or baseload power.

(62) Solar+Battery Solution

(63) Of course, solar could mimic the loop solution by the addition of enough batteries, but at considerable cost. Instead of just adding a 200 MW loop solution, the solar developer would need to add 500 MW of solar capacity, requiring a massively expanded surface footprint and 200 MW of 8-hour battery storage—resulting in inevitable increased costs and delay.

(64) As a variation to the example, FIG. 11 depicts an arrangement using a windmill 36 as the prime mover.

(65) Referring now to FIG. 12, shown is a further variation to the example. Numeral 40 represents a geographic area on which power distribution centres 42 are arranged to provide electrical delivery via 44 to the power transmission grid (not shown). As is known, the grid has an output capacity. The centres 42 contribute to a power production system over the geographic area 40 with a designed maximum power production quantity and a second effective or “real” power production quantity on the grid.

(66) Clearly, over an expanse of area 40 between centres 42, there are occasionally “brownouts” or other delivery anomalies that occur for a variety of reasons known to those skilled such as is spikes of heavy user demand or redistribution between centres 42.

(67) In order to alleviate inconsistent delivery issues, loop arrangements, L, may be integrated on the circuit of centres 42, such as between adjacent electrically communicating centres 42. As with the previous examples and specification herein, the closed loop configuration can be provided within the underlying geologic formation to produce a predetermined energy output from available potential thermal capacity attributed to the formation.

(68) The working fluid can then be circulated as has been discussed and selectively thermally discharged through said power production arrangement 22 to maintain power production to the capacity throughout said power transmission grid. This accordingly mitigates the anomalies or irregularities noted above.

(69) Depending on the geographic area and other factors, a main distribution hub 46 comprising a plurality of loop arrangements, L, could augment or replace some or all of centres 42 and individually positioned loops, L.