Waste heat is often created as a byproduct of industrial processes where flowing streams of high-temperature liquids, gases, or fluids must be exhausted into the environment or removed in some way in an effort to maintain the operating temperatures of the industrial process equipment. Some industrial processes utilize heat exchanger devices to capture and recycle waste heat back into the process via other process streams. However, the capturing and recycling of waste heat is generally infeasible by industrial processes that utilize high temperatures or have insufficient mass flow or other unfavorable conditions.
Waste heat can be converted into useful energy by a variety of turbine generator or heat engine systems that employ thermodynamic methods, such as Rankine cycles. Rankine cycles and similar thermodynamic cycles are typically steam-based processes that recover and utilize waste heat to generate steam for driving an expander, such as a turbine, connected to an electric generator, a pump, and/or another device. As an alternative to steam-based, thermodynamic cycles, an organic Rankine cycle utilizes a lower boiling-point working fluid, instead of water. Exemplary lower boiling-point working fluids include hydrocarbons, such as light hydrocarbons (e.g., propane or butane) and halogenated hydrocarbon, such as hydrochlorofluorocarbons (HCFCs) or hydrofluorocarbons (HFCs) (e.g., R245fa).
A synchronous power generator is a commonly employed turbine generator utilized for generating electrical energy in large scales (e.g., megawatt scale) throughout the world for both commercial and non-commercial use. The synchronous power generator generally supplies electricity to an electrical bus or grid (e.g., an alternating current bus) that usually has a varying load or demand over time. In order to be properly connected, the frequency of the synchronous power generator must be tuned and maintained to match the frequency of the electrical bus or grid. Severe damage may occur to the synchronous power generator as well as the electrical bus or grid should the frequency of the synchronous power generator become unsynchronized with the frequency of the electrical bus or grid.
Turbine generator systems also may suffer an overspeed condition during the generation of electricity—generally—due to high electrical demands during peak usage times. Turbine generator systems may be damaged due to an increasing rotational speed of the moving parts, such as turbines, generators, and/or gears, as well as a deficit in lubricating and cooling such turbomachinery. In addition, the turbines and pumps utilized in turbine generator systems are susceptible to fail due to thermal shock when exposed to substantial and imminent temperature differentials. Such rapid change of temperature generally occurs when the turbine or pump is exposed to a supercritical working fluid. The thermal shock may cause valves, blades, and other parts to crack and result in catastrophic damage to the unit.
The control of the turbine driven pump, such as a turbopump, is quite relevant to the operation and efficiency of an advanced Rankine cycle process. Generally, the control of the turbopump is often not precise enough to achieve the most efficient or maximum operating conditions without damaging the turbopump. Also, during operations, the turbopump generally requires proper lubrication and temperature regulation—often provided by a bearing or seal gas. The turbopump and/or turbomachinery components of the turbopump have very close tolerances and may be susceptible to immediate damage if there is an interruption of the bearing seal gas. If too much or not enough pressure is applied to a thrust bearing of the turbopump, then the rotor of the turbopump is likely to rub against stationary parts, such that the turbopump damages itself and ceases to operate.
Therefore, there is a need for a heat engine system, a turbopump system, and methods for generating mechanical and electrical energy, whereby pressures, temperatures, and lubrication within the turbomachinery is controlled at acceptable levels while maintaining or increasing the efficiency for operating the heat engine system.
Embodiments of the invention generally provide a heat engine system, a turbopump system, and methods for lubricating a turbopump in the heat engine system while generating mechanical and electrical energy. The systems and methods described herein provide proper lubrication and cooling to turbomachinery components of a turbopump by controlling pressures applied to a thrust bearing in the turbopump. The applied pressure on the thrust bearing may be controlled by a turbopump back-pressure regulator valve that may be modulated, controlled, or otherwise adjusted to maintain proper pressures within a plurality of bearing pockets disposed on each of two opposing surfaces of the thrust bearing. Pocket pressure ratios, such as a turbine-side pocket pressure ratio (P1) and a pump-side pocket pressure ratio (P2), may be monitored and adjusted by a process control system. In some exemplary embodiments, in order to prevent damage to the thrust bearing and/or other turbomachinery components, the systems and methods may utilize advanced control theory of sliding mode, the multi-variables of the pocket pressure ratios P1 and P2, and regulating the bearing fluid to maintain a supercritical state.
The heat engine system and the method described herein are configured to efficiently generate valuable mechanical and electrical energy from thermal energy, such as a heated stream (e.g., a waste heat stream). The heat engine system utilizes a working fluid in a supercritical state (e.g., sc-CO2) and/or a subcritical state (e.g., sub-CO2) contained within a working fluid circuit for capturing or otherwise absorbing thermal energy of the waste heat stream with one or more heat exchangers. The thermal energy is transformed to mechanical energy by a power turbine and/or a drive turbine and subsequently transformed to electrical energy by the power generator coupled to the power turbine. The heat engine system contains several integrated sub-systems managed by the process control system for maximizing the efficiency of the heat engine system while generating electricity.
In one exemplary embodiment, a turbopump system for circulating or pressurizing a working fluid within a working fluid circuit is provided and contains a turbopump, a drive turbine, a pump portion, a driveshaft, a thrust bearing, and a housing. The thrust bearing of the turbopump may be circumferentially disposed around the driveshaft and between the drive turbine and the pump portion. The housing of the turbopump may be disposed at least partially encompassing the driveshaft and the thrust bearing. The turbopump system also contains a bearing fluid supply line, a bearing fluid drain line, and a turbopump back-pressure regulator valve, and is operatively connected or coupled to the process control system. The process control system may be operatively connected to the turbopump back-pressure regulator valve and configured to adjust the turbopump back-pressure regulator valve with a control algorithm embedded in a computer system. The bearing fluid supply line may be fluidly coupled to the housing and configured to provide a bearing fluid into the housing and the bearing fluid drain line may be fluidly coupled to the housing and configured to remove the bearing fluid from the housing. The turbopump back-pressure regulator valve may be fluidly coupled to the bearing fluid drain line and configured to control flow through the bearing fluid drain line.
In some exemplary embodiments, the thrust bearing contains a cylindrical body, a turbine-side thrust face, a pump-side thrust face, a circumferential side surface, and a central orifice defined by and extending through the cylindrical body. The cylindrical body of the thrust bearing may have an inner portion and an outer portion aligned with a common central axis. The circumferential side surface may extend along the circumference of the cylindrical body and between the pump-side thrust face and the turbine-side thrust face. The central orifice extends through the cylindrical body along the central axis and may be configured to provide passage of the driveshaft therethrough.
The turbine-side thrust face has a plurality of bearing pockets, such as turbine-side bearing pockets, extending below the turbine-side thrust face and facing the drive turbine. Similarly, the pump-side thrust face has a plurality of bearing pockets, such as pump-side bearing pockets, extending below the pump-side thrust face and facing the pump portion. Generally, the plurality of pump-side bearing pockets contains from about 2 bearing pockets to about 12 bearing pockets, for example, about 6 bearing pockets, and the plurality of turbine-side bearing pockets contains from about 2 bearing pockets to about 12 bearing pockets, for example, about 6 bearing pockets.
In one or more exemplary embodiments, the control algorithm contains a sliding mode controller configured to provide a sliding mode control method for controlling the turbopump back-pressure regulator valve. The control algorithm generally contains a plurality of loop controllers configured to control the turbopump back-pressure regulator valve while adjusting values of pocket pressure ratios for bearing surfaces of the thrust bearing. The plurality of loop controllers may be configured to adjust, modulate, or otherwise control the turbopump back-pressure regulator valve in order maintain or obtain a balanced thrust of the turbopump. The control algorithm may be incorporated or otherwise contained within the computer system as part of the process control system.
The control algorithm may contain at least a primary governing loop controller, a secondary governing loop controller, and a tertiary governing loop controller. In some exemplary embodiments, the control algorithm may be configured to calculate valve positions for the turbopump back-pressure regulator valve for providing a pump-side pocket pressure ratio (P2) of about 0.25 or less with the primary governing loop controller, a turbine-side pocket pressure ratio (P1) of about 0.25 or greater with the secondary governing loop controller, and a bearing fluid supply pressure at or greater than a critical pressure value for the bearing fluid.
In one exemplary embodiment, the primary governing loop controller may be configured to adjust the turbopump back-pressure regulator valve for maintaining a pump-side pocket pressure ratio (P2) of about 0.30 or less, such as about 0.25 or less, such as about 0.20 or less, such as about 0.15 or less. In another exemplary embodiment, the primary governing loop controller may be configured to activate and adjust the turbopump back-pressure regulator valve if the pump-side pocket pressure ratio (P2) of about 0.25 or greater is detected by the process control system. The pump-side thrust face has a plurality of pump-side bearing pockets extending below the pump-side thrust face and facing the pump portion. The pump-side pocket pressure ratio (P2) may be measured in the pump-side bearing pockets. In one exemplary embodiment, the plurality of pump-side bearing pockets contains about 10 bearing pockets or less and the pump-side pocket pressure ratio (P2) is about 0.25 or less.
In one exemplary embodiment, the secondary governing loop controller may be configured to adjust the turbopump back-pressure regulator valve for maintaining the turbine-side pocket pressure ratio (P1) of about 0.30 or less, such as about 0.25 or less, such as about 0.20 or less, such as about 0.15 or less. In another exemplary embodiment, the secondary governing loop controller may be configured to activate and adjust the turbopump back-pressure regulator valve if the turbine-side pocket pressure ratio (P1) of about 0.25 or greater is detected by the process control system. The turbine-side pocket pressure ratio (P1) may be measured on a turbine-side thrust face of the thrust bearing. The turbine-side thrust face has a plurality of turbine-side bearing pockets extending below the turbine-side thrust face and facing the drive turbine. The turbine-side pocket pressure ratio (P1) may be measured and monitored in the turbine-side bearing pockets, such as with a probe or a sensor at the pressure tap. In one exemplary embodiment, the plurality of turbine-side bearing pockets contains about 10 bearing pockets or less and the turbine-side pocket pressure ratio (P1) is about 0.25 or less.
In one exemplary embodiment, the tertiary governing loop controller may be configured to activate and adjust the turbopump back-pressure regulator valve if an undesirable pressure of the bearing fluid is detected by the process control system. The undesirable pressure of the bearing fluid may be detected at or near the bearing fluid supply line. In one example, the undesirable pressure of the bearing fluid may be about 5% greater than the supercritical pressure of the bearing fluid or less. In another exemplary embodiment, the tertiary governing loop controller may be configured to adjust the turbopump back-pressure regulator valve for maintaining the bearing fluid in a supercritical state. In other exemplary embodiments, the tertiary governing loop controller may be configured to adjust the turbopump back-pressure regulator valve for maintaining a bearing drain pressure of about 1,055 psi or greater.
In one or more exemplary embodiments, the bearing fluid is carbon dioxide or at least contains carbon dioxide. In other embodiments, a portion of the working fluid may be diverted from the working fluid circuit or another source (e.g., storage tank or conditioning system) and utilized as the bearing fluid. In some exemplary embodiments, the bearing fluid and the working fluid contain carbon dioxide.
In another exemplary embodiment, a method for lubricating and/or cooling the turbopump in the heat engine system is provided and includes circulating and/or pressuring the working fluid throughout the working fluid circuit with the turbopump and transferring thermal energy from a heat source stream to the working fluid through at least one heat exchanger fluidly coupled to and in thermal communication with the high pressure side of the working fluid circuit and may be configured to be fluidly coupled to and in thermal communication with the heat source stream. The method further includes measuring and monitoring a turbine-side pocket pressure ratio (P1), a pump-side pocket pressure ratio (P2), a bearing fluid supply pressure, and a bearing fluid drain pressure via the process control system operatively coupled to the working fluid circuit, as described by one or more embodiments. The turbine-side pocket pressure ratio (P1) may be measured and/or monitored in at least one turbine-side bearing pocket of a plurality of turbine-side bearing pockets disposed on a turbine-side thrust face of the thrust bearing within the turbopump. The pump-side pocket pressure ratio (P2) may be measured and/or monitored in at least one pump-side bearing pocket of a plurality of pump-side bearing pockets disposed on a pump-side thrust face of the thrust bearing. The bearing fluid supply pressure may be measured and/or monitored in at least one bearing supply pressure line disposed upstream of the thrust bearing. The bearing fluid drain pressure may be measured and/or monitored in at least one bearing drain pressure line disposed downstream of the thrust bearing.
The method also includes controlling the turbopump back-pressure regulator valve by the primary governing loop controller embedded in the process control system. The turbopump back-pressure regulator valve may be fluidly coupled to a bearing fluid drain line disposed downstream of the thrust bearing and the primary governing loop controller may be configured to modulate the turbopump back-pressure regulator valve while adjusting the pump-side pocket pressure ratio (P2). The method further includes controlling the turbopump back-pressure regulator valve by the secondary governing loop controller embedded in the process control system. The secondary governing loop controller may be configured to modulate the turbopump back-pressure regulator valve while adjusting the turbine-side pocket pressure ratio (P1). The method also includes controlling the turbopump back-pressure regulator valve by the tertiary governing loop controller embedded in the process control system. The tertiary governing loop controller may be configured to modulate the turbopump back-pressure regulator valve while adjusting the bearing fluid supply pressure to be at or greater than a critical pressure value for the bearing fluid and maintain the bearing fluid in a supercritical state.
In another exemplary embodiment, a method for lubricating and/or cooling the turbopump in the heat engine system is provided and includes controlling the turbopump back-pressure regulator valve by the primary governing loop controller embedded in the process control system and modulating or controlling the turbopump back-pressure regulator valve while adjusting the pump-side pocket pressure ratio (P2). The turbopump back-pressure regulator valve may be fluidly coupled to a bearing fluid drain line disposed downstream of the thrust bearing. The primary governing loop controller may be configured to modulate the turbopump back-pressure regulator valve while adjusting the pump-side pocket pressure ratio (P2).
The method further includes detecting an undesirable value of the turbine-side pocket pressure ratio (P1) via the process control system and subsequently activating the secondary governing loop controller embedded in the process control system, deactivating the primary governing loop controller, and decreasing the turbine-side pocket pressure ratio (P1) to a desirable value. The undesirable value of the turbine-side pocket pressure ratio (P1) is greater than a predetermined threshold value of the turbine-side pocket pressure ratio (P1) and the desirable value of the turbine-side pocket pressure ratio (P1) is at or less than the predetermined threshold value of the turbine-side pocket pressure ratio (P1). The secondary governing loop controller may be configured to decrease the turbine-side pocket pressure ratio (P1) by modulating the turbopump back-pressure regulator valve.
The method also includes detecting an undesirable value of the bearing fluid supply pressure via the process control system and subsequently activating the tertiary governing loop controller embedded in the process control system, deactivating the primary governing loop controller or the secondary governing loop controller, and increasing the bearing fluid supply pressure to a desirable value. The undesirable value of the bearing fluid supply pressure is less than a critical pressure value for the bearing fluid and the desirable value of the bearing fluid supply pressure is at or greater than a critical pressure value for the bearing fluid. The tertiary governing loop controller may be configured to increase the bearing fluid supply pressure by modulating the turbopump back-pressure regulator valve while increasing the bearing fluid drain pressure.
In one exemplary embodiment, the method may further include adjusting the pump-side pocket pressure ratio (P2) by modulating the turbopump back-pressure regulator valve with the primary governing loop controller to obtain or maintain the pump-side pocket pressure ratio (P2) of about 0.25 or less. In another exemplary embodiment, the method may also include adjusting the turbine-side pocket pressure ratio (P1) by modulating the turbopump back-pressure regulator valve with the secondary governing loop controller to obtain or maintain the turbine-side pocket pressure ratio (P1) of about 0.25 or greater. In another exemplary embodiment, the method may further include adjusting the turbopump back-pressure regulator valve with the tertiary governing loop controller to obtain or maintain the bearing drain pressure of about 1,055 psi or greater. Generally, the bearing fluid supply pressure may be increased until the bearing fluid is in a supercritical state. In one exemplary embodiment, the method further includes regulating and maintaining the bearing fluid in contact with the thrust bearing to be in a supercritical state. In another exemplary embodiment, the method includes modulating the turbopump back-pressure regulator valve to control the flow of the bearing fluid passing through the bearing fluid drain line. The turbopump back-pressure regulator valve is adjusted to partially opened-positions that are within a range from about 35% to about 80% of being in a fully opened-position.
In another exemplary embodiment, a heat engine system contains a working fluid circuit, at least one heat exchanger, a power turbine or other expander, a rotating shaft, at least one of the recuperators, a condenser, a start pump, a turbopump system, and a process control system. The working fluid circuit may contain the working fluid and having a high pressure side and a low pressure side, wherein a portion of the working fluid circuit contains the working fluid in a supercritical state. The heat exchangers may be fluidly coupled to and in thermal communication with the high pressure side of the working fluid circuit, configured to be fluidly coupled to and in thermal communication with a heat source stream, and configured to transfer thermal energy from the heat source stream to the working fluid within the high pressure side.
The power turbine may be fluidly coupled to the working fluid circuit, disposed between the high pressure side and the low pressure side, configured to convert a pressure drop in the working fluid to mechanical energy. The rotating shaft may be coupled to the power turbine and configured to drive a device (e.g., a generator/alternator or a pump/compressor) with the mechanical energy. In one example, the rotating shaft may be coupled to and configured to drive a power generator. The recuperators may be fluidly coupled to the working fluid circuit and configured to transfer thermal energy from the working fluid in the low pressure side to the working fluid in the high pressure side. The start pump may be fluidly coupled to the working fluid circuit, disposed between the low pressure side and the high pressure side, and configured to circulate or pressurize the working fluid within the working fluid circuit.
The drive turbine of the turbopump may be disposed between the high and low pressure sides of the working fluid circuit and may be configured to convert a pressure drop in the working fluid to mechanical energy. The pump portion of the turbopump may be disposed between the high and low pressure sides of the working fluid circuit and may be configured to circulate or pressurize the working fluid within the working fluid circuit. The driveshaft of the turbopump may be coupled to and between the drive turbine and the pump portion, such that the drive turbine may be configured to drive the pump portion via the driveshaft.
In other exemplary embodiments disclosed herein, a method for generating mechanical and electrical energy with the heat engine system includes circulating the working fluid within the working fluid circuit, such that the working fluid circuit has the high pressure side and the low pressure side and at least a portion of the working fluid circuit contains the working fluid in a supercritical state (e.g., sc-CO2). The method also includes transferring thermal energy from the heat source stream to the working fluid by at least one heat exchanger fluidly coupled to and in thermal communication with the high pressure side of the working fluid circuit. The method further includes flowing the working fluid into the power turbine and converting the thermal energy from the working fluid to mechanical energy of the power turbine and converting the mechanical energy into electrical energy by a power generator coupled to the power turbine.
Embodiments of the present disclosure are best understood from the following detailed description when read with the accompanying Figures. It is emphasized that, in accordance with the standard practice in the industry, various features are not drawn to scale. In fact, the dimensions of the various features may be arbitrarily increased or reduced for clarity of discussion.
Embodiments of the invention generally provide heat engine systems and methods for generating electricity with such heat engine systems.
A heat source stream 110 may be flowed through heat exchangers 120, 130, and/or 150 disposed within the waste heat system 100. The heat exchangers 120, 130, and/or 150 are fluidly coupled to and in thermal communication with the high pressure side of the working fluid circuit 202, configured to be fluidly coupled to and in thermal communication with a heat source stream 110, and configured to transfer thermal energy from the heat source stream 110 to the working fluid. Thermal energy may be absorbed by the working fluid within the working fluid circuit 202 and the heated working fluid may be circulated through a power turbine 228 within the power generation system 220.
The power turbine 228 may be disposed between the high pressure side and the low pressure side of the working fluid circuit 202 and fluidly coupled to and in thermal communication with the working fluid. The power turbine 228 may be configured to convert thermal energy to mechanical energy by a pressure drop in the working fluid flowing between the high and the low pressure sides of the working fluid circuit 202. A power generator 240 is coupled to the power turbine 228 and configured to convert the mechanical energy into electrical energy, a power outlet 242 electrically coupled to the power generator 240 and configured to transfer the electrical energy from the power generator 240 to an electrical grid 244. The power generation system 220 generally contains a rotating shaft 230 and a gearbox 232 coupled between the power turbine 228 and the power generator 240.
The heat engine system 90 generally contains several pumps, such as a turbopump 260 and a start pump 280, disposed within the working fluid circuit 202 and fluidly coupled between the low pressure side and the high pressure side of the working fluid circuit 202. The turbopump 260 and the start pump 280 may be operative to circulate and/or pressurize the working fluid throughout the working fluid circuit 202. The start pump 280 has a pump portion 282 and a motor-drive portion 284. The start pump 280 is generally an electric motorized pump or a mechanical motorized pump, and may be a variable frequency driven pump.
The turbopump 260 contains a pump portion 262, a drive turbine 264, a driveshaft 267, a thrust bearing 310, and a bearing housing 268. The pump portion 262 may be disposed between the high and low pressure sides of the working fluid circuit 202 and may be configured to circulate or pressurize the working fluid within the working fluid circuit 202. The pump inlet on the pump portion 262 is generally disposed in the low pressure side and the pump outlet on the pump portion 262 is generally disposed in the high pressure side. The drive turbine 264 may be disposed between the high and low pressure sides of the working fluid circuit 202 and may be configured to convert a pressure drop in the working fluid to mechanical energy. The drive turbine 264 of the turbopump 260 may be fluidly coupled to the working fluid circuit 202 downstream of the heat exchanger 150 and the pump portion 262 of the turbopump 260 may be fluidly coupled to the working fluid circuit 202 upstream of the heat exchanger 120. The driveshaft 267 may be coupled to and between the drive turbine 264 and the pump portion 262, such that the drive turbine 264 may be configured to drive the pump portion 262 via the driveshaft 267. The thrust bearing 310 may be circumferentially disposed around the driveshaft 267 and between the drive turbine 264 and the pump portion 262. The bearing housing 268 may be disposed at least partially encompassing the driveshaft 267 and the thrust bearing 310.
In some embodiments, a secondary heat exchanger, such as a heat exchanger 150, may be utilized to provide heated, pressurized working fluid to the drive turbine 264 for powering the turbopump 260. The heat exchanger 150 may be fluidly coupled to and in thermal communication with the heat source stream 110 and independently fluidly coupled to and in thermal communication with the working fluid in the working fluid circuit 202. The heated, pressurized working fluid may be utilized to move, drive, or otherwise power the drive turbine 264.
The process control system 204 contains a control algorithm embedded in a computer system 206 and the control algorithm contains a governing loop controller. The governing controller is generally utilized to adjust values throughout the working fluid circuit 202 for controlling the temperature, pressure, flowrate, and/or mass of the working fluid at specified points therein. In some embodiments, the governing loop controller may configured to monitor and maintain, and/or to adjust if needed, desirable threshold values of pocket pressure ratios for a thrust bearing 310 (
The bearing fluid supply line 296 may be fluidly coupled to the bearing housing 268 and configured to provide a bearing fluid from the bearing fluid supply 292, into the bearing housing 268, and to the thrust bearing 310, as depicted in
In one or more exemplary embodiments, the bearing fluid is carbon dioxide or at least contains carbon dioxide. In other embodiments, a portion of the working fluid may be diverted from the working fluid circuit 202 or another source (e.g., storage tank or conditioning system) and utilized as the bearing fluid. Therefore, the bearing fluid and the working fluid may each independently contain carbon dioxide, such as supercritical carbon dioxide.
The turbopump back-pressure regulator valve 290 may be fluidly coupled to the bearing fluid drain line 298 and configured to control flow through the bearing fluid drain line 298, such as between the bearing housing 268 and the bearing fluid return 294. The turbopump back-pressure regulator valve 290 may be configured to control the pressure, via back-pressure, within the bearing fluid drain line 298, the bearing fluid drain manifold 299, the bearing drain pressure line 289, the turbine-side bearing pockets 332 and the pump-side bearing pockets 342, the bearing supply pressure lines 287, and the bearing fluid supply manifold 297.
In other exemplary embodiments, as depicted in
The turbine-side thrust face 330 has a plurality of bearing pockets, such as turbine-side bearing pockets 332, extending below the turbine-side thrust face 330 and facing the drive turbine 264. Similarly, the pump-side thrust face 340 has a plurality of bearing pockets, such as pump-side bearing pockets 342, extending below the pump-side thrust face 340 and facing the pump portion 262. Generally, the plurality of pump-side bearing pockets 342 contains from about 2 bearing pockets to about 12 bearing pockets and the plurality of turbine-side bearing pockets 332 contains from about 2 bearing pockets to about 12 bearing pockets. In one exemplary embodiment, the plurality of pump-side bearing pockets 342 contains from about 4 bearing pockets to about 8 bearing pockets, for example, about 6 bearing pockets and the plurality of turbine-side bearing pockets 332 contains from about 4 bearing pockets to about 8 bearing pockets, for example, about 6 bearing pockets.
In some exemplary embodiments, each bearing pocket of the turbine-side bearing pockets 332 and the pump-side bearing pockets 342 may have a surface area, as measured on the lower surface of the pocket area, within a range from about 0.05 in2 (about 0.32 cm2) to about 1 in2 (about 6.45 cm2), more narrowly within a range from about 0.08 in2 (about 0.52 cm2) to about 0.8 in2 (about 5.16 cm2), more narrowly within a range from about 0.1 in2 (about 0.65 cm2) to about 0.5 in2 (about 3.23 cm2), and more narrowly within a range from about 0.2 in2 (about 1.29 cm2) to about 0.3 in2 (about 2.94 cm2), for example, about 0.25 in2 (about 1.61 cm2). Also, each bearing pocket of the turbine-side bearing pockets 332 and the pump-side bearing pockets 342 may have a pocket depth within a range from about 0.010 in (about 0.25 mm) to about 0.060 in (about 1.62 mm), more narrowly within a range from about 0.015 in (about 0.38 mm) to about 0.050 in (about 1.27 mm), more narrowly within a range from about 0.020 in (about 0.51 mm) to about 0.040 in (about 1.02 mm), and more narrowly within a range from about 0.028 in (about 0.71 mm) to about 0.032 in (about 0.81 mm), for example, about 0.030 in (about 0.76 mm).
Each of the turbine-side bearing pockets 332 contains a pocket orifice 334 and each of the pump-side bearing pockets 342 contains a pocket orifice 344. The bearing pockets 332, 342 are configured to receive the bearing fluid from the bearing supply pressure lines 287 on each side of the thrust bearing 310 and to discharge the bearing fluid into their respective pocket orifices 334, 344. The pocket orifices 334, 344 extend from their respective bearing pockets 332, 342, through the inner portion 314, through the outer portion 316, out of the circumferential side surface 350 and to the bearing fluid drain manifold 299. In another exemplary embodiment, each of the turbine-side thrust face 330 and the pump-side thrust face 340 has at least one pressure tap, such as a pressure tap 336 in one of the turbine-side bearing pockets 332 and a pressure tap 346 in one of the pump-side bearing pockets 342.
The circumferential side surface 350 may extend along the circumference of the cylindrical body 312 and between the pump-side thrust face 340 and the turbine-side thrust face 330. The central orifice 322 extends through the cylindrical body 312 along the central axis 320 and may be configured to provide passage of the driveshaft 267 therethrough.
The turbopump 260 may further contain one or more pressure monitor ports 301, as depicted in
In one or more exemplary embodiments, the control algorithm contains a sliding mode controller configured to provide a sliding mode control method for controlling the turbopump back-pressure regulator valve 290. The control algorithm generally contains a plurality of loop controllers configured to control the turbopump back-pressure regulator valve 290 while adjusting values of pocket pressure ratios for bearing surfaces of the thrust bearing 310. The plurality of loop controllers may be configured to adjust, modulate, or otherwise control the turbopump back-pressure regulator valve 290 in order maintain or obtain a balanced thrust of the turbopump 260. The control algorithm may be incorporated or otherwise contained within the computer system 206 as part of the process control system 204.
The turbine-side pocket pressure ratio (P1), the pump-side pocket pressure ratio (P2), and the thrust force (Fthrust) may be calculated with the following equations:
P1=(PP1−Pdrain)/(Psupply−Pdrain),
P2=(PP2−Pdrain)/(Psupply−Pdrain), and
Fthrusf=TApocket(PP1−PP2),
where:
PP1 is the pocket pressure on the turbine-side thrust face 330 in the turbine-side bearing pocket 332 and may be measured at the pressure tap 336,
PP2 is the pocket pressure on the pump-side thrust face 340 in the pump-side bearing pocket 342 and may be measured at the pressure tap 346,
Psupply is the supply pressure of the bearing fluid and may be measured in the bearing supply pressure line 287, the bearing fluid supply manifold 297, and/or the bearing fluid supply line 296,
Pdrain is the drain pressure of the bearing fluid and may be measured in the bearing drain pressure line 289, the bearing fluid drain manifold 299, and/or the bearing fluid drain line 298,
Fthrust=is the thrust force, such as the thrust bearing load capacity in each direction, and
TApocket is the total area of the bearing pockets, which is the product of the number of—pocket is bearing pockets on one thrust face and the surface area of the bearing pocket.
In one exemplary embodiment, the primary governing loop controller may be configured to adjust the turbopump back-pressure regulator valve 290 for maintaining the pump-side pocket pressure ratio (P2) of about 0.30 or less, such as about 0.25 or less, such as about 0.20 or less, such as about 0.15 or less. In another exemplary embodiment, the primary governing loop controller may be configured to activate and adjust the turbopump back-pressure regulator valve 290 if a pump-side pocket pressure ratio (P2) of about 0.25 or greater is detected by the process control system 204. The pump-side pocket pressure ratio (P2) may be measured and monitored on a pump-side thrust face 340 of the thrust bearing 310, such as with a probe or a sensor at the pressure tap 346. The pump-side thrust face 340 has a plurality of pump-side bearing pockets 342 extending below the pump-side thrust face 340 and facing the pump portion 262. The pump-side pocket pressure ratio (P2) may be measured in the pump-side bearing pockets 342. In one exemplary embodiment, the plurality of pump-side bearing pockets 342 contains about 10 bearing pockets or less and the pump-side pocket pressure ratio (P2) is about 0.25 or less.
In one exemplary embodiment, the secondary governing loop controller may be configured to adjust the turbopump back-pressure regulator valve 290 for maintaining the turbine-side pocket pressure ratio (P1) of about 0.30 or less, such as about 0.25 or less, such as about 0.20 or less, such as about 0.15 or less. In another exemplary embodiment, the secondary governing loop controller may be configured to activate and adjust the turbopump back-pressure regulator valve 290 if the turbine-side pocket pressure ratio (P1) of about 0.25 or greater is detected by the process control system 204. The turbine-side pocket pressure ratio (P1) may be measured on a turbine-side thrust face 330 of the thrust bearing 310. The turbine-side thrust face 330 has a plurality of turbine-side bearing pockets 332 extending below the turbine-side thrust face 330 and facing the drive turbine 264. The turbine-side pocket pressure ratio (P1) may be measured and monitored in the turbine-side bearing pockets 332, such as with a probe or a sensor at the pressure tap 336. In one exemplary embodiment, the plurality of turbine-side bearing pockets 332 contains about 10 bearing pockets or less and the turbine-side pocket pressure ratio (P1) is about 0.25 or less.
In one exemplary embodiment, the tertiary governing loop controller may be configured to activate and adjust the turbopump back-pressure regulator valve 290 if an undesirable pressure of the bearing fluid is detected by the process control system 204. The undesirable pressure of the bearing fluid may be detected at or near the bearing fluid supply line 296. In one example, the undesirable pressure of the bearing fluid may be about 5% greater than the supercritical pressure of the bearing fluid or less.
In another exemplary embodiment, the tertiary governing loop controller may be configured to adjust the turbopump back-pressure regulator valve 290 for maintaining the bearing fluid in a supercritical state. In other exemplary embodiments, the tertiary governing loop controller may be configured to adjust the turbopump back-pressure regulator valve 290 for maintaining a bearing drain pressure of about 1,055 psi or greater. In other exemplary embodiments, the thrust force (Fthrust), such as the thrust bearing load capacity in each direction, may be within a range from about 4,000 pound-force (lbf) (about 17.8 kilonewton (kN) to about 8,000 lbf (about 35.6 kN), more narrowly within a range from about 5,000 lbf (about 22.2 kN) to about 7,000 lbf (about 31.1 kN), and more narrowly within a range from about 5,500 lbf (about 24.5 kN) to about 6,200 lbf (about 27.6 kN), for example, about 5,700 lbf (about 25.4 kN).
In another exemplary embodiment, a method for lubricating and/or cooling the turbopump 260 in the heat engine systems 90, 200 is provided and includes circulating and/or pressuring the working fluid throughout the working fluid circuit 202 with the turbopump 260, wherein the working fluid circuit 202 has a high pressure side and a low pressure side and at least a portion of the working fluid is in a supercritical state and transferring thermal energy from the heat source stream 110 to the working fluid through at least one of the heat exchangers 120, 130, 150. The heat exchangers 120, 130, 150 may be fluidly coupled to and in thermal communication with the high pressure side of the working fluid circuit 202 and fluidly coupled to and in thermal communication with the heat source stream 110.
The method further includes measuring and monitoring a turbine-side pocket pressure ratio (P1), a pump-side pocket pressure ratio (P2), a bearing fluid supply pressure, and a bearing fluid drain pressure via the process control system 204 operatively coupled to the working fluid circuit 202, wherein the turbine-side pocket pressure ratio (P1) may be measured and/or monitored in at least one turbine-side bearing pocket 332 of a plurality of turbine-side bearing pockets 332 disposed on a turbine-side thrust face 330 of the thrust bearing 310 within the turbopump 260, the pump-side pocket pressure ratio (P2) may be measured and/or monitored in at least one pump-side bearing pocket 342 of a plurality of pump-side bearing pockets 342 disposed on a pump-side thrust face 340 of the thrust bearing 310, the bearing fluid supply pressure may be measured and/or monitored in at least one bearing supply pressure line 287 disposed upstream of the thrust bearing 310, and the bearing fluid drain pressure may be measured and/or monitored in at least one bearing drain pressure line 289 disposed downstream of the thrust bearing 310.
The method also includes controlling the turbopump back-pressure regulator valve 290 by the primary governing loop controller embedded in the process control system 204. The turbopump back-pressure regulator valve 290 may be fluidly coupled to the bearing fluid drain line 298 disposed downstream of the thrust bearing 310 and the primary governing loop controller may be configured to modulate the turbopump back-pressure regulator valve 290 while adjusting the pump-side pocket pressure ratio (P2). The method further includes controlling the turbopump back-pressure regulator valve 290 by the secondary governing loop controller embedded in the process control system 204. The secondary governing loop controller may be configured to modulate the turbopump back-pressure regulator valve 290 while adjusting the turbine-side pocket pressure ratio (P1). The method also includes controlling the turbopump back-pressure regulator valve 290 by the tertiary governing loop controller embedded in the process control system 204. The tertiary governing loop controller may be configured to modulate the turbopump back-pressure regulator valve 290 while adjusting the bearing fluid supply pressure to be at or greater than a critical pressure value for the bearing fluid and maintain the bearing fluid in a supercritical state.
In another exemplary embodiment, a method for lubricating and/or cooling the turbopump 260 in the heat engine systems 90, 200 is provided and includes controlling the turbopump back-pressure regulator valve 290 by the primary governing loop controller embedded in the process control system 204, wherein the turbopump back-pressure regulator valve 290 may be fluidly coupled to the bearing fluid drain line 298 disposed downstream of the thrust bearing 310 and the primary governing loop controller may be configured to modulate the turbopump back-pressure regulator valve 290 while adjusting the pump-side pocket pressure ratio (P2).
The method further includes detecting an undesirable value of the turbine-side pocket pressure ratio (P1) via the process control system 204 and subsequently activating the secondary governing loop controller embedded in the process control system 204, deactivating the primary governing loop controller, and decreasing the turbine-side pocket pressure ratio (P1) to a desirable value. The undesirable value of the turbine-side pocket pressure ratio (P1) is greater than a predetermined threshold value of the turbine-side pocket pressure ratio (P1) and the desirable value of the turbine-side pocket pressure ratio (P1) is at or less than the predetermined threshold value of the turbine-side pocket pressure ratio (P1). The secondary governing loop controller may be configured to decrease the turbine-side pocket pressure ratio (P1) by modulating the turbopump back-pressure regulator valve 290. The method also includes detecting an undesirable value of the bearing fluid supply pressure via the process control system 204 and subsequently activating the tertiary governing loop controller embedded in the process control system 204, deactivating the primary governing loop controller or the secondary governing loop controller, and increasing the bearing fluid supply pressure to a desirable value. The undesirable value of the bearing fluid supply pressure is less than a critical pressure value for the bearing fluid and the desirable value of the bearing fluid supply pressure is at or greater than a critical pressure value for the bearing fluid. The tertiary governing loop controller may be configured to increase the bearing fluid supply pressure by modulating the turbopump back-pressure regulator valve 290 while increasing the bearing fluid drain pressure.
In one exemplary embodiment, the method may further include adjusting the pump-side pocket pressure ratio (P2) by modulating the turbopump back-pressure regulator valve 290 with the primary governing loop controller to obtain or maintain a pump-side pocket pressure ratio (P2) of about 0.25 or less. In another exemplary embodiment, the method may also include adjusting the turbine-side pocket pressure ratio (P1) by modulating the turbopump back-pressure regulator valve 290 with the secondary governing loop controller to obtain or maintain a turbine-side pocket pressure ratio (P1) of about 0.25 or greater. In another exemplary embodiment, the method may further include adjusting the turbopump back-pressure regulator valve 290 with the tertiary governing loop controller to obtain or maintain the bearing drain pressure of about 1,055 psi or greater.
Generally, the bearing fluid supply pressure may be increased until the bearing fluid is in a supercritical state. In one exemplary embodiment, the method further includes regulating and maintaining the bearing fluid in a supercritical state and in physical contact or thermal communication with the thrust bearing 310. The relatively cool temperature of the supercritical bearing fluid (e.g., sc-CO2) helps to prevent damage to the thrust bearing 310.
In another exemplary embodiment, the method includes modulating the turbopump back-pressure regulator valve 290 to control the flow of the bearing fluid passing through the bearing fluid drain line 298. The turbopump back-pressure regulator valve 290 is adjusted to partially opened-positions that are within a range from about 35% to about 80% of being in a fully opened-position. Therefore, the valve position or modulation range of the turbopump back-pressure regulator valve 290 may be within a range from about 10% to about 95% of being in a fully opened-position, more narrowly, within a range from about 20% to about 90% of being in a fully opened-position, more narrowly, within a range from about 30% to about 85% of being in a fully opened-position, and more narrowly, within a range from about 35% to about 80% of being in a fully opened-position. In one exemplary embodiment, such as at the start-up of the start pump 280, the valve position or modulation range of the turbopump back-pressure regulator valve 290 may be within a range from about 50% to about 75%, more narrowly, within a range from about 55% to about 70% of being in a fully opened-position, and more narrowly, within a range from about 60% to about 65% of being in a fully opened-position.
In one or more embodiments described herein,
The heat engine system 200 further contains the power turbine 228 disposed between the high pressure side and the low pressure side of the working fluid circuit 202, fluidly coupled to and in thermal communication with the working fluid, and configured to convert thermal energy to mechanical energy by a pressure drop in the working fluid flowing between the high and the low pressure sides of the working fluid circuit 202. The heat engine system 200 also contains a power generator 240 coupled to the power turbine 228 and configured to convert the mechanical energy into electrical energy, the power outlet 242 electrically coupled to the power generator 240 and configured to transfer the electrical energy from the power generator 240 to the electrical grid 244.
The heat engine system 200 further contains the turbopump 260 which has a drive turbine 264 and the pump portion 262. The pump portion 262 of the turbopump 260 may be fluidly coupled to the low pressure side of the working fluid circuit 202 by an inlet configured to receive the working fluid from the low pressure side of the working fluid circuit 202, fluidly coupled to the high pressure side of the working fluid circuit 202 by an outlet configured to release the working fluid into the high pressure side of the working fluid circuit 202, and configured to circulate the working fluid within the working fluid circuit 202. The drive turbine 264 of the turbopump 260 may be fluidly coupled to the high pressure side of the working fluid circuit 202 by an inlet configured to receive the working fluid from the high pressure side of the working fluid circuit 202, fluidly coupled to the low pressure side of the working fluid circuit 202 by an outlet configured to release the working fluid into the low pressure side of the working fluid circuit 202, and configured to rotate the pump portion 262 of the turbopump 260.
In some embodiments, the heat exchanger 150 may be configured to be fluidly coupled to and in thermal communication with the heat source stream 110. Also, the heat exchanger 150 may be fluidly coupled to and in thermal communication with the high pressure side of the working fluid circuit 202. Therefore, thermal energy may be transferred from the heat source stream 110, through the heat exchanger 150, and to the working fluid within the working fluid circuit 202. The heat exchanger 150 may be fluidly coupled to the working fluid circuit 202 upstream of the outlet of the pump portion 262 of the turbopump 260 and downstream of the inlet of the drive turbine 264 of the turbopump 260. The drive turbine throttle valve 263 may be fluidly coupled to the working fluid circuit 202 downstream of the heat exchanger 150 and upstream of the inlet of the drive turbine 264 of the turbopump 260. The working fluid containing the absorbed thermal energy flows from the heat exchanger 150 to the drive turbine 264 of the turbopump 260 via the drive turbine throttle valve 263. Therefore, in some embodiments, the drive turbine throttle valve 263 may be utilized to control the flowrate of the heated working fluid flowing from the heat exchanger 150 to the drive turbine 264 of the turbopump 260.
In some embodiments, the recuperator 216 may be fluidly coupled to the working fluid circuit 202 and configured to transfer thermal energy from the working fluid within the low pressure side to the working fluid within the high pressure side of the working fluid circuit 202. In other embodiments, a recuperator 218 may be fluidly coupled to the working fluid circuit 202 downstream of the outlet of the pump portion 262 of the turbopump 260 and upstream of the heat exchanger 150 and configured to transfer thermal energy from the working fluid within the low pressure side to the working fluid within the high pressure side of the working fluid circuit 202.
The waste heat system 100 also contains an inlet 104 for receiving the heat source stream 110 and an outlet 106 for passing the heat source stream 110 out of the waste heat system 100. The heat source stream 110 flows through and from the inlet 104, through the heat exchanger 120, through one or more additional heat exchangers, if fluidly coupled to the heat source stream 110, and to and through the outlet 106. In some examples, the heat source stream 110 flows through and from the inlet 104, through the heat exchangers 120, 150, and 130, respectively, and to and through the outlet 106. The heat source stream 110 may be routed to flow through the heat exchangers 120, 130, 150, and/or additional heat exchangers in other desired orders.
The heat source stream 110 may be a waste heat stream such as, but not limited to, gas turbine exhaust stream, industrial process exhaust stream, or other combustion product exhaust streams, such as furnace or boiler exhaust streams. The heat source stream 110 may be at a temperature within a range from about 100° C. to about 1,000° C., or greater than 1,000° C., and in some examples, within a range from about 200° C. to about 800° C., more narrowly within a range from about 300° C. to about 700° C., and more narrowly within a range from about 400° C. to about 600° C., for example, within a range from about 500° C. to about 550° C. The heat source stream 110 may contain air, carbon dioxide, carbon monoxide, water or steam, nitrogen, oxygen, argon, derivatives thereof, or mixtures thereof. In some embodiments, the heat source stream 110 may derive thermal energy from renewable sources of thermal energy, such as solar or geothermal sources.
In some embodiments, the types of working fluid that may be circulated, flowed, or otherwise utilized in the working fluid circuit 202 of the heat engine system 200 include carbon oxides, hydrocarbons, alcohols, ketones, halogenated hydrocarbons, ammonia, amines, aqueous, or combinations thereof. Exemplary working fluids that may be utilized in the heat engine system 200 include carbon dioxide, ammonia, methane, ethane, propane, butane, ethylene, propylene, butylene, acetylene, methanol, ethanol, acetone, methyl ethyl ketone, water, derivatives thereof, or mixtures thereof. Halogenated hydrocarbons may include hydrochlorofluorocarbons (HCFCs), hydrofluorocarbons (HFCs) (e.g., 1,1,1,3,3-pentafluoropropane (R245fa)), fluorocarbons, derivatives thereof, or mixtures thereof.
In many embodiments described herein, the working fluid circulated, flowed, or otherwise utilized in the working fluid circuit 202 of the heat engine system 200, and the other exemplary circuits disclosed herein, may be or may contain carbon dioxide (CO2) and mixtures containing carbon dioxide. Generally, at least a portion of the working fluid circuit 202 contains the working fluid in a supercritical state (e.g., sc-CO2). Carbon dioxide utilized as the working fluid or contained in the working fluid for power generation cycles has many advantages over other compounds typical used as working fluids, since carbon dioxide has the properties of being non-toxic and non-flammable and is also easily available and relatively inexpensive. Due in part to a relatively high working pressure of carbon dioxide, a carbon dioxide system may be much more compact than systems using other working fluids. The high density and volumetric heat capacity of carbon dioxide with respect to other working fluids makes carbon dioxide more “energy dense” meaning that the size of all system components can be considerably reduced without losing performance. It should be noted that use of the terms carbon dioxide (CO2), supercritical carbon dioxide (sc-CO2), or subcritical carbon dioxide (sub-CO2) is not intended to be limited to carbon dioxide of any particular type, source, purity, or grade. For example, industrial grade carbon dioxide may be contained in and/or used as the working fluid without departing from the scope of the disclosure.
In other exemplary embodiments, the working fluid in the working fluid circuit 202 may be a binary, ternary, or other working fluid blend. The working fluid blend or combination can be selected for the unique attributes possessed by the fluid combination within a heat recovery system, as described herein. For example, one such fluid combination includes a liquid absorbent and carbon dioxide mixture enabling the combined fluid to be pumped in a liquid state to high pressure with less energy input than required to compress carbon dioxide. In another exemplary embodiment, the working fluid may be a combination of carbon dioxide (e.g., sub-CO2 or sc-CO2) and one or more other miscible fluids or chemical compounds. In yet other exemplary embodiments, the working fluid may be a combination of carbon dioxide and propane, or carbon dioxide and ammonia, without departing from the scope of the disclosure.
The working fluid circuit 202 generally has a high pressure side and a low pressure side and contains a working fluid circulated within the working fluid circuit 202. The use of the term “working fluid” is not intended to limit the state or phase of matter of the working fluid. For instance, the working fluid or portions of the working fluid may be in a liquid phase, a gas phase, a fluid phase, a subcritical state, a supercritical state, or any other phase or state at any one or more points within the heat engine system 200 or thermodynamic cycle. In one or more embodiments, the working fluid is in a supercritical state over certain portions of the working fluid circuit 202 of the heat engine system 200 (e.g., a high pressure side) and in a subcritical state over other portions of the working fluid circuit 202 of the heat engine system 200 (e.g., a low pressure side).
Generally, the high pressure side of the working fluid circuit 202 contains the working fluid (e.g., sc-CO2) at a pressure of about 15 MPa or greater, such as about 17 MPa or greater or about 20 MPa or greater. In some examples, the high pressure side of the working fluid circuit 202 may have a pressure within a range from about 15 MPa to about 30 MPa, more narrowly within a range from about 16 MPa to about 26 MPa, more narrowly within a range from about 17 MPa to about 25 MPa, and more narrowly within a range from about 17 MPa to about 24 MPa, such as about 23.3 MPa. In other examples, the high pressure side of the working fluid circuit 202 may have a pressure within a range from about 20 MPa to about 30 MPa, more narrowly within a range from about 21 MPa to about 25 MPa, and more narrowly within a range from about 22 MPa to about 24 MPa, such as about 23 MPa.
The low pressure side of the working fluid circuit 202 contains the working fluid (e.g., CO2 or sub-CO2) at a pressure of less than 15 MPa, such as about 12 MPa or less or about 10 MPa or less. In some examples, the low pressure side of the working fluid circuit 202 may have a pressure within a range from about 4 MPa to about 14 MPa, more narrowly within a range from about 6 MPa to about 13 MPa, more narrowly within a range from about 8 MPa to about 12 MPa, and more narrowly within a range from about 10 MPa to about 11 MPa, such as about 10.3 MPa. In other examples, the low pressure side of the working fluid circuit 202 may have a pressure within a range from about 2 MPa to about 10 MPa, more narrowly within a range from about 4 MPa to about 8 MPa, and more narrowly within a range from about 5 MPa to about 7 MPa, such as about 6 MPa.
In some examples, the high pressure side of the working fluid circuit 202 may have a pressure within a range from about 17 MPa to about 23.5 MPa, and more narrowly within a range from about 23 MPa to about 23.3 MPa while the low pressure side of the working fluid circuit 202 may have a pressure within a range from about 8 MPa to about 11 MPa, and more narrowly within a range from about 10.3 MPa to about 11 MPa.
The heat engine system 200 further contains the power turbine 228 disposed between the high pressure side and the low pressure side of the working fluid circuit 202, disposed downstream of the heat exchanger 120, and fluidly coupled to and in thermal communication with the working fluid. The power turbine 228 may be configured to convert a pressure drop in the working fluid to mechanical energy whereby the absorbed thermal energy of the working fluid is transformed to mechanical energy of the power turbine 228. Therefore, the power turbine 228 is an expansion device capable of transforming a pressurized fluid into mechanical energy, generally, transforming high temperature and pressure fluid into mechanical energy, such as rotating a shaft.
The power turbine 228 may contain or be a turbine, a turbo, an expander, or another device for receiving and expanding the working fluid discharged from the heat exchanger 120. The power turbine 228 may have an axial construction or radial construction and may be a single-staged device or a multi-staged device. Exemplary turbines that may be utilized in power turbine 228 include an expansion device, a geroler, a gerotor, a valve, other types of positive displacement devices such as a pressure swing, a turbine, a turbo, or any other device capable of transforming a pressure or pressure/enthalpy drop in a working fluid into mechanical energy. A variety of different types of expanding devices may be utilized as the power turbine 228 to achieve various performance properties.
The power turbine 228 is generally coupled to the power generator 240 by the rotating shaft 230. The gearbox 232 is generally disposed between the power turbine 228 and the power generator 240 and adjacent or encompassing the rotating shaft 230. The rotating shaft 230 may be a single piece or contain two or more pieces coupled together. In one or more examples, a first segment of the rotating shaft 230 extends from the power turbine 228 to the gearbox 232, a second segment of the rotating shaft 230 extends from the gearbox 232 to the power generator 240, and multiple gears are disposed between and coupled to the two segments of the rotating shaft 230 within the gearbox 232.
In some configurations, the heat engine system 200 also provides for the delivery of a portion of the working fluid, seal gas, bearing gas, air, or other gas into a chamber or housing, such as a housing 238 within the power generation system 220 for purposes of cooling one or more parts of the power turbine 228. In other configurations, the rotating shaft 230 includes a seal assembly (not shown) designed to prevent or capture any working fluid leakage from the power turbine 228. Additionally, a working fluid recycle system may be implemented along with the seal assembly to recycle seal gas back into the working fluid circuit 202 of the heat engine system 200.
The power generator 240 may be a generator, an alternator (e.g., permanent magnet alternator), or other device for generating electrical energy, such as transforming mechanical energy from the rotating shaft 230 and the power turbine 228 to electrical energy. The power outlet 242 may be electrically coupled to the power generator 240 and configured to transfer the generated electrical energy from the power generator 240 and to the electrical grid 244. The electrical grid 244 may be or include an electrical grid, an electrical bus (e.g., plant bus), power electronics, other electric circuits, or combinations thereof. The electrical grid 244 generally contains at least one alternating current bus, alternating current grid, alternating current circuit, or combinations thereof. In one example, the power generator 240 is a generator and is electrically and operatively connected or coupled to the electrical grid 244 via the power outlet 242. In another example, the power generator 240 is an alternator and is electrically and operatively connected to power electronics (not shown) via the power outlet 242. In another example, the power generator 240 is electrically connected to power electronics which are electrically connected to the power outlet 242.
The power electronics may be configured to convert the electrical power into desirable forms of electricity by modifying electrical properties, such as voltage, current, or frequency. The power electronics may include converters or rectifiers, inverters, transformers, regulators, controllers, switches, resisters, storage devices, and other power electronic components and devices. In other embodiments, the power generator 240 may contain, be coupled with, or be other types of load receiving equipment, such as other types of electrical generation equipment, rotating equipment, a gearbox (e.g., the gearbox 232), or other device configured to modify or convert the shaft work created by the power turbine 228. In one embodiment, the power generator 240 is in fluid communication with a cooling loop having a radiator and a pump for circulating a cooling fluid, such as water, thermal oils, and/or other suitable refrigerants. The cooling loop may be configured to regulate the temperature of the power generator 240 and power electronics by circulating the cooling fluid to draw away generated heat.
The heat engine system 200 also provides for the delivery of a portion of the working fluid into a chamber or housing of the power turbine 228 for purposes of cooling one or more parts of the power turbine 228. In one embodiment, due to the potential need for dynamic pressure balancing within the power generator 240, the selection of the site within the heat engine system 200 from which to obtain a portion of the working fluid is critical because introduction of this portion of the working fluid into the power generator 240 should respect or not disturb the pressure balance and stability of the power generator 240 during operation. Therefore, the pressure of the working fluid delivered into the power generator 240 for purposes of cooling is the same or substantially the same as the pressure of the working fluid at an inlet of the power turbine 228. The working fluid is conditioned to be at a desired temperature and pressure prior to being introduced into the power turbine 228. A portion of the working fluid, such as the spent working fluid, exits the power turbine 228 at an outlet of the power turbine 228 and is directed to one or more heat exchangers or recuperators, such as recuperators 216 and 218. The recuperators 216 and 218 may be fluidly coupled to the working fluid circuit 202 in series with each other. The recuperators 216 and 218 are operative to transfer thermal energy between the high pressure side and the low pressure side of the working fluid circuit 202.
In one embodiment, the recuperator 216 is fluidly coupled to the low pressure side of the working fluid circuit 202, disposed downstream of a working fluid outlet on the power turbine 228, and disposed upstream of the recuperator 218 and/or the condenser 274. The recuperator 216 may be configured to remove at least a portion of thermal energy from the working fluid discharged from the power turbine 228. In addition, the recuperator 216 is also fluidly coupled to the high pressure side of the working fluid circuit 202, disposed upstream of the heat exchanger 120 and/or a working fluid inlet on the power turbine 228, and disposed downstream of the heat exchanger 130. The recuperator 216 may be configured to increase the amount of thermal energy in the working fluid prior to flowing into the heat exchanger 120 and/or the power turbine 228. Therefore, the recuperator 216 is operative to transfer thermal energy between the high pressure side and the low pressure side of the working fluid circuit 202. In some examples, the recuperator 216 may be a heat exchanger configured to cool the low pressurized working fluid discharged or downstream of the power turbine 228 while heating the high pressurized working fluid entering into or upstream of the heat exchanger 120 and/or the power turbine 228.
Similarly, in another embodiment, the recuperator 218 is fluidly coupled to the low pressure side of the working fluid circuit 202, disposed downstream of a working fluid outlet on the power turbine 228 and/or the recuperator 216, and disposed upstream of the condenser 274. The recuperator 218 may be configured to remove at least a portion of thermal energy from the working fluid discharged from the power turbine 228 and/or the recuperator 216. In addition, the recuperator 218 is also fluidly coupled to the high pressure side of the working fluid circuit 202, disposed upstream of the heat exchanger 150 and/or a working fluid inlet on the drive turbine 264 of turbopump 260, and disposed downstream of a working fluid outlet on the pump portion 262 of the turbopump 260. The recuperator 218 may be configured to increase the amount of thermal energy in the working fluid prior to flowing into the heat exchanger 150 and/or the drive turbine 264. Therefore, the recuperator 218 is operative to transfer thermal energy between the high pressure side and the low pressure side of the working fluid circuit 202. In some examples, the recuperator 218 may be a heat exchanger configured to cool the low pressurized working fluid discharged or downstream of the power turbine 228 and/or the recuperator 216 while heating the high pressurized working fluid entering into or upstream of the heat exchanger 150 and/or the drive turbine 264.
A cooler or a condenser 274 may be fluidly coupled to and in thermal communication with the low pressure side of the working fluid circuit 202 and may be configured or operative to control a temperature of the working fluid in the low pressure side of the working fluid circuit 202. The condenser 274 may be disposed downstream of the recuperators 216 and 218 and upstream of the start pump 280 and the turbopump 260. The condenser 274 receives the cooled working fluid from the recuperator 218 and further cools and/or condenses the working fluid which may be recirculated throughout the working fluid circuit 202. In many examples, the condenser 274 is a cooler and may be configured to control a temperature of the working fluid in the low pressure side of the working fluid circuit 202 by transferring thermal energy from the working fluid in the low pressure side to a cooling loop or system outside of the working fluid circuit 202.
A cooling media or fluid is generally utilized in the cooling loop or system by the condenser 274 for cooling the working fluid and removing thermal energy outside of the working fluid circuit 202. The cooling media or fluid flows through, over, or around while in thermal communication with the condenser 274. Thermal energy in the working fluid is transferred to the cooling fluid via the condenser 274. Therefore, the cooling fluid is in thermal communication with the working fluid circuit 202, but not fluidly coupled to the working fluid circuit 202. The condenser 274 may be fluidly coupled to the working fluid circuit 202 and independently fluidly coupled to the cooling fluid. The cooling fluid may contain one or multiple compounds and may be in one or multiple states of matter. The cooling fluid may be a media or fluid in a gaseous state, a liquid state, a subcritical state, a supercritical state, a suspension, a solution, derivatives thereof, or combinations thereof.
In many examples, the condenser 274 is generally fluidly coupled to a cooling loop or system (not shown) that receives the cooling fluid from a cooling fluid return 278a and returns the warmed cooling fluid to the cooling loop or system via a cooling fluid supply 278b. The cooling fluid may be water, carbon dioxide, or other aqueous and/or organic fluids (e.g., alcohols and/or glycols), air or other gases, or various mixtures thereof that is maintained at a lower temperature than the temperature of the working fluid. In other examples, the cooling media or fluid contains air or another gas exposed to the condenser 274, such as an air steam blown by a motorized fan or blower. A filter 276 may be disposed along and in fluid communication with the cooling fluid line at a point downstream of the cooling fluid supply 278b and upstream of the condenser 274. In some examples, the filter 276 may be fluidly coupled to the cooling fluid line within the process system 210.
The heat engine system 200 further contains several pumps, such as the turbopump 260 and the start pump 280, disposed within the working fluid circuit 202 and fluidly coupled between the low pressure side and the high pressure side of the working fluid circuit 202. The turbopump 260 and the start pump 280 are operative to circulate the working fluid throughout the working fluid circuit 202. The start pump 280 is generally a motorized pump and may be utilized to initially pressurize and circulate the working fluid in the working fluid circuit 202. Once a predetermined pressure, temperature, and/or flowrate of the working fluid is obtained within the working fluid circuit 202, the start pump 280 may be taken off line, idled, or turned off and the turbopump 260 is utilize to circulate the working fluid during the electricity generation process. The working fluid may enter the pump portion 262 of the turbopump 260 and the pump portion 282 of the start pump 280 from the low pressure side of the working fluid circuit 202 and may be discharged from the pump portions 262, 282 into the high pressure side of the working fluid circuit 202.
The start pump 280 may be a motorized pump, such as an electric motorized pump, a mechanical motorized pump, or other type of pump. Generally, the start pump 280 may be a variable frequency motorized drive pump and contains a pump portion 282 and a motor-drive portion 284. The motor-drive portion 284 of the start pump 280 contains a motor and a drive including a driveshaft and gears. In some examples, the motor-drive portion 284 has a variable frequency drive, such that the speed of the motor may be regulated by the drive. The pump portion 282 of the start pump 280 is driven by the motor-drive portion 284 coupled thereto. The pump portion 282 has an inlet for receiving the working fluid from the low pressure side of the working fluid circuit 202, such as from the condenser 274 and/or the mass management system 270. The pump portion 282 has an outlet for releasing the working fluid into the high pressure side of the working fluid circuit 202.
A start pump inlet valve 283 and a start pump outlet valve 285 may be utilized to control the flow of the working fluid passing through the start pump 280. The start pump inlet valve 283 may be fluidly coupled to the low pressure side of the working fluid circuit 202 upstream of the pump portion 282 of the start pump 280 and may be utilized to control the flowrate of the working fluid entering the inlet of the pump portion 282. The start pump outlet valve 285 may be fluidly coupled to the high pressure side of the working fluid circuit 202 downstream of the pump portion 282 of the start pump 280 and may be utilized to control the flowrate of the working fluid exiting the outlet of the pump portion 282.
The drive turbine 264 of the turbopump 260 may be driven by heated working fluid, such as the working fluid flowing from the heat exchanger 150. The drive turbine 264 is fluidly coupled to the high pressure side of the working fluid circuit 202 by an inlet configured to receive the working fluid from the high pressure side of the working fluid circuit 202, such as flowing from the heat exchanger 150. The drive turbine 264 is fluidly coupled to the low pressure side of the working fluid circuit 202 by an outlet configured to release the working fluid into the low pressure side of the working fluid circuit 202.
The pump portion 262 of the turbopump 260 may be driven via the driveshaft 267 coupled to the drive turbine 264. The pump portion 262 of the turbopump 260 may be fluidly coupled to the low pressure side of the working fluid circuit 202 by an inlet configured to receive the working fluid from the low pressure side of the working fluid circuit 202. The inlet of the pump portion 262 may be configured to receive the working fluid from the low pressure side of the working fluid circuit 202, such as from the condenser 274 and/or the mass management system 270. Also, the pump portion 262 may be fluidly coupled to the high pressure side of the working fluid circuit 202 by an outlet configured to release the working fluid into the high pressure side of the working fluid circuit 202 and circulate the working fluid within the working fluid circuit 202.
The driveshaft 267 may be a single piece or contain two or more pieces coupled together. In one or more examples, a first segment of the driveshaft 267 extends from the drive turbine 264 to the gearbox, a second segment of the rotating shaft 230 extends from the gearbox to the pump portion 262, and multiple gears are disposed between and coupled to the two segments of the driveshaft 267 within the gearbox.
In one configuration, the working fluid released from the outlet on the drive turbine 264 is returned into the working fluid circuit 202 downstream of the recuperator 216 and upstream of the recuperator 218. In one or more embodiments, the turbopump 260, including piping and valves, is optionally disposed on a turbopump skid 266, as depicted in
A drive turbine bypass valve 265 is generally coupled between and in fluid communication with a fluid line extending from the inlet on the drive turbine 264 with a fluid line extending from the outlet on the drive turbine 264. The drive turbine bypass valve 265 is generally opened to bypass the turbopump 260 while using the start pump 280 during the initial stages of generating electricity with the heat engine system 200. Once a predetermined pressure and temperature of the working fluid is obtained within the working fluid circuit 202, the drive turbine bypass valve 265 is closed and the heated working fluid is flowed through the drive turbine 264 to start the turbopump 260.
A drive turbine throttle valve 263 may be coupled between and in fluid communication with a fluid line extending from the heat exchanger 150 to the inlet on the drive turbine 264 of the turbopump 260. The drive turbine throttle valve 263 may be configured to modulate the flow of the heated working fluid into the drive turbine 264 which in turn—may be utilized to adjust the flow of the working fluid throughout the working fluid circuit 202. Additionally, a valve 293 may be utilized to control the flow of the working fluid passing through the high pressure side of the recuperator 218 and through the heat exchanger 150. The additional thermal energy absorbed by the working fluid from the recuperator 218 and the heat exchanger 150 is transferred to the drive turbine 264 for powering or otherwise driving the pump portion 262 of the turbopump 260. The valve 293 may be utilized to provide and/or control back pressure for the drive turbine 264 of the turbopump 260.
A drive turbine attemperator valve 295 may be fluidly coupled to the working fluid circuit 202 via an attemperator bypass line 291 disposed between the outlet on the pump portion 262 of the turbopump 260 and the inlet on the drive turbine 264 and/or disposed between the outlet on the pump portion 282 of the start pump 280 and the inlet on the drive turbine 264. The attemperator bypass line 291 and the drive turbine attemperator valve 295 may be configured to flow the working fluid from the pump portion 262 or 282, around and avoid the recuperator 218 and the heat exchanger 150, and to the drive turbine 264, such as during a warm-up or cool-down step of the turbopump 260. The attemperator bypass line 291 and the drive turbine attemperator valve 295 may be utilized to warm the working fluid with the drive turbine 264 while avoiding the thermal heat from the heat source stream 110 via the heat exchangers, such as the heat exchanger 150.
The check valve 261 may be disposed downstream of the outlet of the pump portion 262 of the turbopump 260 and the check valve 281 may be disposed downstream of the outlet of the pump portion 282 of the start pump 280. The check valves 261 and 281 are flow control safety valves and may be utilized to release an over-pressure, regulate the directional flow, or prohibit backflow of the working fluid within the working fluid circuit 202. The check valve 261 may be configured to prevent the working fluid from flowing upstream towards or into the outlet of the pump portion 262 of the turbopump 260. Similarly, check valve 281 may be configured to prevent the working fluid from flowing upstream towards or into the outlet of the pump portion 282 of the start pump 280.
The drive turbine throttle valve 263 is fluidly coupled to the working fluid circuit 202 upstream of the inlet of the drive turbine 264 of the turbopump 260 and configured to control a flow of the working fluid flowing into the drive turbine 264. The power turbine bypass valve 219 is fluidly coupled to the power turbine bypass line 208 and configured to modulate, adjust, or otherwise control the working fluid flowing through the power turbine bypass line 208 for controlling the flowrate of the working fluid entering the power turbine 228.
The power turbine bypass line 208 is fluidly coupled to the working fluid circuit 202 at a point upstream of an inlet of the power turbine 228 and at a point downstream of an outlet of the power turbine 228. The power turbine bypass line 208 may be configured to flow the working fluid around and avoid the power turbine 228 when the power turbine bypass valve 219 is in an open-position. The flowrate and the pressure of the working fluid flowing into the power turbine 228 may be reduced or stopped by adjusting the power turbine bypass valve 219 to the open-position. Alternatively, the flowrate and the pressure of the working fluid flowing into the power turbine 228 may be increased or started by adjusting the power turbine bypass valve 219 to the closed-position due to the backpressure formed through the power turbine bypass line 208.
The power turbine bypass valve 219 and the drive turbine throttle valve 263 may be independently controlled by the process control system 204 that is communicably connected, wired and/or wirelessly, with the power turbine bypass valve 219, the drive turbine throttle valve 263, and other parts of the heat engine system 200. The process control system 204 is operatively connected to the working fluid circuit 202 and a mass management system 270 and is enabled to monitor and control multiple process operation parameters of the heat engine system 200.
In one or more embodiments, the working fluid circuit 202 provides a bypass flowpath for the start pump 280 via the start pump bypass line 224 and a start pump bypass valve 254, as well as a bypass flowpath for the turbopump 260 via the turbopump bypass line 226 and a turbopump bypass valve 256. One end of the start pump bypass line 224 is fluidly coupled to an outlet of the pump portion 282 of the start pump 280 and the other end of the start pump bypass line 224 is fluidly coupled to a fluid line 229. Similarly, one end of a turbopump bypass line 226 is fluidly coupled to an outlet of the pump portion 262 of the turbopump 260 and the other end of the turbopump bypass line 226 is coupled to the start pump bypass line 224. In some configurations, the start pump bypass line 224 and the turbopump bypass line 226 merge together as a single line upstream of coupling to a fluid line 229. The fluid line 229 extends between and is fluidly coupled to the recuperator 218 and the condenser 274. The start pump bypass valve 254 may be disposed along the start pump bypass line 224 and fluidly coupled between the low pressure side and the high pressure side of the working fluid circuit 202 when in a closed-position. Similarly, the turbopump bypass valve 256 may be disposed along the turbopump bypass line 226 and fluidly coupled between the low pressure side and the high pressure side of the working fluid circuit 202 when in a closed-position.
The heat engine system 200 further contains a drive turbine throttle valve 263 fluidly coupled to the working fluid circuit 202 upstream of the inlet of the drive turbine 264 of the turbopump 260 and configured to modulate a flow of the working fluid flowing into the drive turbine 264, a power turbine bypass line 208 fluidly coupled to the working fluid circuit 202 upstream of an inlet of the power turbine 228, fluidly coupled to the working fluid circuit 202 downstream of an outlet of the power turbine 228, and configured to flow the working fluid around and avoid the power turbine 228, a power turbine bypass valve 219 fluidly coupled to the power turbine bypass line 208 and configured to modulate a flow of the working fluid flowing through the power turbine bypass line 208 for controlling the flowrate of the working fluid entering the power turbine 228, and a process control system 204 operatively connected to the heat engine system 90 or 200, wherein the process control system 204 may be configured to adjust the drive turbine throttle valve 263 and the power turbine bypass valve 219.
A heat exchanger bypass line 160 is fluidly coupled to a fluid line 131 of the working fluid circuit 202 upstream of the heat exchangers 120, 130, and/or 150 by a heat exchanger bypass valve 162, as illustrated in
In one or more embodiments, the working fluid circuit 202 provides release valves 213a, 213b, 213c, and 213d, as well as release outlets 214a, 214b, 214c, and 214d, respectively in fluid communication with each other. Generally, the release valves 213a, 213b, 213c, and 213d remain closed during the electricity generation process, but may be configured to automatically open to release an over-pressure at a predetermined value within the working fluid. Once the working fluid flows through the valve 213a, 213b, 213c, or 213d, the working fluid is vented through the respective release outlet 214a, 214b, 214c, or 214d. The release outlets 214a, 214b, 214c, and 214d may provide passage of the working fluid into the ambient surrounding atmosphere. Alternatively, the release outlets 214a, 214b, 214c, and 214d may provide passage of the working fluid into a recycling or reclamation step that generally includes capturing, condensing, and storing the working fluid.
The release valve 213a and the release outlet 214a are fluidly coupled to the working fluid circuit 202 at a point disposed between the heat exchanger 120 and the power turbine 228. The release valve 213b and the release outlet 214b are fluidly coupled to the working fluid circuit 202 at a point disposed between the heat exchanger 150 and the turbo portion 264 of the turbopump 260. The release valve 213c and the release outlet 214c are fluidly coupled to the working fluid circuit 202 via a bypass line that extends from a point between the valve 293 and the pump portion 262 of the turbopump 260 to a point on the turbopump bypass line 226 between the turbopump bypass valve 256 and the fluid line 229. The release valve 213d and the release outlet 214d are fluidly coupled to the working fluid circuit 202 at a point disposed between the recuperator 218 and the condenser 274.
A computer system 206, as part of the process control system 204, contains a multi-controller algorithm utilized to control the drive turbine throttle valve 263, the power turbine bypass valve 219, the heat exchanger bypass valve 162, the power turbine throttle valve 250, the power turbine trim valve 252, as well as other valves, pumps, and sensors within the heat engine system 200. In one embodiment, the process control system 204 is enabled to move, adjust, manipulate, or otherwise control the heat exchanger bypass valve 162, the power turbine throttle valve 250, and/or the power turbine trim valve 252 for adjusting or controlling the flow of the working fluid throughout the working fluid circuit 202. By controlling the flow of the working fluid, the process control system 204 is also operable to regulate the temperatures and pressures throughout the working fluid circuit 202.
In another embodiment, the heat engine system 90 may further contain the bearing gas supply line 196 fluidly coupled to and between the inventory supply line 182 and a bearing-containing device 194, as depicted in
In other embodiments, the transfer pump 170 may also be configured to transfer the working fluid from the mass control tank 286 to the bearing housings 238, 268 that completely, substantially, or partially encompass or otherwise enclose bearings contained within a system component.
The mass control tank 286 and the working fluid circuit 202 share the working fluid (e.g., carbon dioxide)—such that the mass control tank 286 may receive, store, and disperse the working fluid during various operational steps of the heat engine system 90. In one embodiment, the transfer pump 170 may be utilized to conduct inventory control by removing working fluid from the working fluid circuit 202, storing working fluid, and/or adding working fluid into the working fluid circuit 202. In another embodiment, the transfer pump 170 may be utilized during a startup process to transfer or otherwise deliver the working fluid—as a cooling agent—from the mass control tank 286 to bearings contained within the bearing housing 268 of the turbopump 260, the bearing housing 238 of the power generation system 220, and/or other system components containing bearings (e.g., rotary equipment or turbo machinery).
Exemplary structures of the bearing housing 238 or 268 may completely or substantially encompass or enclose the bearings as well as all or part of turbines, generators, pumps, driveshafts, gearboxes, or other components shown or not shown for heat engine system 90. The bearing housing 238 or 268 may completely or partially include structures, chambers, cases, housings, such as turbine housings, generator housings, driveshaft housings, driveshafts that contain bearings, gearbox housings, derivatives thereof, or combinations thereof.
In one or more embodiments disclosed herein, at least one bearing gas supply line 196 may be fluidly coupled to and disposed between the transfer pump 170 and at least one bearing housing (e.g., bearing housing 238 or 268) substantially encompassing, enclosing, or otherwise surrounding the bearings of one or more system components. The bearing gas supply line 196 may have or otherwise split into multiple spurs or segments of fluid lines, such as bearing gas supply lines 196a and 196b, which each independently extends to a specified bearing housing 238 or 268, respectively, as illustrated in
In some embodiments, the overall efficiency of the heat engine system 200 and the amount of power ultimately generated can be influenced by the inlet or suction pressure at the pump when the working fluid contains supercritical carbon dioxide. In order to minimize or otherwise regulate the suction pressure of the pump, the heat engine system 200 may incorporate the use of a mass management system (“MMS”) 270. The mass management system 270 controls the inlet pressure of the start pump 280 by regulating the amount of working fluid entering and/or exiting the heat engine system 200 at strategic locations in the working fluid circuit 202, such as at tie-in points, inlets/outlets, valves, or conduits throughout the heat engine system 200. Consequently, the heat engine system 200 becomes more efficient by increasing the pressure ratio for the start pump 280 to a maximum possible extent.
The mass management system 270 contains at least one vessel or tank, such as a storage vessel, a fill vessel, and/or a mass control tank (e.g., mass control tank 286), fluidly coupled to the low pressure side of the working fluid circuit 202 via one or more valves, such as inventory supply valve 184. The valves are moveable—as being partially opened, fully opened, and/or closed—to either remove working fluid from the working fluid circuit 202 or add working fluid to the working fluid circuit 202. Exemplary embodiments of the mass management system 270, and a range of variations thereof, are found in U.S. Pat. No. 8,613,195, the contents of which are incorporated herein by reference to the extent consistent with the present disclosure. Briefly, however, the mass management system 270 may include a plurality of valves and/or connection points, each in fluid communication with the mass control tank 286. The valves may be characterized as termination points where the mass management system 270 is operatively connected to the heat engine system 200. The connection points and valves may be configured to provide the mass management system 270 with an outlet for flaring excess working fluid or pressure, or to provide the mass management system 270 with additional/supplemental working fluid from an external source, such as a fluid fill system.
In some embodiments, the mass control tank 286 may be configured as a localized storage tank for additional/supplemental working fluid that may be added to the heat engine system 200 when needed in order to regulate the pressure or temperature of the working fluid within the working fluid circuit 202 or otherwise supplement escaped working fluid. By controlling the valves, the mass management system 270 adds and/or removes working fluid mass to/from the heat engine system 200 with or without the need of a pump, thereby reducing system cost, complexity, and maintenance.
In some examples, the mass control tank 286 is part of the mass management system 270 and is fluidly coupled to the working fluid circuit 202. At least one connection point, such as a working fluid feed 288, may be a fluid fill port for the mass control tank 286 of the mass management system 270. Additional or supplemental working fluid may be added to the mass management system 270 from an external source, such as a fluid fill system via the working fluid feed 288. Exemplary fluid fill systems are described and illustrated in U.S. Pat. No. 8,281,593, the contents of which are incorporated herein by reference to the extent consistent with the present disclosure.
In another embodiment described herein, bearing gas and seal gas may be supplied to the turbopump 260 or other devices contained within and/or utilized along with the heat engine system 200. One or multiple streams of bearing gas and/or seal gas may be derived from the working fluid within the working fluid circuit 202 and contain carbon dioxide in a gaseous, subcritical, or supercritical state. In some exemplary embodiments, the bearing gas or fluid is flowed by the start pump 280, from a bearing gas supply and/or a bearing gas supply, into the working fluid circuit 202, through a bearing gas supply line (not shown), and to the bearings within the power generation system 220. In other exemplary embodiments, the bearing gas or fluid is flowed by the start pump 280, from the working fluid circuit 202, through a bearing gas supply line (not shown), and to the bearings within the turbopump 260. In some examples, the bearing fluid supply 292 may be a connection point or valve that feeds into a seal gas system. The bearing fluid supply 292 may contain an independent source or tank of the bearing fluid or the bearing fluid supply 292 may be a source of the working fluid (e.g., sc-OO2), such as from the working fluid circuit 202, the mass management system 270, the transfer pump 170, or other sources.
The bearing fluid return 294 is generally coupled to the bearing fluid drain line 298 and configured to receive the bearing fluid downstream of the bearing housing 268, as depicted in
In several exemplary embodiments, the process control system 204 may be communicably connected, wired and/or wirelessly, with numerous sets of sensors, valves, and pumps, in order to process the measured and reported temperatures, pressures, and mass flowrates of the working fluid at the designated points within the working fluid circuit 202. In response to these measured and/or reported parameters, the process control system 204 may be operable to selectively adjust the valves in accordance with a control program or algorithm, thereby maximizing operation of the heat engine system 200.
The process control system 204 may operate with the heat engine system 200 semi-passively with the aid of several sets of sensors. The first set of sensors is arranged at or adjacent the suction inlet of the turbopump 260 and the start pump 280 and the second set of sensors is arranged at or adjacent the outlet of the turbopump 260 and the start pump 280. The first and second sets of sensors monitor and report the pressure, temperature, mass flowrate, or other properties of the working fluid within the low and high pressure sides of the working fluid circuit 202 adjacent the turbopump 260 and the start pump 280. The third set of sensors is arranged either inside or adjacent the mass control tank 286 of the mass management system 270 to measure and report the pressure, temperature, mass flowrate, or other properties of the working fluid within the mass control tank 286. Additionally, an instrument air supply (not shown) may be coupled to sensors, devices, or other instruments within the heat engine system 200 and/or the mass management system 270 that may utilized a gaseous source, such as nitrogen or air.
In some embodiments described herein, the waste heat system 100 may be disposed on or in a waste heat skid 102 fluidly coupled to the working fluid circuit 202, as well as other portions, sub-systems, or devices of the heat engine system 200. The waste heat skid 102 may be fluidly coupled to a source of and an exhaust for the heat source stream 110, a main process skid 212, a power generation skid 222, and/or other portions, sub-systems, or devices of the heat engine system 200.
In one or more configurations, the waste heat system 100 disposed on or in the waste heat skid 102 generally contains inlets 122, 132, and 152 and outlets 124, 134, and 154 fluidly coupled to and in thermal communication with the working fluid within the working fluid circuit 202. The inlet 122 may be disposed upstream of the heat exchanger 120 and the outlet 124 may be disposed downstream of the heat exchanger 120. The working fluid circuit 202 may be configured to flow the working fluid from the inlet 122, through the heat exchanger 120, and to the outlet 124 while transferring thermal energy from the heat source stream 110 to the working fluid by the heat exchanger 120. The inlet 152 may be disposed upstream of the heat exchanger 150 and the outlet 154 may be disposed downstream of the heat exchanger 150. The working fluid circuit 202 may be configured to flow the working fluid from the inlet 152, through the heat exchanger 150, and to the outlet 154 while transferring thermal energy from the heat source stream 110 to the working fluid by the heat exchanger 150. The inlet 132 may be disposed upstream of the heat exchanger 130 and the outlet 134 may be disposed downstream of the heat exchanger 130. The working fluid circuit 202 may be configured to flow the working fluid from the inlet 132, through the heat exchanger 130, and to the outlet 134 while transferring thermal energy from the heat source stream 110 to the working fluid by the heat exchanger 130.
In one or more configurations, the power generation system 220 may be disposed on or in the power generation skid 222 generally contains inlets 225a, 225b and an outlet 227 fluidly coupled to and in thermal communication with the working fluid within the working fluid circuit 202. The inlets 225a, 225b are upstream of the power turbine 228 within the high pressure side of the working fluid circuit 202 and are configured to receive the heated and high pressure working fluid. In some examples, the inlet 225a may be fluidly coupled to the outlet 124 of the waste heat system 100 and configured to receive the working fluid flowing from the heat exchanger 120 and the inlet 225b may be fluidly coupled to the outlet 241 of the process system 210 and configured to receive the working fluid flowing from the turbopump 260 and/or the start pump 280. The outlet 227 may be disposed downstream of the power turbine 228 within the low pressure side of the working fluid circuit 202 and may be configured to provide the low pressure working fluid. In some examples, the outlet 227 may be fluidly coupled to the inlet 239 of the process system 210 and configured to flow the working fluid to the recuperator 216.
A filter 215a may be disposed along and in fluid communication with the fluid line at a point downstream of the heat exchanger 120 and upstream of the power turbine 228. In some examples, the filter 215a is fluidly coupled to the working fluid circuit 202 between the outlet 124 of the waste heat system 100 and the inlet 225a of the process system 210.
The portion of the working fluid circuit 202 within the power generation system 220 is fed the working fluid by the inlets 225a and 225b. A power turbine stop valve 217 is fluidly coupled to the working fluid circuit 202 between the inlet 225a and the power turbine 228. The power turbine stop valve 217 may be configured to control the working fluid flowing from the heat exchanger 120, through the inlet 225a, and into the power turbine 228 while in an open-position. Alternatively, the power turbine stop valve 217 may be configured to cease the flow of working fluid from entering into the power turbine 228 while in a closed-position.
A power turbine attemperator valve 223 is fluidly coupled to the working fluid circuit 202 via an attemperator bypass line 211 disposed between the outlet on the pump portion 262 of the turbopump 260 and the inlet on the power turbine 228 and/or disposed between the outlet on the pump portion 282 of the start pump 280 and the inlet on the power turbine 228. The attemperator bypass line 211 and the power turbine attemperator valve 223 may be configured to flow the working fluid from the pump portion 262 or 282, around and avoid the recuperator 216 and the heat exchangers 120 and 130, and to the power turbine 228, such as during a warm-up or cool-down step. The attemperator bypass line 211 and the power turbine attemperator valve 223 may be utilized to warm the working fluid with heat coming from the power turbine 228 while avoiding the thermal heat from the heat source stream 110 flowing through the heat exchangers, such as the heat exchangers 120 and 130. In some examples, the power turbine attemperator valve 223 may be fluidly coupled to the working fluid circuit 202 between the inlet 225b and the power turbine stop valve 217 upstream of a point on the fluid line that intersects the incoming stream from the inlet 225a. The power turbine attemperator valve 223 may be configured to control the working fluid flowing from the start pump 280 and/or the turbopump 260, through the inlet 225b, and to a power turbine stop valve 217, the power turbine bypass valve 219, and/or the power turbine 228.
The power turbine bypass valve 219 is fluidly coupled to a turbine bypass line that extends from a point of the working fluid circuit 202 upstream of the power turbine stop valve 217 and downstream of the power turbine 228. Therefore, the bypass line and the power turbine bypass valve 219 are configured to direct the working fluid around and avoid the power turbine 228. If the power turbine stop valve 217 is in a closed-position, the power turbine bypass valve 219 may be configured to flow the working fluid around and avoid the power turbine 228 while in an open-position. In one embodiment, the power turbine bypass valve 219 may be utilized while warming up the working fluid during a start-up operation of the electricity generating process. An outlet valve 221 is fluidly coupled to the working fluid circuit 202 between the outlet on the power turbine 228 and the outlet 227 of the power generation system 220.
In one or more configurations, the process system 210 may be disposed on or in the main process skid 212 generally contains inlets 235, 239, and 255 and outlets 231, 237, 241, 251, and 253 fluidly coupled to and in thermal communication with the working fluid within the working fluid circuit 202. The inlet 235 is upstream of the recuperator 216 and the outlet 154 is downstream of the recuperator 216. The working fluid circuit 202 may be configured to flow the working fluid from the inlet 235, through the recuperator 216, and to the outlet 237 while transferring thermal energy from the working fluid in the low pressure side of the working fluid circuit 202 to the working fluid in the high pressure side of the working fluid circuit 202 by the recuperator 216. The outlet 241 of the process system 210 is downstream of the turbopump 260 and/or the start pump 280, upstream of the power turbine 228, and configured to provide a flow of the high pressure working fluid to the power generation system 220, such as to the power turbine 228. The inlet 239 is upstream of the recuperator 216, downstream of the power turbine 228, and configured to receive the low pressure working fluid flowing from the power generation system 220, such as to the power turbine 228. The outlet 251 of the process system 210 is downstream of the recuperator 218, upstream of the heat exchanger 150, and configured to provide a flow of working fluid to the heat exchanger 150. The inlet 255 is downstream of the heat exchanger 150, upstream of the drive turbine 264 of the turbopump 260, and configured to provide the heated high pressure working fluid flowing from the heat exchanger 150 to the drive turbine 264 of the turbopump 260. The outlet 253 of the process system 210 is downstream of the pump portion 262 of the turbopump 260 and/or the pump portion 282 of the start pump 280, couples a bypass line disposed downstream of the heat exchanger 150 and upstream of the drive turbine 264 of the turbopump 260, and configured to provide a flow of working fluid to the drive turbine 264 of the turbopump 260.
Additionally, a filter 215c may be disposed along and in fluid communication with the fluid line at a point downstream of the heat exchanger 150 and upstream of the drive turbine 264 of the turbopump 260. In some examples, the filter 215c is fluidly coupled to the working fluid circuit 202 between the outlet 154 of the waste heat system 100 and the inlet 255 of the process system 210.
In another embodiment described herein, as illustrated in
In exemplary embodiments described herein, the turbopump back-pressure regulator valve 290 may provide or maintain proper pressure to control the thrust of the pocket pressure ratios referred to as the turbine-side pocket pressure ratio (P1) and the pump-side pocket pressure ratio (P2). In some exemplary embodiments, methods described herein include utilizing advanced control theory of sliding mode, the multi-variables of the turbine-side pocket pressure ratio (P1) and the pump-side pocket pressure ratio (P2) and regulating the bearing fluid (e.g., CO2) in the supercritical state or phase are coordinated to be maintained within limits that prevent damage to the thrust bearing 310 of the turbopump 260.
In exemplary embodiments described herein, the turbopump back-pressure regulator valve 290 may be closed or at a zero valve position when both the start pump 280 and the turbopump 260 have not yet been turned on during the startup of the heat engine systems 90, 200. The turbopump back-pressure regulator valve 290 may be closed in order to prevent a flow of the bearing fluid from back feeding through the bearing fluid supply 292 and bypass any filters (e.g., CO2 filter) for the turbopump 260. At the time when the start pump 280 is turned on, the turbopump back-pressure regulator valve 290 may be adjusted to a partially opened-position that is within a range from about 60% to about 65% of being in a fully opened-position. When operations (or running of) the turbopump 260 is detected, such as by head rise, P2 pressure, and turbopump speed, the turbopump back-pressure regulator valve 290 may be placed into automatic control using the control algorithm via the process control system 204 and the computer system 206.
In exemplary embodiments, the control algorithm contains at least a primary governing loop controller, a secondary governing loop controller, and a tertiary governing loop controller. The control algorithm may be configured to calculate valve positions for the turbopump back-pressure regulator valve 290 for providing a pump-side pocket pressure ratio (P2) of a desirable value or range with the primary governing loop controller, a turbine-side pocket pressure ratio (P1) of a desirable value or range with the secondary governing loop controller, and a bearing fluid supply pressure at or greater than a critical pressure value for the bearing fluid. In one exemplary embodiment, the primary governing loop controller controls the pump-side pocket pressure ratio (P2) to a value of about 0.15. In the event that the turbine-side pocket pressure ratio (P1) approaches its alarm value of about 0.30, the secondary governing loop controller assumes control of the turbopump back-pressure regulator valve 290 to balance the thrust on the turbopump 260. If at any time during operation of the heat engine systems 90, 200, the bearing fluid supply pressure for the turbopump 260 begins to fall below supercritical pressure, the tertiary governing loop controller assumes control of the turbopump back-pressure regulator valve 290 to bring the pressure back into the supercritical pressure region. In some examples, during the controller(s) automatic operation, and while the turbopump 260 is in operation, hard limits may be induced on the valve position to force the turbopump back-pressure regulator valve 290 from going to a fully-opened position or a fully-closed position.
The methods provide the extensive use of sliding mode control to coordinate the competing variables and maintain such variables within limits to protect the bearing pressures within the turbopump 260. In one example, the method includes controlling pocket pressure ratios to maintain a “balanced thrust” of the turbopump 260. In another example, the method includes controlling a controller to ensure that the bearing fluid supply pressure for the turbopump 260 is maintained in the supercritical region for the specific bearing fluid, such as carbon dioxide.
It is to be understood that the present disclosure describes several exemplary embodiments for implementing different features, structures, or functions of the invention. Exemplary embodiments of components, arrangements, and configurations are described herein to simplify the present disclosure, however, these exemplary embodiments are provided merely as examples and are not intended to limit the scope of the disclosure. Additionally, the present disclosure may repeat reference numerals and/or letters in the various exemplary embodiments and across the Figures provided herein. This repetition is for the purpose of simplicity and clarity and does not in itself dictate a relationship between the various exemplary embodiments and/or configurations discussed in the various Figures. Moreover, the formation of a first feature over or on a second feature in the present disclosure may include embodiments in which the first and second features are formed in direct contact, and may also include embodiments in which additional features may be formed interposing the first and second features, such that the first and second features may not be in direct contact. Finally, the exemplary embodiments described herein may be combined in any combination of ways, i.e., any element from one exemplary embodiment may be used in any other exemplary embodiment without departing from the scope of the disclosure.
Additionally, certain terms are used throughout the written description and claims to refer to particular components. As one skilled in the art will appreciate, various entities may refer to the same component by different names, and as such, the naming convention for the elements described herein is not intended to limit the scope of the disclosure, unless otherwise specifically defined herein. Further, the naming convention used herein is not intended to distinguish between components that differ in name but not function. Further, in the written description and in the claims, the terms “including,” “containing,” and “comprising” are used in an open-ended fashion, and thus should be interpreted to mean “including, but not limited to”. All numerical values in this disclosure may be exact or approximate values unless otherwise specifically stated. Accordingly, various embodiments of the disclosure may deviate from the numbers, values, and ranges disclosed herein without departing from the intended scope. Furthermore, as it is used in the claims or specification, the term “or” is intended to encompass both exclusive and inclusive cases, i.e., “A or B” is intended to be synonymous with “at least one of A and B,” unless otherwise expressly specified herein.
The foregoing has outlined features of several embodiments so that those skilled in the art may better understand the present disclosure. Those skilled in the art should appreciate that they may readily use the present disclosure as a basis for designing or modifying other processes and structures for carrying out the same purposes and/or achieving the same advantages of the embodiments introduced herein. Those skilled in the art should also realize that such equivalent constructions do not depart from the spirit and scope of the present disclosure, and that they may make various changes, substitutions and alterations herein without departing from the spirit and scope of the present disclosure.
This application is a continuation of U.S. application Ser. No. 15/523,485, filed May 1, 2017, now issued as U.S. Pat. No. 10,570,777, which was a national stage application of PCT/US2015/057756, now expired, which was filed on Nov. 3, 2014, the disclosures of which are incorporated herein by reference to the extent not inconsistent with the present disclosure.
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Number | Date | Country | |
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20200208536 A1 | Jul 2020 | US |
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62074192 | Nov 2014 | US |
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Parent | 15523485 | US | |
Child | 16800420 | US |