CN211975319U - Power generation system - Google Patents
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- CN211975319U CN211975319U CN202020451871.6U CN202020451871U CN211975319U CN 211975319 U CN211975319 U CN 211975319U CN 202020451871 U CN202020451871 U CN 202020451871U CN 211975319 U CN211975319 U CN 211975319U
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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- Y02E10/00—Energy generation through renewable energy sources
- Y02E10/20—Hydro energy
Abstract
The utility model discloses a power generation system, which comprises a high-pressure gas system, a gas-liquid mixing system, a hydraulic power generator set, a channel switching system, a control system and a water flow compensation pressure circulating system, wherein the high-pressure gas system, the gas-liquid mixing system, the hydraulic power generator set and the water flow compensation pressure circulating system are connected through the channel switching system and are controlled by the control system; the compressed air pumped by the water pump adopts a variable pipeline characteristic down-conversion operation mode, so that the water pump can always operate near a high-efficiency area, high efficiency is maintained, and electric energy consumed by pumping the water pump is reduced; the water turbine is stable near a rated water head in the power generation process, so that the water turbine can operate near a highest efficiency area to generate more electric energy. And less electric energy is consumed, more electric energy is added, so that the overall electric conversion efficiency of the system is higher. The system has the functions of conventional compressed air energy storage and large-scale electric energy storage of pumped storage power stations, and has the characteristics of no dependence on terrain difference, high efficiency, long running time and the like.
Description
Technical Field
The utility model relates to a new forms of energy storage and electricity generation technical field, concretely relates to power generation system.
Background
With the development of large-scale wind energy/photovoltaic resources, the development of wind power/photovoltaic in China keeps the strong momentum of rapid development, and as late as 2018, the installed capacity of renewable energy in China reaches 7.28 hundred million kilowatts and accounts for about 38.3 percent of the installed capacity of all the electric power, but the contradiction between the rapid development of new energy power generation and the relative lag of power grid construction is increasingly obvious. The large-scale wind power/photovoltaic energy access power grid with the characteristics of randomness, intermittence, anti-regulation, large output fluctuation and the like has great influence on the voltage stability, transient stability and frequency stability of the system, the national water electricity abandonment in 2018 reaches 691 hundred million kilowatt hours, the wind electricity abandonment in 2018 reaches 277 million kilowatt hours, and the light electricity abandonment reaches 54.9 million kilowatt hours. Therefore, the phenomena of wind abandonment, light abandonment and water abandonment are widely existed, the problems of difficult grid connection of wind power/photovoltaic energy, difficult absorption after grid connection and the like seriously restrict the change of an energy structure, and the technical characteristics [ J ] of a new generation electric power system in China in energy transformation, China Motor engineering newspaper, document [2] thank exism, Zhangmin, Rojinshan and the like, and a future electric power system evolution model [ J ] of new energy large-scale access, China Motor engineering newspaper, 2018 and 38 (2).
At present, the energy storage modes mainly comprise: pumped storage, compressed air storage, hydrogen energy, battery storage, flywheel storage, superconducting storage and the like. However, the mature energy storage technologies mainly include pumped storage, storage battery storage and compressed air storage. The pumped storage is limited by various factors such as water resources, topography, geology and the like, the investment cost is high, the construction period is long, and flexible arrangement and large-scale popularization and application are difficult. The storage battery has the advantages of quick response, high conversion efficiency and the like, but has safety problems in operation and certain influence on the environment in production and manufacturing. Compared with other two technologies, Compressed Air Energy Storage (CAES) has the characteristics of large energy storage scale, long storage period, small environmental pollution, low requirement on terrain and the like, and is one of the development directions with great potential in the field of large-scale energy storage at present. However, the traditional compressed air energy storage power station represented by the German Huntorf compressed air energy storage power station and the American McIntosh compressed air energy storage power station has the problems of dependence on external natural gas fuel supplement, influence on the environment, low high-pressure air electric energy conversion efficiency (less than 50 percent), dependence on large-volume cave resources and inflexible arrangement. At present, the most advanced heat insulation compressed air storage usually needs a large-volume abandoned mine and a cave with at least ten thousand cubic meters for storing high-pressure air, has the defects of serious dependence on cave resources, inflexible arrangement and high investment cost (dozens of billions of RMB), is in a heat insulation process in the energy storage and release processes, and has the problems of easy escape of heat and low conversion efficiency.
SUMMERY OF THE UTILITY MODEL
The utility model discloses to the problem that exists among the above-mentioned prior art, a power generation system is proposed, build pressure and follow-up run mends gas leakage when moving through utilizing air compressor to carry out the first operation of system, adjust the completion energy storage to the rotational speed under becoming the pipeline characteristic through utilizing the water pump, make technical scheme power generation system, both had conventional hydroelectric set start-stop machine rapidly, regulating speed is fast, accommodation broad, clean pollution-free characteristics, had the function of the extensive storage electric energy of conventional compressed air energy storage power station, the energy storage power station of drawing water again, and do not rely on features such as relief difference, efficient, operating duration are long.
The utility model provides a following technical scheme:
a power generation system comprises a high-pressure gas system, a gas-liquid mixing system, a hydraulic power generator set, a channel switching system, a control system and a water flow compensation pressure circulating system, wherein the high-pressure gas system, the gas-liquid mixing system, the hydraulic power generator set and the water flow compensation pressure circulating system are connected through the channel switching system and are controlled by the control system;
the high-pressure gas system comprises N1Parallel high-pressure gas systems, N1≥1；
Each group of high-pressure gas subsystems comprises an air compression device and a high-pressure gas storage container which are sequentially and correspondingly connected, and the air compression device is used for providing the initial operating pressure of the high-pressure gas storage container and supplementing the pressure lost by gas leakage in the operating process of the high-pressure gas storage container;
the gas-liquid mixing system at least comprises 1 group of high-pressure gas-liquid mixing subsystems; the water flow compensation pressure circulating system comprises a water pump connected with the reservoir, a water pump variable frequency motor and a connecting valve between the water pump and the reservoir and between the water pump and the high-pressure gas-liquid mixing subsystem;
the ratio of the volume of the high-pressure gas storage container to the volume of the steam-water mixing container of the high-pressure gas-liquid mixing subsystem is 0.1-20;
the inlet of the air compression device is communicated with external normal-pressure air, the outlet of the air compression device is communicated with the inlet of a corresponding high-pressure air storage container, the outlet of the high-pressure air storage container is connected with the air inlet of the high-pressure gas-liquid mixing subsystem through a pressure adjusting control device, the liquid outlet of the high-pressure gas-liquid mixing subsystem is connected with the liquid inlet of a reservoir through a hydraulic generator set, the liquid outlet of the reservoir is connected with the high-pressure gas-liquid mixing subsystem through a water flow compensation pressure circulating system;
the volume of the water storage tank is more than or equal to the sum of the volumes of all the steam-water mixing containers.
When energy is stored, the water pump is driven by a variable frequency motor to pump water to a steam-water mixing container, and preset pressure air in the steam-water mixing container is compressed to form a pipeline characteristic-variable energy-saving operation mode with real-time change of water outlet pressure;
during power generation, the pressure difference between the steam-water mixing container and a set pressure value is monitored in real time, and the opening of a pressure control valve between the high-pressure gas storage container and the steam-water mixing container is controlled by adopting a pressure closed-loop control strategy, so that the pressure in the steam-water mixing container is maintained in a constant range.
In the running process of the water pump, the rotating speed of the water pump is continuously and smoothly adjusted according to the characteristic curve of the water pump in the pumping process, a continuous track curve M is formed at the intersection point of the characteristic curve of the water pump and the pipeline along with the continuous rising of the characteristic curve of the pipeline in the pumping process, and the rotating speed of the water pump is adjusted according to the track curve M;
the continuous and smooth adjustment of the rotating speed of a water pump characteristic curve in the pumping process is described as follows, the air pressure of a steam-water mixing container is given, the pressure of the steam-water mixing container is basically maintained unchanged within a tiny time dt on the assumption of pipeline characteristics and an initial value H of a water pump head, the pipeline characteristics are basically unchanged, and the corresponding flow Q is obtained according to a pipeline characteristic equation; according to the efficiency curves of the water pump at different rotating speeds, a peak efficiency-flow curve eta (f) (Q) and a peak efficiency-rotating speed curve eta (f) (n) of the water pump can be obtained; calculating the efficiency of the water pump according to the flow Q and a curve eta of the peak efficiency-flow rate of the water pump, wherein the eta of the peak efficiency-rotating speed of the water pump is f (n); the head Hp of the water pump can be obtained by taking the obtained rotating speed n, flow rate Q and water pump head characteristic curve H as f (Q, n); comparing Hp and Hc with an assumed initial water head value H, and maintaining the difference value within a set error range; and if the error range is exceeded, adjusting the initial value H of the water head until the error requirement is met.
The technical scheme of the utility model is characterized in that a water flow compensation pressure circulating system, namely a water pump is introduced, and the water in the reservoir is compensated into the gas-liquid mixing container by the water pump, so that the pressure of the gas-water mixing container is stably adjusted by matching with an air compression device; according to the topological structure, the water pump can always run near the high-efficiency area, high efficiency is maintained, and electric energy consumption of the water pump in pumping is reduced;
furthermore, an independent communication pipeline is arranged between the gas-liquid mixing subsystem and the hydraulic generator set, and an independent communication pipeline is arranged between the gas-liquid mixing subsystem and the water flow compensation pressure circulation system.
The pipeline between the gas-liquid mixing subsystem and the water turbine is independent, namely, the pipeline is not shared with the water pump, so that the peak regulation is realized by the pipeline characteristic of the water pump;
furthermore, the gas-liquid mixing system comprises M groups of high-pressure gas-liquid mixing subsystems which are parallel, wherein M is more than or equal to 2, a gas inlet of each group of high-pressure gas-liquid mixing subsystems is connected with an outlet of a high-pressure gas storage container through a pressure adjusting control device, a liquid outlet of each group of high-pressure gas-liquid mixing subsystems is connected with a liquid inlet of a reservoir through a hydraulic generator set, and the liquid outlet of the reservoir is connected to liquid inlets of the groups of high-pressure gas-liquid mixing subsystems through an;
wherein the volume ratio of the M groups of steam-water mixing containers to the volume of the high-pressure gas storage container is 0.1-20.
A plurality of groups of hydraulic generator sets in the power station can share 1 high-pressure gas storage container, and the 1 high-pressure gas storage container can utilize large containers such as waste mines and underground aquifer caves to build the power station, so that the overall investment cost of the power station can be saved, and the economy of the whole power station construction is improved.
Furthermore, the gas-liquid mixing system comprises N groups of high-pressure gas-liquid mixing subsystems which are parallel, wherein N is more than or equal to 2, the N groups of high-pressure gas-liquid mixing subsystems which are parallel share one high-pressure gas-liquid mixing subsystem, a liquid outlet of the high-pressure gas-liquid mixing subsystem is connected with a liquid inlet of a reservoir through N hydraulic generator sets which are parallel, and a liquid outlet of the reservoir is connected to a liquid inlet of the high-pressure gas-liquid mixing subsystem through N water flow compensation pressure circulating systems which are parallel;
wherein the ratio of the volume of the steam-water mixing container to the volume of the high-pressure gas storage container is 0.1-20.
Multiple groups of hydraulic generator sets can share 1 steam-water mixing container, and simultaneously use a plurality of water pumps and a plurality of water turbines, so that the installed capacity of a power station is increased, and the flexibility of power regulation and power distribution of the power station is improved;
further, the high-pressure gas storage container and the steam-water mixing container in the high-pressure gas-liquid mixing subsystem adopt any one of an underground pit well, an underground cave, a waste mine, a developed salt well/mine, an aquifer cave, a ground gas storage device or an underwater gas storage container.
Furthermore, the hydraulic turbine of the hydraulic generator set has a low specific speed of 100 m-kW-200 m-kW and an ultra-low specific speed of 10 m-kW-100 m-kW, and is an impulse turbine, an industrial turbine or a hydraulic turbine.
Furthermore, the inlet angle of the water turbine is in the range of 100-150 degrees, and the outlet angle of the water turbine is in the range of 10-40 degrees.
The water turbine is stable near a rated water head in the power generation process, so that the water turbine can operate near a highest efficiency area to generate more electric energy. And less electric energy is consumed, more electric energy is added, so that the overall electric conversion efficiency of the system is higher.
Further, the gas pressure in a steam-water mixing container in the gas-liquid mixing system is not lower than 2 MPa.
Further, the hydraulic generator set comprises a water turbine and a water turbine generator, and the water turbine generator is a synchronous generator, a doubly-fed generator or a permanent magnet generator.
The hydraulic generator set mainly realizes the conversion from mechanical energy to electric energy;
furthermore, the control system comprises a speed regulating system, an excitation system, a monitoring system, a protection system and an air pressure control system of a water turbine and a hydraulic generator in the hydraulic generator set.
The control system is mainly used for adjusting and controlling the rotating speed, power, voltage and air pressure of the water-turbine generator set and ensuring the normal operation of the power generation state and the energy storage state of the power generation system;
the channel switching system comprises an air valve and a liquid valve which are connected among the water turbine, the water pump, the air compressor, the steam-water mixing container and the high-pressure air storage container, and the switching of the running state of the system is realized.
Advantageous effects
The technical scheme provided by the utility model is a power generation system, which comprises a high-pressure gas system, a gas-liquid mixing system, a hydraulic power generator set, a channel switching system, a control system and a water flow compensation pressure circulating system, wherein the high-pressure gas system, the gas-liquid mixing system, the hydraulic power generator set and the water flow compensation pressure circulating system are connected through the channel switching system and are controlled by the control system; the system changes the operation mode of the system through a control system and a channel switching system to convert abundant new energy electric energy into air energy to be stored in a high-pressure air system, converts abundant electric energy into liquid pressure energy to be stored in a gas-liquid mixing container, and converts the air energy stored in the high-pressure air system into electric energy by controlling the channel switching system, the control system and the gas-liquid mixing system through a hydraulic generator set; the system has the characteristics of rapid start and stop of the conventional hydroelectric generating set, high adjusting speed, wide adjusting range, cleanness and no pollution, has the function of large-scale electric energy storage of the conventional compressed air energy storage power station, and has the characteristics of no dependence on terrain fall, high efficiency, long operation time and the like.
Compared with the power generation system in the prior art, the system has the following advantages:
(1) in the power generation system provided by the technical scheme of the utility model, the connection relation among the high-pressure steam-water mixing container, the reservoir and the water turbine is single, so that the system structure is simpler and the operation is more convenient;
(2) the technical proposal of the utility model is that the supplement of the air pressure in the steam-water mixing container in the power generation system during the operation process is realized mainly by pumping water by a water pump under the variable pipeline characteristic, and the required electric energy is less; the air pressure is supplemented by mainly depending on the compression of an air compressor in the prior art, because the air in a container exchanges heat with water and a wall in the process of pumping water and compressing the air by a water pump, the process is approximate to an isothermal compression process, heat escapes less from the wall of the air compressor in the compression process of the air compressor, electric energy consumed by the air compressor is mainly converted into high-temperature and high-pressure air, the process is approximate to adiabatic compression (isentropic compression), and the energy consumption in the isothermal compression process is less than that in the isentropic process according to a pressure-volume diagram in the isentropic compression and isothermal compression processes;
the compressed air pumped by the water pump adopts a variable pipeline characteristic down-conversion operation mode, so that the water pump can always operate near a high-efficiency area, high efficiency is maintained, and electric energy consumed by pumping the water pump is reduced; the water turbine is stable near a rated water head in the power generation process, so that the water turbine can operate near a highest efficiency area to generate more electric energy. And less electric energy is consumed, more electric energy is added, so that the overall electric conversion efficiency of the system is higher.
(3) The power generation system provided by the technical scheme of the utility model has two operation modes, and the system absorbs redundant electric energy from the power grid in the energy storage mode, converts the electric energy into compressed air, stores the compressed air in the high-pressure gas system and converts the electric energy into liquid pressure energy; under the power generation mode, high-pressure gas can be released under the action of the control system, so that the gas-liquid mixing system is in a high-pressure state, high-pressure liquid flow drives the hydraulic generator set to convert air energy into electric energy, and the high-pressure gas maintains constant pressure required by power generation through the regulating valve.
(4) The variable pipeline characteristic variable frequency operation is adopted in the water pumping process of the water pump, the operation stability of the water pump and the variable frequency motor is better, the vibration and the swing of the unit are smaller, and the service life is longer; the high-pressure gas storage container adopts a water-bearing stratum gas storage container and a waste mine, so that the construction cost of the whole power station is lower, the investment cost recovery period of the power station is shorter, and the economy is better.
Drawings
Fig. 1 is a schematic block diagram of a power generation system according to the technical solution of the present invention;
FIG. 2 is a schematic diagram of a power generation system according to an embodiment of the present invention;
FIG. 3 is a schematic structural diagram of a power generation system according to an example of the present invention;
FIG. 4 is a schematic structural diagram of a power generation system according to a third embodiment of the present invention;
FIG. 5 is a schematic structural diagram of a power generation system according to an example of the present invention;
fig. 6 is a schematic view of pressure changes of the steam-water mixing container and the high-pressure air storage container in a working cycle according to the technical scheme of the present invention;
fig. 7 is a schematic view of the control and adjustment of the reclaimed water pump in the technical scheme of the utility model;
FIG. 8 is a schematic diagram of a characteristic curve of a water pump variable pipeline in the technical scheme of the present invention;
description of reference numerals: 110-a gas compressor motor, 111-an air compressor, 112-a high-pressure gas storage container, 113-a pressure regulation control device I, 114-a pressure one-way valve, 115-a pressure control valve, 116-a first steam-water mixing container, 117-a water pump, 118-a water pump variable frequency motor, 119-an impulse water turbine, 120-a water turbine generator, 121-a water reservoir, 122-a first air valve, 123-a second air valve, 124-a third air valve, 125-a first water valve, 126-a second water valve and 127-a third water valve; 220-a fourth water valve, 221-a fifth water valve; 330-aquifer gas storage container, 331-pressure regulation control device II, 332-pressure regulation control device III, 333-second steam-water mixing container; 430-a sixth water valve, 431-a seventh water valve, 432-an eighth water valve, 433-a ninth water valve.
Detailed Description
The invention will be further described with reference to the accompanying drawings and examples.
As shown in fig. 1, the utility model provides a power generation system, which comprises a high-pressure gas system, a gas-liquid mixing system, a hydraulic power generator set, a channel switching system, a control system and a water flow compensation pressure circulating system, wherein the high-pressure gas system, the gas-liquid mixing system, the hydraulic power generator set and the water flow compensation pressure circulating system are connected through the channel switching system and are controlled by the control system;
the high-pressure gas system comprises N1Parallel high-pressure gas systems, N1≥1；
Each group of high-pressure gas subsystems comprises an air compression device and a high-pressure gas storage container which are sequentially and correspondingly connected, and the air compression device is used for providing the initial operating pressure of the high-pressure gas storage container and supplementing the pressure lost by gas leakage in the operating process of the high-pressure gas storage container;
the gas-liquid mixing system at least comprises 1 group of high-pressure gas-liquid mixing subsystems; the water flow compensation pressure circulating system comprises a water pump connected with the reservoir, a water pump variable frequency motor and a connecting valve between the water pump and the reservoir and between the water pump and the high-pressure gas-liquid mixing subsystem;
the ratio of the volume of the high-pressure gas storage container to the volume of the steam-water mixing container of the high-pressure gas-liquid mixing subsystem is 0.1-20;
the inlet of the air compression device is communicated with external normal-pressure air, the outlet of the air compression device is communicated with the inlet of a corresponding high-pressure air storage container, the outlet of the high-pressure air storage container is connected with the air inlet of the high-pressure gas-liquid mixing subsystem through a pressure adjusting control device, the liquid outlet of the high-pressure gas-liquid mixing subsystem is connected with the liquid inlet of a reservoir through a hydraulic generator set, the liquid outlet of the reservoir is connected with the high-pressure gas-liquid mixing subsystem through a water flow compensation pressure circulating system;
the volume of the water storage tank is more than or equal to the sum of the volumes of all the steam-water mixing containers;
when energy is stored, the water pump is driven by a variable frequency motor, water is pumped to the steam-water mixing container, air in the steam-water mixing container is compressed, and a pipeline characteristic-variable energy-saving operation mode with real-time change of water outlet pressure is formed;
during power generation, the pressure difference between the steam-water mixing container and a set pressure value is monitored in real time, and the state of a pressure control valve between the high-pressure gas storage container and the steam-water mixing container is controlled by adopting a pressure closed-loop control strategy, so that the pressure in the steam-water mixing container is maintained in a constant range.
The high-pressure gas storage container and the gas-liquid mixing system container in the high-pressure gas-liquid mixing subsystem are not limited to any one of an underground pit well, an underground cave, a waste mine, a developed salt well/mine, an aquifer cave, a ground gas storage device or an underwater gas storage container.
The water turbine in the hydraulic generator set is a low specific speed 100 m-kW-200 m-kW and ultra-low specific speed 10 m-kW-100 m-kW water turbine, and the water turbine is an impulse water turbine, an industrial turbine or a hydraulic turbine. The inlet angle of the water turbine is in the range of 110-150 degrees, and the outlet angle of the water turbine is in the range of 10-40 degrees.
The water turbine in the scheme can be operated near the highest efficiency region to generate more electric energy by being stabilized near the rated water head in the power generation process of the water turbine. And less electric energy is consumed, more electric energy is added, so that the overall electric conversion efficiency of the system is higher.
And the gas pressure in a steam-water mixing container in the gas-liquid mixing system is not lower than 2 MPa.
The hydraulic generator set comprises a water turbine and a hydraulic generator, and mainly realizes the conversion from mechanical energy to electric energy;
the control system comprises a speed regulating system, an excitation system, a monitoring system, a protection system and an air pressure control system of a water turbine and a hydraulic generator in the hydraulic generator set.
The control system is mainly used for adjusting and controlling the rotating speed, power, voltage and air pressure of the water-turbine generator set and ensuring the normal operation of the power generation state and the energy storage state of the power generation system;
the channel switching system comprises an air valve and a liquid valve which are connected among the water turbine, the water pump, the air compressor, the steam-water mixing container and the high-pressure air storage container, and the switching of the running state of the system is realized.
In the following embodiments, the liquid in the steam-water mixing container uses water as a working medium, and the water turbine in the hydraulic generator set is exemplified by an impulse turbine.
In a first embodiment, fig. 2 shows an implementation of the system. In fig. 2, the air compressor 111 or compressor, high pressure air reservoir, forms one of the implementations of the high pressure air system; the steam-water mixing container and the water storage tank form one implementation mode of a gas-liquid system; the first air valve 122, the second air valve 123, the first water valve 125, the third water valve 127, the second water valve 126, the pressure one-way valve 114, the pressure control valve 115 and pipelines among different devices form one implementation mode of a channel switching system; impulse turbine 119 and turbine generator 120 form one of the implementations of a hydraulic generator set; auxiliary control systems such as a speed regulating system, an excitation system, a monitoring system, a protection system and an air pressure control system of the impulse turbine and a generator thereof form one of specific implementation modes of the control system; the liquid uses water as a working medium; the air compressor or the air compressor, the high-pressure air storage container, the water pump and the variable frequency motor auxiliary control system form one of the concrete implementation modes of the pressure stabilizing system; the liquid uses water as the working medium.
One mode of operation of the system is described as follows:
the system is in an initial state that water flow is located in the reservoir 121, only liquid reaching the lowest water level exists in the steam-water mixing container, and when the system enters an energy storage stage for the first time, the air compressor 111 compresses normal pressure air to a set pressure value under the driving of the air compressor motor 110 to establish initial pressures of a high-pressure air storage container and the steam-water mixing container; and opening the third water valve 127, the first water valve 125 and the second air valve 123, closing the second water valve 126 and the third air valve 124, starting the water pump to pump the water flow in the water reservoir into the steam-water mixing container, further increasing the air pressure in the high-pressure air storage container and the steam-water mixing container, and stopping pumping and compressing the water when the liquid level in the steam-water mixing container reaches a set maximum value. The power generation state can be ready to be entered at any time. As shown in fig. 7 and 8, the rotation speed of the water pump is continuously and smoothly adjusted by the characteristic curve of the water pump in the water pumping process, a continuous track curve M is formed at the intersection point of the characteristic curve of the water pump and the characteristic curve of the pipeline in the water pumping process, and the flow of the water pump is adjusted according to the track curve M under the pressure of the given steam-water mixing container, so that the water pump runs near a high-efficiency region. Before power generation, the first air valve 122 and the third water valve 127 are closed, and the second air valve 123, the first water valve 125 and the second water valve 126 are opened. If the pressure in the steam-water mixing container is too high and is larger than the set pressure value for power generation, the pressure can be adjusted through the air pressure adjusting valve; the high-pressure gas expands and the displacement water flow pushes the impulse turbine to rotate so as to convert the high-pressure air energy into the rotary mechanical energy, and the rotary mechanical energy is converted into electric energy under the action of the generator and output to the power grid. If the load needs to be adjusted in the power generation process, the adjustment can be realized by adjusting the nozzle and the deflector, and the adjustment can also be realized by changing the rotating speed of the impulse turbine.
For more clear description of the working states of the water pump and the air compressor and the pressure change process in the high-pressure air storage container and the steam-water mixing container, one working mode of the cycle is depicted as fig. 6, and the area a: the method comprises the steps that an air compressor is initially pressurized, a water pump pressurizing and energy storing stage of an area B is adopted, the pressure line type in a steam-water mixing container at the outlet of a pipeline is increased, an area C waits for a power generation stage, a steam-water mixing container deflating and pressure reducing stage of an area D is adopted, and a steam-water mixing container power generation and high-pressure air storage container pressure stabilizing stage of an area E is adopted. After the power generation is finished, the state of Point7 is consistent with the state of Point2, and the water pump can be started again to enter a pressurization energy storage stage to perform a new cycle of energy storage-power generation circulation.
In the second embodiment, fig. 3 shows an implementation of the system. In FIG. 3, the air compressor or compressor, the high pressure air reservoir, forms one implementation of a high pressure air system; the steam-water mixing container and the water storage tank form one implementation mode of a gas-liquid system; the first air valve 122, the second air valve 123, the second water valve 126, the fourth water valve 220, the fifth water valve 221, the third water valve 127, the pressure one-way valve 114, the pressure control valve 115 and pipelines among different devices form one implementation mode of a channel switching system; the impulse turbine and the generator thereof form one of the realization modes of the hydraulic generator set; auxiliary control systems such as a speed regulating system, an excitation system, a monitoring system, a protection system and an air pressure control system of the impulse turbine and a generator thereof form one of specific implementation modes of the control system; the liquid uses water as a working medium; the air compressor or the air compressor, the high-pressure air storage container, the water pump and the motor auxiliary control system form one of the concrete realization modes of the pressure stabilization system; the liquid uses water as the working medium. The system works in a similar way to the system described in the first embodiment. The mode is different from the mode shown in figure 2 in that a water inlet pipeline of the impulse turbine is separated from a water outlet pipeline of the water pump, so that the output of the impulse turbine can be reduced and the water pump is started to increase the power load when the load is reduced or the power load is converted from a power generation state to the power load in grid-connected operation, the drop of the water level in the steam-water mixing container is compensated, and the rapid switching from the power generation state to the power load state can be realized.
In a third embodiment, fig. 4 shows an implementation of the system. In FIG. 4, the air compressor or compressor, aquifer reservoir, forms one implementation of a high-pressure air system; the steam-water mixing container and the water storage tank form one implementation mode of a gas-liquid system; the first air valve 122, the second pressure regulation control device 331, the third pressure regulation control device 332, the second water valve 126, the fifth water valve 221, the fourth water valve 220, the third water valve 127 and pipelines among different devices form one of the realization modes of a channel switching system; the #1 to # N water turbines and the generators thereof form one of the realization modes of the hydraulic generator set; auxiliary control systems such as a speed regulating system, an excitation system, a monitoring system, a protection system and an air pressure control system of #1 to # N water turbines and generators thereof form one of specific implementation modes of the control system; the liquid uses water as a working medium; the air compressor, the high-pressure air storage container, the #1 to # M water pumps and the motor auxiliary control system thereof form one of the concrete realization modes of the pressure stabilization system; the liquid uses water as the working medium.
One mode of operation of the system is described below.
When the system is in an initial state, water flow is located in the water storage tank, only liquid reaching the lowest water level exists in the steam-water mixing container, and when the system enters an energy storage stage for the first time, the compressor compresses normal pressure air to a set pressure value under the driving of the motor to establish initial pressures of the air storage container and the steam-water mixing container; and opening the fourth water valve 220 and the third water valve 127, closing the second water valve 126, the second pressure regulation control device 331 and the third pressure regulation control device 332, starting the No. 1 to No. N water pumps according to a certain strategy to pump the water flow in the water storage tank into the gas-water mixing container, further increasing the air pressure in the gas storage container and the gas-water mixing container, and stopping pumping the water and the air when the liquid level in the gas-water mixing container reaches a set maximum value. The power generation state can be ready to be entered at any time.
Before power generation, the first air valve 122 is closed, and the corresponding second pressure regulating control device 331, the corresponding third pressure regulating control device 332, the corresponding second water valve 126 and the corresponding fifth water valve 221 are opened according to a certain strategy. If the pressure in the steam-water mixing container is too high and is larger than the set pressure value for power generation, the pressure can be adjusted through the air pressure adjusting valve; the high-pressure gas expands and squeezes water flow to push the #1 to # N water turbines to rotate, so that the high-pressure air energy is converted into rotary mechanical energy, and the rotary mechanical energy is converted into electric energy under the action of the generator and is output to a power grid.
If the load needs to be adjusted in the power generation process, the load can be adjusted through the power of a single machine, and the load can also be adjusted through changing the output combination of different units.
In the fourth embodiment, fig. 5 shows an implementation of the system. In FIG. 5, the air compressor or compressor, aquifer reservoir, forms one implementation of a high-pressure air system; the steam-water mixing container and the water storage tank form one implementation mode of a gas-liquid system; the first air valve 122, the first pressure regulation control device 113, the eighth water valve 432, the second water valve 126, the fifth water valve 221, the ninth water valve 433, the seventh water valve 431, the third water valve 127, the fourth water valve 220, the sixth water valve 430 and pipelines among different devices form one of the realization modes of a channel switching system; the #1 to # N water turbines and the generators thereof form one of the realization modes of the hydraulic generator set; auxiliary control systems such as a speed regulating system, an excitation system, a monitoring system, a protection system and an air pressure control system of #1 to # N water turbines and generators thereof form one of specific implementation modes of the control system; the liquid uses water as a working medium; the air compressor, the high-pressure air storage container, the #1 to # M water pumps and the motor auxiliary control system thereof form one of the concrete realization modes of the pressure stabilization system; the liquid uses water as the working medium.
The liquid uses water as the working medium. The working mode of the system is similar to that of the system described in the fourth embodiment, and details are not repeated. Different from fig. 4, the high-pressure steam-water mixing container of a plurality of units shares 1 unit.
In the above example, the rotation speed of the water pump is continuously and smoothly adjusted according to the characteristic curve of the water pump during the water pumping process, and as the characteristic curve of the pipeline continuously rises during the water pumping process, the intersection point of the characteristic curve and the pipeline forms a continuous track curve M, as shown in fig. 8, the flow rate of the water pump is adjusted according to the track curve M under the given pressure of the steam-water mixing container, so that the water pump operates in the vicinity of the high-efficiency region.
The description of the continuous and smooth adjustment of the rotating speed of the water pump characteristic curve in the water pumping process is shown in fig. 7, the air pressure of the steam-water mixing container is given, the pressure of the steam-water mixing container is basically maintained unchanged within a minute time dt on the assumption of pipeline characteristics and a water pump head initial value H, the pipeline characteristics are basically unchanged, and the corresponding flow Q is obtained according to a pipeline characteristic equation; according to the efficiency curves of the water pump at different rotating speeds, a peak efficiency-flow curve eta (f) (Q) and a peak efficiency-rotating speed curve eta (f) (n) of the water pump can be obtained; calculating the efficiency of the water pump according to the flow Q and a curve eta of the peak efficiency-flow rate of the water pump, wherein the eta of the peak efficiency-rotating speed of the water pump is f (n); the head Hp of the water pump can be obtained by taking the obtained rotating speed n, flow rate Q and water pump head characteristic curve H as f (Q, n); comparing Hp and Hc with an assumed initial water head value H, and maintaining the difference value within a set error range; and if the error range is exceeded, adjusting the initial value H of the water head until the error requirement is met.
In the above embodiment, the ratio of the volume of the steam-water mixing container to the volume of the high-pressure gas storage container is 0.1 to 20.
Finally, it should be noted that the above embodiments are only used for further detailed description of the objects, technical solutions and advantages of the present invention, and it should be understood that the above embodiments are only examples of the present invention, and are not intended to limit the present invention, and any modifications, equivalent substitutions and improvements made within the spirit and principle of the present invention should be included in the scope of the present invention.
Claims (10)
1. A power generation system is characterized by comprising a high-pressure gas system, a gas-liquid mixing system, a hydraulic power generator set, a channel switching system, a control system and a water flow compensation pressure circulating system, wherein the high-pressure gas system, the gas-liquid mixing system, the hydraulic power generator set and the water flow compensation pressure circulating system are connected through the channel switching system and are controlled by the control system;
the high-pressure gas system comprises N1Parallel high-pressure gas systems, N1≥1；
Each group of high-pressure gas subsystems comprises an air compression device and a high-pressure gas storage container which are sequentially and correspondingly connected, and the air compression device is used for providing the initial operating pressure of the high-pressure gas storage container and supplementing the pressure lost by gas leakage in the operating process of the high-pressure gas storage container;
the gas-liquid mixing system at least comprises 1 group of high-pressure gas-liquid mixing subsystems; the water flow compensation pressure circulating system comprises a water pump connected with the reservoir, a water pump variable frequency motor and a connecting valve between the water pump and the reservoir and between the water pump and the high-pressure gas-liquid mixing subsystem;
the ratio of the volume of the high-pressure gas storage container to the volume of the steam-water mixing container of the high-pressure gas-liquid mixing subsystem is 0.1-20;
the inlet of the air compression device is communicated with external normal-pressure air, the outlet of the air compression device is communicated with the inlet of a corresponding high-pressure air storage container, the outlet of the high-pressure air storage container is connected with the air inlet of the high-pressure gas-liquid mixing subsystem through a pressure adjusting control device, the liquid outlet of the high-pressure gas-liquid mixing subsystem is connected with the liquid inlet of a reservoir through a hydraulic generator set, the liquid outlet of the reservoir is connected with the high-pressure gas-liquid mixing subsystem through a water flow compensation pressure circulating system;
the volume of the water storage tank is more than or equal to the sum of the volumes of all the steam-water mixing containers.
2. The power generation system of claim 1, wherein a separate communication pipeline is arranged between the gas-liquid mixing subsystem and the hydraulic generator set, and a separate communication pipeline is arranged between the gas-liquid mixing subsystem and the water flow compensation pressure circulation system.
3. The power generation system of claim 2, wherein the gas-liquid mixing system comprises M groups of high-pressure gas-liquid mixing subsystems which are arranged in parallel, M is more than or equal to 2, a gas inlet of each group of high-pressure gas-liquid mixing subsystems is connected with an outlet of the high-pressure gas storage container through a pressure regulation control device, a liquid outlet of each group of high-pressure gas-liquid mixing subsystems is connected with a liquid inlet of the reservoir through a hydraulic generator set, and a liquid outlet of the reservoir is connected with a liquid inlet of each group of high-pressure gas-liquid mixing subsystems through an independent water;
wherein the volume ratio of the M groups of steam-water mixing containers to the volume of the high-pressure gas storage container is 0.1-20.
4. The power generation system of claim 2, wherein the gas-liquid mixing system comprises N groups of high-pressure gas-liquid mixing subsystems which are parallel, N is more than or equal to 2, the N groups of high-pressure gas-liquid mixing subsystems share one high-pressure gas-liquid mixing subsystem, a liquid outlet of the high-pressure gas-liquid mixing subsystem is connected with a liquid inlet of a reservoir through N hydraulic generator sets which are parallel, and the liquid outlet of the reservoir is connected to a liquid inlet of the high-pressure gas-liquid mixing subsystem through N water flow compensation pressure circulating systems which are parallel;
wherein the ratio of the volume of the steam-water mixing container to the volume of the high-pressure gas storage container is 0.1-20.
5. The power generation system of claim 1, wherein the high pressure gas storage vessel and the vapor-water mixing vessel of the high pressure gas-liquid mixing subsystem are any one of underground wells, underground caverns, abandoned mines, developed salt wells/mines, aquifer caverns, surface gas storage devices or underwater gas storage vessels.
6. The power generation system of claim 1, wherein the hydraulic turbine of the hydraulic power generator set has a low specific speed of 100 m-kW to 200 m-kW and an ultra-low specific speed of 10 m-kW to 100 m-kW, and the hydraulic turbine is a pelton turbine, an industrial turbine or a hydraulic turbine.
7. An electrical power generation system according to claim 6, wherein the turbine inlet angle is in the range 100 ° to 150 ° and the outlet angle is in the range 10 ° to 40 °.
8. The power generation system of claim 1, wherein the gas pressure in the steam-water mixing container in the gas-liquid mixing system is not lower than 2 MPa.
9. The power generation system of claim 1, wherein the hydro-generator set comprises a water turbine, a hydro-generator, and the hydro-generator is a synchronous generator, a doubly-fed generator, or a permanent magnet generator.
10. The power generation system of claim 1, wherein the control system comprises a governor system, an excitation system, a monitoring system, a protection system and a pneumatic control system for the hydraulic generator set including the turbine and the hydro-generator.
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN113904588A (en) * | 2021-10-28 | 2022-01-07 | 国网湖南省电力有限公司 | Fluctuating pressure power generation control method and device of power generation-energy storage system |
| CN114094568A (en) * | 2021-10-28 | 2022-02-25 | 国网湖南省电力有限公司 | Fluctuating pressure power generation control method and system of power generation-energy storage system |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN113904588A (en) * | 2021-10-28 | 2022-01-07 | 国网湖南省电力有限公司 | Fluctuating pressure power generation control method and device of power generation-energy storage system |
| CN114094568A (en) * | 2021-10-28 | 2022-02-25 | 国网湖南省电力有限公司 | Fluctuating pressure power generation control method and system of power generation-energy storage system |
| WO2023071809A1 (en) * | 2021-10-28 | 2023-05-04 | 国网湖南省电力有限公司 | Fluctuation pressure power generation control method and device for power generation-energy storage system |
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