CN105673107B - The supercritical carbon dioxide electricity generation system and method for the heat collection combined driving of groove tower - Google Patents

The supercritical carbon dioxide electricity generation system and method for the heat collection combined driving of groove tower Download PDF

Info

Publication number
CN105673107B
CN105673107B CN201610036862.9A CN201610036862A CN105673107B CN 105673107 B CN105673107 B CN 105673107B CN 201610036862 A CN201610036862 A CN 201610036862A CN 105673107 B CN105673107 B CN 105673107B
Authority
CN
China
Prior art keywords
carbon dioxide
supercritical carbon
working medium
heat
pressure side
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201610036862.9A
Other languages
Chinese (zh)
Other versions
CN105673107A (en
Inventor
韩巍
金红光
姜迎春
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Institute of Engineering Thermophysics of CAS
Original Assignee
Institute of Engineering Thermophysics of CAS
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Institute of Engineering Thermophysics of CAS filed Critical Institute of Engineering Thermophysics of CAS
Priority to CN201610036862.9A priority Critical patent/CN105673107B/en
Publication of CN105673107A publication Critical patent/CN105673107A/en
Application granted granted Critical
Publication of CN105673107B publication Critical patent/CN105673107B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E10/00Energy generation through renewable energy sources
    • Y02E10/40Solar thermal energy, e.g. solar towers
    • Y02E10/46Conversion of thermal power into mechanical power, e.g. Rankine, Stirling or solar thermal engines

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)

Abstract

A kind of the supercritical carbon dioxide electricity generation system and method for the heat collection combined driving of groove tower, the system include the tower thermal-arrest subsystem of high temperature, low temperature slot type thermal-arrest subsystem and supercritical carbon dioxide Brayton cycle power generation sub-system.The tower thermal-arrest subsystem of high temperature is the main source of system input energy, for heating supercritical carbon dioxide fluid, lifts the acting ability of supercritical carbon dioxide as high temperature heat source;Low temperature slot type thermal-arrest subsystem, for making up the backheat deficiency of high-pressure side working medium, improves the heat exchange efficiency of system as auxiliary thermal source;Supercritical carbon dioxide Brayton cycle power generation sub-system is used for the heat exchange efficiency using low-grade thermal source lifting system, reduce in regenerator due to high-pressure side and low-pressure side heat transfer temperature difference are big and caused by heat loss.The present invention takes full advantage of overcritical working medium and lacks this characteristic in Near The Critical Point work done during compression, reduces compression power consumption;Compared to recompression Brayton cycle, recompression machine is eliminated, simplifies system architecture.

Description

The supercritical carbon dioxide electricity generation system and method for the heat collection combined driving of groove tower
Technical field
The present invention relates to regenerative resource applied technical field, overcritical the two of especially a kind of heat collection combined driving of groove tower Carbonoxide electricity generation system and method.
Background technology
The method for improving solar energy power plant efficiency has a lot, and most effective of which method is to improve power cycle, super to face Boundary's carbon dioxide Brayton cycle is arisen at the historic moment.
Supercritical carbon dioxide is a kind of preferable working medium for enclosed TRT, and its cost is very low, non-combustible, nothing Corrosivity, chemical property are stable, can be applied not only to solar energy thermal-power-generating power cycle, can also be applied to nuclear energy, Heat energy and the dynamical system that fossil fuel is thermal source.
The density of supercritical carbon dioxide is larger, and the size of turbomachinery is smaller, compared to traditional power circulating device, with Supercritical carbon dioxide for working medium power cycle structure closely, it will reduce the floor space of power set.In addition, Because supercritical carbon dioxide is not in phase transition process in the circulating cycle, the Temperature Matching degree with thermal source is good, improves heat exchange effect Rate;Meanwhile turbomachinery is also because working medium increases the service life without phase transition process.Because carbon dioxide is near point of proximity The density of (31.1 DEG C, 7.39MPa) is very big, and compressibility is smaller, and the power of compressor is relatively low, and it is super that the power consumption of compressor is smaller The main reason for critical carbon dioxide Brayton cycle efficiency is higher;When turbine-inlet temperature is 650 DEG C, the cycling hot of system Efficiency can reach 50%.It is expected that future, with the application of high-temperature material, the inlet temperature of high-performance turbine can reach 700 DEG C, the system circulation thermal efficiency will be close to 53% at that time.
Supercritical carbon dioxide Brayton cycle mainly has two kinds of endless form at present, be respectively simple Brayton cycle and Recompress Brayton cycle.For simple Brayton cycle because the regenerator internal heat temperature difference is larger, irreversible loss is larger, compares Traditional endless form, the raising of cycle efficieny and unobvious.And it is then more consumption part compressions to recompress Brayton cycle Work(, greatly reduce heat recovery process irreversible loss.The cycle efficieny of system is obviously improved, but recompresses drawing for machine Enter, make the structure of system relative complex, system building cost increases.
The supercritical carbon dioxide electricity generation system and method for a kind of heat collection combined driving of groove tower proposed by the present invention, using not The mode utilized with grade external heat source complementation solves regenerator heat exchange mismatch problem, while improving the thermal efficiency, letter Change the structure of system, reduce the equipment investment of system and the land area of solar energy thermal-power-generating factory.The present invention is further Reduce solar energy thermal-power-generating cost and provide theoretical foundation, play an important roll to solar energy thermal-power-generating development.
The content of the invention
(1) technical problems to be solved
At present, although simply closely, economy is higher, thermal effect for the structure of supercritical carbon dioxide Brayton cycle Rate improves and unobvious, this be due to the heat transfer temperature difference of regenerator mesohigh side and low-pressure side working medium it is excessive caused by;Recompression Bretton is provided with high/low temperature regenerator, and sets up recompression machine, solves the problems, such as that regenerator heat transfer temperature difference is big, but disappear more Partial shrinkage work(is consumed, system is more complicated.The present invention is in view of the above-mentioned problems, propose a kind of the super of heat collection combined driving of groove tower Critical carbon dioxide electricity generation system and method, using different grade solar heat-collection complementation Application ways, release energy in regenerator Put side and receiving side more matches, while system structural compactness is kept, improve cycle efficieny.
(2) technical scheme
In order to solve the above technical problems, the invention provides a kind of supercritical carbon dioxide of heat collection combined driving of groove tower hair Electric system and method, the system include the tower thermal-arrest subsystem of high temperature, low temperature slot type thermal-arrest subsystem and supercritical carbon dioxide Brayton cycle power generation sub-system, wherein:The tower thermal-arrest subsystem of high temperature, it is the master of system input energy as high temperature heat source Source is wanted, for heating supercritical carbon dioxide fluid, lifts the acting ability of supercritical carbon dioxide;Low temperature slot type thermal-arrest System, as auxiliary thermal source, for making up the backheat deficiency of high-pressure side working medium, improve the heat exchange efficiency of system;Overcritical dioxy Change carbon Bretton circulating generation subsystem, for the heat exchange efficiency using low-grade thermal source lifting system, reduce in regenerator Due to high-pressure side and low-pressure side heat transfer temperature difference are big and caused by heat loss.
In such scheme, the tower thermal-arrest subsystem of high temperature includes heliostat field 1, tower 2 and heat dump 3, wherein, heat absorption Device 3 is located at the top of tower 2, and entrance is connected to the high temperature regenerator 6 of supercritical carbon dioxide Brayton cycle power generation sub-system High pressure side outlet, outlet are connected to the turbine 4 of supercritical carbon dioxide Brayton cycle power generation sub-system;Heat dump 3, which absorbs, to be come From the solar energy of heliostat field 1, heating is by the supercritical carbon dioxide working medium of therein to supercritical carbon dioxide mine-laying The inlet temperature of the turbine 4 of circulating generation subsystem.
In such scheme, the low temperature slot type thermal-arrest subsystem includes endothermic tube 13 and parabola groove mirror field 12, wherein, heat absorption Pipe 13 absorbs the solar energy from parabolic groove type mirror field 12, heats the supercritical carbon dioxide working medium of shunting;Endothermic tube 13 enters Mouth is connected to the current divider 11 of supercritical carbon dioxide Brayton cycle power generation sub-system, and outlet is connected to supercritical carbon dioxide The entrance of the blender 8 of Brayton cycle power generation sub-system.
In such scheme, the supercritical carbon dioxide Brayton cycle power generation sub-system includes turbine 4, generator 5, height Warm regenerator 6, cryogenic regenerator 7, blender 8, cooler 9, compressor 10 and current divider 11 wherein, after being heated by heat dump 3 Supercritical carbon dioxide working medium, into turbine 4 and the expansion work in turbine 4, then sequentially enter the low of high temperature regenerator 6 Pressure side, the low-pressure side of cryogenic regenerator 7 and cooler 9 are cooled down;By a series of above-mentioned coolings, supercritical carbon dioxide work Matter enters back into after compressor 10 compresses close to critical condition and forms High-pressure supercritical carbon dioxide working medium;The outlet of compressor 10 It is connected with current divider 11, High-pressure supercritical carbon dioxide working medium is after the shunting of current divider 11, all the way into cryogenic regenerator 7 High-pressure side, enter blender 8, the high pressure of cryogenic regenerator 7 after the endothermic tube 13 of low temperature slot type collecting system heats all the way Side outlet is connected to blender 8;Blended mixed height of the High-pressure supercritical carbon dioxide working medium through high temperature regenerator 6 of device 8 Press side entrance to enter high temperature regenerator 6 and carry out backheat, then the supercritical carbon dioxide working medium after backheat is again introduced into high temperature tower The heat dump 3 of formula collection thermal sub-system.
In such scheme, the endothermic tube 13 is used for the supercritical carbon dioxide working medium for heating shunting, makes its temperature with warp The temperature for crossing the supercritical carbon dioxide working medium of the heating of cryogenic regenerator 7 is identical.
In such scheme, the entrance of the compressor 10 is connected to cooler 9, and outlet is connected to current divider 11, for carrying The pressure of supercritical carbon dioxide working medium is risen, forms High-pressure supercritical carbon dioxide working medium;Compressor 10 is in carbon dioxide working medium Near The Critical Point it is compressed, make full use of carbon dioxide to compress small advantage in Near The Critical Point, reduce compressor Power consumption.
In such scheme, the current divider 11 is used to High-pressure supercritical carbon dioxide working medium being divided into two-way, all the way directly Backheat is carried out into the high-pressure side of cryogenic regenerator 7, another way enters endothermic tube 13, ensures cryogenic regenerator high-pressure side and low pressure The working medium mass flow ratio of side meets heat transfer requirements.
In such scheme, the outlet of the blender 8 is connected to the entrance of high temperature regenerator 6, for by cryogenic regenerator 7 The working medium of working medium and endothermic tube 13 outlet of high pressure side outlet is well mixed.
To reach above-mentioned purpose, present invention also offers a kind of generating of the supercritical carbon dioxide of heat collection combined driving of groove tower Method, this method include:Heat dump 3 absorbs the solar energy from heliostat field 1, and the overcritical dioxy of therein is passed through in heating Change carbon working medium;Supercritical carbon dioxide working medium after being heated by heat dump 3, into turbine 4 and the expansion work in turbine 4, so The low-pressure side of high temperature regenerator 6, the low-pressure side of cryogenic regenerator 7 and cooler 9 is sequentially entered afterwards to be cooled down;Through supercooling Afterwards, supercritical carbon dioxide working medium enters back into after compressor 10 compresses close to critical condition and forms High-pressure supercritical carbon dioxide Working medium;High-pressure supercritical carbon dioxide working medium is after the shunting of current divider 11, all the way into the high-pressure side of cryogenic regenerator 7, all the way Enter blender 8 after the endothermic tube 13 of low temperature slot type collecting system heats;The blended mixed High-pressure supercritical two of device 8 High pressure side inlet of the carbonoxide working medium through high temperature regenerator 6 enters high temperature regenerator 6 and carries out backheat, then overcritical after backheat Carbon dioxide working medium is again introduced into the heat dump 3 of the tower thermal-arrest subsystem of high temperature.
In such scheme, the endothermic tube 13 absorbs the solar energy from parabolic groove type mirror field 12, heats the super of shunting and faces Boundary's carbon dioxide working medium.
(3) beneficial effect
From above-mentioned technical scheme as can be seen that the invention has the advantages that:
1st, the supercritical carbon dioxide electricity generation system and method for the heat collection combined driving of groove tower proposed by the invention, by high temperature High temperature heat source of the tower collecting system as carbon dioxide Brayton cycle electricity generation system, it is the main next of system dynamic circulation Source;Auxiliary thermal source using low temperature slot type collecting system as system, it is the work through cryogenic regenerator backheat after being shunted for heating Mass flow, the heat balance of cryogenic regenerator is maintained, embodying can cascade utilization theory.
2nd, the supercritical carbon dioxide electricity generation system and method for the heat collection combined driving of groove tower proposed by the invention, is eliminated Recompression machine, compared to existing recompression Brayton Cycle system, working medium does not shunt before cooler is entered, but is compressing Machine outlet manifold.So all working medium is all to enter compressor compresses in Near The Critical Point, takes full advantage of overcritical dioxy Change characteristic of the carbon in " high density " and " intimate incompressible " of Near The Critical Point, reduce compression power consumption, improve system Acting ability, generated energy are improved obviously, and optimize systematic function.
3rd, the supercritical carbon dioxide electricity generation system of the heat collection combined driving of groove tower proposed by the invention and method, use are low Warm slot type collecting system replaces recompression machine, reduces compression power consumption, while solves cryogenic regenerator energy release side heat The problem of insufficient, obtain the cryogenic regenerator identical heat exchange efficiency with recompression Brayton Cycle system.It is of the invention abundant The advantages of make use of parabola groove collecting system, tower collecting system, and the solar energy heating to different grades has carried out step profit With i.e. parabola groove Jing Chang is respectively used to the low temperature backheat and overheat of supercritical carbon dioxide with the solar energy that heliostat field is collected into Process.
Brief description of the drawings
Fig. 1 is showing for the supercritical carbon dioxide electricity generation system of the heat collection combined driving of groove tower according to the embodiment of the present invention 1 It is intended to.
Fig. 2 is showing for the supercritical carbon dioxide electricity generation system of the heat collection combined driving of groove tower according to the embodiment of the present invention 2 It is intended to.
Embodiment
For the object, technical solutions and advantages of the present invention are more clearly understood, below in conjunction with specific embodiment, and reference Accompanying drawing, the present invention is described in more detail.
As shown in figure 1, Fig. 1 is the supercritical carbon dioxide hair of the heat collection combined driving of groove tower according to the embodiment of the present invention 1 The schematic diagram of electric system, the system include low temperature slot type thermal-arrest subsystem, the tower thermal-arrest subsystem of high temperature and overcritical titanium dioxide Carbon Bretton circulating generation subsystem, wherein:Low temperature slot type thermal-arrest subsystem, as auxiliary thermal source, for making up high-pressure side work The backheat deficiency of matter, the heat exchange efficiency of system is improved, reduced in regenerator because high-pressure side and low-pressure side heat transfer temperature difference are made greatly Into heat loss;The tower thermal-arrest subsystem of high temperature, it is the main source of system input energy, for heating as high temperature heat source Supercritical carbon dioxide fluid, lift the acting ability of supercritical carbon dioxide;Supercritical carbon dioxide Brayton cycle generates electricity Subsystem, for the interior energy of high-temperature supercritical carbon dioxide to be converted into electric energy.
The tower thermal-arrest subsystem of high temperature includes heliostat field 1, tower 2 and heat dump 3, wherein, heat dump 3 is located at the top of tower 2 Portion, entrance are connected to the high pressure side outlet of the high temperature regenerator 6 of supercritical carbon dioxide Brayton cycle power generation sub-system, outlet It is connected to the turbine 4 of supercritical carbon dioxide Brayton cycle power generation sub-system;Heat dump 3 is absorbed from heliostat field 1 too It is positive can, heating is by the supercritical carbon dioxide working medium of therein to supercritical carbon dioxide Brayton cycle power generation sub-system Turbine 4 inlet temperature.
Low temperature slot type thermal-arrest subsystem includes endothermic tube 13 and parabola groove mirror field 12, wherein, endothermic tube 13 is absorbed from throwing The solar energy of thing slot type mirror field 12, heat the supercritical carbon dioxide working medium of shunting;The entrance of endothermic tube 13 is connected to overcritical The current divider 11 of carbon dioxide Brayton cycle power generation sub-system, outlet are connected to the generating of supercritical carbon dioxide Brayton cycle The entrance of the blender 8 of subsystem.
Supercritical carbon dioxide Brayton cycle power generation sub-system includes turbine 4, generator 5, high temperature regenerator 6, low temperature Regenerator 7, blender 8, cooler 9, compressor 10 and current divider 11, wherein, the overcritical titanium dioxide after being heated by heat dump 3 Carbon working medium, into turbine 4 and the expansion work in turbine 4, then sequentially enter low-pressure side, the low temperature backheat of high temperature regenerator 6 The low-pressure side and cooler 9 of device 7 are cooled down;By a series of above-mentioned coolings, supercritical carbon dioxide working medium is close to critical shape State, enter back into after compressor 10 compresses and form High-pressure supercritical carbon dioxide working medium;The outlet of compressor 10 is the same as the phase of current divider 11 Connection, High-pressure supercritical carbon dioxide working medium is after the shunting of current divider 11, all the way into the high-pressure side of cryogenic regenerator 7, all the way Enter blender 8 after the endothermic tube 13 of low temperature slot type collecting system heats, the high pressure side outlet of cryogenic regenerator 7 is connected to Blender 8;High pressure side inlet of the blended mixed High-pressure supercritical carbon dioxide working medium of device 8 through high temperature regenerator 6 enters High temperature regenerator 6 carries out backheat, and then the supercritical carbon dioxide working medium after backheat is again introduced into the tower thermal-arrest subsystem of high temperature Heat dump 3.
In Fig. 1, endothermic tube 13 is used for the supercritical carbon dioxide working medium for heating shunting, makes its temperature is same to pass through low temperature backheat The temperature for the supercritical carbon dioxide working medium that device 7 heats is identical.The entrance of compressor 10 is connected to condenser 9, and outlet is connected to Current divider 11, for lifting the pressure of supercritical carbon dioxide working medium, form High-pressure supercritical carbon dioxide working medium;Compressor 10 It is compressed in the Near The Critical Point of carbon dioxide working medium, makes full use of carbon dioxide to be compressed in Near The Critical Point small excellent Gesture, reduce compressor power consumption.Current divider 11 is used to High-pressure supercritical carbon dioxide working medium being divided into two-way, is directly entered all the way low The high-pressure side of warm regenerator 7 carries out backheat, and another way enters endothermic tube 13, ensures the work of cryogenic regenerator high-pressure side and low-pressure side Matter mass flow ratio meets heat transfer requirements.The outlet of blender 8 is connected to the high pressure side inlet of high temperature regenerator 6, for inciting somebody to action The working medium that the working medium and endothermic tube 13 that cryogenic regenerator 7 exports export is well mixed.
The supercritical carbon dioxide of the heat collection combined driving of groove tower based on the foundation embodiment of the present invention 1 shown in Fig. 1 generates electricity The schematic diagram of system, present invention also offers a kind of slot type and the supercritical carbon dioxide mine-laying of tower collecting system joint driving Circulating generation method, this method include following technological process:Heat dump 3 absorbs the solar energy from heliostat field 1, heating warp Cross the supercritical carbon dioxide working medium of therein;Supercritical carbon dioxide working medium after being heated by heat dump 3, into turbine 4 And the expansion work in turbine 4, then sequentially enter the low-pressure side of high temperature regenerator 6, the low-pressure side of cryogenic regenerator 7 and cooling Device 9 is cooled down;After supercooling, supercritical carbon dioxide working medium enters back into shape after compressor 10 compresses close to critical condition Into High-pressure supercritical carbon dioxide working medium;High-pressure supercritical carbon dioxide working medium is after the shunting of current divider 11, all the way into low temperature The high-pressure side of regenerator 7, enter blender 8 after backheat, heated all the way by the endothermic tube 13 of low temperature slot type collecting system laggard Enter blender 8;Blended mixed high pressure side inlet of the High-pressure supercritical carbon dioxide working medium through high temperature regenerator 6 of device 8 enters Enter high temperature regenerator 6 and carry out backheat, then the supercritical carbon dioxide working medium after backheat is again introduced into the tower thermal-arrest subsystem of high temperature The heat dump 3 of system.Wherein, endothermic tube 13 absorbs the solar energy from parabolic groove type mirror field 13, heats the overcritical dioxy of shunting Change carbon working medium.
Referring once again to Fig. 1, Fig. 1 is the overcritical titanium dioxide of the heat collection combined driving of groove tower according to the embodiment of the present invention 1 The schematic diagram of carbon electricity generation system, the system include:Heliostat field 1, tower 2, heat dump 3, turbine 4, generator 5, high temperature regenerator 6th, cryogenic regenerator 7, blender 8, cooler 9, compressor 10, current divider 11, parabola groove mirror field 12 and endothermic tube 13.Specific stream Cheng Wei:Heliostat field 1 collect too can radiation energy, absorbed by heat dump 3 and be converted into heat energy, heat super facing in heat dump 3 Boundary's carbon dioxide working medium, the working medium of HTHP enter the expansion work of turbine 4, and the overcritical working medium after expansion sequentially enters high temperature The low-pressure side of regenerator 6, the low-pressure side of cryogenic regenerator 7, cooler 9, by a series of coolings, overcritical working medium is close to critical State, enter back into compressor 10 and compress, the outlet of compressor 10 is connected with current divider 11, and High-pressure supercritical working medium is through current divider 11 After shunting, all the way into the high-pressure side backheat heating of cryogenic regenerator 7, all the way by the endothermic tube 13 of low temperature slot type collecting system Heating, the two reaches identical temperature in the entrance of blender 8, after blended device 8 mixes, into the high pressure of high temperature regenerator 6 Side backheat, the working medium after backheat enter back into heat dump 3 and absorbed heat, and complete a circulation.
Fig. 2 is refer to, Fig. 2 is the supercritical carbon dioxide hair of the heat collection combined driving of groove tower according to the embodiment of the present invention 2 The schematic diagram of electric system.The system includes:It is heliostat field 1, tower 2, heat dump 3, turbine 4, generator 5, high temperature regenerator 6, low Warm regenerator 7, blender 8, cooler 9, compressor 10, current divider 11, parabola groove mirror field 12, endothermic tube 13, cryogenic heat exchanger 14th, high-temperature heat-exchanging 15, the cold tank 16 of high-temperature heat accumulation device, the hot tank 17 of high-temperature heat accumulation device, hot tank 18, the low temperature of low-temperature heat accumulating device The cold tank 19 and pump 20,21,22,23 of storage heater.Idiographic flow is:Solar radiation is poly- through heliostat field 1 and parabola groove mirror field 12 Collect on heat dump 3 and endothermic tube 13,3 and 13 be respectively heat absorption working medium with fused salt and conduction oil (or fused salt).High-temperature molten salt stream Enter high-temperature heat-exchanging 15 after the hot tank 17 of high-temperature heat accumulation device, the cold tank 16 of high-temperature heat accumulation device is entered after heat release;From endothermic tube Hot tank 18 of the conduction oil (or fused salt) through low-temperature heat accumulating device of 13 outflows enters cryogenic heat exchanger 14, and Low Temperature Storage is entered after heat release The cold tank 19 of hot device.Fused salt and conduction oil (or fused salt) after heat release enter heat dump 3 and endothermic tube 13 after pump pressure-raising respectively In, absorb the solar energy that heliostat field and parabola groove Jing Chang are collected into.In supercritical carbon dioxide Brayton cycle electricity generation system Supercritical carbon dioxide heat exchange occurs with fused salt in high-temperature heat-exchanging 15, working medium is heated to the inlet temperature of turbine 4 550℃;The supercritical carbon dioxide of HTHP expansion work in turbine 4, a part of work(driving generator 5 generates electricity, another Part is used for the compression power consumption of compressor 10, and the high temperature refrigerant after expansion respectively enters high temperature regenerator 6 and cryogenic regenerator 7 Low-pressure side, backheat is carried out to high-pressure side carbon dioxide, then cooled down through cooler 9, make the temperature of supercritical carbon dioxide is close to face Boundary's temperature, enter back into compressor 10;In compressor 10, supercritical carbon dioxide is compressed to 20MPa.In order to low temperature backheat Device 7 carries out heat balance, improves heat exchange efficiency, to control the mass flow of the high-pressure side of cryogenic regenerator 7 and low-pressure side working medium, because And the working medium after compressing is shunted before cryogenic regenerator 7 is entered by current divider 11, wherein about 64% working medium enters The high-pressure side of cryogenic regenerator 7, and exchanged heat with low-pressure side working medium, remaining working medium enters 14 same conduction oil of cryogenic heat exchanger (or fused salt) is exchanged heat.In the outlet of cryogenic regenerator 7, the supercritical carbon dioxide of two stock streams reaches identical temperature, Enter 6 further backheat of high temperature regenerator after blended device 8 is well mixed, enter back into high-temperature heat-exchanging 15 and realize a circulation.
Examples 1 and 2 are simulated, the thermodynamic parameter of main streams is as shown in table 1 in system, when turbine entrance is At 550 DEG C, the net generating efficiency of solar energy reaches 26.9%.
Major parameter in the embodiment of table 1
Slot type proposed by the invention and the supercritical carbon dioxide Brayton cycle hair of tower collecting system joint driving Electric system and method, simple Brayton cycle and recompression Brayton cycle are improved, add low temperature slot type thermal-arrest With heating system, recompression machine is instead of, while compression power consumption is reduced, makes the cold and hot side matching of heat recovery process more reasonable, Significantly reduce heat recovery process irreversible loss.
Particular embodiments described above, the purpose of the present invention, technical scheme and beneficial effect are carried out further in detail Describe in detail it is bright, should be understood that the foregoing is only the present invention specific embodiment, be not intended to limit the invention, it is all Within the spirit and principles in the present invention, any modification, equivalent substitution and improvements done etc., it should be included in the guarantor of the present invention Within the scope of shield.

Claims (8)

1. a kind of supercritical carbon dioxide electricity generation system of the heat collection combined driving of groove tower, it is characterised in that the system includes high temperature Tower collection thermal sub-system, low temperature slot type thermal-arrest subsystem and supercritical carbon dioxide Brayton cycle power generation sub-system, wherein:
The tower thermal-arrest subsystem of high temperature, it is the main source of system input energy, for heating overcritical two as high temperature heat source Carbon oxide fluid, lift the acting ability of supercritical carbon dioxide;
Low temperature slot type thermal-arrest subsystem, as auxiliary thermal source, for making up the backheat deficiency of high-pressure side working medium, improve changing for system The thermal efficiency;
Supercritical carbon dioxide Brayton cycle power generation sub-system, for being imitated using the heat exchange of low-grade thermal source lifting system Rate, reduce in regenerator due to high-pressure side and low-pressure side heat transfer temperature difference are big and caused by heat loss;
Wherein, low temperature slot type thermal-arrest subsystem converts solar energy into low temperature heat energy, with heating part stream of supercritical carbon dioxide Body, make its temperature identical with the Temperature of Working of cryogenic regenerator high pressure side outlet;The tower thermal-arrest subsystem of high temperature turns solar energy High temperature heat is turned to, the on high-tension side supercritical carbon dioxide fluid of high temperature regenerator is come from heating;
The supercritical carbon dioxide Brayton cycle power generation sub-system includes turbine (4), generator (5), high temperature regenerator (6), cryogenic regenerator (7), blender (8), cooler (9), compressor (10) and current divider (11), wherein, by heat dump (3) Supercritical carbon dioxide working medium after heating, into turbine (4) and the expansion work in turbine (4), then sequentially enter high temperature The low-pressure side of regenerator (6), the low-pressure side of cryogenic regenerator (7) and cooler (9) are cooled down;By above-mentioned a series of cold But, supercritical carbon dioxide working medium forms High-pressure supercritical titanium dioxide close to critical condition after entering back into compressor (10) compression Carbon working medium;The same current divider in outlet (11) of compressor (10) is connected, and High-pressure supercritical carbon dioxide working medium is through current divider (11) After shunting, all the way into the high-pressure side of cryogenic regenerator (7), heated all the way by the endothermic tube (13) of low temperature slot type collecting system Enter blender (8) afterwards, the high pressure side outlet of cryogenic regenerator (7) is connected to blender (8);Blended device (8) is mixed High pressure side inlet of the High-pressure supercritical carbon dioxide working medium through high temperature regenerator (6) enters high temperature regenerator (6) and carries out backheat, warp Supercritical carbon dioxide working medium after backheat is again introduced into the heat dump (3) of the tower thermal-arrest subsystem of high temperature.
2. the supercritical carbon dioxide electricity generation system of the heat collection combined driving of groove tower according to claim 1, it is characterised in that The tower thermal-arrest subsystem of high temperature includes heliostat field (1), tower (2) and heat dump (3), wherein, heat dump (3) is located at tower (2) top, entrance are connected to the high-pressure side of the high temperature regenerator (6) of supercritical carbon dioxide Brayton cycle power generation sub-system Outlet, outlet are connected to the turbine (4) of supercritical carbon dioxide Brayton cycle power generation sub-system;Heat dump (3), which absorbs, to be come from The solar energy of heliostat field (1), heating is by the supercritical carbon dioxide working medium of therein to supercritical carbon dioxide mine-laying The inlet temperature of the turbine (4) of circulating generation subsystem.
3. the supercritical carbon dioxide electricity generation system of the heat collection combined driving of groove tower according to claim 1, it is characterised in that The low temperature slot type thermal-arrest subsystem includes endothermic tube (13) and parabola groove Jing Chang (12), wherein, endothermic tube (13), which absorbs, to be come from The solar energy of parabolic groove type mirror field (12), heat the supercritical carbon dioxide working medium of shunting;The entrance of endothermic tube (13) is connected to The current divider (11) of supercritical carbon dioxide Brayton cycle power generation sub-system, outlet are connected to supercritical carbon dioxide Bretton The entrance of the blender (8) of circulating generation subsystem.
4. the supercritical carbon dioxide electricity generation system of the heat collection combined driving of groove tower according to claim 1, it is characterised in that Supercritical carbon dioxide working medium of the endothermic tube (13) for heating shunting, makes its temperature add with by cryogenic regenerator (7) The temperature of the supercritical carbon dioxide working medium of heat is identical.
5. the supercritical carbon dioxide electricity generation system of the heat collection combined driving of groove tower according to claim 1, it is characterised in that The entrance of the compressor (10) is connected to cooler (9), and outlet is connected to current divider (11), for lifting overcritical titanium dioxide The pressure of carbon working medium, form High-pressure supercritical carbon dioxide working medium;Near The Critical Point of the compressor (10) in carbon dioxide working medium It is compressed, makes full use of carbon dioxide in the small advantage of Near The Critical Point compressibility, reduction compressor power consumption.
6. the supercritical carbon dioxide electricity generation system of the heat collection combined driving of groove tower according to claim 1, it is characterised in that The current divider (11) is used to High-pressure supercritical carbon dioxide working medium being divided into two-way, is directly entered cryogenic regenerator (7) all the way High-pressure side carry out backheat, another way enters endothermic tube (13), ensure the mass flow of cryogenic regenerator (7) high-pressure side working medium with The ratio of the mass flow of low-pressure side working medium meets heat transfer requirements.
7. the supercritical carbon dioxide electricity generation system of the heat collection combined driving of groove tower according to claim 1, it is characterised in that The outlet of the blender (8) is connected to the high pressure side inlet of high temperature regenerator (6), for by cryogenic regenerator (7) high-pressure side The working medium of working medium and endothermic tube (13) outlet of outlet is well mixed.
A kind of 8. supercritical carbon dioxide electricity-generating method of the heat collection combined driving of groove tower, applied to any one of claim 1 to 7 The supercritical carbon dioxide electricity generation system of the described heat collection combined driving of groove tower, it is characterised in that this method includes:
Heat dump (3) absorbs the solar energy from heliostat field (1), and the supercritical carbon dioxide work of therein is passed through in heating Matter;
Supercritical carbon dioxide working medium after being heated by heat dump (3), into turbine (4) and the expansion work in turbine (4), so The low-pressure side of high temperature regenerator (6), the low-pressure side of cryogenic regenerator (7) and cooler (9) is sequentially entered afterwards to be cooled down;
After supercooling, supercritical carbon dioxide working medium forms high pressure close to critical condition after entering back into compressor (10) compression Supercritical carbon dioxide working medium;
High-pressure supercritical carbon dioxide working medium is after current divider (11) shunting, all the way into the high-pressure side of cryogenic regenerator (7), one Road enters blender (8) after endothermic tube (13) heating of low temperature slot type collecting system;The endothermic tube (13), which absorbs, to be come from The solar energy of parabolic groove type mirror field (12), heat the supercritical carbon dioxide working medium of shunting;
High pressure side inlet of the blended mixed High-pressure supercritical carbon dioxide working medium of device (8) through high temperature regenerator (6) enters High temperature regenerator (6) carries out backheat, and then the supercritical carbon dioxide working medium after backheat is again introduced into the tower thermal-arrest subsystem of high temperature The heat dump (3) of system.
CN201610036862.9A 2016-01-20 2016-01-20 The supercritical carbon dioxide electricity generation system and method for the heat collection combined driving of groove tower Active CN105673107B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610036862.9A CN105673107B (en) 2016-01-20 2016-01-20 The supercritical carbon dioxide electricity generation system and method for the heat collection combined driving of groove tower

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610036862.9A CN105673107B (en) 2016-01-20 2016-01-20 The supercritical carbon dioxide electricity generation system and method for the heat collection combined driving of groove tower

Publications (2)

Publication Number Publication Date
CN105673107A CN105673107A (en) 2016-06-15
CN105673107B true CN105673107B (en) 2018-03-23

Family

ID=56301652

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610036862.9A Active CN105673107B (en) 2016-01-20 2016-01-20 The supercritical carbon dioxide electricity generation system and method for the heat collection combined driving of groove tower

Country Status (1)

Country Link
CN (1) CN105673107B (en)

Families Citing this family (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107131017A (en) * 2017-04-27 2017-09-05 西安交通大学 Circulation therrmodynamic system and control method based on supercritical carbon dioxide axial flow compressor Yu axial-flow turbine coaxial configuration
CN107023447A (en) * 2017-06-22 2017-08-08 哈尔滨锅炉厂有限责任公司 Using carbon dioxide as the groove type solar solar-thermal generating system of collection hot working fluid
CN107237656B (en) * 2017-07-26 2020-03-31 西安交通大学 Coaxial structure of supercritical carbon dioxide centrifugal compressor and axial flow turbine
CN107327325B (en) * 2017-08-03 2023-08-29 上海发电设备成套设计研究院有限责任公司 Supercritical carbon dioxide and liquid metal combined cycle system
CN107401431B (en) * 2017-09-08 2023-03-14 西安热工研究院有限公司 Supercritical carbon dioxide generalized carnot circulation system
CN107355265B (en) * 2017-09-08 2023-08-11 西安热工研究院有限公司 Supercritical carbon dioxide efficient flexible cogeneration system
CN107630726B (en) * 2017-09-26 2023-08-29 上海发电设备成套设计研究院有限责任公司 Multi-energy hybrid power generation system and method based on supercritical carbon dioxide circulation
CN108361163B (en) * 2017-12-05 2023-10-13 北京石油化工学院 Power generation system
CN108612571B (en) * 2018-07-04 2024-05-03 西安热工研究院有限公司 Supercritical carbon dioxide Brayton cycle working medium adjusting system and method
CN109113821A (en) * 2018-08-01 2019-01-01 王闯业 A kind of wide width energy cycle engine
CN109098803A (en) * 2018-09-13 2018-12-28 中国核动力研究设计院 Heat stepped utilization method and its system based on supercritical carbon dioxide
CN110043337B (en) * 2019-04-22 2023-11-28 西安交通大学 Carbon dioxide transcritical flow state thermodynamic cycle system and working method
CN110159375A (en) * 2019-05-24 2019-08-23 华北电力大学 Tower type solar-fire coal coupling heat source carbon dioxide electricity generation system and method
CN112302744A (en) * 2019-08-02 2021-02-02 四季洋圃生物机电股份有限公司 Supercritical power generation system
CN110905747B (en) * 2019-11-28 2021-07-13 西安石油大学 Combined power cycle power generation system utilizing high-temperature solar energy and LNG cold energy
CN111102142A (en) * 2019-12-03 2020-05-05 西安理工大学 Tower type solar thermal power generation system based on supercritical fluid
CN112696242B (en) * 2020-11-30 2023-02-28 合肥通用机械研究院有限公司 A reposition of redundant personnel regulation and control system for supercritical carbon dioxide recompression circulation
CN112832882B (en) * 2021-01-27 2023-03-21 中冶华天南京工程技术有限公司 Heating furnace energy-saving system based on supercritical carbon dioxide and operation method
CN113958379B (en) * 2021-09-18 2023-08-08 浙江高晟光热发电技术研究院有限公司 Supercritical carbon dioxide Brayton cycle power generation system and method
CN114135351A (en) * 2021-12-01 2022-03-04 中国核动力研究设计院 Two-stage parallel supercritical carbon dioxide recompression circulating system and method

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4215553A (en) * 1978-06-26 1980-08-05 Sanders Associates, Inc. Energy conversion system
JPS5675915A (en) * 1979-08-09 1981-06-23 Setsuo Yamamoto Power generator
CN101539123B (en) * 2008-03-19 2011-06-29 中国科学院工程热物理研究所 Groove-tower combined two-stage heat-storage solar-heat power generation system
CN104632560A (en) * 2015-02-09 2015-05-20 南京瑞柯徕姆环保科技有限公司 Method and system for closing type Britten-Rankine combined cycle solar heat power generation
CN105201579A (en) * 2015-10-16 2015-12-30 上海晶电新能源有限公司 Supercritical carbon dioxide power generation system based on secondary reflection condensation heat-absorption technique

Also Published As

Publication number Publication date
CN105673107A (en) 2016-06-15

Similar Documents

Publication Publication Date Title
CN105673107B (en) The supercritical carbon dioxide electricity generation system and method for the heat collection combined driving of groove tower
CN107630726B (en) Multi-energy hybrid power generation system and method based on supercritical carbon dioxide circulation
CN207829962U (en) Nuclear energy based on supercritical carbon dioxide cycle and solar energy hybrid power system
CN105863977B (en) A kind of supercritical carbon dioxide Brayton cycle electricity generation system and method
CN102435000B (en) Solar energy system combined cooling and electricity based on ammonia water mixed refrigerant
CN103032912B (en) Solar integrated Rankine-Rankine system floor heating device
CN107355265B (en) Supercritical carbon dioxide efficient flexible cogeneration system
CN109441741A (en) It is a kind of based on supercritical carbon dioxide circulation can peak regulation energy-storage system and its control method
CN107940789A (en) A kind of new cool and thermal power combined generating system based on movable solar energy heat collector
CN107355269A (en) A kind of supercritical carbon dioxide and helium combined cycle system
CN109681279A (en) A kind of the supercritical carbon dioxide electricity generation system and method for the energy storage containing liquid air
CN104632559B (en) One kind is with CO2It is the method for electric generation using solar energy and electricity generation system of working medium
CN108661731A (en) A kind of overcritical Brayton cycle electricity generation system and method with cold-storage
CN206530370U (en) Using the Brayton Cycle system of supercritical carbon dioxide
CN206539381U (en) A kind of supercritical carbon dioxide cycle generating system based on combustion gas and solar heat
CN206016878U (en) A kind of coal base supercritical carbon dioxide electricity generation system containing solar energy preheating
CN205779516U (en) A kind of band accumulation of heat and the CO of refrigeration2brayton cycle solar-thermal generating system
CN207348915U (en) Multipotency hybrid power system based on supercritical carbon dioxide circulation
CN108643982A (en) A kind of overcritical Brayton cycle electricity generation system and method that band refrigeration is cooling
CN104747389B (en) A kind of liquefied natural gas gasifying system and method based on solar energy circulating generation
CN216342359U (en) Combined heat and power device for carbon dioxide power generation and geothermal energy coupling
CN115031283B (en) Thermoelectric flexible storage and supply system and operation method thereof
CN207647560U (en) Supercritical carbon dioxide and helium combined cycle system
CN106437904B (en) A kind of coal base supercritical carbon dioxide electricity generation system of solar energy medium temperature preheating
CN206739403U (en) A kind of heating system of providing multiple forms of energy to complement each other of cascaded utilization of energy

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant