CN213144666U - Trough type photo-thermal power generation system with functions of decoupling heat collection, heat storage and heat release power generation - Google Patents
Trough type photo-thermal power generation system with functions of decoupling heat collection, heat storage and heat release power generation Download PDFInfo
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Abstract
The utility model provides a trough type photothermal power generation system of decoupling heat collection heat storage and heat release power generation, which is characterized in that the system comprises an HTF circulation subsystem, a heat storage medium circulation subsystem, a steam circulation subsystem and a trough type mirror field, wherein, the operation of the HTF circulation subsystem (1) is only decided by meteorological conditions without considering the output of a steam turbine, the heat collection heat storage link of the heat storage medium circulation subsystem (2) is only decided by HTF parameters from the trough type mirror field (4), the heat release power generation link is only decided by the heat storage medium heat storage amount and the output of the steam turbine without considering the meteorological conditions, the trough type photothermal power generation system of decoupling heat collection heat storage and heat release power generation is beneficial to decoupling the heat collection heat storage link and the heat release power generation link of the trough type photothermal power generation system with heat storage, the influence of incident solar energy fluctuation on the output of the steam turbine is reduced, and the, the difficulty and complexity of equipment operation and power station operation are reduced.
Description
Technical Field
The utility model belongs to the technical field of the solar photothermal utilization, concretely relates to through decoupling zero thermal-arrest heat-retaining link and exothermic power generation link and simplify the novel solar thermal power generation system that power station operation, stable power station were exerted power.
Background
Solar photo-thermal Power (CSP) is a Solar concentrating thermal Power technology, which collects direct radiation (DNI) of the sun by means of various concentrating mirrors, collects heat by heating fluid working media (HTF), and generates high-temperature steam by a steam generation system (including a preheater, an evaporator and a superheater but not including a reheater, and then "SGS") to drive a turbine to generate Power. The CSP is divided into four types, namely tower type, groove type, Fresnel type and disc type, according to the current global transportation or construction project, the groove type technology is used for a plurality of projects, and the CSP is divided into a groove type system with heat storage and a groove type system without heat storage according to whether a heat storage system is arranged or not. Fig. 1 is a typical trough solar power generation system with heat storage, which works on the principle that a plurality of trough parabolic concentrator collectors are arranged in series and parallel to form a mirror field, vacuum heat collecting tubes are installed at focal lines of the parabolic collectors, and sunlight is converged on the heat collecting tubes through the mirror surfaces of the collectors. The heat transfer fluid flows in the heat collecting pipe, the solar energy converged by the mirror field is absorbed and then the temperature is raised to a higher temperature, and then according to the output requirement of the power station, the heat is transferred to water in the steam generation system through further heat exchange to generate steam to drive a steam turbine generator unit to generate power, or the heat is transferred to a heat storage medium in the heat storage system to be stored, or the heat and the steam turbine generator unit are simultaneously carried out. After the sunshine intensity is weakened or sunset, the HTF absorbs heat of the heat storage medium from the heat storage system and rises to a higher temperature, and the HTF and part of HTF from the mirror field or the HTF independently enter the steam generation system to generate steam to drive the steam turbine generator unit to generate electricity.
The trough-type photo-thermal power station using the power generation system of fig. 1 has been in operation for more than ten years to date, accounting for 40% of the total loading capacity of trough-type technology. However, years of operation practices of the groove type power stations with heat storage show that the operation modes of the power stations are as many as seven and eight, the complexity of the overall operation is high, the difficulty and the complexity of switching among the operation modes are greatly increased due to the limitation of various objective conditions such as valve opening and closing time, pump body starting and stopping time, equipment/pipeline thermal inertia, lowest flow/load/temperature of the equipment, flow distribution of each pipeline, forward and reverse flow directions of working media in an oil-salt heat exchanger and the like, and therefore the requirement on skills of operators of the groove type photo-thermal power stations is always high. In addition, when the trough type power generation system of fig. 1 is used, the process steps under two working conditions of directly absorbing heat from the mirror field to generate steam and independently taking heat from the heat storage system to generate steam are different, wherein the former is mirror field-HTF-steam, the latter is mirror field-HTF-heat storage medium-HTF-steam, and the latter is more heat exchange steps, so that the finally generated steam temperature is lower, the difference between the two is generally about 14 ℃, and the temperature of main steam entering a steam turbine is different, thereby requiring the steam turbine to have two design working conditions, which not only increases the complexity of the steam turbine design, moreover, because the efficiency of the steam turbine is different under the two design working conditions, a series of operations of adjusting the steam volume, the HTF flow and the heat storage medium flow must be carried out in real time to stabilize the final power output, thereby increasing the complexity of the operation of the steam turbine and the power station.
In recent years, due to the requirements of power grid dispatching, peak regulation and consumption, a photo-thermal power generation system with heat storage is more favored by people, and particularly in the projects of a photo-thermal and photovoltaic mixed power station, a peak regulation energy storage power station and a multi-energy complementary comprehensive energy base, the requirement trend of the photo-thermal system on the heat storage time is longer and longer, such as 8 hours or longer. When sunshine is sufficient daytime, the photothermal power station can give way for the photovoltaic preferentially, the photovoltaic can be emitted to the greatest extent, and most of the photothermal mirror field collection can be conveyed to the heat storage system for storage. After sunlight is weakened or sunset, most/all of the heat is extracted from the heat storage system by the photo-heat to generate electricity so as to compensate for the reduction of the output of the photovoltaic system. As described above, when the system takes heat from the heat storage system to generate power, because the temperature of the main steam is low and the efficiency of the steam turbine is low, when the heat storage time of the photo-thermal system is increased and the equivalent time of the steam turbine generating power with low efficiency is increased, the energy lost by the trough photo-thermal system will be increased, the power generation amount will be reduced, and the economy will be deteriorated.
In summary, the existing trough power generation system with heat storage has the following disadvantages:
1. the operation mode is various, and the integral operation is complex;
2. the technical requirements on operators are high, and the overall automatic operation trend of the system is not facilitated;
3. the temperature of the main steam has two design working conditions, so that the design of the steam turbine also needs to consider the two design working conditions, the design complexity is increased, and the difficulty of the operation of the steam turbine and a power station is increased;
4. under the trend that the heat storage time of the photo-thermal power station configuration is longer and longer, and the running time of the power station for independently taking heat from the heat storage system to generate power is longer and longer, the energy loss of a typical groove type system caused by an intermediate heat exchange link is increased, the generated energy is reduced, and the economical efficiency is deteriorated.
Disclosure of Invention
In order to overcome the shortcoming that current slot type power generation system of taking the heat-retaining exists, the utility model provides a slot type photothermal power generation system of decoupling zero thermal-arrest heat-retaining and exothermic electricity generation, reduce as far as possible under the prerequisite of changing former flow and equipment, decoupling zero thermal-arrest heat-retaining and exothermic electricity generation link, make the slot type photothermal system of taking the heat-retaining more accord with present "light and heat + photovoltaic" hybrid power station, peak shaving energy storage power station, the complementary comprehensive energy base of multipotency is to the longer energy storage time of photothermal system, "daytime energy storage let way + evening peak shaving and exert oneself", reduce system operation mode simultaneously, the degree of difficulty and the complexity of reduction system operation, reduce the technical requirement to the operation personnel, be favorable to the development of the whole automatic operation of future system.
An object of the utility model is to provide a slot type solar-thermal power generation system of decoupling zero thermal-arrest heat-retaining and exothermic electricity generation, the system includes: the system comprises an HTF circulation subsystem (1), a heat storage medium circulation subsystem (2), a steam circulation subsystem (3) and a groove type mirror field (4), wherein the operation of the HTF circulation subsystem (1) is only determined by meteorological conditions without considering the output of a steam turbine, a heat collection and storage link of the heat storage medium circulation subsystem (2) is only determined by HTF parameters from the groove type mirror field (4), and a heat release and power generation link is only determined by the heat storage medium heat storage amount and the output of the steam turbine without considering the meteorological conditions.
Preferably, the HTF circulation subsystem (1) comprises an HTF heat storage medium heat exchanger (5), an expansion tank system (6) and an HTF circulation pump (7), wherein the outlet of the trough mirror field (4) is connected with the HTF inlet of the HTF heat storage medium heat exchanger (5), the HTF outlet of the HTF heat storage medium heat exchanger (5) is connected with the inlet of the expansion tank system (6), the outlet of the expansion tank system (6) is connected with the inlet of the HTF circulation pump (7), the outlet of the HTF circulation pump (7) is connected with the inlet of the trough mirror field (4), thereby forming the HTF circulation subsystem (1) for circulating HTF, wherein HTF circulates and flows only in the HTF circulation subsystem (1) by the driving of the HTF circulation pump (7), and is only used for conveying the heat collected by the trough mirror field (4) to the HTF heat storage medium heat exchanger (5) and transferring the heat to the HTF heat storage heat exchanger (7) in a heat exchange manner The medium cannot directly enter a steam generation system to generate steam or directly enter a reheater to heat the steam; the expansion tank system (6) is used to absorb the volume change of the HTF due to temperature change in the circulation process.
Preferably, the heat storage medium circulation subsystem (2) comprises a cold tank (8), a cold heat storage medium pump (9), a hot tank (10), a hot heat storage medium pump (11) and a heat storage medium SGS (12), wherein an inlet of the cold heat storage medium pump (9) is immersed below the liquid level of the cold heat storage medium in the cold tank (8); in order to increase the flexibility of system adjustment, an outlet of the cold-state heat storage medium pump (9) is connected with a heat storage medium inlet of the HTF-heat storage medium heat exchanger (5) so that a cold-state heat storage medium at an outlet of the cold-state heat storage medium pump (9) enters the HTF-heat storage medium heat exchanger (5), a branch is additionally arranged to be connected with a hot-state heat storage medium at an outlet of the hot-state heat storage medium pump (11), the on-off of the branch is controlled by a valve, and therefore after the cold-state heat storage medium and the hot-state heat storage medium are mixed in a preheating stage of the heat storage medium SGS (12), the temperature of the heat storage medium entering the heat storage medium SGS (12) is rapidly controlled, and the starting time of; the heat storage medium outlet of the HTF-heat storage medium heat exchanger (5) is respectively connected with the inlet of the cold tank (8) and the inlet of the hot tank (10) through two pipelines, the two pipelines are both controlled to be on and off through a valve, the inlet of the thermal state heat storage medium pump (11) is immersed below the liquid level of the thermal state heat storage medium in the hot tank (10), the outlet of the thermal state heat storage medium pump (11) is respectively connected with the inlet of the heat storage medium SGS (12) and the inlet of the heat storage medium steam reheater (13) of the steam circulation subsystem (3), the outlet of the heat storage medium SGS (12) and the outlet of the heat storage medium steam reheater (13) are both connected with the inlet of the cold tank (8) so as to form the heat storage medium circulation subsystem (2) for the heat storage medium to circularly flow, and the heat storage medium only circularly flows in the heat storage medium circulation subsystem (2), for absorbing heat from the HTF, storing heat, and releasing heat to water/steam.
Preferably, the steam cycle subsystem (3) adopts a steam Rankine cycle system, and comprises a heat storage medium steam reheater (13), a steam turbine (14), a condenser (15), a condensate pump (16), a heater (17) and a deaerator (18), superheated steam generated by a heat storage medium SGS (12) and reheated steam generated by the heat storage medium steam reheater (13) enter the steam turbine (14) to do work and generate power, exhaust steam is condensed into water through the condenser (15), and then enters the heat storage medium SGS (12) again to generate steam after passing through the condensate pump (16), the heater (17) and the deaerator (18), and the cycle is repeated, wherein the heat storage medium SGS (12) comprises a superheater, an evaporator and a heat storage preheater.
Preferably, the HTF and the heat storage medium are both liquid in the designed working temperature range and are two different media, wherein the HTF is a medium with a freezing point of 100 ℃ or below, and the heat storage medium is a medium with a freezing point of more than 100 ℃.
Preferably, the HTF heat storage medium heat exchanger (5), the heat storage medium SGS (12) and the heat storage medium steam reheater (13) are arranged in parallel in a single row, two rows or multiple rows, so that the redundancy of equipment and the flexibility of system adjustment are increased.
Preferably, the cold tanks (8) are used in pairs with the hot tanks (10), in number of one or more pairs.
Preferably, the outlet of the heat storage medium steam reheater (13) is connected to the evaporator inlet of the heat storage medium SGS (12).
The operation method of the groove type photo-thermal power generation system for decoupling heat collection, heat storage and heat release power generation comprises the following steps:
step 1, HTF circularly flows in an HTF circulation subsystem 1 under the driving of a circulating pump 7, heat collected by a groove type mirror field 4 is conveyed to an HTF-heat storage medium heat exchanger 5 and is transferred to a heat storage medium in a heat exchange mode, and an expansion tank system 6 absorbs volume change of the HTF caused by temperature change in the circulation process;
step 3, the thermal-state heat storage medium stored in the thermal tank 10 flows into the heat storage medium SGS12 and the heat storage medium steam reheater 13 from the thermal tank 10 under the driving of the thermal-state heat storage medium pump 11, the flow distribution of the medium in the thermal-state heat storage medium SGS12 and the heat storage medium steam reheater 13 is controlled through a valve, superheated steam generated by the heat storage medium SGS12 and reheated steam generated by the heat storage medium steam reheater 13 enter a steam turbine 14 to do work and generate power, exhaust steam is condensed into water through a condenser 15, and then enters the heat storage medium SGS12 again to generate steam after passing through a condensate pump 16, a heater 17 and a deaerator 18; the thermal-state heat storage medium transfers heat to water/water vapor in the heat storage medium SGS12 and the heat storage medium steam reheater 13, then the temperature is reduced, and finally the heat storage medium returns to the cold tank 8 again;
the steps 1 and 2 occur simultaneously to realize heat collection and heat storage, the step 3 is heat release and power generation, the step 3 can be carried out when a thermal state heat storage medium is in the thermal tank 10, the influence of solar radiation fluctuation on the steps 1 and 2 is not needed to be considered, and the decoupling of the heat collection and heat storage and the heat release and power generation is realized.
The utility model has the advantages that: 1) the heat collection and heat storage and heat release power generation links of the groove type photo-thermal power generation system with heat storage are decoupled, on one hand, the influence of incident solar energy fluctuation on steam generation and steam turbine output is reduced, the thermal inertia of the heat storage medium is fully utilized to achieve the purpose of stabilizing the output of the steam generation system and a steam turbine, on the other hand, the system operation mode is reduced, the operation of the HTF circulation subsystem (1) is only determined by meteorological conditions without considering the output of the steam turbine, the operation of the HTF-heat storage medium heat exchanger (5) and the cold-state heat storage medium pump (9) is only determined by the HTF parameters from the groove type mirror field (4), the HTF-heat storage medium heat exchanger (5) only needs to consider a single operation direction without considering two reversible operation directions of heat absorption and heat release, the operation of the thermal-state heat storage medium pump (11) is only determined by the liquid level of the thermal-state heat storage medium in the thermal, these measures contribute to reducing the difficulty and complexity of equipment operation and plant operation, and ultimately to reducing the technical requirements on the operating personnel. 2) Under all the operation modes, the steam turbine only needs one set of main steam design parameters, namely only needs one design working condition, so that the design of the steam turbine is simplified, and the difficulty of the operation of the steam turbine is reduced. 3) Compared with a typical groove type photo-thermal power generation system with heat storage, the heat storage medium directly releases heat to water/water vapor to generate superheated steam, so that intermediate links of heat exchange to HTF (high temperature coefficient) are reduced, and heat exchange end difference loss is reduced, so that the temperature of main steam is increased, and the power generation efficiency of a steam turbine under the working condition of heat release and power generation of the heat storage medium is increased. The method is particularly important under the current trends of longer and longer heat storage time required to be configured for the photothermal power station and longer equivalent running time of the photothermal power station for independently taking heat from the heat storage system to generate electricity, and the design of the power station is more consistent with the expected requirements of a photothermal and photovoltaic mixed power station, a peak-shaving energy storage power station and a multi-energy complementary comprehensive energy base on the photothermal system.
In order to make the aforementioned and other objects, features and advantages of the present invention comprehensible, preferred embodiments accompanied with figures are described in detail below.
Drawings
Fig. 1 illustrates a typical thermal power generation system with thermal storage in a trough configuration.
FIG. 2 is a novel groove type photo-thermal heat storage power generation system for decoupling heat collection and heat storage and heat release power generation.
Wherein the reference numerals denote:
1-an HTF circulation subsystem; 2-a heat storage medium circulation subsystem; 3-a steam cycle subsystem; 4-a trough mirror field; 5-HTF-heat storage medium heat exchanger; 6-expansion tank system; 7-HTF circulating pump; 8-cooling the tank; 9-cold heat storage medium pump; 10-heating the tank; 11-a thermal state heat storage medium pump; 12-heat storage medium SGS; 13-heat storage medium steam reheater; 14-a steam turbine; 15-a condenser; 16-a condensate pump; 17-a heater; 18-deaerator.
Detailed Description
The novel groove type photo-thermal power generation system for decoupling heat collection, heat storage and heat release power generation as shown in figure 2 is characterized in that a fluid working medium HTF in the embodiment is 26.5% of biphenyl-73.5% of diphenyl ether heat conducting oil, the freezing point is 12 ℃, the designed working temperature is 50-400 ℃, a heat storage medium is a binary inorganic salt mixture of 60% of sodium nitrate and 40% of potassium nitrate, the freezing point is 238 ℃, and the designed working temperature is 290-400 ℃. The heat conducting oil and the molten salt are both in liquid state within the respective designed working temperature range. The trough-type photothermal heat storage power generation system of this embodiment includes:
a heat conducting oil circulation subsystem 1; a molten salt circulation subsystem 2; a steam circulation subsystem 3 and a trough mirror field 4. The operation of the heat conduction oil circulation subsystem 1 is only determined by meteorological conditions without considering the output of a steam turbine, the heat collection and storage link of the molten salt circulation subsystem 2 is only determined by HTF parameters from the groove type mirror field 4, and the heat release and power generation link is only determined by the heat storage medium heat storage amount and the output of the steam turbine without considering the meteorological conditions.
Wherein the heat conducting oil circulation subsystem 1 comprises a heat conducting oil-molten salt heat exchanger 5, an expansion tank system 6 and a heat conducting oil circulating pump 7, wherein an outlet of the groove type mirror field 4 is connected with a heat conducting oil inlet of the heat conducting oil-molten salt heat exchanger 5, a heat conducting oil outlet of the heat conducting oil-molten salt heat exchanger 5 is connected with an inlet of the expansion tank system 6, an outlet of the expansion tank system 6 is connected with an inlet of the heat conducting oil circulating pump 7, and an outlet of the heat conducting oil circulating pump 7 is connected with an inlet of the groove type mirror field 4, thereby forming the heat conducting oil circulation subsystem 1 for circulating and flowing heat conducting oil, wherein the heat conducting oil only circulates and flows in the heat conducting oil circulation subsystem 1 through the driving of the heat conducting oil circulating pump 7, is only used for conveying the heat collected by the groove type mirror field 4 to, the steam does not directly enter a reheater to heat the steam; the expansion tank system 6 is used to absorb the volume change of the HTF due to temperature changes during the cycle.
The molten salt circulation subsystem 2 comprises a cold salt tank 8, a cold salt pump 9, a hot salt tank 10, a hot salt pump 11 and a molten salt SGS12, wherein an inlet of the cold salt pump 9 is submerged below the level of the cold salt in the cold salt tank 8; in order to increase the flexibility of system adjustment, an outlet of a cold salt pump 9 is connected with a heat storage medium inlet of a heat conduction oil-molten salt heat exchanger 5 so that cold salt at the outlet of the cold salt pump 9 enters the heat conduction oil-molten salt heat exchanger 5, a branch is additionally arranged to be connected with hot salt at the outlet of a hot salt pump 11, and the on-off of the branch is controlled by a valve, so that after cold salt and hot salt are mixed in a molten salt SGS12 starting preheating stage, the temperature of the heat storage medium entering molten salt SGS12 is rapidly controlled, and the starting time of equipment is shortened; an outlet of a heat storage medium of the heat conduction oil-molten salt heat exchanger 5 is respectively connected with an inlet of a cold salt tank 8 and an inlet of a hot salt tank 10 through two pipelines, on-off of the two pipelines is controlled through a valve, an inlet of a hot salt pump 11 is immersed below the level of hot salt in the hot salt tank 10, an outlet of the hot salt pump 11 is respectively connected with an inlet of a molten salt medium SGS12 and an inlet of a molten salt steam reheater 13 of the steam circulation subsystem 3, an outlet of a molten salt SGS12 and an outlet of the molten salt steam reheater 13 are respectively connected with the inlet of the cold salt tank 8, so that a molten salt circulation subsystem 2 for molten salt circulation flow is formed, and molten salt only circularly flows in the molten salt circulation subsystem 2 and is used for absorbing heat from molten salt, storing heat and releasing heat to water/steam. The cold salt flows into the oil-salt heat exchanger 5 from the cold salt tank 8 under the driving of the cold salt pump 9, the temperature rises after heat transfer oil heat is absorbed, the flow direction of the molten salt is controlled through a valve according to the outlet temperature of the molten salt, namely when the outlet temperature reaches a target value of 386 ℃, the molten salt flows into the hot salt tank 10 for storage, and otherwise, the molten salt flows back to the cold salt tank 8 again. The hot salt in the hot salt tank 10 flows from the hot salt tank 10 into the molten salt SGS12 and the molten salt steam reheater 13 under the driving of the hot salt pump 11, the flow distribution of the hot salt in the hot salt tank and the molten salt steam reheater can be controlled through valves, and the temperature of the hot salt is reduced after the hot salt transfers heat to water/steam in the two sets of equipment, and the hot salt finally returns to the cold salt tank 8. The connecting branch of 9 exports of cold salt pump and 11 exports of hot salt pump can be through mixing cold state fused salt and hot molten salt at fused salt SGS12 start-up stage, and the molten salt temperature that enters into fused salt SGS12 is controlled fast to shorten fused salt SGS 12's equipment start-up preheating time, increase the flexibility that the system adjusted. The molten salt SGS12 includes a superheater, an evaporator, a preheater device and the like.
The steam circulation subsystem 3 is a traditional steam Rankine circulation system, namely superheated steam generated by the molten salt SGS12 and reheated steam generated by the molten salt steam reheater 13 enter a steam turbine 14 to do work and generate power, exhaust steam is condensed into water through a condenser 15, and then enters the molten salt SGS12 again to generate steam after passing through a condensate pump 16, a heater 17 and a deaerator 18, and the circulation is carried out.
In this embodiment, the heat exchange working mediums of the molten salt SGS12 and the molten salt steam reheater 13 are both molten salt-water/steam.
In this embodiment, the oil-salt heat exchanger 5, the molten salt SGS12, and the molten salt steam reheater 13 are all arranged in two rows of 2 × 50%. Of course, the skilled person can choose a single-column, multi-column parallel arrangement according to the technical knowledge in the art, thereby altering the redundancy of the device and the flexibility of the system adjustment, in particular, when changing from a double column to a single column, the redundancy and flexibility are reduced; redundancy and flexibility are increased when changing from two columns to multiple columns.
In this embodiment, the cold salt tank 8 and the hot salt tank 10 are used in pairs, and the number is one pair.
Of course, in this embodiment, the outlet of the molten salt steam reheater 13 may be connected to the inlet of the evaporator in the molten salt SGS12, so as to reduce the exothermic temperature difference of the molten salt in the molten salt steam reheater 13, thereby reducing the temperature difference gradient of the single device of the molten salt steam reheater 13, facilitating the simplification of the device design, reducing the thermal stress during operation, and prolonging the device life.
In this embodiment, conduction oil, fused salt are liquid at design operating temperature within range, and both are two kinds of media inequality, and wherein HTF except selecting the conduction oil, the freezing point is also all within the protection scope of the utility model at 100 ℃ and other media below, including one or more in following: organic synthetic oil, silicone oil, glycol solution or low-melting-point melting inorganic salt mixture, and other heat storage media with freezing points above 100 ℃ besides molten salt can be selected, which belong to the protection scope of the patent, and include one or more of the following: a binary fused inorganic salt mixture, a ternary fused inorganic salt mixture, or a multiple fused inorganic salt mixture. The organic synthetic oil is biphenyl-diphenyl ether, terphenyl or modified terphenyl, quaterphenyl, alkyl aromatic hydrocarbon or isopropyl biphenyl mixture; the binary molten inorganic salt mixture is a sodium nitrate-potassium nitrate mixture; the ternary molten inorganic salt mixture is a potassium nitrate-sodium nitrite mixture. Of course, other HTFs and heat storage media suitable for the systems and methods of the present invention may be selected by those skilled in the art.
The operation method of the groove type photo-thermal power generation system for decoupling heat collection, heat storage and heat release power generation comprises the following steps:
step 1, HTF circularly flows in an HTF circulation subsystem 1 under the driving of a circulating pump 7, heat collected by a groove type mirror field 4 is conveyed to an HTF-heat storage medium heat exchanger 5 and is transferred to a heat storage medium in a heat exchange mode, and an expansion tank system 6 absorbs volume change of the HTF caused by temperature change in the circulation process;
step 3, the thermal-state heat storage medium stored in the thermal tank 10 flows into the heat storage medium SGS12 and the heat storage medium steam reheater 13 from the thermal tank 10 under the driving of the thermal-state heat storage medium pump 11, the flow distribution of the medium in the thermal-state heat storage medium SGS12 and the heat storage medium steam reheater 13 is controlled through a valve, superheated steam generated by the heat storage medium SGS12 and reheated steam generated by the heat storage medium steam reheater 13 enter a steam turbine 14 to do work and generate power, exhaust steam is condensed into water through a condenser 15, and then enters the heat storage medium SGS12 again to generate steam after passing through a condensate pump 16, a heater 17 and a deaerator 18; the thermal-state heat storage medium transfers heat to water/water vapor in the heat storage medium SGS12 and the heat storage medium steam reheater 13, then the temperature is reduced, and finally the heat storage medium returns to the cold tank 8 again;
the steps 1 and 2 occur simultaneously to realize heat collection and heat storage, the step 3 is heat release and power generation, the step 3 can be carried out when a thermal state heat storage medium is in the thermal tank 10, the influence of solar radiation fluctuation on the steps 1 and 2 is not needed to be considered, and the decoupling of the heat collection and heat storage and the heat release and power generation is realized.
The embodiment decouples the heat collection and storage and heat release power generation links of the groove type photo-thermal power generation system with heat storage, on one hand, the influence of incident solar energy fluctuation on steam generation and steam turbine output is reduced, the thermal inertia of a heat storage medium is fully utilized to achieve the purpose of stabilizing the steam generation system and the steam turbine output, on the other hand, the system operation mode is reduced, the operation of the heat conduction oil circulation subsystem 1 is only determined by meteorological conditions without considering the steam turbine output, the operation of the heat conduction oil-molten salt heat exchanger 5 and the cold salt pump 9 is only determined by heat conduction oil parameters from the groove type mirror field 4, the heat conduction oil-molten salt heat exchanger 5 only needs to consider a single operation direction without considering two reversible operation directions of heat absorption and heat release, the operation of the hot salt pump 11 is only determined by the liquid level of hot salt in the hot salt tank 10 and the steam turbine output, and the measures are beneficial to reducing the difficulty and, and ultimately reduces the technical requirements on the operators. Under all the operation modes, the steam turbine only needs one set of main steam design parameters, namely only needs one design working condition, so that the design of the steam turbine is simplified, and the difficulty of the operation of the steam turbine is reduced. Compared with a typical groove type photo-thermal power generation system with heat storage, the heat storage medium directly releases heat to water/water steam to generate superheated steam, so that intermediate links for firstly conducting heat exchange to hot oil are reduced, and heat exchange end difference loss is reduced, so that the temperature of main steam is increased, and the power generation efficiency of a steam turbine under the working condition of heat release and power generation of the heat storage medium is improved. The method is particularly important under the current trends of longer and longer heat storage time required to be configured for the photothermal power station and longer equivalent running time of the photothermal power station for independently taking heat from the heat storage system to generate electricity, and the design of the power station is more consistent with the expected requirements of a photothermal and photovoltaic mixed power station, a peak-shaving energy storage power station and a multi-energy complementary comprehensive energy base on the photothermal system.
While the present invention has been described with reference to the particular illustrative embodiments, it is not to be restricted by the embodiments but only by the appended claims. It will be understood by those skilled in the art that variations and modifications of the embodiments of the present invention may be made without departing from the scope and spirit of the invention.
Claims (8)
1. The utility model provides a decoupling zero thermal-arrest heat-retaining and slot type solar-thermal power generation system of exothermic electricity generation which characterized in that the system includes: the system comprises an HTF circulation subsystem (1), a heat storage medium circulation subsystem (2), a steam circulation subsystem (3) and a groove type mirror field (4), wherein the operation of the HTF circulation subsystem (1) is only determined by meteorological conditions without considering the output of a steam turbine, a heat collection and storage link of the heat storage medium circulation subsystem (2) is only determined by HTF parameters from the groove type mirror field (4), and a heat release and power generation link is only determined by the heat storage medium heat storage amount and the output of the steam turbine without considering the meteorological conditions.
2. The trough type photo-thermal power generation system for decoupling heat collection, heat storage and heat release power generation of claim 1, wherein: the HTF circulation subsystem (1) comprises an HTF heat storage medium heat exchanger (5), an expansion tank system (6) and an HTF circulation pump (7), wherein the outlet of the trough-type mirror field (4) is connected with the HTF inlet of the HTF heat storage medium heat exchanger (5), the HTF outlet of the HTF heat storage medium heat exchanger (5) is connected with the inlet of the expansion tank system (6), the outlet of the expansion tank system (6) is connected with the inlet of the HTF circulation pump (7), the outlet of the HTF circulation pump (7) is connected with the inlet of the trough-type mirror field (4) so as to form the HTF circulation subsystem (1) for circulating HTF, wherein HTF only circulates in the HTF circulation subsystem (1) under the driving of the HTF circulation pump (7) and only is used for conveying the heat collected by the trough-type mirror field (4) to the HTF heat storage medium heat exchanger (5) and transferring the heat to the heat storage medium in a heat exchange manner, the steam cannot directly enter a steam generation system to generate steam or directly enter a reheater to heat the steam; the expansion tank system (6) is used to absorb the volume change of the HTF due to temperature change in the circulation process.
3. The trough type photo-thermal power generation system for decoupling heat collection, heat storage and heat release power generation of claim 2, wherein: the heat storage medium circulation subsystem (2) comprises a cold tank (8), a cold heat storage medium pump (9), a hot tank (10), a hot heat storage medium pump (11) and a heat storage medium SGS (12), wherein an inlet of the cold heat storage medium pump (9) is immersed below the liquid level of the cold heat storage medium in the cold tank (8), and the heat storage medium SGS (12) comprises a superheater, an evaporator and a preheater device; in order to increase the flexibility of system adjustment, an outlet of the cold-state heat storage medium pump (9) is connected with a heat storage medium inlet of the HTF-heat storage medium heat exchanger (5) so that a cold-state heat storage medium at an outlet of the cold-state heat storage medium pump (9) enters the HTF-heat storage medium heat exchanger (5), a branch is additionally arranged to be connected with a hot-state heat storage medium at an outlet of the hot-state heat storage medium pump (11), the on-off of the branch is controlled by a valve, and therefore after the cold-state heat storage medium and the hot-state heat storage medium are mixed in a preheating stage of the heat storage medium SGS (12), the temperature of the heat storage medium entering the heat storage medium SGS (12) is rapidly controlled, and the starting time of; the heat storage medium outlet of the HTF-heat storage medium heat exchanger (5) is respectively connected with the inlet of the cold tank (8) and the inlet of the hot tank (10) through two pipelines, the two pipelines are both controlled to be on and off through a valve, the inlet of the thermal state heat storage medium pump (11) is immersed below the liquid level of the thermal state heat storage medium in the hot tank (10), the outlet of the thermal state heat storage medium pump (11) is respectively connected with the inlet of the heat storage medium SGS (12) and the inlet of the heat storage medium steam reheater (13) of the steam circulation subsystem (3), the outlet of the heat storage medium SGS (12) and the outlet of the heat storage medium steam reheater (13) are both connected with the inlet of the cold tank (8), so that the heat storage medium circulation subsystem (2) for the heat storage medium to circularly flow is formed, and the heat storage medium only circularly flows in the heat storage medium circulation subsystem (2), for absorbing heat from the HTF, storing heat, and releasing heat to water/steam.
4. The trough type photo-thermal power generation system for decoupling heat collection, heat storage and heat release power generation of claim 3, wherein: the steam circulation subsystem (3) adopts a steam Rankine cycle system and comprises a heat storage medium steam reheater (13), a steam turbine (14), a condenser (15), a condensate pump (16), a heater (17) and a deaerator (18), superheated steam generated by a heat storage medium SGS (12) and reheated steam generated by the heat storage medium steam reheater (13) enter the steam turbine (14) to do work and generate power, exhaust steam is condensed into water through the condenser (15), and then enters the heat storage medium SGS (12) again to generate steam after passing through the condensate pump (16), the heater (17) and the deaerator (18), and the cycle is repeated.
5. The trough type photo-thermal power generation system for decoupling heat collection, heat storage and heat release power generation of claim 1, wherein: the HTF and the heat storage medium are both in liquid state within the designed working temperature range and are two different media, wherein the HTF is a medium with a freezing point of 100 ℃ or below, and the heat storage medium is a medium with a freezing point of more than 100 ℃.
6. The trough-type solar-thermal power generation system for decoupling heat collection, heat storage and heat release power generation of claim 4, wherein: the HTF-heat storage medium heat exchanger (5), the heat storage medium SGS (12) and the heat storage medium steam reheater (13) are arranged in parallel in a single row, double rows or multiple rows, and therefore the redundancy of equipment and the flexibility of system adjustment are increased.
7. The trough-type solar-thermal power generation system for decoupling heat collection, heat storage and heat release power generation of claim 6, wherein: the cold tanks (8) and the hot tanks (10) are used in pairs, and the number of the cold tanks and the hot tanks is one or more.
8. The trough-type solar-thermal power generation system for decoupling heat collection, heat storage and heat release power generation of claim 4, wherein: the outlet of the heat storage medium steam reheater (13) is connected with the inlet of an evaporator in the heat storage medium SGS (12).
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