CN214403694U - Double-machine coupling thermodynamic system based on double-reheating coal electric unit - Google Patents
Double-machine coupling thermodynamic system based on double-reheating coal electric unit Download PDFInfo
- Publication number
- CN214403694U CN214403694U CN202023278571.1U CN202023278571U CN214403694U CN 214403694 U CN214403694 U CN 214403694U CN 202023278571 U CN202023278571 U CN 202023278571U CN 214403694 U CN214403694 U CN 214403694U
- Authority
- CN
- China
- Prior art keywords
- double
- pressure cylinder
- regenerative drive
- steam turbine
- boiler
- 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
Links
Images
Landscapes
- Control Of Turbines (AREA)
Abstract
The utility model discloses a double-machine coupling thermodynamic system based on a double reheating coal electric unit, which comprises a main steam turbine generator unit, a regenerative drive steam turbine generator unit, a water supply system and a condensed water system; the main steam turbine generator set boiler, the ultrahigh pressure cylinder, the primary boiler reheater, the high pressure cylinder, the secondary boiler reheater, the intermediate pressure cylinder and the low pressure cylinder; the regenerative drive steam turbine generator unit comprises a regenerative drive steam turbine; the water supply system comprises a deaerator, a water supply pump and a plurality of high-pressure heaters, wherein the final-stage high-pressure heater is communicated with the boiler, the deaerator and the high-pressure heaters are respectively communicated with the regenerative drive steam turbine, and the water supply pump is in transmission connection with the regenerative drive steam turbine. The utility model has the advantages that: the utility model discloses reduced the higher backheat extraction superheat degree in the conventional system, reduced the irreversible loss of backheat system heat transfer, improved backheat cycle efficiency.
Description
Technical Field
The utility model relates to a turbo-generator technical field, specific theory is based on duplex coupling thermodynamic system of twice reheat coal electric unit.
Background
The energy resources of China, rich coal, deficient oil and deficient gas, determine that the power industry pattern mainly based on coal-fired power generation cannot be fundamentally changed for a long time. Coal-fired power generation also produces large amounts of pollution and greenhouse gas emissions while providing a strong support in socioeconomic development. In order to protect the environment and save resources, how to improve the coal-fired power generation efficiency becomes a problem which is more and more emphasized in the industry.
The steam parameters of the coal-fired generator set are continuously improved due to the continuous improvement of the high-temperature performance of the material, so that higher cycle efficiency is obtained, the coal consumption of the generator set is further reduced, and the emission of greenhouse gases and other pollutants is reduced.
In the late 90 th of 20 th century and in the early 21 st century, the European Union, the United states and Japan have started the advanced Ultra Supercritical (USC) power generation technical research plan of 700 ℃ and above, and provide a technology for the next generation of thermal power equipment. The advanced ultra-supercritical power generation plan of AD700 started in 1 month in 1998 in European Union aims to establish a demonstration power station with the grade of 500MW and 700 ℃/720 ℃/35MPa, and combines technical measures of deep coupling of a machine furnace and flue gas waste heat utilization, reduction of back pressure, reduction of pipeline resistance, improvement of water supply temperature and the like to enable the unit efficiency to reach more than 50%. In 2010, 7 months and 23 days, the national energy agency establishes the national ultra-supercritical coal-fired power generation technology innovation alliance and marks that China formally starts related technology research and development. In recent years, domestic coal-fired power generating units at 630 ℃, 650 ℃ and 700 ℃ are under development.
According to the thermodynamic basic principle, initial parameters such as steam pressure and temperature are improved, the average endothermic temperature of the Rankine cycle can be improved, and the method is one of the most direct ways for improving the cycle efficiency of the coal-fired power generation system. However, as the initial steam parameter continues to increase, other problems arise: the extraction superheat degree of the regenerative system is continuously increased, the irreversible loss of heat exchange of the steam side and the water side in the regenerative heater is increased, and the economic benefit brought by steam parameter promotion is weakened. The higher the steam parameter is, the more prominent this contradiction is; the greater the number of reheats, the more significant this weakening effect. For the problem, the traditional solution at present is to add an external steam cooler to the reheated part of the reheated extraction steam to reduce the superheat degree of the reheated extraction steam. However, the method can only reduce the superheat degree and heat exchange loss of the regenerative steam extraction which are respectively contradictory and prominent after reheating, and cannot radically realize the cascade utilization of regenerative steam extraction energy; the grade of the material of the regenerative steam extraction pipeline provided with the external steam cooler can only be reduced, and the problem of high material cost of the regenerative steam extraction pipeline cannot be completely solved.
SUMMERY OF THE UTILITY MODEL
For overcoming the not enough of prior art, the utility model aims to provide a duplex coupling thermodynamic system based on secondary reheat coal electric unit for reduce the heat transfer superheat degree of secondary reheat coal fired power generation unit reheat back regenerative steam extraction by a wide margin, can show and improve regenerative steam extraction energy level utilization efficiency, can reduce high temperature material's application range, reduce power station investment cost simultaneously.
The utility model discloses a following technical scheme realizes: the double-machine coupling thermodynamic system based on the double reheating coal-electricity unit comprises a main steam turbine generator unit, a regenerative drive steam turbine generator unit, a water supply system and a condensate system;
the main steam turbine generator set comprises a boiler, an ultrahigh pressure cylinder, a primary boiler reheater, a high pressure cylinder, a secondary boiler reheater, an intermediate pressure cylinder and a low pressure cylinder which are sequentially communicated according to the steam circulation direction;
the regenerative drive steam turbine generator unit comprises a regenerative drive steam turbine of which the inlet end is communicated with the outlet end of the ultrahigh pressure cylinder;
the water supply system comprises a deaerator, a water supply pump and a plurality of high-pressure heaters which are sequentially communicated according to a water flow sequence, wherein the final-stage high-pressure heater is communicated with the boiler, the deaerator and the high-pressure heaters are respectively communicated with the regenerative drive steam turbine, and the water supply pump is in transmission connection with the regenerative drive steam turbine;
the condensate system comprises a condenser, a condensate pump and a multi-stage low-pressure heater which are sequentially communicated according to a water flow sequence, the condenser and the multi-stage low-pressure heater are respectively communicated with a low-pressure cylinder, and a final-stage low-pressure heater is communicated with a deaerator.
Further, for better realization the utility model discloses, backheat formula drive steam turbine and feed pump between be provided with speed adjusting device.
Further, for better realization the utility model discloses, backheating formula drive steam turbine be connected with power balance generator.
Further, for better realization the utility model discloses, backheat formula drive steam turbine, feed pump, speed adjusting device and power balance generator coaxial coupling.
Further, for better realization the utility model discloses, backheating formula drive steam turbine steam exhaust end intercommunication have a low pressure feed water heater, be provided with the governing valve between backheating formula drive steam turbine and the low pressure feed water heater.
Further, for better realization the utility model discloses, backheat formula drive steam turbine exhaust end and governing valve between the pipeline communicate in next-level low pressure feed water heater.
Further, for better realization the utility model discloses, the exit end of ultrahigh pressure jar and backheat formula drive steam turbine between be provided with the governing valve.
Further, for better realization the utility model discloses, ultrahigh pressure jar, high pressure jar, intermediate pressure jar and low pressure jar coaxial coupling and connect in main generator.
Further, for better realization the utility model discloses, boiler and ultrahigh pressure jar between be provided with the governing valve, be provided with the governing valve between boiler and the high-pressure jar, be provided with the governing valve between high-pressure jar and the intermediate pressure jar.
The double-machine coupling method based on the double-reheat coal electric unit is characterized in that: the steam provided by the boiler sequentially passes through the ultrahigh pressure cylinder to do work, the primary reheater of the boiler absorbs heat, the high pressure cylinder to do work, the secondary reheater of the boiler absorbs heat, the intermediate pressure cylinder to do work and the low pressure cylinder to do work, the ultrahigh pressure cylinder is used for providing the steam for the regenerative drive steam turbine, and the regenerative steam extraction from the regenerative drive steam turbine is used.
The beneficial effect that this scheme obtained is:
the utility model discloses a part does not pass through the reheater, the steam of expansion work has been in backheating formula drive turbo generator, according to backheating heater enthalpy rise rational distribution's principle, extract from backheating steam extraction formula feed water pump steam turbine assorted position, be used for replacing the great backheating steam extraction of partial superheat degree that main steam turbine bore in the conventional backheating system, thereby furthest has reduced the higher backheating steam extraction superheat degree in the conventional system, the irreversible loss of backheating system heat transfer has been reduced, backheating circulation efficiency has been improved, can be better than prior art the generating efficiency of improvement coal fired power plant; meanwhile, the regenerative steam extraction temperature is greatly reduced, the material grade of devices such as regenerative steam extraction pipelines and heaters can be reduced, the application range of high-temperature materials is reduced, and the investment cost of power stations is further reduced.
Drawings
FIG. 1 is a schematic structural diagram of the present embodiment;
the system comprises a boiler 1, a boiler 2, an ultrahigh pressure cylinder, a high pressure cylinder 3, a medium pressure cylinder 4, a low pressure cylinder 5, a main generator 6, a regenerative drive turbine 7, a water feed pump 8, a speed regulating device 9, a power balance generator 10, a water supply system 11, a deaerator 12, a condensate system 13, a condensate pump 14, a condenser 15, a regulating valve 16, a high pressure heater 17 and a low pressure heater 18.
Detailed Description
The present invention will be described in further detail with reference to examples, but the present invention is not limited thereto.
Example 1:
as shown in fig. 1, in this embodiment, the double-machine coupling thermodynamic system based on the double reheating coal-electric machine set includes a main steam turbine generator unit, a regenerative drive steam turbine generator unit, a water supply system 11 and a condensate system 13;
the main steam turbine generator set comprises a boiler 1, an ultrahigh pressure cylinder 2, a primary boiler reheater, a high pressure cylinder 3, a secondary boiler reheater, an intermediate pressure cylinder 4 and a low pressure cylinder 5 which are sequentially communicated according to the steam circulation direction;
the regenerative drive steam turbine generator unit comprises a regenerative drive steam turbine 7, the inlet end of which is communicated with the outlet end of the ultrahigh pressure cylinder 2;
the water supply system comprises a deaerator 12, a water supply pump 8 and a plurality of high-pressure heaters 17 which are sequentially communicated according to a water flow sequence, wherein the final-stage high-pressure heater 17 is communicated with the boiler 1, the deaerator 12 and the high-pressure heaters 17 are respectively communicated with the regenerative drive turbine 7, and the water supply pump 8 is in transmission connection with the regenerative drive turbine 7;
the condensate system 13 comprises a condenser 15, a condensate pump 14 and a multi-stage low-pressure heater 18 which are sequentially communicated according to a water flow sequence, the condenser 15 and the multi-stage low-pressure heater 18 are respectively communicated with the low-pressure cylinder 5, and the final-stage low-pressure heater 18 is communicated with the deaerator 12.
The steam absorbed by the superheater of the boiler 1 enters the ultrahigh pressure cylinder 2 of the steam turbine to expand and do work, and then most of the steam enters the primary reheater of the boiler to absorb heat. The steam after the heat absorption of the primary reheater of the boiler enters the high-pressure cylinder 3 of the steam turbine to expand and do work, and then enters the secondary reheater of the boiler to absorb heat. And the steam after the heat absorption of the secondary reheater of the boiler sequentially enters the intermediate pressure cylinder 4 and the low pressure cylinder 5 of the steam turbine to expand and do work. After the exhaust steam discharged by the low pressure cylinder 5 is condensed into water by the condenser 15, the water enters the boiler 1 after being sequentially pressurized by the condensate pump 14, heated by the low pressure heater 18, further pressurized by the feed pump 8 and further heated by the high pressure heater 17, and the whole circulation process is completed.
Through making feed pump 8 be connected with backheat formula drive steam turbine 7, can directly utilize the work that steam was done in backheat formula drive steam turbine 7 to drive feed pump 8 pressurization pump water, save extra power supply, improve energy utilization.
In addition, the scheme realizes that the regenerative steam extraction from the regenerative drive turbine 7 is utilized to replace the regenerative steam extraction provided by the high-pressure cylinder 3 and the medium-pressure cylinder 4 in the conventional thermodynamic system. Because the reheating process of the boiler reheater is not carried out, the superheat degree of the backheating steam extraction steam of the backheating type driving steam turbine 7 is small, the irreversible heat exchange loss of the corresponding backheating heater is greatly reduced, and the backheating circulation efficiency is improved. Meanwhile, as the regenerative steam extraction temperature is greatly reduced, the material grade of devices such as a regenerative steam extraction pipeline, a high-pressure heater 17 and the like can be reduced, the application range of high-temperature materials is reduced, and the investment cost of a power station is further reduced.
Example 2:
on the basis of the above embodiments, in the present embodiment, a speed adjusting device 9 is disposed between the regenerative drive turbine 7 and the feed water pump 8. The torque output by the regenerative drive turbine 7 is regulated according to the speed regulation device 9 and then output to the water feed pump 8, so that the rotating speed of the water feed pump 8 meets the design requirement.
In this embodiment, the regenerative drive turbine 7 is connected to a power balance generator 10. The regenerative drive turbine 7 drives the residual power of the water feeding pump 8 to drive the power balance generator 10 to be converted into electric energy, so that the power balance effect is achieved, and the power utilization rate of the steam in the regenerative drive turbine 7 is improved.
In this embodiment, the regenerative drive turbine 7, the feed pump 8, and the speed adjusting device 9 are coaxially connected to the power balance generator 10. The whole structure of the regenerative drive steam turbine generator unit can be simplified, and the number of used intermediate connecting pieces is reduced, so that the energy conversion and utilization rate are improved. The space can be reasonably planned and the space utilization rate can be improved during installation.
By connecting the feed water pump 8 and the power balance generator 10 to both ends of the rotary shaft of the regenerative drive turbine 7, both ends of the rotary shaft of the regenerative drive turbine 7 can be balanced in stress.
Example 3:
on the basis of the above embodiments, in the present embodiment, the exhaust end of the regenerative drive turbine 7 is communicated with a low-pressure heater 18, and a regulating valve 16 is disposed between the regenerative drive turbine 7 and the low-pressure heater 18. Therefore, the exhaust steam of the regenerative drive steam turbine 7 can enter the high-pressure heater 17 and the low-pressure heater 18, and compared with the situation that the exhaust steam of the regenerative drive steam turbine 7 completely enters the high-pressure heater 17, the exhaust steam pressure of the regenerative drive steam turbine 7 can be reduced, and the effect of flow balance is achieved. The exhaust steam pressure from the regenerative drive turbine 7 to the low-pressure heater 18 can be adjusted by means of the regulating valve 16.
In this embodiment, the pipeline between the exhaust end of the regenerative drive turbine 7 and the regulating valve 16 is communicated with the next-stage low-pressure heater 18, so that part of the exhaust steam of the regenerative drive turbine 7 can enter the two-stage low-pressure heaters 18 at the same time, thereby further reducing the exhaust steam pressure of the regenerative drive turbine 7 and enhancing the flow balance effect. The exhaust steam pressures entering the two-stage low-pressure heater 18 can be adjusted by the regulating valve 16, so that the exhaust steam pressures entering the low-pressure heater 18 are kept balanced.
The regenerative drive turbine 7 provides regenerative extraction steam except for a first-stage high-pressure heater 17 and a last-stage low-pressure heater 18; the extraction stage number of the regenerative drive turbine 7 is determined according to the specific design, and the extraction stage number respectively enters a part of the high-pressure heater 17, the deaerator 12 and the corresponding low-pressure heater 18 to heat the feed water and the condensed water. The outlet end of the feed water pump 8 is communicated with a pipeline between the high-pressure heater 17 and the deaerator 12.
Example 4:
in addition to the above embodiments, in the present embodiment, a regulating valve 16 is disposed between the outlet end of the ultra-high pressure cylinder 2 and the regenerative drive turbine 7. The power generated by the regenerative drive turbine 7 is provided with a certain surplus power except for meeting the requirement of the water feed pump 8, and is used for driving the power balance generator 10 to convert into electric energy, and the power balance generator 10 is used for adjusting and meeting the power requirement of the water feed pump 8, so that in the normal operation of the regenerative drive turbine 7, the valve can be kept fully opened by the adjusting valve 16 between the outlet end of the ultrahigh pressure cylinder 2 and the regenerative drive turbine 7, throttling loss is avoided, the regenerative drive turbine 7 operates under the most efficient working condition, and higher power generation efficiency is obtained.
By adjusting the adjusting valve 16 between the outlet end of the ultra-high pressure cylinder 2 and the regenerative drive turbine 7, the steam inlet amount entering the regenerative drive turbine 7 from the ultra-high pressure cylinder 2 is reduced, and the load-variable corresponding capacity and the primary frequency modulation adjusting capacity of the main steam turbine generator set can be enhanced.
Example 5:
in addition to the above embodiments, in the present embodiment, the ultrahigh pressure cylinder 2, the high pressure cylinder 3, and the intermediate pressure cylinder 4 are coaxially connected to the low pressure cylinder 5 and connected to the main power generator 6. Therefore, the ultrahigh pressure cylinder 2, the high pressure cylinder 3, the intermediate pressure cylinder 4, the low pressure cylinder 5 and the main generator 6 can coaxially rotate, so that the rotating shaft is uniformly stressed, the use of intermediate connecting pieces and transmission pieces is reduced, the production cost is reduced, and the energy conversion efficiency is improved.
In this embodiment, a regulating valve 16 is provided between the boiler 1 and the ultra-high pressure cylinder 2, a regulating valve 16 is provided between the boiler 1 and the high pressure cylinder 3, and a regulating valve 16 is provided between the high pressure cylinder 3 and the intermediate pressure cylinder 4. Thereby facilitating the control of the flow rate of the exhaust steam.
In this embodiment, other undescribed contents are the same as those in the above embodiment, and thus are not described again.
The above is only the preferred embodiment of the present invention, not to the limitation of the present invention in any form, all the technical matters of the present invention all fall into the protection scope of the present invention to any simple modification and equivalent change of the above embodiments.
Claims (9)
1. Double-machine coupling thermodynamic system based on double reheat coal-electricity unit, its characterized in that: comprises a main steam turbine generator unit, a regenerative drive steam turbine generator unit, a water supply system (11) and a condensed water system (13);
the main steam turbine generator set comprises a boiler (1), an ultrahigh pressure cylinder (2), a primary boiler reheater, a high pressure cylinder (3), a secondary boiler reheater, an intermediate pressure cylinder (4) and a low pressure cylinder (5) which are sequentially communicated according to the steam circulation direction;
the regenerative drive steam turbine generator unit comprises a regenerative drive steam turbine (7) with an inlet end communicated with an outlet end of the ultrahigh pressure cylinder (2);
the water supply system comprises a deaerator (12), a water supply pump (8) and a plurality of high-pressure heaters (17) which are sequentially communicated according to a water flow sequence, wherein the final-stage high-pressure heater (17) is communicated with the boiler (1), the deaerator (12) and the high-pressure heaters (17) are respectively communicated with the regenerative drive turbine (7), and the water supply pump (8) is in transmission connection with the regenerative drive turbine (7);
the condensate system (13) comprises a condenser (15), a condensate pump (14) and a multi-stage low-pressure heater (18) which are sequentially communicated according to a water flow sequence, the condenser (15) and the multi-stage low-pressure heater (18) are respectively communicated with a low-pressure cylinder (5), and a final-stage low-pressure heater (18) is communicated with a deaerator (12).
2. The double-machine coupling thermodynamic system based on the double reheating coal-electric unit as claimed in claim 1, wherein: and a speed regulating device (9) is arranged between the regenerative drive turbine (7) and the water feeding pump (8).
3. The double-machine coupling thermodynamic system based on the double reheating coal-electric unit as claimed in claim 2, wherein: the regenerative drive turbine (7) is connected with a power balance generator (10).
4. The double-machine coupling thermodynamic system based on the double reheating coal-electric unit as claimed in claim 3, wherein: the regenerative drive turbine (7), the water feed pump (8) and the speed regulating device (9) are coaxially connected with the power balance generator (10).
5. The double-machine coupling thermodynamic system based on the double reheating coal-electric unit as claimed in claim 1, wherein: the exhaust end of the regenerative drive turbine (7) is communicated with a low-pressure heater (18), and a regulating valve (16) is arranged between the regenerative drive turbine (7) and the low-pressure heater (18).
6. The double-machine coupling thermodynamic system based on the double reheating coal-electric unit as claimed in claim 5, wherein: and a pipeline between the exhaust end of the regenerative drive steam turbine (7) and the regulating valve (16) is communicated with a next-stage low-pressure heater (18).
7. The double-machine coupling thermodynamic system based on the double reheating coal-electric unit as claimed in claim 1, wherein: and an adjusting valve (16) is arranged between the outlet end of the ultrahigh pressure cylinder (2) and the regenerative drive turbine (7).
8. The double-machine coupling thermodynamic system based on the double reheating coal-electric unit as claimed in claim 1, wherein: the ultrahigh pressure cylinder (2), the high pressure cylinder (3) and the intermediate pressure cylinder (4) are coaxially connected with the low pressure cylinder (5) and are connected with the main generator (6).
9. The double-machine coupling thermodynamic system based on the double reheating coal-electric unit as claimed in claim 8, wherein: an adjusting valve (16) is arranged between the boiler (1) and the ultrahigh pressure cylinder (2), an adjusting valve (16) is arranged between the boiler (1) and the high pressure cylinder (3), and an adjusting valve (16) is arranged between the high pressure cylinder (3) and the intermediate pressure cylinder (4).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202023278571.1U CN214403694U (en) | 2020-12-30 | 2020-12-30 | Double-machine coupling thermodynamic system based on double-reheating coal electric unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202023278571.1U CN214403694U (en) | 2020-12-30 | 2020-12-30 | Double-machine coupling thermodynamic system based on double-reheating coal electric unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN214403694U true CN214403694U (en) | 2021-10-15 |
Family
ID=78042804
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202023278571.1U Active CN214403694U (en) | 2020-12-30 | 2020-12-30 | Double-machine coupling thermodynamic system based on double-reheating coal electric unit |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN214403694U (en) |
-
2020
- 2020-12-30 CN CN202023278571.1U patent/CN214403694U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN112814751A (en) | Double-machine coupling thermodynamic system based on double-reheating coal electric unit and coupling method | |
| WO2017219656A1 (en) | Gas turbine and pressurized water reactor steam turbine combined circulation system | |
| CN109826681B (en) | Industrial heating system for gas-steam combined cycle unit steam extraction integration and operation method thereof | |
| CN109855147B (en) | Combined cycle device based on heat supply and power peak regulation coupling and operation method thereof | |
| CN111022138B (en) | Supercritical carbon dioxide power generation system based on absorption heat pump waste heat recovery | |
| CN109854315B (en) | Heating system for gas-steam combined cycle unit steam extraction integration and operation method thereof | |
| CN108119200A (en) | A kind of new bottom type back pressure heat supply steam turbine and its operation method | |
| CN106761982A (en) | A kind of new part backheating gas turbine combined cycle system | |
| CN111749744A (en) | Hot primary air heating system of secondary reheating coal-fired power generating unit | |
| CN210509309U (en) | Steam complementary energy utilization coupling steam extraction heat supply system for thermoelectric unit electric power peak regulation | |
| CN203499735U (en) | Combined cycle co-generation system | |
| CN109630221B (en) | Secondary reheating unit system suitable for deep peak shaving and method thereof | |
| CN111167590A (en) | Lignite-based coal mill capacity-increasing and efficiency-improving device and method thereof | |
| CN214741510U (en) | Waste heat auxiliary heating condensate system for supercritical carbon dioxide circulation cold end | |
| CN112833378B (en) | Reheating system capable of improving heat supply capacity | |
| CN210530935U (en) | Double-machine regenerative system with multiple shafts arranged | |
| CN109296413B (en) | Bypass secondary reheating power generation device and method cooled by deep seawater | |
| CN111237734A (en) | Three-stage regenerative intermediate reheating supercritical carbon dioxide coal-fired power generation system and operation method | |
| CN210179723U (en) | Combined cycle device based on heat supply and electric power peak regulation coupling | |
| CN214403694U (en) | Double-machine coupling thermodynamic system based on double-reheating coal electric unit | |
| CN109763869B (en) | Heat accumulation coupling steam extraction integrated system for cascade utilization of combined cycle energy and operation method thereof | |
| CN114776411B (en) | Integrated heat storage coal-fired power generation system and working method | |
| CN107143391A (en) | A kind of new middle backheating gas turbine combined cycle system | |
| CN115478921A (en) | Multi-energy-level utilization system suitable for thermal generator set | |
| CN201420574Y (en) | Device for low temperature waste heat power generation by applying screw expander |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |