CN206875399U - A kind of supercritical carbon dioxide double reheat coal-fired electric generation furnace system - Google Patents

A kind of supercritical carbon dioxide double reheat coal-fired electric generation furnace system Download PDF

Info

Publication number
CN206875399U
CN206875399U CN201720448106.7U CN201720448106U CN206875399U CN 206875399 U CN206875399 U CN 206875399U CN 201720448106 U CN201720448106 U CN 201720448106U CN 206875399 U CN206875399 U CN 206875399U
Authority
CN
China
Prior art keywords
wall
flue
reheat
double reheat
antetheca
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
CN201720448106.7U
Other languages
Chinese (zh)
Inventor
向军
张晨浩
周敬
胡松
苏胜
汪一
江龙
徐俊
许凯
肖鸣
肖一鸣
廖广
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.)
Huazhong University of Science and Technology
Original Assignee
Huazhong University of Science and Technology
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 Huazhong University of Science and Technology filed Critical Huazhong University of Science and Technology
Priority to CN201720448106.7U priority Critical patent/CN206875399U/en
Application granted granted Critical
Publication of CN206875399U publication Critical patent/CN206875399U/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
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/34Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery

Abstract

It the utility model is related to a kind of supercritical carbon dioxide double reheat coal-fired electric generation furnace system, it includes burner hearth and flue, burner hearth is vertically arranged, the side wall of burner hearth is made up of cooling wall and reheating wall, cooling wall is located at below reheating wall, the middle part of cooling wall and lower area are provided with burner, hot wall is made up of single reheat wall and double reheat wall again, the terrain clearance of single reheat wall and double reheat wall is equal or close, and the classification of flue interior edge flow of flue gas direction is provided with superheater module and reheater module.The beneficial effects of the utility model are, then the novel in structural design of hot wall, on the premise of not increasing furnace height and being also not required to be horizontal by chamber design, realize three-level heat absorption and acting, the utilization rate of the energy is high;Be the single reheat wall and double reheat wall that particular combination may be selected by appropriate valve opening and closing, i.e. the heating surface area of single reheat wall and double reheat wall can adjust, therefore can flexible modulation hot working fluid again temperature, ensure that again the degree of superheat of hot working fluid is up to standard.

Description

A kind of supercritical carbon dioxide double reheat coal-fired electric generation furnace system
Technical field
The utility model belongs to advanced field of generating equipment, and in particular to a kind of supercritical carbon dioxide double reheat is coal-fired Electricity generation boiler system.
Background technology
Because the discharge of the efficiency, reduction pollutant that improve generating set is an eternal topic, therefore some are new general Ideo-motor Force system is paid close attention to.The physical property of supercritical carbon dioxide is special, and under identical burden requirement, work is used as using it The electricity generation system of matter is smaller, more compact structure, can save floor occupying area, reduce cost, simultaneously because its energy density It is bigger than water, it is more efficient as the steam generator system of working medium using supercritical carbon dioxide in the case of existing steel high temperature resistant level.
Under the background of carbon dioxide discharge-reduction, as collecting carbonic anhydride, research on utilization go deep into, it will help faced with super Boundary's carbon dioxide is the development of the electricity generation system of working medium.Retrieve Patents and find that there is presently no collecting carbonic anhydride, profit With the case being combined together with the electricity generation system using supercritical carbon dioxide as working medium, as patent 201610038208.1 is a kind of Coal base supercritical carbon dioxide Brayton cycle double split flow efficient power generation system, a kind of 201510117556.3 Novel supercriticals two Carbonoxide coal-burning boiler.
In supercritical carbon dioxide double reheat coal-fired electric generation furnace system implementation process, hot working fluid again sometimes be present The problem of temperature overheating degree is not up to standard.For this problem, solution of the prior art is as follows:Patent of invention 201610654055.3 a kind of supercritical carbon dioxide Boiler radiation heated surface arrangement method, it is in hearth combustor lower disposed Reheating working medium radiation heating-surface, the method for arranging main working medium radiation heating-surface in burner peripheral region and upper area, it is not Foot part is:Can only realize that single reheat is done work, can not double reheat acting, and cascaded utilization of energy rate is low, causes energy Amount wastes;A kind of Novel supercritical carbon dioxide coal-burning boiler of patent of invention 201510117556.3, its be horizontal furnace structure and It arranges the attached wall radiation cooling heating surface of three ranks in burner hearth, and it is disadvantageous in that:On the one hand, three ranks is attached The ratio of wall radiation cooling heating surface and position be it is certain, its be unable to burning inside flexible adaptation different load lower hearth and Heat transfer situation, spirit can not be carried out to the degree of superheat deficiency problem of single reheat working medium and double reheat working medium under different load Regulation living, on the other hand, horizontal furnace structure has the defects of its is intrinsic, flue gas stream bottom horizontal flow sheet and thermal current can be spontaneous upward, So relative superiority or inferiority is low in flue-gas temperature on same section, temperature field actual distribution differs with design can be larger, and heat exchange is bad, by The utilizing status in hot face is bad, while it must be drained using more powerful blower fan to flue gas, and energy consumption is higher.Therefore it is existing There is the effective means for lacking in technology and solving reheating working medium degree of superheat problem not up to standard.
Utility model content
For deficiency of the prior art, the utility model provides a kind of supercritical carbon dioxide double reheat coal fired power generation Steam generator system, it can carry out flexible modulation to single reheat working medium, the degree of heat of double reheat working medium, effectively to solve its mistake The problem of temperature is not up to standard.
The technical scheme that the utility model solves above-mentioned technical problem is as follows:A kind of supercritical carbon dioxide double reheat combustion Coal power generation steam generator system, including burner hearth and flue, the burner hearth are vertically arranged, one end of the flue and the upper end of the burner hearth Portion is connected, and the side wall of the burner hearth is made up of cooling wall and reheating wall, and the cooling wall is located at below the reheating wall, described cold But the middle part of wall and lower area are provided with burner, and the hot wall again is made up of single reheat wall and double reheat wall, described The terrain clearance of single reheat wall and double reheat wall is equal or close, and the flue interior edge flow of flue gas direction classification is provided with Superheater module and reheater module.
On the basis of above-mentioned technical proposal, the utility model can also do following improvement.
Further, the cross section of the burner hearth is rectangle, and the hot wall again is made up of antetheca, rear wall, left wall and right wall, institute The upper and lower ends for stating antetheca, rear wall, left wall and right wall are each provided with independent header, and the single reheat wall is by before described In wall, rear wall, left wall and right wall any one, two or three and corresponding independent header composition, remaining wall and its two The independent header composition double reheat wall at end.Each in antetheca, rear wall, left wall and right wall is set in the upper and lower ends of oneself There is independent independent header, it is ensured that the convenient single reheat wall and double reheat wall for realizing multiple combinations.Existing boiler The section of burner hearth be rectangle mostly, therefore the section of burner hearth of utility model steam generator system provided by the utility model is preferably also Rectangle.Section of burner hearth is rectangle, then length and width are different, therefore the endotherm area of antetheca rear wall is different from the endotherm area of left wall right wall, This causes single reheat wall and double reheat wall to have more kinds of different combinations, to facilitate the temperature for adjusting again hot working fluid.
Further, the single reheat wall is made up of the antetheca and rear wall and corresponding independent header, it is described it is secondary again Hot wall is made up of the left wall and right wall and corresponding independent header.
Further, the single reheat wall is made up of the antetheca and left wall and corresponding independent header, it is described it is secondary again Hot wall is made up of the rear wall and right wall and corresponding independent header.
Further, the single reheat wall is made up of the antetheca, rear wall and left wall and corresponding independent header, and described two Secondary hot wall again is made up of the right wall and corresponding independent header.
Further, the superheater module includes pendant superheater, the hyperthermia and superheating set gradually along flow of flue gas direction Device and low temperature superheater, the reheater module include the high temperature reheater group set gradually along flow of flue gas direction and low temperature again Hot device group, the high temperature reheater group includes a high temperature reheater being arranged in parallel and secondary high-temperature reheater (is arranged in parallel Refer to that a high temperature reheater and secondary high-temperature reheater are set on flow of flue gas direction in same position, flue gas passes through simultaneously Both), the low-temperature reheater group includes a low-temperature reheater being arranged in series and secondary low-temperature reheater, and (being arranged in series is Refer to a low-temperature reheater and secondary low-temperature reheater successively to set on flow of flue gas direction, first pass through once during flow of flue gas Low-temperature reheater, then by secondary low-temperature reheater).
Further, the flue is made up of horizontal flue and vertical flue, the both ends of the horizontal flue respectively with it is described The upper end connection of burner hearth and the vertical flue, be provided with the horizontal flue pendant superheater, high temperature superheater and High temperature reheater group, the vertical flue are disposed with gas baffle, economizer and air preheater along flow of flue gas direction, The side of the gas baffle is provided with the low temperature superheater, and the opposite side of the gas baffle is provided with the cold reheat Device group.
Further, high temperature reheater outlet and the outlet of secondary high-temperature reheater by independent pipeline and Corresponding valve connects with four independent headers of the antetheca, rear wall, left wall and right wall lower end respectively, the antetheca, Rear wall, left wall and four independent headers of right wall upper end by independent pipeline and corresponding valve respectively with gas-turbine High pressure cylinder entrance connected with gas-turbine intermediate pressure cylinder entrance, the outlet of the pendant superheater and the ultra-high pressure cylinder entrance of gas-turbine Connection.
Further, the cooling wall is 0.5L≤L in the length of vertical direction1< L, the hot wall again is in vertical direction Length is 0 < L2≤ 0.5L, L are furnace height, L1It is cooling wall in the length of vertical direction, L2It is hot wall again in vertical direction Length.
Compared with prior art, the beneficial effects of the utility model are:
(1) novel in structural design of hot wall, including the single reheat wall and double reheat that terrain clearance is close or equal again Wall, that is, along a vertical plane two parts (including but is not limited to this kind of situation) will be split into by hot wall again, do not increasing burner hearth Height and also it is not required on the premise of being horizontal type structure by chamber design, it is working medium in cooling wall to realize using supercritical carbon dioxide After super-pressure acting after place's heat absorption, the high pressure after heat absorption at single reheat wall are done work and absorbed heat at double reheat wall In, low pressure acting, without the inherent shortcoming of horizontal chamber furnace (oven), heat transfer efficiency is high, can twice work doing, to cascaded utilization of energy, the energy Utilization ratio is high.
(2) heating surface area of single reheat wall and double reheat wall of the present utility model can be according to appropriate adjustment be needed, i.e., Its recept the caloric it is adjustable, single reheat wall can select in the wall of front, rear, left and right four any one, two or three, it is remaining For double reheat wall, the single reheat acting and double reheat acting of different load are suitable for, is by appropriate valve opening and closing May be selected the single reheat wall and double reheat wall of particular combination, thus can flexible modulation hot working fluid again temperature, ensure thermal technology again The degree of superheat of matter is up to standard.
Brief description of the drawings
Fig. 1 is a kind of signal of supercritical carbon dioxide double reheat coal-fired electric generation furnace system provided by the utility model Figure;
Fig. 2 is diagrammatic cross-section of the steam generator system along A-A shown in Fig. 1;
Fig. 3 is the connection relationship diagram of each part of steam generator system shown in Fig. 1.
In accompanying drawing, the list of parts representated by each label is as follows:
1. cooling wall;2. burner;3. hot wall again;3-1. single reheat walls;3-2. double reheat walls;4. screen formula overheats Device;5. high temperature superheater;A 6. high temperature reheater;7. secondary high-temperature reheater;A 8. low-temperature reheater;9. two low temperature Reheater;10. low temperature superheater;11. economizer;12. air preheater;13. compressor;14. ultra-high pressure cylinder;15. high pressure cylinder; 16. intermediate pressure cylinder;17. low pressure (LP) cylinder.
Embodiment
Principle of the present utility model and feature are described below in conjunction with drawings and the specific embodiments, example is only used In explaining the utility model, the scope of the utility model is not intended to limit.
As shown in Figures 1 to 3, the utility model provides a kind of supercritical carbon dioxide double reheat coal-fired electric generation furnace system System, including burner hearth and flue, the burner hearth are vertically arranged, and the side wall of the burner hearth is made up of cooling wall 1 and reheating wall 3, described For cooling wall 1 positioned at the lower section of reheating wall 3, the middle part of the cooling wall 1 and lower area are provided with burner 2, the reheating Wall 3 is made up of single reheat wall 3-1 and double reheat wall 3-2, and single reheat wall 3-1 and double reheat the wall 3-2's is liftoff Highly equal or close, the flue interior edge flow of flue gas direction classification is provided with superheater module and reheater module.
Further, the cross section of the burner hearth is rectangle, and the reheating wall 3 is made up of antetheca, rear wall, left wall and right wall, The antetheca, rear wall, the upper and lower ends of left wall and right wall are each provided with independent header, the single reheat wall 3-1 by In the antetheca, rear wall, left wall and right wall any one, two or three and corresponding independent header composition.
Further, the superheater module includes pendant superheater 4, the hyperthermia and superheating set gradually along flow of flue gas direction Device 5 and low temperature superheater 10, the reheater module include the high temperature reheater group that is set gradually along flow of flue gas direction and low Warm reheater group, the high temperature reheater group include the high temperature reheater 6 and secondary high-temperature reheater 7 being set up in parallel, institute State a low-temperature reheater 8 and secondary low-temperature reheater 9 that low-temperature reheater group includes being arranged in series.
Further, the flue is made up of horizontal flue and vertical flue, the both ends of the horizontal flue respectively with it is described The upper end of burner hearth and the vertical flue is connected, and the pendant superheater 4, high temperature superheater 5 are provided with the horizontal flue With high temperature reheater group, it is pre- that the vertical flue along flow of flue gas direction is disposed with gas baffle, economizer 11 and air Hot device 12, the side of the gas baffle are provided with the low temperature superheater 10, and the opposite side of the gas baffle is set State low-temperature reheater group.
Further, the cooling wall 1 is 0.5L≤L in the length of vertical direction1< L, the reheating wall 3 is in vertical direction Length be 0 < L2≤ 0.5L, L are furnace height, L1It is cooling wall 1 in the length of vertical direction, L2It is reheating wall 3 vertical The length in direction.
Specifically, the connected mode of each part is as shown in Figure 3:The outlet of compressor 13 connects with the entrance of economizer 11, saves The outlet of coal device 11 connects with the entrance independence header of cooling wall 1, and cooling wall 1 exports independent header and connected with the entrance of low temperature superheater 10 Logical, the outlet of low temperature superheater 10 connects with the entrance of high temperature superheater 5, and the outlet of high temperature superheater 5 connects with the entrance of pendant superheater 4 Logical, the outlet of pendant superheater 4 connects with the entrance of ultra-high pressure cylinder 14 of gas-turbine;Gas-turbine ultra-high pressure cylinder 14 exports and a low temperature The entrance of reheater 8 connects, and an outlet of low-temperature reheater 8 connects with an entrance of high temperature reheater 6, a high temperature reheating Device 6 export and secondary high-temperature reheater 7 export by independent pipeline and corresponding valve respectively with the antetheca, after Wall, left wall connect with four independent headers of right wall lower end, the antetheca, rear wall, left wall and four institutes of right wall upper end Independent header is stated by independent pipeline and corresponding valve respectively with being pressed in the entrance of high pressure cylinder 15 and gas-turbine of gas-turbine The entrance of cylinder 16 connects, and the outlet of gas-turbine high pressure cylinder 15 connects with the secondary entrance of low-temperature reheater 9, the secondary low-temperature reheater 9 outlets connect with the entrance of secondary high-temperature reheater 7, and the outlet of steamer intermediate pressure cylinder 16 connects with the entrance of low pressure (LP) cylinder 17, institute The outlet for stating low pressure (LP) cylinder 17 connects with compressor 13, completes whole cyclic process.
, can be by controlling the keyings of respective valves, flexibly according to single reheat and the specific burden requirement of double reheat The various combination in the antetheca, rear wall, left wall and right wall and corresponding independent header is selected to respectively constitute single reheat wall 3-1 With double reheat wall 3-2.
Embodiment 1
As shown in Fig. 2 under specific burden requirement, using antetheca, rear wall and corresponding independent header as single reheat wall 3-1, left wall and right wall and corresponding independent header are double reheat wall 3-2.
The opening and closing situation of valve and specific connected relation are as follows:Outlet of high temperature reheater 6 and the antetheca and rear wall The valve opening on connecting pipe between the independence header of respective lower end, the outlet of secondary high-temperature reheater 7 and the left wall and the right side The respective valve opening on the connecting pipe between lower end independence header of wall, the antetheca and rear wall each upper end independence header with The valve opening on connecting pipe between the entrance of high pressure cylinder 15 of gas-turbine, the respective upper end independence header of the left wall and right wall The valve opening on connecting pipe between the entrance of intermediate pressure cylinder 16 of gas-turbine;Meanwhile a high temperature reheater 6 exports and institute The valve stated on the connecting pipe of left wall and right wall each between lower end independence header is closed, the outlet of secondary high-temperature reheater 7 with Each the valve on the connecting pipe between lower end independence header is closed for the antetheca and rear wall, the antetheca and rear wall each on The valve on the connecting pipe between the entrance of intermediate pressure cylinder 16 of independent header and gas-turbine is held to close, the left wall and right wall are each Valve on connecting pipe between upper end independence header and the entrance of high pressure cylinder 15 of gas-turbine is closed.
Embodiment 2
Under another specific burden requirement, using antetheca, left wall and corresponding independent header as single reheat wall 3-1, after Wall and right wall and corresponding independent header are double reheat wall 3-2.
The opening and closing situation of valve and specific connected relation are as follows:Outlet of high temperature reheater 6 and the antetheca and left wall The valve opening on connecting pipe between the independence header of respective lower end, the outlet of secondary high-temperature reheater 7 and the rear wall and the right side The respective valve opening on the connecting pipe between lower end independence header of wall, the antetheca and left wall each upper end independence header with The respective upper end independence header of the valve opening on connecting pipe between the entrance of high pressure cylinder 15 of gas-turbine, the rear wall and right wall The valve opening on connecting pipe between the entrance of intermediate pressure cylinder 16 of gas-turbine;Meanwhile a high temperature reheater 6 exports and institute The valve stated on the connecting pipe of rear wall and right wall each between lower end independence header is closed, the outlet of secondary high-temperature reheater 7 with The valve of the antetheca and left wall each on the connecting pipe between lower end independence header is closed, the antetheca and left wall each on The valve on the connecting pipe between the entrance of intermediate pressure cylinder 16 of independent header and gas-turbine is held to close, the rear wall and right wall are each Valve on connecting pipe between upper end independence header and the entrance of high pressure cylinder 15 of gas-turbine is closed.
Embodiment 3
Under other specific burden requirement, using antetheca, rear wall and left wall and corresponding independent header as single reheat wall 3-1, right wall and corresponding independent header are double reheat wall 3-2.
The opening and closing situation of valve and specific connected relation are as follows:The outlet of high temperature reheater 6 and the antetheca, rear wall and The respective valve opening on the connecting pipe between lower end independence header of left wall, the outlet of secondary high-temperature reheater 7 and the right wall The valve opening on connecting pipe between the independence header of lower end, the antetheca, rear wall and left wall each upper end independence header with The valve opening on connecting pipe between the entrance of high pressure cylinder 15 of gas-turbine, the right wall upper end independence header and gas-turbine The valve opening on connecting pipe between the entrance of intermediate pressure cylinder 16;Meanwhile an outlet of high temperature reheater 6 and the right wall lower end Valve on connecting pipe between independent header is closed, and the outlet of secondary high-temperature reheater 7 is each with the antetheca, rear wall and left wall Closed from the valve on the connecting pipe between the independence header of lower end, the respective upper end independence header of the antetheca, rear wall and left wall Valve on connecting pipe between the entrance of intermediate pressure cylinder 16 of gas-turbine is closed, the right wall upper end independence header and gas-turbine The entrance of high pressure cylinder 15 between connecting pipe on valve close.
I.e. after load changes, according to the tool of the single reheat working medium of reality and double reheat working medium degree of superheat deficiency Body situation, by adjust different valve opening and closings or aperture to single reheat wall 3-1 and double reheat wall 3-2 endotherm area and Working medium flow is allocated adjustment, so that the degree of superheat of single reheat working medium and double reheat working medium is up to standard.
Preferred embodiment of the present utility model is the foregoing is only, it is all in this practicality not to limit the utility model Within new spirit and principle, any modification, equivalent substitution and improvements made etc., guarantor of the present utility model should be included in Within the scope of shield.

Claims (9)

1. a kind of supercritical carbon dioxide double reheat coal-fired electric generation furnace system, including burner hearth and flue, the burner hearth are vertical Set, one end of the flue connects with the top of the burner hearth, it is characterised in that the side wall of the burner hearth is by cooling wall (1) Hot wall (3) forms again, and the cooling wall (1) is below the hot wall (3) again, the middle part and bottom of the cooling wall (1) Region is provided with burner (2), and the hot wall again (3) is made up of single reheat wall (3-1) and double reheat wall (3-2), described The terrain clearance of single reheat wall (3-1) and double reheat wall (3-2) is equal or close, the flue interior edge flow of flue gas direction Classification is provided with superheater module and reheater module.
2. a kind of supercritical carbon dioxide double reheat coal-fired electric generation furnace system according to claim 1, its feature exist In the hot wall again (3) is made up of antetheca, rear wall, left wall and right wall, the antetheca, rear wall, the upper and lower ends of left wall and right wall Independent header is each provided with, the single reheat wall (3-1) is by any one in the antetheca, rear wall, left wall and right wall Individual, two or three and corresponding independent header composition.
3. a kind of supercritical carbon dioxide double reheat coal-fired electric generation furnace system according to claim 2, its feature exist In the single reheat wall (3-1) is made up of the antetheca and rear wall and corresponding independent header, the double reheat wall (3- 2) it is made up of the left wall and right wall and corresponding independent header.
4. a kind of supercritical carbon dioxide double reheat coal-fired electric generation furnace system according to claim 2, its feature exist In the single reheat wall (3-1) is made up of the antetheca and left wall and corresponding independent header, the double reheat wall (3- 2) it is made up of the rear wall and right wall and corresponding independent header.
5. a kind of supercritical carbon dioxide double reheat coal-fired electric generation furnace system according to claim 2, its feature exist In the single reheat wall (3-1) is made up of the antetheca, rear wall and left wall and corresponding independent header, the double reheat Wall (3-2) is made up of the right wall and corresponding independent header.
6. a kind of supercritical carbon dioxide double reheat coal-fired electric generation furnace system according to any one of claim 1 to 5, Characterized in that, the superheater module includes pendant superheater (4), the high temperature superheater set gradually along flow of flue gas direction (5) and low temperature superheater (10), the reheater module include the high temperature reheater group set gradually along flow of flue gas direction and Low-temperature reheater group, the high temperature reheater group include a high temperature reheater (6) and the secondary high-temperature reheater being arranged in parallel (7), the low-temperature reheater group includes a low-temperature reheater (8) and the secondary low-temperature reheater (9) being arranged in series.
7. a kind of supercritical carbon dioxide double reheat coal-fired electric generation furnace system according to claim 6, its feature exist In, the flue is made up of horizontal flue and vertical flue, the both ends of the horizontal flue respectively with the burner hearth and described perpendicular The upper end of straight flue is connected, and the pendant superheater (4), high temperature superheater (5) and high temperature are provided with again in the horizontal flue Hot device group, the vertical flue are disposed with gas baffle, economizer (11) and air preheater along flow of flue gas direction (12), the side of the gas baffle is provided with the low temperature superheater (10), and the opposite side of the gas baffle is set State low-temperature reheater group.
8. a kind of supercritical carbon dioxide double reheat coal-fired electric generation furnace system according to claim 6, its feature exist In the hot wall again (3) is made up of antetheca, rear wall, left wall and right wall, the antetheca, rear wall, the upper and lower ends of left wall and right wall Independent header is each provided with, a high temperature reheater (6) outlet and the outlet of secondary high-temperature reheater (7) pass through The four independent headers of independent pipeline and corresponding valve respectively with the antetheca, rear wall, left wall and right wall lower end connect Logical, the antetheca, rear wall, left wall and four independent headers of right wall upper end pass through independent pipeline and corresponding valve Connected respectively with high pressure cylinder (15) entrance and gas-turbine intermediate pressure cylinder (16) entrance of gas-turbine, pendant superheater (4) go out Mouth connects with ultra-high pressure cylinder (14) entrance of gas-turbine.
9. a kind of supercritical carbon dioxide double reheat coal-fired electric generation furnace system according to claim 6, its feature exist In the cooling wall (1) is 0.5L≤L1 < L in the length of vertical direction, and the hot wall again (3) is in the length of vertical direction 0 < L2≤0.5L, L is furnace height, and L1 is length of the cooling wall (1) in vertical direction, and L2 is hot wall (3) again in vertical direction Length.
CN201720448106.7U 2017-04-26 2017-04-26 A kind of supercritical carbon dioxide double reheat coal-fired electric generation furnace system Active CN206875399U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201720448106.7U CN206875399U (en) 2017-04-26 2017-04-26 A kind of supercritical carbon dioxide double reheat coal-fired electric generation furnace system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201720448106.7U CN206875399U (en) 2017-04-26 2017-04-26 A kind of supercritical carbon dioxide double reheat coal-fired electric generation furnace system

Publications (1)

Publication Number Publication Date
CN206875399U true CN206875399U (en) 2018-01-12

Family

ID=61344382

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201720448106.7U Active CN206875399U (en) 2017-04-26 2017-04-26 A kind of supercritical carbon dioxide double reheat coal-fired electric generation furnace system

Country Status (1)

Country Link
CN (1) CN206875399U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106979512A (en) * 2017-04-26 2017-07-25 华中科技大学 A kind of supercritical carbon dioxide double reheat coal-fired electric generation furnace system
CN112989511A (en) * 2021-02-09 2021-06-18 华中科技大学 Boiler design method and system of supercritical carbon dioxide unit and storage medium

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106979512A (en) * 2017-04-26 2017-07-25 华中科技大学 A kind of supercritical carbon dioxide double reheat coal-fired electric generation furnace system
CN112989511A (en) * 2021-02-09 2021-06-18 华中科技大学 Boiler design method and system of supercritical carbon dioxide unit and storage medium
CN112989511B (en) * 2021-02-09 2024-04-19 华中科技大学 Boiler design method, system and storage medium of supercritical carbon dioxide unit

Similar Documents

Publication Publication Date Title
CN106979512A (en) A kind of supercritical carbon dioxide double reheat coal-fired electric generation furnace system
CN106195983B (en) Coal-fired supercritical carbon dioxide Brayton cycle electricity generation system
CN206036988U (en) Take gas recirculation's overcritical CO2 boiler plant
CN108180470B (en) The fire coal circulating fluid bed boiler of supercritical carbon dioxide and electricity generation system and electricity-generating method
CN108071430B (en) The workflow of supercritical CO 2 Brayton cycle coal generating system working medium and flue gas
CN205897088U (en) Super supercritical carbon dioxide brayton cycle coal -fired generating unit
CN106402831B (en) One kind being used for supercritical CO2The double-flue boiler of Brayton cycle electricity generation system
CN106195984B (en) Novel coal supercritical carbon dioxide Brayton cycle single-stage shunts electricity generation system
CN104728823A (en) Novel supercritical carbon dioxide coal-fired boiler
CN207944993U (en) A kind of integrated supercritical CO2The coal-fired double reheat Turbo-generator Set of cycle
CN107883365A (en) A kind of supercritical carbon dioxide reheating coal fired power generation face-fired boiler system
CN106285805B (en) A kind of coal base supercritical carbon dioxide Brayton cycle electricity generation system of intermediate preheating
CN110230518A (en) A kind of coal base supercritical CO2Brayton cycle electricity generation system and method
CN109944652A (en) Supercritical carbon dioxide circulating flue gas waste heat recycles coal generating system and operation method
CN107120642A (en) A kind of supercritical carbon dioxide CFBB heating system and heating means
CN206875399U (en) A kind of supercritical carbon dioxide double reheat coal-fired electric generation furnace system
CN106247306B (en) A kind of supercritical carbon dioxide boiler heating surface arrangement preventing overtemperature of tube wall
CN205332163U (en) High -efficient power generation system of coal -based super supercritical carbon dioxide brayton cycle double split flow
CN107101187A (en) A kind of supercritical carbon dioxide boiler heating system and heating means
CN107906498B (en) Supercritical carbon dioxide circulating fluidized bed combustion coal boiler and its electricity generation system of driving
CN108036295B (en) The CO2 working medium of supercritical CO 2 Brayton cycle coal-fired electric generation furnace shunts drag-reduction system
CN106122938A (en) A kind of can the double reheat system of power station boiler of homoiothermic flexibly
CN106090865A (en) A kind of supercritical carbon dioxide Boiler radiation heated surface arrangement method
CN108844051A (en) It is a kind of to use supercritical CO2For the new test boiler of working medium
CN105953217B (en) The 1000MW ultra supercritical double reheat boilers of high reheat steam temperature wide regulating ratio

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant