Patent Grant
11624355
Embodiments of this disclosure relate to generating geothermal power, and more particularly, to a modular heat exchange assembly for use as part of systems and methods for generating and controlling generation of geothermal power in an organic Rankine cycle (ORC) operation that can be operated in the vicinity of a hydrocarbon production operation to thereby supply electrical power to one or more of in-field operational equipment, a grid power structure, and an energy storage device.
Organic Rankine cycle (ORC) operations have been used for generation of power in applications such as for hydrocarbon production at pumping stations and/or in the vicinity of wellhead operations. Typically, ORC generators utilize a working fluid loop that flows in a loop wherein the working fluid is heated to cause the working fluid in the loop to change phases from a liquid to a vapor. The vaporous working fluid may then flow to a gas expander, causing the gas expander to rotate. The rotation of the gas expander may cause a generator to generate electrical power. The vaporous working fluid may then flow to a condenser or heat sink. The condenser or heat sink may cool the working fluid, causing the working fluid to change phase from the vapor to the liquid. The working fluid may circulate through the loop in such a continuous manner, thus the geothermal generator may generate electrical power.
Heat exchangers within geothermal generators often are not built to withstand high pressures, and/or substantial heat flows. In addition, construction of ORC power systems in the field can be difficult particularly to provide and/or construction such power systems quickly and with sufficient capacity for a desired level of power generation. It further can be difficult to modify and/or change components in the field, particularly at more remote sites.
Accordingly, Applicants have recognized a need for systems and methods for generation of power in an organic Rankine cycle (ORC) operation that includes components and/or systems to facilitate ease of construction and/or customizable power generation systems for supplying electrical power to one or more of in-field operational equipment, a grid power structure, and an energy storage device. The present disclosure is directed to embodiments of such systems and methods.
The present disclosure is generally directed to systems and methods for generating and controlling generation of electrical power in an organic Rankine cycle (ORC) operation at a remote site, such as in the vicinity of a wellhead during hydrocarbon production to thereby supply electrical power to one or more of in-field operational equipment, a grid power structure, and an energy storage device. In embodiments, the present disclosure provides a mobile heat generation unit that is constructed with a series of components to provide a transportable module that can be transported and located at a site, such as a site for hydrocarbon production.
By way of example and not limitation, in embodiments, the hydrocarbon production site can include a wellhead and/or pumping station that produces a heated wellhead fluid that, as it exits the wellhead, may be under high-pressure and at a high temperature. Other heated liquid or heated gas flows also are produced by various in-field components or equipment, such as fracturing equipment, pumpjacks, compressors, drilling rigs, engines used to drive pumps, gas coolers, or compressors, etc. In an embodiment, such equipment can act as a heat source or supply of a heated fluid, e.g. a high temperature or high pressure gas or liquid, and can be coupled or connected to the modular mobile heat generation unit that can be supplied to the site as a pre-configured unit or module including at least one heat exchanger. The at least one heat exchanger may be a high-pressure heat exchanger configured to withstand the high-pressure of the wellhead fluid from a wellhead and indirectly transfer heat from the flow of the wellhead fluid to the flow of a working fluid. Other types of heat exchangers configured to transfer heat from other heat sources, such as heated exhaust gases from one or more engines at the site driving pumps or compressors, to a working fluid.
In embodiments, the mobile heat generation unit can be formed with at least two heat exchangers that can be selected based upon site requirements and installed with a substantially standardized series of components for transport as a pre-packaged unit or module that is easily transported to the site and installed or “plugged-in” as a component of a geothermal power generation system. The mobile heat generation unit can be transported to a site, such as a drilling, fracking or pumping site, as an effectively pre-packaged, standalone module or unit, and in embodiments, can be configured with a working footprint of approximately the size of a shipping container, e.g. being formed as a cube or substantially rectangular container.
At the site, the mobile heat generation unit will be connected to the one or more heat sources, such as by ducting or piping, to receive a heated fluid flow therefrom; and further will be connected to an ORC unit in a substantially closed loop. As heat is transferred from the incoming heated fluid flow, e.g. the wellhead fluid, exhaust gas, etc., to the working fluid passing through the mobile heat generation unit, the at least one heat exchanger causes heat from the heated fluid flow to be transferred to the working fluid to cause it to be substantially heated from its liquid phase to or close to a vapor phase. The heated working fluid flows through the ORC unit to drive operation of a generator to generate electrical power via rotation of a gas expander of the ORC unit. Such an operation may be defined as or may be an ORC operation or process. The ORC unit further may be an off-the-shelf unit, connectable to the mobile heat generation unit as a stand-alone component or device.
Accordingly, aspects of the present disclosure include a system for generating power in an organic Rankine cycle (ORC) operation, comprising: at least one ORC unit configured to generate electrical power; and at least one mobile heat generation unit in fluid communication with at least one ORC unit and with one or more heat sources supplying a high pressure or high temperature fluid to the heat exchange unit; wherein the mobile heat generation unit is configured as a transportable module and comprises: a frame having an upper portion, a lower portion and a plurality of sides defining a chamber; at least one heat exchanger mounted within the chamber and connected to at least one of the one or more heat sources; a fluid recirculation system at least partially located within the chamber and comprising: a fluid intake conduit coupled to a return line in fluid communication with the at least one ORC unit for receiving a working fluid at a first temperature from the at least one ORC unit; a fluid outlet conduit coupled to a heated fluid supply line in fluid communication with the at least one ORC unit for supplying the working fluid thereto, wherein the working fluid is output to the fluid supply line for supply to the ORC unit at a second temperature that is higher than the first temperature; a pump connected to the fluid intake conduit and configured to pump the working fluid received through the fluid intake conduit through the fluid recirculation system; and a piping array, including a first section of piping extending between the pump and the at least one heat exchanger for supplying the working fluid to the at least one heat exchanger, and a second section of piping extending between the at least one heat exchanger and the fluid outlet conduit; wherein as the working fluid passes along the piping array and through the at least one heat exchanger, heat from the high pressure or high temperature fluid supplied to the at least one heat exchanger from the one or more heat sources is transferred to the working fluid so as to heat the working fluid to a second temperature that is greater than the first temperature; and a controller positioned within the frame, the controller having programming configured to monitor temperature, pressure, or a combination thereof of a working fluid passing along a fluid recirculation loop defined between the mobile heat generation unit and at least one ORC unit, and for regulating flow of the working fluid through the at least one heat exchanger for transfer of heat from the flow of a heated fluid to the working fluid for supply to the at least one ORC unit.
In embodiments, the controller can include programming configured to communicate with one or more sensors configured to monitor temperature and pressure of the working fluid passing through the piping array, and, in response to readings from such sensors, control operation of the pump for regulating flow of the working fluid through the piping array and at least one heat exchanger to substantially maximize the transfer of heat to the working fluid supplied to the at least one ORC unit without substantially vaporizing the working fluid.
In embodiments of the system, the at least one mobile heat generation unit includes at least two heat exchangers configured to extract heat from a compressed gas, a heated exhaust gas, a heated liquid, or combination thereof. In some embodiments, the at least one heat exchanger is mounted within the chamber at an elevated position adjacent the upper portion of the frame.
In some embodiments of the system, the at least one mobile heat generation unit further comprises an air separator along the second section of piping, the air separator configured to remove penetrates from the working fluid.
In embodiments of the system, the at least one mobile heat generation unit has a length of at least approximately fifteen feet. In other embodiments, the at least one mobile heat generation unit has a length of between approximately fifteen feet and approximately forty feet. In some embodiments, the at least one mobile heat generation unit comprises a substantially square or a substantially rectangular shape.
In embodiments of the system, the at least one mobile heat generation unit further comprises a plurality of cover panels positioned along the upper and lower portions and the sides of the frame, so as to substantially enclose the chamber, wherein at least some of the cover panels are configured to be removable from the frame to enable access to the chamber. In some embodiments, one or more of the cover panels along the upper portion are removable to enable removal and replacement of the at least one heat exchanger.
In embodiments of the system, the at least one mobile heat generation unit further comprises an expansion tank located in fluid communication with the second section of piping, wherein the controller includes programming configured to regulate flow of the working fluid into the expansion tank so as to reduce the pressure of the working fluid.
In embodiments of the system, the chamber of the frame comprises a plurality of quadrants including at least a first quadrant defining a control cabinet housing the controller, and a second quadrant defining a working area in which the at least one heat exchanger and the fluid recirculation system are located.
In embodiments, the system further comprises a power and data connection extending between the at least one ORC unit and the at least one mobile heat generation unit; wherein the at least one ORC unit includes a controller; and wherein the controller of the at least one mobile heat generation unit is couple to the controller of the at least one ORC unit.
In embodiments, the at least one mobile heat generation unit further comprises a backup power system configured to supply power to the controller and for operation of one or more dump valves for release of the working fluid from the fluid recirculation system upon loss of power from a direct power supply.
In another aspect, a system for generating geothermal power in an organic Rankin cycle (ORC) operation in the vicinity of a wellhead during hydrocarbon production for supplying electrical power to in-field equipment, a grid power structure, energy storage devices, or combinations thereof, is provided, the system comprising at least one mobile heat generation unit; one or more conduits configured to divert a flow of heated fluid from one or more heat sources to the at least one mobile heat generation unit; wherein the at least one mobile heat generation unit comprises at least one heat exchanger; a pump configured to pump a flow of a working fluid through the at least one heat exchanger; and a first fluid path extending through the at least one heat exchanger and along which the flow of heated fluid is received from at least one of the one or more conduits and is directed through the at least one heat exchanger, and a second fluid path extending through the at least one heat exchanger and along which the flow of a working fluid directed through the at least one heat exchanger for indirectly transferring heat from the flow of heated fluid passing through the at least one heat exchanger along the first fluid path to the flow of the working fluid passing through the at least one heat exchanger along the second fluid path to cause the working fluid be heated so as to change phases from a liquid substantially to a vapor; and an ORC unit including a generator, a gas expander, pump, and a partial flow path for the flow of the working fluid through the gas expander, generator, and pump; wherein a substantially closed fluid recirculation loop for the working fluid is defined between the at least one mobile heat generation unit and the ORC unit when connected to the second fluid path of the mobile heat generation unit; wherein the flow of the heated working fluid into the ORC unit causes the generator thereof to generate electrical power via rotation of the gas expander of the ORC operation, after which the working fluid is cooled so as to cause the working fluid to change phases to the liquid phase, whereupon the liquid state working fluid is recirculated back to the at least one mobile heat generation unit for reheating; and wherein the at least one heat mobile heat generation unit comprises a transportable pre-packaged module.
In embodiments, the at least one mobile heat generation unit includes a substantially rectangular frame defining a working footprint having a length of approximately fifteen feet to approximately twenty feet, and a width of at least about eight feet.
In embodiments, the at least one mobile heat generation unit includes at least two heat exchangers configured to extract heat from a compressed gas, a heated exhaust gas, a heated liquid, or combination thereof.
In another aspect of the present disclosure, a mobile heat generation unit is provided for use in generating heat for an organic Rankine cycle (ORC) power operation for generation of electrical power, and can comprise a transportable package including a frame defining a footprint, the package further comprising at least one heat exchanger; a connecting pipe extending between the at least one heat exchanger and a heat source and configured to direct a flow of a high pressure or high temperature fluid from the heat source to the at least one heat exchanger; a controller having programming configured to monitor temperature, pressure, or a combination thereof of a working fluid passing along a fluid recirculation loop defined between the mobile heat generation unit and at least one ORC unit, and for regulating flow of the working fluid through the at least one heat exchanger for transfer of heat from the flow of the high pressure or high temperature fluid to the working fluid; and a fluid recirculation system comprising a fluid intake conduit coupled in fluid communication with the at least one ORC unit for receiving the working fluid at a first temperature from the at least one ORC unit; a fluid outlet conduit in fluid communication with the at least one ORC unit for supplying the working fluid thereto, wherein the working fluid is supplied to the ORC unit at a second temperature that is higher than the first temperature; a pump connected to the fluid intake conduit, the pump and configured to pump the working fluid received through the fluid intake conduit through the fluid recirculation system; and a piping array, including a first section of piping extending between the pump and the at least one heat exchanger for supplying the working fluid to the at least one heat exchanger, and a second section of piping extending between the at least one heat exchanger and the fluid outlet conduit; and wherein as the working fluid passes along the piping array and through the at least one heat exchanger, heat from the high pressure or high temperature fluid supplied to the at least one heat exchanger from the heat source is transferred to the working fluid so as to heat the working fluid to the second temperature for supply to the at least one ORC unit.
In embodiments of the mobile heat generation unit, the frame comprises upper and lower portions and sides defining a chamber, and a plurality of cover panels positioned along the upper and lower portions and the sides of the frame, so as to substantially enclose the chamber, wherein at least some of the cover panels are configured to be removable from the frame to enable access to the chamber. In some embodiments, the at least one mobile heat generation unit includes a frame defining a working foot print having a length of approximately 15 to approximately 20 feet, and a width of at least about 8 feet.
In embodiments, the mobile heat generation unit further comprises a power and data connection extending between the at least one ORC unit and the at least one mobile heat generation unit for transmission of power and data between the at least one ORC unit and at least one mobile heat generation unit; wherein the at least one ORC unit includes a controller; and wherein the controller of the at least one mobile heat generation unit is coupled to the controller of the at least one ORC unit.
In embodiments, the mobile heat generation unit further comprises a backup power system configured to supply power to the unit controller, a series of sensors, including one or more sensors adopted to monitor ambient environment weather condition of one or more drainage valves for release of the working fluid from the fluid recirculation system upon loss of power from a direct power supply.
According to another aspect, an embodiment of the disclosure is directed to a method for generating geothermal power in an organic Rankine cycle (ORC) operation in the vicinity of a wellhead during hydrocarbon production to thereby supply electrical power to one or more of in-field operational equipment, a grid power structure, and an energy storage device. The method may include, prior to hydrocarbon production, opening, to at least a partially opened position, one or more heat exchanger valves positioned between one or more heat exchangers and a wellhead fluid flow line. The method may include, during hydrocarbon production at a wellhead, determining, based on feedback from one or more temperature sensors, a temperature of an organic working fluid in a working fluid flow line, the temperature of the organic working fluid based on heat transfer from a flow of wellhead fluid from the wellhead to the organic working fluid. The method may include, in response to a determination that the temperature of the organic working fluid is greater than or equal to a vaporous phase change threshold of an organic working fluid, maintaining the at least partially open position of the one or more heat exchanger valves to allow continuous diversion of the flow of the wellhead fluid to one or more heat exchangers to facilitate transfer of heat from the flow of the wellhead fluid to the organic working fluid through the one or more heat exchangers, thereby to change phases of the organic working fluid from a liquid to a vapor within the one or more heat exchangers so as to cause a gas expander, in fluid communication with the one or more heat exchangers, to rotate a generator to generate electrical power from the ORC operation.
In embodiments, the temperature of the organic working fluid may be determined continuously or at one or more time intervals. The time intervals may be one or more of 1 minute, 5 minutes, 10 minutes, 20 minutes, 30 minutes, or 1 hour. The method may include, in response to a determination that the temperature of the organic working fluid at each of a specified number of the one or more time intervals is less than the vaporous phase change threshold, opening a wellhead fluid valve and closing the one or more heat exchanger valves. The specified number of the one or more time intervals may be equivalent to at least 6 determinations of the temperature of the organic working fluid over 1 hour, at least 6 determinations of the temperature of the organic working fluid over 2 hours, or at least 12 determinations of the temperature of the organic working fluid over 3 hours.
In another embodiment, the method may include, in response to the opening of the wellhead fluid valve and closing of the one or more heat exchanger valves, determining a temperature of the flow of the wellhead fluid. The method may further include, in response to a determination that the temperature of the flow of the wellhead fluid is greater than or equal to the vaporous phase change temperature, opening the one or more heat exchanger valves and closing the wellhead fluid valve.
In another embodiment, the method may include determining a flow rate and a pressure of the flow of the wellhead fluid from the wellhead. The method may include determining a flow rate and a pressure of the flow of the wellhead fluid from the one or more heat exchangers. The method may further include adjusting the one or more heat exchanger valves and wellhead fluid valve to meet a production threshold, based on flow rate and pressure of the flow of the wellhead fluid from the wellhead and from the one or more heat exchangers.
In another embodiment, the one or more heat exchangers and the generator in combination may be included in and collectively defined as an ORC unit and wherein the ORC unit comprises a modular single-pass ORC unit. The ORC unit may be configured to connect to and interface with one or more other ORC units based on one or more of power demands and the flow of the wellhead fluid from the wellhead. The one or more of the one or more heat exchangers may be stand-alone units and the generator may be included in and defines an ORC unit.
In an embodiment, the amount of the flow of wellhead fluid diverted may comprise substantially an entire flow of wellhead fluid. The amount of the flow of wellhead fluid diverted may be based on one or more of the temperature, flow rate, or pressure of the flow of wellhead fluid.
In an embodiment, the vaporous phase change threshold may be about 50 degrees Celsius or higher. The one or more of the one or more heat exchangers may include (a) a high-pressure rated shell heat exchanger or (b) a high pressure rated tube heat exchanger.
In another embodiment, the method may include, in response to a determination that the wellhead is producing wellhead fluid, determining whether the one or more heat exchanger valves are open. The method may further include, in response to a determination that the one or more heat exchanger valves are closed, adjustingly opening one or more heat exchanger valves and adjustingly closing the wellhead fluid valve to a selected, at least partially closed position to allow sufficient flow to prevent hydrocarbon production impact.
Another embodiment of the disclosure is directed to a method for generating geothermal power in an organic Rankin cycle operation in the vicinity of a wellhead during hydrocarbon production to thereby supply electrical power to one or more of in-field operational equipment, a grid power structure, and an energy storage device. The method may include connecting one or more high-pressure heat exchangers to a wellhead fluid flow line of one or more wellheads at a well thereby defining a fluid path from the wellhead fluid flow line of one or more wellheads through the one or more high pressure heat exchangers. The method may include connecting one or more ORC units to the one or more high-pressure heat exchangers. In embodiments, the ORC unit may be an off-the-shelf unit, connectable to one or more heat exchangers, while in other embodiments, the ORC unit may be a high-pressure ORC unit and may include the high-pressure heat exchanger apparatus.
The method may include opening one or more heat exchanger valves positioned between the one or more heat exchangers and wellhead fluid flow line of one or more wellheads, to allow continuous diversion of the flow of the one or more wellhead fluids during hydrocarbon production to the one or more high-pressure heat exchangers to facilitate transfer of heat from a flow of the one or more wellheads fluid from the one or more wellheads to a flow of working fluid through the one or more high-pressure heat exchangers, thereby to change phases of the organic working fluid from a liquid to a vapor within the one or more heat exchangers so as to cause a gas expander, in fluid communication with the one or more heat exchangers, to rotate a generator to generate electrical power from the ORC operation. The method may include during hydrocarbon production at one or more of the one or more wellheads, determining, based on feedback from one or more temperature sensors corresponding to the flow of working fluid exiting the one or more high-pressure heat exchangers to a corresponding ORC unit, a temperature of the flow of the working fluid. The method may include, in response to a determination that the temperature is above a vaporous phase change threshold of the working fluid, maintaining at least a partially opened position of the one or more heat exchanger valves.
In another embodiment, an intermediary heat exchanger connects one or more of the high-pressure heat exchangers to the one or more ORC units, the intermediary heat exchanger including an intermediary working fluid including a vaporous phase change threshold greater than that of the vaporous phase change threshold of the working fluid. The one or more high-pressure heat exchangers facilitate transfer of heat from the flow of the one or more wellhead fluids to the intermediary working fluid, and wherein the intermediary heat exchanger facilitates transfer of heat from the intermediate working fluid to the working fluid.
In another embodiment, the one or more ORC units are modular and mobile and the one or more high-pressure heat exchangers are modular and mobile.
In another embodiment, the method of may include, in response to a determination that the temperature is below a vaporous phase change threshold of the working fluid, adjustingly increasing an open position of the one or more heat exchanger valves. The method may further include, in response to an increased open position of the one or more heat exchanger valves and a determination that the temperature is below the vaporous phase change threshold of the working fluid, opening one or more wellhead fluid valves and closing the one or more heat exchanger valves.
In other aspects, a method for generating geothermal power in an organic Rankin cycle operation during hydrocarbon production to supply electrical power to one or more of in-field operational equipment, a grid power structure, and an energy storage device comprises locating one or more mobile heat generation units at a hydrocarbon production site; wherein the one or more mobile heat generation units each comprise a package having at least one heat exchanger, a controller, and a fluid recirculation system including a pump, a fluid inlet conduit through which a flow of a working fluid is received in a substantially liquid phase, a fluid outlet conduit through which the working fluid is supplied in a substantially vapor phase, and an array of piping defining a fluid path extending from the pump through the at least one heat exchanger and to the fluid outlet conduit; connecting the at least one heat exchanger of the one or more mobile heat generation units to a heat source thereby defining a fluid path extending from the heat source through the at least one heat exchanger; connecting one or more ORC units to the at least one heat exchanger; opening one or more valves positioned between the at least one heat exchanger and the heat source connected thereto to enable a flow of heated fluid along the fluid path extending from the heat source through the at least one heat exchanger, and pumping the working fluid along the fluid path extending from the pump through the at least one heat exchanger and to the fluid outlet conduit; wherein the at least one heat exchanger transfers heat from the flow of heated fluid to the working fluid pumped through the at least one heat exchanger, to cause a change in phase of the working fluid from a liquid to a vapor, which is thereafter supplied to the one or more ORC units to drive a generator for generation of electrical power from the ORC operation.
In embodiments, the method may include connecting one or more ORC units to the one or more high-pressure heat exchangers of one or more mobile heat generation units. The method may include opening one or more heat exchanger valves positioned between the one or more heat exchangers and a wellhead fluid flow line of one or more wellheads, to allow continuous diversion of the flow of the one or more wellhead fluids during hydrocarbon production to the one or more high-pressure heat exchangers to facilitate transfer of heat from a flow of the one or more wellheads fluid from the one or more wellheads to a flow of working fluid through the one or more high-pressure heat exchangers, thereby to change phases of the organic working fluid from a liquid to a vapor within the one or more heat exchangers so as to cause a gas expander, in fluid communication with the one or more heat exchangers, to rotate a generator to generate electrical power from the ORC operation.
In embodiments, the method also may include, during hydrocarbon production at one or more of the one or more wellheads, intermittently determining, based on feedback from one or more temperature sensors corresponding to the flow of working fluid exiting the one or more high-pressure heat exchangers to a corresponding ORC unit, a temperature of the flow of the working fluid. The method may include, in response to a determination that the temperature is above a vaporous phase change threshold of the working fluid, maintaining at least a partially opened position of the one or more heat exchanger valves. In some embodiments, the method may further include, in response to a determination that a series of the intermittently determined temperatures of the flow of working fluid each is below a vaporous phase change threshold, opening a wellhead fluid valve positioned at a point on the wellhead fluid flow line to allow wellhead fluid to flow therethrough and closing the one or more heat exchanger valves.
In other embodiments, the method may include, in response to the closing of the one or more heat exchanger valves, determining, based on feedback from one or more temperature sensors corresponding to the flow of wellhead fluid flowing through the wellhead fluid line, a temperature of the flow of the wellhead fluid flow, and, in response to a determination that the temperature is above a vaporous phase change threshold, opening the one or more heat exchanger valves and closing the wellhead fluid valve to an at least partially closed position during hydrocarbon production at one or more of the one or more wellheads
In another embodiment, one or more pressure transducers are positioned along the wellhead fluid line in proximity to each of the one or more wellheads and wherein a flow meter is positioned along the wellhead fluid line at a point downstream corresponding to the flow of wellhead fluid exiting the one or more high-pressure heat exchangers to the wellhead fluid line. The at least partially closed position of the wellhead fluid valve may be determined based on a production threshold and a flow rate based on feedback from the flow meter to thereby maintain the flow of wellhead fluid above or at the production threshold.
In another embodiment, the method may include determining, based on feedback from the one or more pressure transducers, a pressure at each of the one or more heat exchangers; and, in response to the pressure at any of the one or more heat exchangers exceeding a pressure threshold of the corresponding one or more heat exchanger, if the wellhead fluid valve is completely closed, opening the wellhead fluid valve to at least a partially open position and closing the one or more heat exchanger valves.
In another embodiment, the method may include in further response to the pressure at any of the one or more heat exchangers exceeding a pressure threshold of the corresponding one or more heat exchanger, opening a corresponding pressure relief valve positioned on each of the one or more heat exchangers to thereby prevent damage to the corresponding one or more heat exchanger.
In an embodiment, the pressure threshold may be up to about 15,000 pounds per square inch (PSI). The working fluid may include one or more of pentafluoropropane, carbon dioxide, ammonia and water mixtures, tetrafluoroethane, isobutene, propane, pentane, perfluorocarbons, and other hydrocarbons. The wellhead fluid may include hydrocarbons. The wellhead fluid may further include a mixture of the hydrocarbons and one or more of water and other chemical residuals.
Yet another aspect of the disclosure is directed to a method for generating geothermal power in an organic Rankin cycle operation in the vicinity of a wellhead during hydrocarbon production to thereby supply electrical power to one or more of in-field operational equipment, a grid power structure, and an energy storage device. The method may include connecting one or more high-pressure heat exchangers to a heat source. In embodiments, the heat source can include a wellhead fluid flow supply line that provides a flow of wellhead fluid from one or more wellheads at a well, defining a fluid path from the wellhead fluid flow line of one or more wellheads through the one or more high pressure heat exchangers. In other embodiments, the heat source can include high pressure or high temperature liquid or gas flows, such as, for example, exhaust gases from natural gas or other fuel driven engines. In addition, in embodiments, the heat exchangers can be provided as part of a mobile heat generation unit that can comprise a pre-packaged module with one or more heat exchangers connected to a pump of a fluid recirculation system, including an array of piping, which mobile heat generation unit can be transported to the site and installed as a substantially stand-alone module or heat generation assembly. In other embodiments, the heat exchangers can be provided separately.
The method may include connecting an ORC unit to the one or more high-pressure heat exchangers, e.g. the heat exchangers of one or more mobile heat generation units. The method may include opening one or more heat exchanger valves positioned between the one or more heat exchangers and wellhead fluid flow line of one or more wellheads, to allow continuous diversion of the flow of the one or more wellhead fluids during hydrocarbon production to the one or more high-pressure heat exchangers to facilitate transfer of heat from a flow of the one or more wellheads fluid from the one or more wellheads to a flow of working fluid through the one or more high-pressure heat exchangers. The method may include opening, to an at least partially open position, one or more ORC unit valves to allow the flow of working fluid to flow into the ORC unit to thereby generate electrical power from the ORC operation of the ORC unit. The method may include, during hydrocarbon production at one or more of the one or more wellheads, intermittently determining, based on feedback from one or more temperature sensors corresponding to the flow of working fluid exiting the one or more high-pressure heat exchangers to the ORC unit, a temperature of the flow of the working fluid. The method may include determining an efficient working fluid flow for each of the one or more high-pressure heat exchangers based on the temperature of the flow of the working fluid from each of the one or more high-pressure heat exchangers and the open position of each of the one or more ORC unit valves. The method may include adjusting the at least partially open position of the one or more ORC unit valves based on the efficient working fluid flow for each of the one or more high-pressure heat exchangers. In another embodiment, the efficient working fluid flow for each of the one or more high-pressure heat exchangers may be based on electrical power output of the ORC unit.
According to other aspects of the present disclosure, a system for generating geothermal power in the vicinity of a wellhead during hydrocarbon production to thereby supply electrical power to one or more of in-field equipment, a grid power structure, and energy storage devices is provided. In embodiments, the system can comprise a first pipe connected to and in fluid communication with a heat source, such as being coupled to the wellhead that can supply high-pressure wellhead fluid to the system for providing heat to generate power; wherein the first pipe is configured to transport wellhead fluid under high-pressure; a first wellhead fluid valve having a first end and second end, the first end of the first wellhead fluid valve connected to and in fluid communication with the first pipe, the first wellhead fluid valve to control flow of wellhead fluid based on an organic working fluid temperature; a heat exchanger valve connected to and in fluid communication with the first pipe, the heat exchanger valve to control flow of wellhead fluid on an organic working fluid temperature; a high-pressure heat exchanger to accept the flow of wellhead fluid when the heat exchanger valve is open, the high-pressure heat exchanger including a first opening and a second opening connected via a first fluidic path and a third opening and a fourth opening connected via a second fluidic path, the first fluidic path and the second fluidic path to facilitate heat transfer from the flow of wellhead fluid to an organic working fluid, the transfer of heat from the wellhead fluid to the organic working fluid to cause the organic working fluid to change phases from a liquid to a vapor, the flow of wellhead fluid flowing into the first opening of the high-pressure heat exchanger from the heat exchanger valve through the first fluidic path and to the second opening of the high-pressure heat exchanger, and a flow of the organic working fluid flowing into the third opening through the second fluidic path and out of the fourth opening; a first temperature sensor connected to the fourth opening, the first temperature sensor to provide the organic working fluid temperature, the organic working fluid temperature defined by a temperature of organic working fluid flowing through the second fluidic path; a second pipe connected to and in fluid communication with the second end of the first wellhead fluid valve and connected to and in fluid communication with the second opening of the high-pressure heat exchanger; a generator connected to and in fluid communication with the fourth opening of the high-pressure heat exchanger, the organic working fluid flowing from the fourth opening to the generator and causing the generator to generate electrical power via rotation of a vapor expander as defined by an ORC operation; a condenser to facilitate heat transfer from the organic working fluid to a coolant; and a pump connected to the condenser to pump the organic working fluid from the condenser to the third opening of the high-pressure heat exchanger.
In embodiments, the heat source can include the flow of wellhead fluid from one or more wellheads at a well, being directed along a fluid path from the wellhead fluid flow line of one or more wellheads through the first pipe one or more high pressure heat exchangers. In other embodiments, the heat source can include high pressure or high temperature liquid or gas flows, such as, for example, exhaust gases from natural gas or other fuel driven engines. In addition, in embodiments, the heat exchangers can be incorporated into mobile heat generation units, which further can include multiple high pressure heat exchangers. In embodiments, the mobile heat generation units comprise a pre-packaged module with one or more heat exchangers connected to a pump of a fluid recirculation system, including an array of piping, which mobile heat generation unit can be transported to the site and installed as a substantially stand-alone module or heat generation assembly. In other embodiments, the heat exchangers can be provided separately.
Each mobile heat generation unit comprises a substantially pre-constructed or pre-packaged module or unit having a frame defining a chamber in which a series of generally common components can be arranged, and can include one or more high pressure heat exchangers of a selected type and/or capacity, a first fluid path extending in a loop from the heat exchanger valve to the one or more heat exchangers for supplying the heated wellhead fluid, and a second fluid path defined by a fluid recirculation system including a pump, a piping array, and fluid inlet and outlet conduits forming a circulation loop with an ORC unit, and though which a working fluid passes and is heated by transfer of heat from the wellhead fluid in the one or more heat exchangers, and is directed through the ORC unit for generation of power thereby, after which the cooled working fluid is directed back into the at least one mobile heat generation unit.
Still other aspects and advantages of these embodiments and other embodiments, are discussed in detail herein. Moreover, it is to be understood that both the foregoing information and the following detailed description provide merely illustrative examples of various aspects and embodiments, and are intended to provide an overview or framework for understanding the nature and character of the claimed aspects and embodiments. Accordingly, these and other objects, along with advantages and features of the present invention herein disclosed, will become apparent through reference to the following description and the accompanying drawings. Furthermore, it is to be understood that the features of the various embodiments described herein are not mutually exclusive and may exist in various combinations and permutations.
These and other features, aspects, and advantages of the disclosure will become better understood with regard to the following descriptions, claims, and accompanying drawings. It is to be noted, however, that the drawings illustrate only several embodiments of the disclosure and, therefore, are not to be considered limiting of the scope of the disclosure.
So that the manner in which the features and advantages of the embodiments of the systems and methods disclosed herein, as well as others that will become apparent, may be understood in more detail, a more particular description of embodiments of systems and methods briefly summarized above may be had by reference to the following detailed description of embodiments thereof, in which one or more are further illustrated in the appended drawings, which form a part of this specification. It is to be noted, however, that the drawings illustrate only various embodiments of the systems and methods disclosed herein and are therefore not to be considered limiting of the scope of the systems and methods disclosed herein as it may include other effective embodiments as well.
The present disclosure is directed to systems and methods for generating geothermal power in an organic Rankine cycle (ORC) operation in the vicinity of a wellhead during hydrocarbon production to thereby supply electrical power to one or more of in-field equipment or operational equipment, a grid power structure, other equipment, and an energy storage device. Wellhead fluids flowing from a wellhead at a well are typically under high-pressure. In-field equipment at the well is not rated for such high pressures. Prior to further processing or transport, the pressure of the flow of the wellhead fluid may be reduced, e.g., from 15,000 PSI to 200 PSI, from 10,000 PSI to 200 PSI, from 2,000 PSI to 200 PSI, or any other range from 20,000 PSI to 100 PSI, based on the pressure rating of the in-field equipment at the well. As the wellhead fluid flows from the wellhead, the temperature of the flow of the wellhead fluid may be at a high temperature, at least partially due to the high pressure of the flow of the wellhead fluid. As the pressure is reduced, the wellhead fluid temperature may also be reduced, as result of the pressure drop. Typically, the heat of the flow of wellhead fluid from the wellhead is not utilized and may be considered heat waste.
Geothermal power generators typically use a looping pipe or pipeline buried at depths with sufficient temperature to allow a working fluid to change phase from liquid to vapor. As the working fluid changes phase from a liquid to a vaporous state, the vaporous state working fluid may flow up the pipe or pipeline to a gas expander. The vaporous state working fluid may flow through and cause the gas expander to rotate. The rotation of the gas expander may cause a generator to generate electrical power, as will be described below. The vaporous state working fluid may flow through the gas expander to a heat sink, condenser, or other cooling apparatus. The heat sink, condenser, or other cooling apparatus may cool the working fluid thereby causing the working fluid to change phases from a vapor to a liquid. Heat exchangers of typical geothermal generators are not rated for high-pressure operations and usually geothermal generators obtain heat from varying underground depths.
In the present disclosure, a high-pressure heat exchanger may be placed or disposed at the well and/or in the vicinity of one or more wellheads. The high-pressure heat exchanger may be connected to the wellhead and may accept a high temperature or heated flow of wellhead fluid. A working fluid may flow through the heat exchanger. As the wellhead fluid and working fluid flows through the high-pressure heat exchanger, the high-pressure heat exchanger may facilitate transfer of heat from the wellhead fluid to the working fluid. A heat exchanger may include two fluidic paths, one for a heated fluid and another for a cool fluid. The fluidic paths may be in close proximity, allowing heat to transfer from the heated fluid to the cool fluid. The fluidic paths may be loops, coils, densely packed piping, tubes, chambers, some other type of path to allow for fluid to flow therethrough, and/or a combination thereof, as will be understood by those skilled in the art. As fluids flow through the heat exchanger, the cool liquid's temperature may increase, while the heated liquid's temperature may decrease.
Additionally, a geothermal generator unit or ORC unit may be disposed, positioned, or placed at the wellhead. The geothermal generator unit or ORC unit may directly connect to the high-pressure heat exchanger, include the high-pressure heat exchanger, or may connect to the high-pressure heat exchanger via an intermediary heat exchanger. As the hot wellhead fluid heats the working fluid, either via direct connection or through an intermediary heat exchanger, the working fluid may change phases from a liquid to a vapor. In such examples, the working fluid utilized may be chosen based on a low boiling point and/or high condensing point. The vaporous state working fluid may flow through the geothermal generator unit or ORC unit to a generator, e.g., a gas expander and generator. The vaporous state working fluid may then flow to a condenser or heat sink, thereby changing state from the vapor to the liquid. Finally, the liquid may be pumped back to the high-pressure heat exchanger. Such a cycle, process, or operation may be considered a Rankine cycle or ORC.
Such systems may include various components, devices, or apparatuses, such as temperature sensors, pressure sensors or transducers, flow meters, control valves, smart valves, valves actuated via control signal, controllers, a master or supervisory controller, other computing devices, computing systems, user interfaces, in-field equipment, and/or other equipment. The controller may monitor and adjust various aspects of the system to ensure that hydrocarbon production continues at a specified rate, that downtime is limited or negligible, and that electrical power is generated efficiently, optimally, economically, and/or to meet or exceed a preselected electrical power output threshold.
As illustrated in
As illustrated in
Further, when the first heat exchanger valve 208 is opened, a second heat exchanger valve 222 connected to a second pipe 217 may be opened, e.g., partially opened or fully opened. The second heat exchanger valve 222 may allow the flow of wellhead fluid to exit the high-pressure heat exchanger 250. Based on the opening of the first heat exchanger valve 208 and second heat exchanger valve 222, a first wellhead fluid valve 210 may be adjusted. Such adjustment may occur to ensure that the production of the wellhead 202 or the production of wellhead fluid from the wellhead 202 may not be impeded or slowed based on a diversion of the flow of the wellhead fluid to the high-pressure heat exchanger 250. Downstream of the first wellhead fluid valve 210, but prior to where the diverted portion of the flow of wellhead fluid is reintroduced to the primary or bypass wellhead fluid flow, a pressure sensor 212 may be disposed, e.g., the pressure sensor 212 may be disposed along pipe 217. In another example, rather than a pressure sensor 212, a flow meter may be disposed along pipe 217, e.g., a wellhead fluid flow meter and/or a downstream flow meter. The wellhead fluid flow meter may measure the flow rate of a fluid exiting the wellhead 202. A downstream flow meter may measure the flow rate of the wellhead fluid at a point downstream of the first wellhead fluid valve 210. Such a pressure sensor 212 or flow meter may be utilized to determine whether the flow of wellhead fluid is at a pressure or flow that does not impede hydrocarbon production. In an example, where the flow is impeded to a degree that the production of hydrocarbons may be inhibited, the first wellhead fluid valve 210 may be opened further, if the first wellhead fluid valve 210 is not already fully opened. If the first wellhead fluid valve 210 is fully opened, the first heat exchanger valve's 208 and second heat exchanger valve's 222 percent open may be adjusted. Other factors may be taken into account for such determinations, such as the pressure or flow from the high-pressure heat exchanger 250, the pressure or flow at the point of a choke valve located further downstream along the second pipe 217, a pressure rating for downstream equipment, and/or the temperature of the wellhead fluid within the high-pressure heat exchanger 250. Once the flow of wellhead fluid passes through the first wellhead fluid valve 210 and/or the second heat exchanger valve 222, the wellhead fluid may flow to in-field equipment 270 for further processing or transport.
Each of the valves described herein, e.g., first heat exchanger valve 208, second heat exchanger valve 222, first wellhead fluid valve 210, and other valves illustrated in the
As illustrated in
In another embodiment, in addition to the first heat exchanger valve 208 and second heat exchanger valve 222, the well 200 may include a first ORC unit valve 295 and a second ORC unit valve 296. Such ORC unit valves 295, 296 may be utilized to control flow of working fluid flowing into the ORC unit 203. Further the ORC unit valves 295, 296 may be utilized when more than one high-pressure heat exchanger 250 corresponding to one or more wellheads are connected to the ORC unit 203. The ORC unit valves 295, 296 may be utilized to optimize or to enable the ORC unit 203 to meet a preselected electrical power output threshold via the flow of working fluid from one or more high-pressure heat exchangers into the ORC unit 203, as will be understood by a person skilled in the art. The flow of working fluid may be adjusted to ensure that the ORC unit 203 produces an amount of electrical power greater than or equal to a preselected electrical power output threshold, based on various factors or operating conditions (e.g., temperature of wellhead fluid flow, temperature of working fluid flow, electrical output 236 of the ORC unit 203, electrical rating of the ORC unit 203, flow and/or pressure of the wellhead fluid, and/or flow and/or pressure of the working fluid). In some examples, the ORC unit valves 295, 296 may initially be fully open or at least partially open and as various factors or operating conditions are determined, then the ORC unit valves 295, 296 for one or more heat exchangers may be adjusted to enable the ORC unit 203 to meet a preselected electrical power output threshold, as will be understood by a person skilled in the art. The preselected electrical power output threshold may be set by a user or may be a predefined value generated by a controller (e.g., controller 272) based on various factors. The various factors may include an ORC unit electrical power rating or output rating or maximum potential temperature of the wellhead fluid and/or working fluid.
As shown, several pairs of sensors may be located adjacent to one another. In other examples, those positions, for example, the pressure sensor's 204 and the temperature sensor's 206 location, may be reversed. In yet another example, each one of the sensors may provide measurements for multiple aspects of the wellhead fluid, e.g., one sensor to provide a combination of flow, pressure, temperature, composition (e.g., amount of components in the wellhead fluid, such as water, hydrocarbons, other chemicals, proppant, etc.), density, or other aspect of the wellhead fluid or working fluid. Each sensor described above may be integrated in or within the pipes or conduits of each device or component, clamped on or over pipes or conduits, and or disposed in other ways, as will be understood by those skilled in the art. Further, the determinations, adjustments, and/or other operations described above may occur or may be performed by or in a controller.
As noted, a high-pressure heat exchanger 250 may be disposed, placed, or installed at a well. The high-pressure heat exchanger 250 may be disposed nearby or at a distance from the wellhead 202. The high-pressure heat exchanger 250 may be a modular and/or mobile apparatus. In such examples, the high-pressure heat exchanger 250 may be brought or moved to a well or site (e.g., via a vehicle, such as a truck), placed at the well or site during hydrocarbon production, and then moved to another well or site at the end of hydrocarbon production. The high-pressure heat exchanger 250 may be disposed on a skid, a trailer, a flatbed truck, inside a geothermal generator unit, or inside an ORC unit 203. Once brought to a well or site, the high-pressure heat exchanger 250 may be secured to the surface at the well. The high-pressure heat exchanger 250 may be configured to withstand pressures in excess of about 5,000 PSI, about 10,000 PSI, about 15,000 PSI, and/or greater. In an example, the high-pressure heat exchanger 250 may be a high-pressure shell and tube heat exchanger, a spiral plate or coil heat exchanger, a heliflow heat exchanger, or other heat exchanger configured to withstand high pressures. In another example, portions of the high-pressure heat exchanger 250 may be configured to withstand high-pressures. For example, if a shell and tube heat exchanger is utilized, the shell and/or tubes may be configured to withstand high-pressures.
In another embodiment, at least one fluidic path of the high-pressure heat exchanger 250 may be coated or otherwise configured to reduce or prevent corrosion. In such examples, a wellhead fluid may be corrosive. To prevent damage to the high-pressure heat exchanger 250 over a period of time, the fluid path for the wellhead fluid may be configured to withstand such corrosion by including a permanent, semi-permanent, or temporary anti-corrosive coating, an injection point for anti-corrosive chemical additive injections, and/or some combination thereof. Further, at least one fluid path of the high-pressure heat exchanger 250 may be comprised of an anti-corrosive material, e.g., anti-corrosive metals or polymers. As noted, the wellhead fluid may flow into the high-pressure heat exchanger 250 at a high pressure. As the high-pressure heat exchanger 250 may operate at high pressure, the high-pressure heat exchange may include pressure relief valves to prevent failures if pressure within the high-pressure heat exchanger 250 were to exceed the pressure rating of the high-pressure heat exchanger 250. Over time, wellhead fluid flowing through the high-pressure heat exchanger 250 may cause a buildup of deposits or scaling. To prevent scaling and/or other related issues, the high-pressure heat exchanger 250 may be injected with scaling inhibitors or other chemicals or may include vibration or radio frequency induction devices.
Once the high-pressure heat exchanger 250 facilitates heat transfer from the wellhead fluid to the working fluid, the working fluid may partially, substantially, or completely change phases from a liquid to a vapor, vaporous state, gas, or gaseous state. The vapor or gas may flow to the ORC unit 203 causing an expander to rotate. The rotation may cause a generator to generate electricity, as will be further described and as will be understood by those skilled in the art. The generated electricity may be provided as an electrical output 236. The electricity generated may be provided to in-field equipment, energy storage devices, equipment at other wells, or to a grid power structure. The working fluid in the high-pressure heat exchanger may be a working fluid to carry heat. Further, the working fluid of the high-pressure heat exchanger 250 may or may not exhibit a vaporous phase change. The working fluid may carry heat to another heat exchanger 205 of the ORC unit 203. As such, heat may be transferred from the wellhead fluid to the working fluid of the high-pressure heat exchanger 250 and heat may be transferred from the working fluid of the high-pressure heat exchanger 250 to the working fluid of the ORC unit 203.
In an example, the working fluid may be a fluid with a low boiling point and/or high condensation point. In other words, a working fluid may boil at lower than typical temperatures, while condensing at higher than typical temperatures. The working fluid may be an organic working fluid. The working fluid may be one or more of pentafluoropropane, carbon dioxide, ammonia and water mixtures, tetrafluoroethane, isobutene, propane, pentane, perfluorocarbons, other hydrocarbons, a zeotropic mixture of pentafluoropentane and cyclopentane, other zeotropic mixtures, and/or other fluids or fluid mixtures. The working fluid's boiling point and condensation point may be different depending on the pressure within the ORC loop 221, e.g., the higher the pressure, the lower the boiling point.
An ORC unit 203 may include a heat exchanger 205 or heater. Connections to the heat exchanger 205 or heater may pass through the exterior of the ORC unit 203. Thus, as an ORC unit 203 is brought or shipped to a well or other location, a user, technician, service person, or other person may connect pipes or hoses from a working fluid heat source (e.g., the high-pressure heat exchanger 250) to the connections on the ORC unit 203, allowing a heat source to facilitate phase change of a second working fluid in the ORC unit 203. In such examples, the working fluid flowing through ORC loop 221 may include water or other organic fluid exhibiting a higher vaporous phase change threshold than the working fluid of the ORC unit 203, to ensure proper heat transfer in heat exchanger 205. Further, the heat exchanger 205 may not be a high-pressure heat exchanger. In such examples, the high-pressure heat exchanger 250 allows for utilization of waste heat from high-pressure wellhead fluids. In another embodiment and as will be described, a high-pressure heat exchanger 250 may be included in the ORC unit 203.
In yet another embodiment, the high-pressure heat exchanger 250 may be considered an intermediary heat exchanger or another intermediary heat exchanger (e.g., intermediary heat exchanger 219) may be disposed between the high-pressure heat exchanger 250 and the ORC unit 203 (as illustrated in
The ORC unit 203 may further include pressure sensors 228, 238, 246 and temperature sensors 230, 240 to determine whether sufficient, efficient, and/or optimal heat transfer is occurring in the heat exchanger 205. A sensor or meter may further monitor electrical power produced via the expander 232 and generator 234. Further, the ORC unit 203 may include a condenser or heat sink 211 to transfer heat from the second working fluid or working fluid of the ORC unit 203. In other words, the condenser or heat sink 211 may cool the second working fluid or working fluid of the ORC unit 203 causing the second working fluid or working fluid of the ORC unit 203 to condense or change phases from vapor to liquid. The ORC unit 203 may also include a working fluid reservoir 298 to store an amount of working fluid, e.g., in a liquid state, to ensure continuous operation of the ORC unit 203. The liquid state working fluid, whether from the working fluid reservoir 298 or directly form the condenser/heat sink 211, may be pumped, via pump 244, back to the heat exchanger 205. Further, the pressure prior to and after pumping, e.g., as measured by the pressure sensors 238, 246, may be monitored to ensure that the working fluid remains at a ORC unit or working fluid loop pressure rating.
As illustrated in
As illustrated in
The system may include, as noted, a temperature sensor 259 and pressure sensor 257 to determine the temperature of the wellhead fluid after the choke valve 252. The system may include temperature sensor 240 to determine the temperature of the working fluid or ORC fluid exiting the heat sink 236 and temperature sensor 238 to determine the temperature of the working fluid or ORC fluid entering the heat sink 236. The pressure and/or temperature of the wellhead fluid may be used to determine whether the heat sink 236 may be utilized based on pressure rating of the heat sink 236 and/or a liquid phase change threshold of the working fluid. In other words, if the flow of wellhead fluid is at a temperature sufficient to cool the working fluid and/or below a pressure rating of the heat sink 236, the heat sink valve 254 may open to allow wellhead fluid to flow through the heat sink 236 to facilitate cooling of the working fluid. In another embodiment, the heat sink valve 254 may initially be fully or partially open. The temperature of the working fluid or ORC fluid may be measured as the fluid enters the heat sink 236 and exits the heat sink 236. If the temperature differential indicates that there is no change or an increase in temperature, based on the temperature of the working fluid or ORC fluid entering the heat sink 236 and then leaving the heat sink 236, then the heat sink valve 254 may be closed. Temperature sensors 238, 240, 256, 262, and pressure sensors 258, 260 may be disposed within the heat sink 236 to ensure that the temperature of the wellhead fluid is suitable for cooling the working fluid and that the pressure of wellhead fluid does not exceed the pressure rating of the heat sink 236.
As illustrated in
As illustrated in
As illustrated in
As the wellhead fluid flows from the wellhead 306, the wellhead fluid may flow to the high-pressure heat exchanger, through a bypass pipe, and/or a combination thereof based on various factors or characteristics, e.g., wellhead fluid temperature and/or pressure and/or working fluid temperature. For example, if the wellhead fluid flow 308 is above a vaporous phase change threshold for a working fluid flow 310, then valve 332 may open, at least partially, to allow the wellhead fluid flow to the high pressure heat exchanger 312. In such examples, the wellhead fluid may continue to flow through the primary or bypass wellhead fluid pipe. As such, valve 330 may remain open, whether completely or at a certain percentage. From the high-pressure heat exchanger 312, the wellhead fluid may flow back to the primary or bypass wellhead fluid pipe, to a condenser 316 or other cooling apparatus, and/or a combination thereof. If the wellhead fluid is at a temperature to provide cooling to the working fluid flow 310, then valve 336 may open to allow wellhead fluid to flow therethrough. In such examples, the valve 334 may close to prevent wellhead fluid from flowing back. If the wellhead fluid is not at a temperature to allow for cooling of the working fluid flow 310, then valve 336 may close or remained closed and valve 334 may open or remain open. From the condenser 316 or the primary or bypass wellhead fluid pipe, the wellhead fluid may flow to in-field equipment 316, storage tanks, and/or other processing equipment at the well. The valves described above may be controlled via controller 320.
In another embodiment, rather than basing the opening and closing of valve 332 and/or valve 336 on wellhead fluid flow 308 temperature, the valve 332 and/or valve 336 may be opened or closed based on the temperature of the working fluid flow 310. For example, prior to activating the wellhead 306 (e.g., allowing wellhead fluid to flow or pumping wellhead fluid from the wellhead 306), valve 332 may be open, fully or partially. As the wellhead fluid flows through the high-pressure heat exchanger 312, the temperature of the working fluid flow 310 may be measured. Based on the working fluid flow 310 temperature, taken at continuously or at periodic intervals, and after a specified period of time, if the working fluid flow 310 does not reach a vaporous phase change temperature, then valve 332 may be closed. Further, such operations may be performed in conjunction with measuring wellhead fluid flow 308 and opening or closing valve 332 based on such measurements.
The wellhead fluid flowing through the high-pressure heat exchanger 312 may be at a temperature to facilitate heat transfer to a working fluid flow 310. The working fluid may further flow, as a vaporous state working fluid flow to an ORC expander/generator 314. The vaporous state working fluid may cause the ORC expander/generator 314 to generate electrical power to be utilized at equipment at the well (e.g., in-field equipment), energy storage device, or a grid power structure (via a transformer and power lines). The working fluid may then flow to a condenser 316 or other cooling apparatus. The condenser 316 or other cooling apparatus may facilitate cooling of the working fluid flow 310 via the wellhead fluid flow, air, another liquid, and/or other types of heat sinks or heat exchangers. The liquid state working fluid may then flow back to the high-pressure heat exchanger 312.
In another embodiment, the high-pressure heat exchanger 312 may connect to an ORC unit/module 340 or one or more ORC units or modules. The number of ORC units/modules may scale based on power to be utilized by in-field equipment, the amount or potential capacity of electricity generation at the well, and/or other factors. After production of hydrocarbons begins, additional ORC units/modules may be added at the well or existing ORC units/modules may be removed from the well.
As used herein, “signal communication” refers to electric communication such as hard wiring two components together or wireless communication for remote monitoring and control/operation, as understood by those skilled in the art. For example, wireless communication may be Wi-Fi®, Bluetooth®, ZigBee, cellular wireless communication, satellite communication, or forms of near field communications. In addition, signal communication may include one or more intermediate controllers or relays disposed between elements that are in signal communication with one another.
The master controller 402 may include instructions 408 to measure temperature at various points or locations of the system (e.g., as illustrated in, for example,
Utilizing the characteristics noted above, the master controller 402 may control various aspects of the system 400. For example, the master controller 402 may include flow control adjustment instructions 412. The system 400 may include one or more valves placed in various locations (For example, but not limited to,
In an example, the system 400 may include a user interface 436, e.g., such as a monitor, display, computing device, smartphones, tablets, and other similar devices as will be understood by those skilled in the art. A user may view data, enter thresholds or limits, monitor status of the equipment, and perform other various tasks in relation to the equipment at the well. For example, a specific flow rate may be set for hydrocarbon production. As a wellhead begins producing hydrocarbons (e.g., wellhead fluids begin flowing from a wellhead), the master controller 402 may monitor flow rate and compare the flow rate to the threshold either set by a user or pre-set in the master controller 402. If the master controller 402 determines that the heat exchanger valves 428 (e.g., via flow control adjustment instructions 412) should be open or are open and that the flow of wellhead fluid is higher or lower than the threshold, the master controller 402 may adjust the appropriate valves, e.g., wellhead fluid valve 426 and/or heat exchanger valves 428. The valve associated with the primary or bypass wellhead fluid pipe, e.g., wellhead fluid valve 426, may open or close by varying degrees based on such determinations.
In another example, the master controller 402 may include instructions 410 to control a pump for the ORC unit, e.g., working fluid pump 424. If heat exchanger valves 428 and condenser valves 432 are closed, the master controller 402 may transmit a signal to shut down or cease operation of the working fluid pump 424, if the working fluid pump 424 is operating. The master controller 402 may further transmit a signal, based on the heat exchanger valves 428 being open, to initiate or start operations of the working fluid pump 424. The working fluid pump 424 may be a fixed pressure pump or a variable frequency pump. The master controller 402 may further include instructions 414 to monitor the power output from an ORC unit or from expanders/generators 434 (e.g., expander/generator A 434A, expander/generator B 434B, and/or up to expander/generator N 434N). If the system 400 utilizes ORC units, the master controller 402 may determine the electrical power generated or output based on an output from, for example, ORC unit controller A 438A, ORC unit controller B 438B, and/or up to ORC unit controller N 438N. If the power output drops to an un-economical or unsustainable level or electrical power generation ceases completely while the heat exchanger valves 428 are open, the master controller 402 may transmit signals to close the heat exchanger valves 428. In another example, the master controller 402 may monitor electrical power output from other wells. The master controller 402 may monitor or meter the amount of electrical power being utilized at each of the wells and/or the amount of electrical power being generated at each of the wells. If an excess of electrical power exists, the master controller 402 may transmit signals causing the excess energy at any particular well to be stored in energy storage devices, transmitted to the grid, and/or transmitted to another well. If a deficit of electrical power exists, the master controller 402 may transmit a signal causing other wells to transmit electrical power to the well experiencing an electrical power deficit. In another example, the metered electrical power may be utilized for commercial trade, to determine a cost of the electricity generated, and/or for use in determining emissions or emission reductions through use of an alternate energy source (e.g., geothermal power).
In another example, the master controller 402 may include instructions to maximize energy output from an ORC unit. In such examples, the ORC unit may be connected to a plurality of high-pressure heat exchangers. Further, each of the high-pressure heat exchangers may connect to one or more wellheads. As a wellhead produces a wellhead fluid, the pressure and temperature of the wellhead fluid may vary, over time, as well as based on the location of the wellhead. The master controller 402 may determine the temperature of the wellhead fluid at each high-pressure heat exchanger and/or the temperature of the working fluid in each high-pressure heat exchanger. Based on these determinations, the master controller 402 may open/close valves associated with one or more particular high-pressure heat exchangers to ensure the most efficient heat transfer. Further, the master controller 402 may determine the amount of electrical power output from the ORC unit. Based on a power rating of the ORC unit (e.g., the maximum power output the ORC unit is able to produce) and/or the amount of electrical power output from the ORC unit, the master controller 402 may adjust valves associated with the one or more particular high-pressure heat exchangers to thereby increase electrical power output. Additional ORC units may be utilized and electrical power output for each may be optimized or efficiently generated. The master controller 402 may determine, for each ORC unit, the optimal amount or efficient amount of heated working fluid flowing from each high-pressure heat exchanger to ensure the highest amount of electrical power possible is generated per ORC unit or that each ORC unit meets a preselected electrical power output threshold. In such examples, each ORC unit may be connected to each high-pressure heat exchanger and the master controller 402 may determine which set of valves to open/close based on such an optimization or electrical power output threshold.
In another example, the master controller 402 may include failover instructions or instructions to be executed to effectively reduce or prevent risk. The failover instructions may execute in the event of ORC unit and/or high-pressure heat exchanger failure or if an ORC unit and/or high-pressure heat exchanger experiences an issue requiring maintenance. For example, the ORC unit and/or high-pressure heat exchanger may have various sensors or meters. Such sensors or meters, when providing measurement to the master controller 402, may indicate a failure in the ORC unit and/or high-pressure heat exchanger. In another example, the master controller 402 may include pre-determined parameters that indicate failures. If the master controller 402 receives such indications, the master controller 402 may open, if not already open, the wellhead fluid valve 1426 and wellhead fluid valve 2430. After the wellhead fluid valve 1426 and wellhead fluid valve 2430 are opened, the master controller 402 may close the heat exchanger valves 428, the condenser valves 432, or any other valve associated with the flow of fluid to the ORC unit and/or high-pressure heat exchanger. In such examples, the master controller 402 may prevent further use of the ORC unit and/or high-pressure heat exchanger until the issue or failure indicated is resolved. Such a resolution may be indicated by a user via the user interface 436 or based on measurements from sensors and/or meters.
In another example, the master controller 402 may, as noted, determine an amount of electrical power output by an ORC unit. The master controller 402 may additionally determine different characteristics of the electrical power output. For example, the master controller 402 may monitor the output voltage and frequency. Further, the master controller 402 may include pre-set or predetermined thresholds, limits, or parameters in relation to the monitored characteristics of the electrical power output. Further still, the master controller 402 may connect to a breaker or switchgear. In the event that the master controller 402 detects that an ORC unit exceeds any of the thresholds, limits, and/or parameters, the master controller 402 may transmit a signal to the breaker or switchgear to break the circuit (e.g., the flow of electricity from the ORC unit to a source) and may shut down the ORC unit (e.g., closing valves preventing further flow to the ORC unit, as described above).
At block 502, the master controller 402 may determine whether the wellhead is active. Such a determination may be made based on sensors located at or near the wellhead, e.g., a pressure sensor indicating a pressure or a flow meter indicating a flow of a wellhead fluid or hydrocarbon stream from the wellhead. In other examples, a user may indicate, via the user interface 436, that the wellhead is active. If the wellhead is not active, the master controller 402 may wait for a specified period of time and make such a determination after the period of time. In an example, the master controller 402 may continuously check for wellhead activity.
At block 504, in response to wellhead activity or during hydrocarbon production, the master controller 402 may determine a wellhead fluid temperature. The wellhead fluid temperature may be measured by a wellhead fluid temperature sensor 1416 disposed at or near the wellhead. The wellhead fluid temperature sensor 1416 may be disposed on or in a pipe. In an example, various other temperature sensors may be disposed at other points in the system 400, e.g., heat exchanger temperature sensor 418, wellhead fluid temperature sensor 2420, condenser temperature sensor 422, and/or other temperature sensors. The temperature measurements provided by such sensors may be utilized by the master controller 402 to determine which valves to open or close.
At block 506, the master controller 402 may determine whether the wellhead fluid is at or above a vaporous phase change temperature threshold of a working fluid. In such examples, the vaporous phase change temperature may be based on the working fluid of the ORC unit. For example, for pentafluoropropane the vaporous phase change temperature or boiling point may be 15.14 degrees Celsius. In another example, or factors may be taken into account when determining whether to open heat exchanger valves 428. For example, whether the pressure is within operating range of a high-pressure heat exchanger, whether the flow rate at a primary or bypass pipeline is sufficient to prevent impedance of hydrocarbon production, whether power generation costs are offset by power generation needs, among other factors.
At block 508, if the wellhead fluid is at or above the vaporous phase change temperature, the master controller 402 may transmit a signal to heat exchanger valves 428 to open to a specified degree. In an example, the heat exchanger valves 428 may be may be fully opened or partially opened. The degree to which the heat exchanger valves 428 opens may depend on the temperature of the wellhead fluid, the flow rate of the wellhead fluid, and/or the pressure of the wellhead fluid.
At block 510, the master controller 402 may close wellhead fluid valves (e.g., wellhead fluid valve 1426) to divert a portion of the flow of wellhead fluids to the high-pressure heat exchanger. The wellhead fluid valves (e.g., wellhead fluid valve 1426) may close partially or completely, depending on various factors, such as heat exchanger flow capacity, current flow rate, current pressure, current temperature, among other factors. Once the wellhead fluid valves (e.g., wellhead fluid valve 1426) are closed, at block 512, a working fluid pump 424 of the ORC unit may begin pumping the working fluid through the ORC loop. At block 514, the master controller 402 may determine whether electricity is being generated. If not, the master controller 402 may check if the wellhead is still active and, if the wellhead is still active, the master controller 402 may adjust the valves (e.g., wellhead fluid valve 1426 and heat exchanger valves 428) as appropriate (e.g., increasing flow through the heat exchanger to facilitate an increase in heat transfer).
At block 516, if the wellhead fluid is lower than the vaporous phase change temperature, the master controller 402 may open or check if the wellhead fluid valves (e.g., wellhead fluid valve 1426) are open. Further, the wellhead fluid valves may already be open to a degree and, at block 516, may open further or fully open, depending on desired wellhead fluid flow. In an example, the wellhead fluid valve (e.g., wellhead fluid valve 1426) may be used, with or without a separate choke valve, to choke or partially choke the wellhead fluid flow. Further, once the wellhead fluid valves are open, at block 518, the master controller 402 may close the heat exchanger valves 428 fully or partially in some cases.
Blocks 602 through 610 correspond to blocks 502 through 610, as described above. Once it has been determined that the heat exchanger valves 428 should be open and after the heat exchanger valves 428 open, wellhead fluid may flow through the heat exchanger and/or the primary or bypass wellhead fluid pipe to a choke valve. The choke valve may reduce the pressure of the wellhead fluid and, thus, reduce the temperature of the wellhead fluid. At block 612, the master controller 402 may determine the reduced pressure wellhead fluid temperature at or near a condenser or heat sink valve based on a measurement from the condenser temperature sensors 422. The master controller 402 may, at block 614, determine whether the wellhead fluid is at cool enough temperatures to facilitate cooling of a working fluid flow. The working fluid may have a condensation point or a temperature at which the working fluid changes phase from a vapor to a liquid. Such a temperature may be utilized as the threshold for such determinations.
At block 616, if the temperature is cool enough, the master controller 402 may open the condenser valves 432, allowing wellhead fluid to flow through the condenser or other cooling apparatus. At block 617 the master controller 402 may transmit a signal to the working fluid pump 424 to start or begin pumping working fluid through an ORC loop. In another example, at block 619, if the temperature of the working fluid is not cool enough to facilitate cooling of the working fluid to any degree, the master controller 402 may close the condenser valves 432. In another example, the master controller 402 may determine the temperature of the reduced pressure wellhead fluid flow and whether the temperature of the reduced pressure wellhead fluid flow, in conjunction with a primary or secondary cooler, may cool the working fluid to a point. The master controller 402, in such examples, may consider the temperature of the working fluid entering the condenser and the temperature of the reduced pressure wellhead fluid flow at or near the condenser valve 432.
As noted and described above, the master controller 402 may, at block 618, determine whether electric power is generated. In another example, if the wellhead temperature is not high enough to produce geothermal power, the master controller 402 may, at block 620, open the wellhead fluid valves. At block 622, the master controller 402 may close, if the heat exchanger valves 428 are open, the heat exchanger valves 428. Finally, at block 624, the master controller 402 may close condenser valves 432.
At block 702, the master controller 702 may determine whether the wellhead is active. Such a determination may be made based on sensors located at or near the wellhead, e.g., a pressure sensor indicating a pressure or a flow meter indicating a flow of a wellhead fluid or hydrocarbon stream from the wellhead. In other examples, a user may indicate, via the user interface 436, that the wellhead is active. If the wellhead is not active, the master controller 402 may wait for a specified period of time and make such a determination after the specified period of time. In an example, the master controller 402 may continuously check for wellhead activity.
At block 704, in response to wellhead activity or during hydrocarbon production, the master controller 402 may open heat exchanger valves 428. At block 706, the master controller 402 may close wellhead fluid valve 1426, at least partially. At block 708, when the heat exchanger valves 428 is open and wellhead fluid valve 1426 is fully or partially closed, working fluid or ORC fluid may be pumped through the ORC unit.
At block 710, the master controller 402 may measure the temperature of the working fluid or ORC fluid. At block 712, the master controller 402 may determine whether the wellhead fluid is at or above a vaporous phase change temperature threshold. In such examples, the vaporous phase change may include when the working fluid or ORC fluid changes from a liquid to a vapor or gas. For example, for pentafluoropropane the vaporous phase change temperature or boiling point may be 15.14 degrees Celsius. In another example, other factors may be taken into account when determining whether to maintain an open percentage of the heat exchanger valves 428. For example, whether the pressure is within operating range of a high-pressure heat exchanger, whether the flow rate at a primary or bypass pipeline is sufficient to prevent impedance of hydrocarbon production, whether power generation costs are offset by power generation needs, among other factors.
At block 712, if the working fluid or ORC fluid is at or above the vaporous phase change temperature, the master controller 402 may determine whether electricity is generated at the ORC unit. If electricity is not generated, the master controller 402 may check, at block 702, whether the wellhead is active and perform the operations of method 700 again.
If the working fluid or ORC fluid, at block 712 is not at a vaporous phase change temperature, then, at block 714, the master controller 402 may first determine whether a first specified period of time has lapsed. The first period of time may be period of time of sufficient length to determine whether or not the working fluid or ORC fluid may reach a vaporous phase change state. Such a first specified period of time may be about an hour or more, two hours, three hours, four hours, or some other length of time during wellhead activity.
If the first specified period of time has not lapsed, at block 716, the master controller 402 may wait a second specified period of time before measuring the temperature of the working fluid or ORC fluid The second specified period of time may be less than the first specified period of time.
If the first specified period of time has lapsed, then the master controller 402 may have determined that, based on the temperature of the working fluid or ORC fluid, that the wellhead fluid may not reach temperatures sufficient to cause a vaporous phase change of the working fluid or ORC fluid. As such, at block 718, the master controller may close the open wellhead fluid valves and, at block 720, close the heat exchanger valves 428.
Blocks for
In addition, after the master controller 402 closes the heat exchanger valves at block 720, the master controller 402 may determine, at block 726, the wellhead fluid temperature at the heat exchanger. At block 728, the master controller may determine whether the wellhead fluid is at a vaporous phase change temperature of the working fluid or ORC fluid. If the wellhead fluid temperature is less than such a value, the master controller 402 may wait and measure the temperature again after a period of time. If the wellhead fluid temperature is greater than or equal to such a value, the master controller 402 may perform the operations of method 701 starting at block 724 again.
At block 802, each of one or more heat exchangers may be connected to one or more wellhead fluid lines. Each of the one or more wellhead fluid lines may correspond to a wellhead. At block 804, an ORC unit may be connected to the one or more heat exchangers. In another example, the system 400 may include one or more ORC units and each of the one or more ORC units may connect to one or more heat exchangers or two or more heat exchangers.
At block 806, heat exchanger valves positioned between the one or more heat exchangers and the one or more wellhead fluid lines may be opened. Once opened, the heat exchanger valves may allow for continuous diversion of the flow of wellhead fluid through the heat exchanger. The flow of wellhead fluid through the heat exchanger may facilitate transfer of heat from the flow of wellhead fluid to a flow of working fluid or intermediate working fluid.
At block 808, ORC unit valves may be opened. The ORC unit valves may initially be fully opened or partially opened. The ORC unit valves, when open, may allow for working fluid from each of the heat exchangers to flow into the ORC unit. Each working fluid flow may be combined and may pass through the ORC unit.
At block 810, the master controller 402 may determine one or more operating conditions of the ORC unit and/or the system 400. The one or more operating conditions may include the flow rate and/or pressure of working fluid flowing through each of the one or more heat exchangers, the flow rate and/or pressure of wellhead fluid flowing through each of the one or more heat exchangers or at any other point downstream of the wellhead, the temperature of the working fluid in each of the one or more heat exchangers, the temperature of wellhead fluid at each of the one or more heat exchangers, the temperature of the combined working fluid flow at the ORC unit, the electrical power output from the ORC unit, and/or the open position of each of the valves included in the system 400.
At block 812, based on the determined operating conditions, the master controller 402 may determine an optimal or efficient working fluid flow of the ORC unit. The optimal or efficient working fluid flow may depend on the temperature of the combined working fluid flowing to the ORC unit. The other operating conditions, described above, may be utilized to determine the optimal or efficient working fluid flow. The optimal or efficient working fluid flow may comprise the combined flow of working fluid flowing into the ORC unit to thereby produce a maximum amount of electrical power possible or to enable the ORC unit to meet a preselected electrical power output threshold. The optimal or efficient working fluid flow may be at a temperature sufficient to produce such an amount of electrical power (e.g., a temperature greater than or equal to the boiling point of the working fluid within the ORC unit). The optimal or efficient working fluid flow may be indicated by the master controller 402 as one or more open positions for each of the ORC unit valves and/or heat exchanger valves.
At block 814, the master controller 402 may, based on a determined optimal or efficient working fluid flow, determine whether to adjust the one or more ORC unit valves. Other valves within the system 400 may be adjusted based on the optimal or efficient working fluid flow, such as one or more heat exchanger valves and/or one or more wellhead fluid valves. If it is determined that the ORC unit valves or any other valves are to be adjusted, the master controller 402, at block 816, may transmit a signal to the valve to be adjusted indicating a new open position or closed position for the valve to adjust to. After the signal is transmitted, the valve may automatically adjust to the position indicated. If the valve is not to be adjusted or after the valves have been adjusted, the master controller 402 may determine operating conditions again. In an example, the master controller 402 may wait for a period of time, allowing the system to adjust to the new temperatures and flow rates or to reach equilibrium, prior to determining the operating conditions.
As noted and as illustrated in
As described and as illustrated in
As illustrated in
As such, a working fluid of a particular high-pressure heat exchanger 906A, 906B, 906N may be heated to a degree sufficient, insufficient, or more than sufficient to cause the working fluid of the ORC equipment 908A, 908B to exhibit a vaporous phase change. Since the temperature of the wellhead fluid varies, a controller (e.g., controller 916A, 916B, up to 916N or master controller 918, as illustrated in
For example, if high-pressure heat exchanger A 906A includes a working fluid at a temperature slightly less than a temperature to cause vaporous phase change, then valves providing working fluid or intermediate working fluid from the high-pressure heat exchanger A 906A to the ORC equipment 908A, 908B may be closed. In another example, if high-pressure heat exchanger B 906B is providing working fluid at a temperature well above a temperature to cause vaporous phase change, then valves providing working fluid or intermediate working fluid from high-pressure heat exchanger B 906B to ORC equipment A 908A and/or to ORC equipment B 908B may be adjusted to positions such that a greater portion of the working fluid or intermediate working fluid is transported to ORC equipment A 908A and/or to ORC equipment B 908B.
In yet another example, all valves for allowing flow of working fluid or intermediate working fluid to the ORC equipment A 908A and/or ORC equipment B 908B may be, at least, in a partially open position. The temperature of the wellhead fluid and/or working fluid of each heat exchanger 906A, 906B, 906N may be determined or measured. Further, the electrical power output of the ORC equipment A 908A and/or ORC equipment B 908B may be determined. The positions of each valve for allowing flow of working fluid or intermediate working fluid to the ORC equipment A 908A and/or ORC equipment B 908B may be adjusted to different partially open positions, fully opened positions, or fully closed positions. Such valve adjustments may be based on maximization of the resultant temperature and heat delivered to the ORC equipment A 908A and/or ORC equipment B 908B once the combined working fluid flows into the ORC equipment 908 A 908A and/or ORC equipment B 908B. The valve adjustments may be based on, rather than or in addition to other factors, the maximization of the electrical power output from the ORC equipment A 908A and/or ORC equipment B 908B. Valve adjustments may further be based on wellhead fluid temperature and/or some combination of the factors described herein.
As noted and described above and as illustrated in
According to another embodiment of the present disclosure shown in
The mobile heat generation unit 1002 shown in the system 1000 (
In the present embodiment, the site (e.g. a well 100 or pumping station as shown in
An example embodiment of a mobile heat generation unit and features thereof is shown in
The heat exchangers 1005 (
The heat exchangers 1005 installed in the mobile heat generation unit will include selected type and/or capacity heat exchangers that can be selected based upon an estimated mass flow volume or range of mass flow volumes of the heated fluid to be supplied thereto. For example, and not limitation, each mobile heat generation unit can be constructed/produced as a substantially standardized or “off-the shelf” heat generation package with between 50%-80% and/or up to 100% selected operative components, such as one or more pumps, piping, etc., and one or more selected heat exchangers that can be pre-installed therein prior to shipment. As used herein, the operative components of the mobile heat generation unit can include the one or more heat exchangers, pumps, piping, valves, sensors, an expansion tank, air separator, and/or other equipment as will be understood by those skilled in the art.
Thus, rather than requiring a custom designed geothermal power generation system wherein components such as individual heat exchangers, pumps etc. are separately transported and assembled at a hydrocarbon production site, including assembling and connecting individual heat exchangers to necessary piping and integrating control thereof in the field, the mobile heat generation unit 1002 provides a compact, transportable and reusable heat generation module or package with one or more heat exchangers of a selected type and/or capacity pre-installed with at least one pump and piping for pumping or recirculating a flow of working fluid therethrough. The entire package further can be easily transported to a hydrocarbon production site or other location and can be quickly and easily connected one or more ORC units and to one or more heat sources, such as to exhaust conduits or ducts 1004 for one or more engines (
As shown in
In embodiments, the transportable package, module or skid defined by the mobile heat generation unit 1002 can be configured with a footprint that is substantially equivalent to that of an ISO shipping container, so as to be adapted for intermodal transportation along highways. For example, the mobile heat generation unit can have a substantially square or rectangular footprint with lengths ranging from about 15 feet to about 40 feet, widths of between about 5 feet to about 14 feet, and heights of between about 6 feet to about 10 feet to accommodate different arrangements and/or numbers of heat exchangers as needed for a particular application, while still enable transport along an interstate highway. Other dimensions also can be provided. In addition, the substantially skeletonized frame 1010 illustrated in
By way of example only, in embodiments, mobile heat generation units can be constructed with 1-2 heat exchangers in a package, skid or module having a length of about 20 feet, a width of approximately 8-10 feet, and a height of at least 8 feet, and can be transported and delivered to a site by a conventional semi-tractor trailer. In other embodiments, the mobile heat generation units can be constructed with a length upwards of approximately 40 feet, a width of approximately 8-10 feet, and a height of at least approximately 8 feet and can incorporate more (e.g. 3-6) heat exchangers. Other varying sizes and configurations of the prepackaged mobile heat generation units according the principals of the present disclosure, also can be provided. The construction of the mobile heat generation unit as a substantially pre-assembled/pre-configured module or package enables production of substantially uniform or generally standardized heat generation units that produced off-site with one or more selected heat exchangers, including high pressure heat exchangers configured to receive heated fluid flows of a selected type, e.g. high temperature high pressure liquid or gas fluid flows, and/or different capacity heat exchangers, packaged therein for ease and efficiency of shipment and installation at a site.
As further illustrated in
The cover panels generally can be formed from a rigid, durable material, such as a corrugated steel or other, similar metal material selected for durability without substantially increasing the weight of the overall package of the mobile heat generation unit, while enclosing and protecting the operative components of the mobile heat generation unit. Other rigid, durable materials also can be used for the cover panels. At least some of the cover panels 1026 further can be releasibly attached or mounted to the peripheral frame beams 1017, such as by a limited number (e.g., 5-10) of bolts, screws or other fasteners or other mechanical connections. As a result, at least a portion of the cover panels can be selectively removable as needed for enabling access to the chamber defined within the frame, and to the operative components of the mobile heat generation unit housed therein.
For example, if there is a need or a desire to change one or more of the heat exchangers 1005 of the mobile heat generation unit 1002, such as to substitute an exhaust heat exchanger for a different capacity or type of heat exchanger (e.g. a heat exchanger designed to extract heat from compressed gas or from a heated fluid or a high pressure fluid such as a wellhead fluid) one or more of the cover panels 1026 along the top or upper portion 1011 of the frame 1010 can be removed, as can one or more of the additional beams or supports 1019 as needed, to enable the removal and/or change-out of one or both of the heat exchangers through the top of the frame.
Such a change-out or substitution of the heat exchangers can be accomplished without requiring a substantial reconstruction of the entire mobile heat generation unit, and can be accomplished in the field e.g. at the hydrocarbon production site or other location, or can be done at a manufacturing or storage facility. The mobile heat generation units of the present disclosure thus can be reconfigured as needed without affecting their ability to be produced and transported to a site as pre-packaged, substantially ready-to-use modular mobile heat generation units that also can be relocated from one site to another without having to substantially deconstruct and the reconstruct the entire heat exchange assembly at each site. In addition, as indicated in
As shown in
A control cabinet or area 1032 can be provided within the second section 1031B, as indicated in
The control area will house a controller 1035 for the mobile heat generation unit 1002. The controller 1035 can include at least one processor and a control panel 1037 that can include a user interface (e.g., display/touch screen, keyboard, etc.), and will be programmed and/or configured to communicate with, monitor and control operation of the various operative components of the mobile heat generation unit. For example, as indicated in
As noted, in the illustrated example embodiment, a pair of exhaust gas heat exchangers 1005 are shown, and can be selected and sized to accommodate an estimated or mass flow. As indicated
As further illustrated in
In addition, it will be understood by those skilled in the art that while a pair of heat exchangers are shown in a present embodiment, in other embodiments, a single heat exchanger could be used, or more than two heat exchangers also can be used, e.g. the mobile heat generation unit can be packaged with 3, 4, 5 or 6 (or more) heat exchangers.
Each mobile heat generation unit further will include a fluid recirculation system 1050, along which the second fluid path 1007 is defined an extends. The fluid recirculation system will including fluid intake conduit 1051 configured to couple to a return line 1052 that is in fluid communication with the at least one ORC 106 unit for receiving the working fluid therefrom; a fluid outlet conduit 1054 configured to couple to a heated working fluid supply line that is in fluid communication with the at least one ORC unit for supplying the heated working fluid to the at least one ORC unit, a pump 1057, and an array of piping 1058 including a first section of piping at 1059A, connecting the pump to the heat exchangers and a second section of piping 1059B connecting the heat exchangers to the fluid outlet conduit. As indicated in
The mobile heat generation unit will be connected to the at least one ORC unit in a substantially closed fluid recirculation loop arrangement whereby the heated working fluid, such as a deionized water mixture or other working fluid such as pentafluoropropane, carbon dioxide, ammonia and water mixture, tetrafluoroethane, isobutene, propane, pentane, perfluorocarbons, and other hydrocarbons mixtures as disclosed above, will be supplied to and returned from the at least one ORC unit. As the working fluid is moved along the second fluid path through the closed fluid recirculation loop defined between the ORC unit and the mobile heat generation unit, the working fluid is heated by transfer of heat from the heated flow passing through the heat exchangers along the first fluid path so that the working fluid will be output and supplied to the ORC unit at a temperature approximately at or above its boiling point, whereupon the liquid working fluid will change from a liquid to vapor phase.
As the heated (e.g. vaporous phase) working fluid is circulated through the ORC unit, it can pass through a gas expander that can rotate so as to drive a generator 1061 for generation of electrical power, such as discussed above with respect to embodiments of the ORC unit as shown in
As discussed with respect to the above embodiments, the ORC unit further generally will include a controller that can monitor the incoming and outgoing working fluid flows, e.g. receiving inputs from a series of sensors 1062 (
As illustrated in
In the embodiment shown in
As indicated, the control valve 1068 of the splitter 1057 can be opened and closed to selectively divert more or less volumes of the working fluid into each of the heat exchangers through an inlet port 1070 adjacent a first or upstream portion thereof. As the working fluid passes through the heat exchangers, heat from the incoming heated fluid flow (e.g. heated exhaust gases passing along the first fluid path) is transferred to the working fluid. The working fluid is heated within the heat exchangers to a second temperature that is greater than the first temperature, and which generally will be at or above a boiling point of the working fluid whereupon the working fluid changes to its a vapor phase as it is output from the heat exchangers through a downstream port 1071 and to the second section of piping 1059B of the array of piping. The heated working fluid thereafter can be fed through a manifold 1072 that can include a control valve 1073 operable to regulate the flow of the heated working fluid from one or both of the heat exchangers for feeding to the ORC unit. The manifold generally will be linked to the fluid outlet conduit 1052, which will extend along a portion of the chamber and will be directed upwardly to the top or upper portion of the chamber, terminating at an outlet coupling or connector 1074 adjacent to the top portion of the frame at the approximately and thereof.
As further illustrated in
In addition, an air separator can be provided along array of piping, for example along the second section of piping. The air separator generally will be configured and can be operable to filter out particulates from the working fluid, and/or to drain or bleed off excess air from the recirculating system 1050, such as on startup of the mobile heat generation unit.
As further illustrated in
The mobile heat generation unit additionally will include UPC battery backup or other alternative power source that can automatically be engaged. In the event that exhaust streams or other incoming streams or flows of the heated fluid fail, and/or the mobile heat generation unit loses a connection to a direct power source (e.g. an ORC unit providing to a direct power source to the mobile heat generation unit is shut down or otherwise the power connection is lost), the battery backup system can be automatically turned on to provide power to the controller 1035 and at least some of the operative components of the mobile heat generation unit.
In embodiments, the mobile heat generation unit further can include one or more drain or dump valves arranged along the array of piping. While the array of piping generally will be insulated to both prevent or reduce the incidence of personnel being burned or otherwise injured when they come into contact with such piping, and protect the piping from subfreezing temperatures, in the event of a system power loss and/or loss of the flows of heated fluid into the mobile heat generation unit, and subfreezing temperatures being detected by the controller, the controller can engage and operate one or more of the drain or dump valves to enable drainage of deionized water out of the array of piping in order to prevent freezing of the deionized water within the piping, which can cause splitting or otherwise damage to the operative components of the mobile heat generation unit.
As noted above, the mobile heat generation unit 1002 according to the present embodiment, can be used in place of one or more high pressure heat exchangers as disclosed with respect to any of the embodiments disclosed and/or taught by the present disclosure. The mobile heat generation unit is designed to provide a transportable, substantially self-contained and ready to operate package or module that can be produced with pre-installed operative components, such as pump and recirculation system, as well as one or more heat exchangers of a selected type and/or capacity, within a substantially standardized footprint. The pre-packaged mobile heat generation unit can be easily transported, such as by a semi-tractor trailer, and can be located and installed at a site being easily and efficiently connected or coupled to a heat source and to an ORC unit at the site, without having to separately ship components such as heat exchangers and assemble such components at the site. Additional mobile heat generation units further can be transported to a job site, and can be connected in series to a previously installed mobile heat generation unit and to additional heat sources, as well as one or more ORC units as needed. The mobile heat generation units further can be removed from a site and readily transferred to another site for use.
It will be understood by those skilled in the art that the mobile heat generation unit according to the principles of the present disclosure further can be utilized with any of the systems and/or methods for generating geothermal power in an ORC operation presented in this disclosure, including systems and methods for generating power in an ORC operation during hydrocarbon production based on working fluid temperature and/or pressure provided in any of the previously discussed embodiments of the present disclosure.
This application is a continuation of U.S. Non-Provisional application Ser. No. 17/657,721, filed Apr. 1, 2022, titled “Modular Mobile Heat Generation Unit for Generation of Geothermal Power in Organic Rankine Cycle Operations,” which claims priority to and the benefit of U.S. Provisional Application No. 63/269,862, filed Mar. 24, 2022, titled “Systems and Methods for Generation of Electrical Power at a Drilling Rig,” and U.S. Provisional Application No. 63/269,572, filed Mar. 18, 2022, titled “Systems and Methods for Generation of Electrical Power at a Drilling Rig,” U.S. Provisional Application No. 63/261,601, filed Sep. 24, 2021, titled “Systems and Methods Utilizing Gas Temperature as a Power Source,” and U.S. Provisional Application No. 63/200,908, filed Apr. 2, 2021, titled “Systems and Methods for Generating Geothermal Power During Hydrocarbon Production,” the disclosures of all of which are incorporated herein by reference in their entireties. U.S. Non-Provisional application Ser. No. 17/657,721 is also a continuation-in-part of U.S. Non-Provisional application Ser. No. 17/657,009, filed Mar. 29, 2022, titled “Systems and Methods for Generation of Electrical Power at a Drilling Rig,” which claims priority to and the benefit of U.S. Provisional Application No. 63/269,862, filed Mar. 24, 2022, titled “Systems and Methods for Generation of Electrical Power at a Drilling Rig,” and U.S. Provisional Application No. 63/269,572, filed Mar. 18, 2022, titled “Systems and Methods for Generation of Electrical Power at a Drilling Rig,” U.S. Provisional Application No. 63/261,601, filed Sep. 24, 2021, titled “Systems and Methods Utilizing Gas Temperature as a Power Source,” and U.S. Provisional Application No. 63/200,908, filed Apr. 2, 2021, titled “Systems and Methods for Generating Geothermal Power During Hydrocarbon Production,” the disclosures of all of which are incorporated herein by reference in their entireties. U.S. Non-Provisional application Ser. No. 17/657,009 is also a continuation-in-part of U.S. Non-Provisional application Ser. No. 17/305,297, filed Jul. 2, 2021, titled “Systems for Generating Geothermal Power in an Organic Rankine Cycle Operation During Hydrocarbon Production Based on Working Fluid Temperature,” which claims priority to and the benefit of U.S. Provisional Application No. 63/200,908, filed Apr. 2, 2021, titled “Systems and Methods for Generating Geothermal Power During Hydrocarbon Production,” the disclosures of all of which are incorporated herein by reference in their entireties. U.S. Non-Provisional application Ser. No. 17/657,009 is a continuation-in-part of U.S. Non-Provisional application Ser. No. 17/578,520, filed Jan. 19, 2022, titled “Systems and Methods Utilizing Gas Temperature as a Power Source,” now U.S. Pat. No. 11,326,550, issued May 10, 2022, which claims priority to and the benefit of U.S. Provisional Application No. 63/261,601, filed Sep. 24, 2021, titled “Systems and Methods Utilizing Gas Temperature as a Power Source,” and U.S. Provisional Application No. 63/200,908, filed Apr. 2, 2021, titled “Systems and Methods for Generating Geothermal Power During Hydrocarbon Production,” the disclosures of all of which are incorporated herein by reference in their entireties. U.S. Non-Provisional application Ser. No. 17/657,009 also further is a continuation-in-part of U.S. Non-Provisional application Ser. No. 17/578,528, filed Jan. 19, 2022, titled “Systems and Methods Utilizing Gas Temperature as a Power Source,” which claims priority to and the benefit of U.S. Provisional Application No. 63/261,601, filed Sep. 24, 2021, titled “Systems and Methods Utilizing Gas Temperature as a Power Source,” and U.S. Provisional Application No. 63/200,908, filed Apr. 2, 2021, titled “Systems and Methods for Generating Geothermal Power During Hydrocarbon Production,” the disclosures of all of which are incorporated herein by reference in their entireties. U.S. Non-Provisional application Ser. No. 17/657,009 still further is a continuation-in-part of U.S. Non-Provisional application Ser. No. 17/578,542, filed Jan. 19, 2022, titled “Systems and Methods Utilizing Gas Temperature as a Power Source,” now U.S. Pat. No. 11,359,576, issued Jun. 14, 2022, which claims priority to and the benefit of U.S. Provisional Application No. 63/261,601, filed Sep. 24, 2021, titled “Systems and Methods Utilizing Gas Temperature as a Power Source,” and U.S. Provisional Application No. 63/200,908, filed Apr. 2, 2021, titled “Systems and Methods for Generating Geothermal Power During Hydrocarbon Production,” the disclosures of all of which are incorporated herein by reference in their entireties. U.S. Non-Provisional application Ser. No. 17/657,009 additionally is a continuation-in-part of U.S. Non-Provisional application Ser. No. 17/578,550, filed Jan. 19, 2022, titled “Systems and Methods Utilizing Gas Temperature as a Power Source,” which claims priority to and the benefit of U.S. Provisional Application No. 63/261,601, filed Sep. 24, 2021, titled “Systems and Methods Utilizing Gas Temperature as a Power Source,” and U.S. Provisional Application No. 63/200,908, filed Apr. 2, 2021, titled “Systems and Methods for Generating Geothermal Power During Hydrocarbon Production,” the disclosures of all of which are incorporated herein by reference in their entireties. U.S. Non-Provisional application Ser. No. 17/657,009 is also a continuation-in-part of U.S. Non-Provisional application Ser. No. 17/650,811, filed Feb. 11, 2022, titled “Systems for Generating Geothermal Power in an Organic Rankine Cycle Operation During Hydrocarbon Production Based on Wellhead Fluid Temperature,” which is a continuation of U.S. Non-Provisional application Ser. No. 17/305,298, filed Jul. 2, 2021, titled “Controller for Controlling Generation of Geothermal Power in an Organic Rankine Cycle Operation During Hydrocarbon Production,” now U.S. Pat. No. 11,280,322, issued Mar. 22, 2022, which claims priority to and the benefit of U.S. Provisional Application No. 63/200,908, filed Apr. 2, 2021, titled “Systems and Methods for Generating Geothermal Power During Hydrocarbon Production,” the disclosures of all of which are incorporated herein by reference in their entireties. U.S. Non-Provisional application Ser. No. 17/657,009 further still is a continuation-in-part of U.S. Non-Provisional application Ser. No. 17/670,827, filed Feb. 14, 2022, titled “Systems and Methods for Generation of Electrical Power in an Organic Rankine Cycle Operation,” now U.S. Pat. No. 11,421,663, issued Aug. 23, 2022, which is a continuation-in-part of U.S. Non-Provisional application Ser. No. 17/305,296, filed Jul. 2, 2021, titled “Controller for Controlling Generation of Geothermal Power in an Organic Rankine Cycle Operation During Hydrocarbon Production,” now U.S. Pat. No. 11,255,315, issued Feb. 22, 2022, which claims priority to and the benefit of U.S. Provisional Application No. 63/200,908, filed Apr. 2, 2021, titled “Systems and Methods for Generating Geothermal Power During Hydrocarbon Production,” the disclosures of all of which are incorporated herein by reference in their entireties. U.S. Non-Provisional application Ser. No. 17/657,009 yet further is a continuation-in-part of U.S. Non-Provisional application Ser. No. 17/682,126, filed Feb. 28, 2022, titled “Systems and Methods for Generation of Electrical Power in an Organic Rankine Cycle Operation,” now U.S. Pat. No. 11,359,612, issued Jun. 14, 2022, which is a continuation of U.S. Non-Provisional application Ser. No. 17/494,936, filed Oct. 6, 2021, titled “Systems and Methods for Generation of Electrical Power in an Organic Rankine Cycle Operation,” now U.S. Pat. No. 11,293,414, issued Apr. 5, 2022, which is a continuation-in-part of U.S. Non-Provisional application Ser. No. 17/305,296, filed Jul. 2, 2021, titled “Controller for Controlling Generation of Geothermal Power in an Organic Rankine Cycle Operation During Hydrocarbon Production,” now U.S. Pat. No. 11,255,315, issued Feb. 22, 2022, which claims priority to and the benefit of U.S. Provisional Application No. 63/200,908, filed Apr. 2, 2021, titled “Systems and Methods for Generating Geothermal Power During Hydrocarbon Production,” the disclosures of all of which are incorporated herein by reference in their entireties.
In the drawings and specification, several embodiments of systems and methods to provide geothermal power in the vicinity of a wellhead during hydrocarbon production have been disclosed, and although specific terms are employed, the terms are used in a descriptive sense only and not for purposes of limitation. Embodiments of systems and methods have been described in considerable detail with specific reference to the illustrated embodiments. However, it will be apparent that various modifications and changes can be made within the spirit and scope of the embodiments of systems and methods as described in the foregoing specification, and such modifications and changes are to be considered equivalents and part of this disclosure.
This application is a continuation of U.S. Non-Provisional application Ser. No. 17/657,721, filed Apr. 1, 2022, titled “Modular Mobile Heat Generation Unit for Generation of Geothermal Power in Organic Rankine Cycle Operations,” which claims priority to and the benefit of U.S. Provisional Application No. 63/269,862, filed Mar. 24, 2022, titled “Systems and Methods for Generation of Electrical Power at a Drilling Rig,” and U.S. Provisional Application No. 63/269,572, filed Mar. 18, 2022, titled “Systems and Methods for Generation of Electrical Power at a Drilling Rig,” U.S. Provisional Application No. 63/261,601, filed Sep. 24, 2021, titled “Systems and Methods Utilizing Gas Temperature as a Power Source,” and U.S. Provisional Application No. 63/200,908, filed Apr. 2, 2021, titled “Systems and Methods for Generating Geothermal Power During Hydrocarbon Production,” the disclosures of all of which are incorporated herein by reference in their entireties. U.S. Non-Provisional application Ser. No. 17/657,721 is also a continuation-in-part of U.S. Non-Provisional application Ser. No. 17/657,009, filed Mar. 29, 2022, titled “Systems and Methods for Generation of Electrical Power at a Drilling Rig,” which claims priority to and the benefit of U.S. Provisional Application No. 63/269,862, filed Mar. 24, 2022, titled “Systems and Methods for Generation of Electrical Power at a Drilling Rig,” and U.S. Provisional Application No. 63/269,572, filed Mar. 18, 2022, titled “Systems and Methods for Generation of Electrical Power at a Drilling Rig,” U.S. Provisional Application No. 63/261,601, filed Sep. 24, 2021, titled “Systems and Methods Utilizing Gas Temperature as a Power Source,” and U.S. Provisional Application No. 63/200,908, filed Apr. 2, 2021, titled “Systems and Methods for Generating Geothermal Power During Hydrocarbon Production,” the disclosures of all of which are incorporated herein by reference in their entireties. U.S. Non-Provisional application Ser. No. 17/657,009 is also a continuation-in-part of U.S. Non-Provisional application Ser. No. 17/305,297, filed Jul. 2, 2021, titled “Systems for Generating Geothermal Power in an Organic Rankine Cycle Operation During Hydrocarbon Production Based on Working Fluid Temperature,” which claims priority to and the benefit of U.S. Provisional Application No. 63/200,908, filed Apr. 2, 2021, titled “Systems and Methods for Generating Geothermal Power During Hydrocarbon Production,” the disclosures of all of which are incorporated herein by reference in their entireties. U.S. Non-Provisional application Ser. No. 17/657,009 is a continuation-in-part of U.S. Non-Provisional application Ser. No. 17/578,520, filed Jan. 19, 2022, titled “Systems and Methods Utilizing Gas Temperature as a Power Source,” now U.S. Pat. No. 11,326,550, issued May 10, 2022, which claims priority to and the benefit of U.S. Provisional Application No. 63/261,601, filed Sep. 24, 2021, titled “Systems and Methods Utilizing Gas Temperature as a Power Source,” and U.S. Provisional Application No. 63/200,908, filed Apr. 2, 2021, titled “Systems and Methods for Generating Geothermal Power During Hydrocarbon Production,” the disclosures of all of which are incorporated herein by reference in their entireties. U.S. Non-Provisional application Ser. No. 17/657,009 also further is a continuation-in-part of U.S. Non-Provisional application Ser. No. 17/578,528, filed Jan. 19, 2022, titled “Systems and Methods Utilizing Gas Temperature as a Power Source,” which claims priority to and the benefit of U.S. Provisional Application No. 63/261,601, filed Sep. 24, 2021, titled “Systems and Methods Utilizing Gas Temperature as a Power Source,” and U.S. Provisional Application No. 63/200,908, filed Apr. 2, 2021, titled “Systems and Methods for Generating Geothermal Power During Hydrocarbon Production,” the disclosures of all of which are incorporated herein by reference in their entireties. U.S. Non-Provisional application Ser. No. 17/657,009 still further is a continuation-in-part of U.S. Non-Provisional application Ser. No. 17/578,542, filed Jan. 19, 2022, titled “Systems and Methods Utilizing Gas Temperature as a Power Source,” now U.S. Pat. No. 11,359,576, issued Jun. 14, 2022, which claims priority to and the benefit of U.S. Provisional Application No. 63/261,601, filed Sep. 24, 2021, titled “Systems and Methods Utilizing Gas Temperature as a Power Source,” and U.S. Provisional Application No. 63/200,908, filed Apr. 2, 2021, titled “Systems and Methods for Generating Geothermal Power During Hydrocarbon Production,” the disclosures of all of which are incorporated herein by reference in their entireties. U.S. Non-Provisional application Ser. No. 17/657,009 additionally is a continuation-in-part of U.S. Non-Provisional application Ser. No. 17/578,550, filed Jan. 19, 2022, titled “Systems and Methods Utilizing Gas Temperature as a Power Source,” which claims priority to and the benefit of U.S. Provisional Application No. 63/261,601, filed Sep. 24, 2021, titled “Systems and Methods Utilizing Gas Temperature as a Power Source,” and U.S. Provisional Application No. 63/200,908, filed Apr. 2, 2021, titled “Systems and Methods for Generating Geothermal Power During Hydrocarbon Production,” the disclosures of all of which are incorporated herein by reference in their entireties. U.S. Non-Provisional application Ser. No. 17/657,009 is also a continuation-in-part of U.S. Non-Provisional application Ser. No. 17/650,811, filed Feb. 11, 2022, titled “Systems for Generating Geothermal Power in an Organic Rankine Cycle Operation During Hydrocarbon Production Based on Wellhead Fluid Temperature,” which is a continuation of U.S. Non-Provisional application Ser. No. 17/305,298, filed Jul. 2, 2021, titled “Controller for Controlling Generation of Geothermal Power in an Organic Rankine Cycle Operation During Hydrocarbon Production,” now U.S. Pat. No. 11,280,322, issued Mar. 22, 2022, which claims priority to and the benefit of U.S. Provisional Application No. 63/200,908, filed Apr. 2, 2021, titled “Systems and Methods for Generating Geothermal Power During Hydrocarbon Production,” the disclosures of all of which are incorporated herein by reference in their entireties. U.S. Non-Provisional application Ser. No. 17/657,009 further still is a continuation-in-part of U.S. Non-Provisional application Ser. No. 17/670,827, filed Feb. 14, 2022, titled “Systems and Methods for Generation of Electrical Power in an Organic Rankine Cycle Operation,” now U.S. Pat. No. 11,421,663, issued Aug. 23, 2022, which is a continuation-in-part of U.S. Non-Provisional application Ser. No. 17/305,296, filed Jul. 2, 2021, titled “Controller for Controlling Generation of Geothermal Power in an Organic Rankine Cycle Operation During Hydrocarbon Production,” now U.S. Pat. No. 11,255,315, issued Feb. 22, 2022, which claims priority to and the benefit of U.S. Provisional Application No. 63/200,908, filed Apr. 2, 2021, titled “Systems and Methods for Generating Geothermal Power During Hydrocarbon Production,” the disclosures of all of which are incorporated herein by reference in their entireties. U.S. Non-Provisional application Ser. No. 17/657,009 yet further is a continuation-in-part of U.S. Non-Provisional application Ser. No. 17/682,126, filed Feb. 28, 2022, titled “Systems and Methods for Generation of Electrical Power in an Organic Rankine Cycle Operation,” now U.S. Pat. No. 11,359,612, issued Jun. 14, 2022, which is a continuation of U.S. Non-Provisional application Ser. No. 17/494,936, filed Oct. 6, 2021, titled “Systems and Methods for Generation of Electrical Power in an Organic Rankine Cycle Operation,” now U.S. Pat. No. 11,293,414, issued Apr. 5, 2022, which is a continuation-in-part of U.S. Non-Provisional application Ser. No. 17/305,296, filed Jul. 2, 2021, titled “Controller for Controlling Generation of Geothermal Power in an Organic Rankine Cycle Operation During Hydrocarbon Production,” now U.S. Pat. No. 11,255,315, issued Feb. 22, 2022, which claims priority to and the benefit of U.S. Provisional Application No. 63/200,908, filed Apr. 2, 2021, titled “Systems and Methods for Generating Geothermal Power During Hydrocarbon Production,” the disclosures of all of which are incorporated herein by reference in their entireties.
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| Number | Date | Country | |
|---|---|---|---|
| 20230003200 A1 | Jan 2023 | US |
| Number | Date | Country | |
|---|---|---|---|
| 63269862 | Mar 2022 | US | |
| 63269572 | Mar 2022 | US | |
| 63261601 | Sep 2021 | US | |
| 63200908 | Apr 2021 | US |
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