CN106090865A - Supercritical carbon dioxide boiler radiation heating surface arrangement method - Google Patents
Supercritical carbon dioxide boiler radiation heating surface arrangement method Download PDFInfo
- Publication number
- CN106090865A CN106090865A CN201610654055.3A CN201610654055A CN106090865A CN 106090865 A CN106090865 A CN 106090865A CN 201610654055 A CN201610654055 A CN 201610654055A CN 106090865 A CN106090865 A CN 106090865A
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- China
- Prior art keywords
- radiation heating
- working medium
- carbon dioxide
- supercritical carbon
- burner
- 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.)
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- 230000005855 radiation Effects 0.000 title claims abstract description 113
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 title claims abstract description 100
- 229910002092 carbon dioxide Inorganic materials 0.000 title claims abstract description 50
- 239000001569 carbon dioxide Substances 0.000 title claims abstract description 50
- 238000000034 method Methods 0.000 title claims abstract description 20
- 238000010438 heat treatment Methods 0.000 title claims abstract description 19
- 238000003303 reheating Methods 0.000 claims abstract description 28
- 239000012530 fluid Substances 0.000 claims description 5
- 230000002093 peripheral effect Effects 0.000 claims description 3
- 239000007769 metal material Substances 0.000 abstract 1
- 238000001816 cooling Methods 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 239000003245 coal Substances 0.000 description 3
- 239000004744 fabric Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 241000790917 Dioxys <bee> Species 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical group [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 239000000956 alloy Substances 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000031018 biological processes and functions Effects 0.000 description 1
- 230000017531 blood circulation Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 230000009897 systematic effect Effects 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B31/00—Modifications of boiler construction, or of tube systems, dependent on installation of combustion apparatus; Arrangements of dispositions of combustion apparatus
- F22B31/08—Installation of heat-exchange apparatus or of means in boilers for heating air supplied for combustion
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22G—SUPERHEATING OF STEAM
- F22G7/00—Steam superheaters characterised by location, arrangement, or disposition
- F22G7/12—Steam superheaters characterised by location, arrangement, or disposition in flues
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23L—SUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
- F23L15/00—Heating of air supplied for combustion
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Heat Treatment Of Articles (AREA)
- Control Of Steam Boilers And Waste-Gas Boilers (AREA)
Abstract
The invention discloses an arrangement method of a water-cooled wall of a radiation heating surface of a supercritical carbon dioxide boiler. The main working medium radiation heating surface is arranged in a burner area, an area above the burner and a furnace top, and the reheating working medium radiation heating surface is arranged in an area below the burner and a cold ash bucket area. The arrangement method enables the inlet section of the radiation heating surface of the main working medium to be just positioned in the area near the burner, namely, the pipe section with the lowest working medium temperature in the whole hearth is arranged in the area with the highest heat load distribution coefficient along the height direction of the hearth, so that the problem that the pipe wall temperature of the radiation heating surface of the high-parameter supercritical carbon dioxide boiler is too high is effectively solved, the safety of the boiler is improved, and the requirement of the radiation heating surface of the supercritical carbon dioxide boiler on high-temperature metal materials is reduced.
Description
Technical field
The invention belongs to the efficient field of thermal power of supercritical carbon dioxide Brayton cycle, be specifically related to a kind of supercritical
Carbon dioxide Boiler radiation heated surface arrangement method.
Background technology
Supercritical carbon dioxide Brayton cycle is one of the most generally acknowledged most potential advanced power cycle.Due to super
Critical carbon dioxide has that energy density is big, heat transfer efficiency high, supercritical carbon dioxide Brayton cycle efficiency power generation
System can reach the efficiency of conventional steam Rankine cycle 700 DEG C in 620 DEG C of temperature ranges, it is not necessary to novel height of redeveloping
Temperature alloy, and equipment size is less than the steam unit of same parameter, application prospect is the best.
The composition feature of China's energy reserves determines coal group of motors and remains China's power industry in coming few decades
Main force, therefore, applies supercritical carbon dioxide Brayton cycle and tallies with the national condition very much at Thermal generation unit, be me
One of technology path of great potential in state's power industry energy-saving and emission-reduction.Send out as supercritical carbon dioxide Brayton cycle fire coal
The nucleus equipment of group of motors, the security relationship of supercritical carbon dioxide boiler, to the stable operation of whole blood circulation, surpasses and faces
The construction cost of boundary's carbon dioxide boiler is also the pith of whole electricity generation system initial cost.Therefore, how by reasonably
Heating surface is arranged, can reduce boiler cost, and can ensure that again the long-term safety of boiler is run is that coal base supercritical carbon dioxide is sent out
One of difficult point of power technology.
Due to carbon dioxide and the difference of water physical property, and the difference of Brayton cycle and Rankine cycle, supercritical dioxy
Change carbon boiler and have significantly difference with traditional supercritical steam boiler.One of them marked difference the most is: dioxy
Changing regenerator heat exchange amount in carbon Brayton cycle very big, high pressure Biological process is heated to the highest temperature and just can enter by the weary gas of turbine
Enter boiler, so the temperature of supercritical carbon dioxide boiler inlet working medium is far above the steam boiler of same parameter.With 25MPa,
As a example by the systematic parameter of 600/600/32 DEG C, the boiler inlet Temperature of Working for the supercritical steam boiler of Rankine cycle is
About 300～320 DEG C, and for the boiler of supercritical carbon dioxide Brayton cycle, its boiler inlet Temperature of Working is about
It it is 500～530 DEG C.Therefore, the tube wall temperature of carbon dioxide Boiler radiation heating surface will be apparently higher than the steam boiler of same parameter.
It addition, in the region that Load Distribution coefficient is high in steam boiler burner hearth, in water-cooling wall, working medium is in large specific heat region, heat exchange system
Number is significantly higher, and in the region that Load Distribution coefficient is higher in the burner hearth of supercritical carbon dioxide boiler, radiation is heated
In face (being equivalent to steam boiler water-cooling wall), working medium works in the region away from large specific heat region, the coefficient of heat transfer only about steam kettle
The 1/2～1/5 of stove water-cooling wall, this temperature mistake being easier to cause supercritical carbon dioxide Boiler radiation heating surface metal pipe-wall
High.Therefore, for the feature of supercritical carbon dioxide boiler, arranged by rational heating surface and reduce radiation heating-surface as far as possible
Tube wall temperature the most necessary.
But the most all rarely have open achievement and patent introduction to relate to solving high parameter supercritical carbon dioxide pot
The method that stove water-cooling wall local wall temperature is too high.
Summary of the invention
The purpose of the present invention is the problem that the supercritical carbon dioxide water screen tube wall temperature solved is too high, it is provided that Yi Zhongchao
Critical carbon dioxide Boiler radiation heated surface arrangement method, the method can effectively reduce high parameter supercritical carbon dioxide boiler
Main working medium radiation heating-surface tube wall temperature, along the wall temperature difference in furnace height direction, reduces main working medium radiation heating-surface tube wall temperature
Peak value.
For reaching above-mentioned purpose, the technical solution adopted in the present invention is:
A kind of supercritical carbon dioxide Boiler radiation heated surface arrangement method, the radiation heating-surface arranged in burner hearth, spoke
Penetrating heating surface and include reheating working medium radiation heating-surface and main working medium radiation heating-surface, reheating working medium radiation heating-surface is with thermal technology again
Matter radiation heating-surface entrance and the outlet of reheating working medium radiation heating-surface, main working medium radiation heating-surface is with main working medium radiation heating-surface
Entrance and the outlet of main working medium radiation heating-surface；Wherein, main working medium radiation heating-surface is arranged in the peripheral region of burner, burner
Upper area and furnace roof, reheating working medium radiation heating-surface is arranged in lower zone and the furnace hopper region of burner.
Described reheating working medium radiation heating-surface and main working medium radiation heating-surface all use the structure of fin panel casing.
Connected by expansion joint between described reheating working medium radiation heating-surface and main working medium radiation heating-surface.
Described main working medium radiation heating-surface entrance is arranged in the position of L/10～L/15 below burner, and wherein L is burner hearth
Highly, the outlet of main working medium radiation heating-surface is arranged in furnace roof.
Described reheating working medium radiation heating-surface entrance is arranged in furnace bottom, and the outlet of reheating working medium radiation heating-surface is arranged in main work
The lower section of matter radiation heating-surface entrance.
Compared with prior art, the method have the advantages that and present invention employs novel radiation heating-surface cloth
Method of putting heating surface internal to supercritical carbon dioxide boiler furnace is arranged, is arranged by main working medium radiation heating-surface especially
Region above burner region, burner and furnace roof, reheating working medium radiation heating-surface is arranged in the region below burner
And furnace hopper region.In this method for arranging, the radiation heating-surface main working medium radiation that in burner hearth, Temperature of Working is minimum is heated
The entrance in face has been disposed in the burner neighboring area that Load Distribution coefficient in burner hearth is the highest, and Temperature of Working in burner hearth
The outlet section of the highest radiation heating-surface main working medium radiation heating-surface has been disposed in burner hearth Load Distribution coefficient
Low furnace roof region.By using this new method for arranging, effectively reduce high parameter supercritical carbon dioxide boiler main
Working medium radiation heating-surface tube wall temperature, along the wall temperature difference in furnace height direction, reduces main working medium radiation heating-surface tube wall temperature
Peak value, while improve the safety of supercritical carbon dioxide boiler, can reduce again the cost of its radiation heating-surface.
The present invention using main working medium radiation heating-surface entrance as the entrance in working medium loop of supercritical carbon dioxide boiler,
By cancelling traditional boiler economizer, reduce further the Temperature of Working of main working medium radiation heating-surface porch, thus enter
One step reduces the tube wall temperature of burner region main working medium radiation heating-surface.
With 25MPa, as a example by the 300MW supercritical carbon dioxide boiler of 600/600 DEG C, can through boiler " water " Cable Power Computation
Knowing: when using traditional main working medium radiation heating-surface method for arranging, the wall temperature of supercritical carbon dioxide Boiler radiation heating surface is
High point is about 640 DEG C, and when using the present invention, the wall temperature peak of supercritical carbon dioxide Boiler radiation heating surface is about 610
℃。
Accompanying drawing explanation
Fig. 1 is the structural representation that the present invention applies in high parameter single reheat supercritical carbon dioxide π type boiler.
Wherein, 1 is reheating working medium radiation heating-surface；1-1 is reheating working medium radiation heating-surface entrance；1-2 is again hot working fluid
Radiation heating-surface exports；2 is main working medium radiation heating-surface；2-1 is main working medium radiation heating-surface entrance；2-2 is the radiation of main working medium
Heating surface exports；3 is high temperature superheater；4 is high temperature reheater；5 is low-temperature reheater；6 is low temperature superheater；7 is low for shunting
Temperature economizer；8 is air preheater；9 is burner.
Detailed description of the invention
With embodiment, the present invention is described in further detail below in conjunction with the accompanying drawings:
The present invention illustrates as a example by π type boiler, but is not limited to π type boiler.
Seeing Fig. 1, present invention resides in the radiation heating-surface arranged in burner hearth, radiation heating-surface includes two parts: reheating
Working medium radiation heating-surface 1 (being equivalent to " secondary soda pop cold wall ") and main working medium radiation heating-surface 2 (are equivalent to that " soda pop is cold
Wall ").The most main working medium radiation heating-surface 2 is arranged in the peripheral region of burner 9, the upper area of burner 9 and furnace roof, then
Hot working fluid radiation heating-surface 1 is arranged in lower zone and the furnace hopper region of burner 9.Reheating working medium radiation heating-surface 1 and master
Working medium radiation heating-surface 2 all uses the structure of membrane type " water " cold wall, reheating working medium radiation heating-surface 1 and main working medium radiation heating-surface
Connected by expansion joint between 2.Main working medium radiation heating-surface entrance 2-1 is arranged in the position of about L/10～L/15 below burner 9
Putting (L is furnace height), main working medium radiation heating-surface outlet 2-2 is arranged in furnace roof.Reheating working medium radiation heating-surface entrance 1-1 cloth
Putting at furnace bottom, reheating working medium radiation heating-surface outlet 1-2 is arranged in the lower section of main working medium radiation heating-surface entrance 2-1.At this cloth
Putting in method, the entrance of the radiation heating-surface main working medium radiation heating-surface that in burner hearth, Temperature of Working is minimum is disposed in
The burner neighboring area that in burner hearth, Load Distribution coefficient is the highest, and the radiation heating-surface that in burner hearth, Temperature of Working is the highest
The outlet section of main working medium radiation heating-surface has been disposed in the furnace roof region that Load Distribution coefficient in burner hearth is minimum, this layout
Mode effectively reduces the supercritical carbon dioxide boiler main working medium radiation heating-surface tube wall temperature wall along furnace height direction
Temperature approach, reduces the peak value of main working medium radiation heating-surface tube wall temperature, in the safety that improve supercritical carbon dioxide boiler
While, the cost of its main working medium radiation heating-surface can be reduced again.Additionally, flue rear portion is provided with shunting low-level (stack-gas) economizer 7
With the air preheater 8 being arranged on below shunting low-level (stack-gas) economizer 7, shunting low-level (stack-gas) economizer 7 is arranged on low temperature superheater 6 and low
The lower section of temperature reheater 5.
The working medium flow of main working medium: boiler main working medium is cold from supercritical carbon dioxide Brayton cycle high temperature regenerator
The High-pressure supercritical carbon dioxide of side outlet, this partial high pressure supercritical carbon dioxide is from main working medium radiation heating-surface entrance 2-1
Enter boiler furnace, flow through the highest burner region tube panel of Load Distribution coefficient, Load Distribution coefficient successively medium
Burner upper area tube panel and the relatively low furnace roof tube panel of Load Distribution coefficient, drawn by main working medium radiation heating-surface outlet 2-2
To low temperature superheater 6, subsequently flow into high temperature superheater 3, be heated to main " steam " design parameter.
The working medium flow of hot working fluid again: boiler hot working fluid again is from supercritical carbon dioxide Brayton cycle high pressure turbine
The middle pressure supercritical carbon dioxide of outlet, presses supercritical carbon dioxide from reheating working medium radiation heating-surface entrance 1-1 in this part
Enter boiler furnace, flow through the relatively low furnace hopper tube panel of Load Distribution coefficient and the medium burning of Load Distribution coefficient successively
Device lower zone tube panel, is caused low-temperature reheater 5 by reheating working medium radiation heating-surface outlet 1-2, subsequently flows into high temperature reheater
4, it is heated to reheating " steam " design parameter.
The present invention considers from the own characteristic of supercritical carbon dioxide boiler, by rational heating surface arrangement, subtracts
Little main working medium radiation heating-surface tube wall temperature, along the wall temperature difference in furnace height direction, reduces main working medium radiation heating-surface tube wall temperature
Degree peak value, improve supercritical carbon dioxide boiler safety, and guarantee safety on the premise of reduce main working medium radiation be subject to
The grade of hot side metal pipe material, reduces boiler cost.
Above-described detailed description of the invention, has been carried out the purpose of the present invention, technical scheme and beneficial effect further
Describe in detail, be it should be understood that the detailed description of the invention that the foregoing is only the present invention, be not limited to this
Bright, all within the spirit and principles in the present invention, any modification, equivalent substitution and improvement etc. done, should be included in the present invention
Protection domain within.
Claims (5)
1. a supercritical carbon dioxide Boiler radiation heated surface arrangement method, it is characterised in that: the radiation arranged in burner hearth
Heating surface, radiation heating-surface includes reheating working medium radiation heating-surface (1) and main working medium radiation heating-surface (2), and reheating working medium radiates
Heating surface (1) exports (1-2) with reheating working medium radiation heating-surface entrance (1-1) and reheating working medium radiation heating-surface, main working medium
Radiation heating-surface (2) exports (2-2) with main working medium radiation heating-surface entrance (2-1) and main working medium radiation heating-surface；Wherein, main
Working medium radiation heating-surface (2) is arranged in the peripheral region of burner (9), the upper area of burner (9) and furnace roof, then hot working fluid
Radiation heating-surface (1) is arranged in lower zone and the furnace hopper region of burner (9).
A kind of supercritical carbon dioxide Boiler radiation heated surface arrangement method the most according to claim 1, it is characterised in that:
Described reheating working medium radiation heating-surface (1) and main working medium radiation heating-surface (2) all use the structure of fin panel casing.
A kind of supercritical carbon dioxide Boiler radiation heated surface arrangement method the most according to claim 1, it is characterised in that:
Connected by expansion joint between described reheating working medium radiation heating-surface (1) and main working medium radiation heating-surface (2).
A kind of supercritical carbon dioxide Boiler radiation heated surface arrangement method the most according to claim 1, it is characterised in that:
Described main working medium radiation heating-surface entrance (2-1) is arranged in the position of burner (9) lower section L/10～L/15, and wherein L is burner hearth
Highly, main working medium radiation heating-surface outlet (2-2) is arranged in furnace roof.
A kind of supercritical carbon dioxide Boiler radiation heated surface arrangement method the most according to claim 1, it is characterised in that:
Described reheating working medium radiation heating-surface entrance (1-1) is arranged in furnace bottom, and reheating working medium radiation heating-surface outlet (1-2) is arranged in master
The lower section of working medium radiation heating-surface entrance (2-1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610654055.3A CN106090865B (en) | 2016-08-10 | 2016-08-10 | Supercritical carbon dioxide boiler radiation heating surface arrangement method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610654055.3A CN106090865B (en) | 2016-08-10 | 2016-08-10 | Supercritical carbon dioxide boiler radiation heating surface arrangement method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106090865A true CN106090865A (en) | 2016-11-09 |
| CN106090865B CN106090865B (en) | 2018-06-22 |
Family
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Family Applications (1)
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| CN201610654055.3A Active CN106090865B (en) | 2016-08-10 | 2016-08-10 | Supercritical carbon dioxide boiler radiation heating surface arrangement method |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106949451A (en) * | 2017-04-26 | 2017-07-14 | 华中科技大学 | A kind of double reheat ultra-supercritical boiler and its heated surface arrangement method |
| CN107906498A (en) * | 2017-10-25 | 2018-04-13 | 东南大学 | Supercritical carbon dioxide circulating fluidized bed combustion coal boiler and its electricity generation system of driving |
| CN108916847A (en) * | 2018-07-13 | 2018-11-30 | 西安热工研究院有限公司 | Using the heat convection supercritical carbon dioxide boiler of large scale flue gas recirculation |
| CN111336493A (en) * | 2020-02-27 | 2020-06-26 | 西安交通大学 | Device and process method for producing low-temperature and low-pressure steam in power station boiler |
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|---|---|---|---|---|
| EP2554803A1 (en) * | 2011-08-02 | 2013-02-06 | Siemens Aktiengesellschaft | Cyclical process assembly and cyclical process method |
| CN104728823A (en) * | 2015-03-17 | 2015-06-24 | 西安热工研究院有限公司 | Novel supercritical carbon dioxide coal-fired boiler |
| CN105526576A (en) * | 2016-01-20 | 2016-04-27 | 西安热工研究院有限公司 | Coal-based supercritical carbon dioxide Brayton cycle double-split-flow efficient power generation system |
-
2016
- 2016-08-10 CN CN201610654055.3A patent/CN106090865B/en active Active
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP2554803A1 (en) * | 2011-08-02 | 2013-02-06 | Siemens Aktiengesellschaft | Cyclical process assembly and cyclical process method |
| CN104728823A (en) * | 2015-03-17 | 2015-06-24 | 西安热工研究院有限公司 | Novel supercritical carbon dioxide coal-fired boiler |
| CN105526576A (en) * | 2016-01-20 | 2016-04-27 | 西安热工研究院有限公司 | Coal-based supercritical carbon dioxide Brayton cycle double-split-flow efficient power generation system |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106949451A (en) * | 2017-04-26 | 2017-07-14 | 华中科技大学 | A kind of double reheat ultra-supercritical boiler and its heated surface arrangement method |
| CN107906498A (en) * | 2017-10-25 | 2018-04-13 | 东南大学 | Supercritical carbon dioxide circulating fluidized bed combustion coal boiler and its electricity generation system of driving |
| CN108916847A (en) * | 2018-07-13 | 2018-11-30 | 西安热工研究院有限公司 | Using the heat convection supercritical carbon dioxide boiler of large scale flue gas recirculation |
| CN111336493A (en) * | 2020-02-27 | 2020-06-26 | 西安交通大学 | Device and process method for producing low-temperature and low-pressure steam in power station boiler |
| CN111336493B (en) * | 2020-02-27 | 2021-01-19 | 西安交通大学 | Device and process method for producing low-temperature and low-pressure steam in power station boiler |
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| Publication number | Publication date |
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| CN106090865B (en) | 2018-06-22 |
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