CN208519750U - A kind of thermal power plant's fused salt accumulation of heat peak regulation system heated using main steam - Google Patents
A kind of thermal power plant's fused salt accumulation of heat peak regulation system heated using main steam Download PDFInfo
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- CN208519750U CN208519750U CN201820379152.0U CN201820379152U CN208519750U CN 208519750 U CN208519750 U CN 208519750U CN 201820379152 U CN201820379152 U CN 201820379152U CN 208519750 U CN208519750 U CN 208519750U
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- 150000003839 salts Chemical class 0.000 title claims abstract description 117
- 238000009825 accumulation Methods 0.000 title claims description 14
- 230000001105 regulatory effect Effects 0.000 claims abstract description 43
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 42
- 238000010438 heat treatment Methods 0.000 claims description 13
- 238000002844 melting Methods 0.000 claims description 12
- 230000008018 melting Effects 0.000 claims description 12
- 239000008236 heating water Substances 0.000 claims description 8
- 238000000034 method Methods 0.000 claims description 7
- 238000003795 desorption Methods 0.000 claims description 3
- 230000005611 electricity Effects 0.000 abstract description 6
- 238000005338 heat storage Methods 0.000 abstract description 6
- 238000010248 power generation Methods 0.000 abstract 1
- 238000010586 diagram Methods 0.000 description 4
- 238000000605 extraction Methods 0.000 description 3
- 238000002485 combustion reaction Methods 0.000 description 2
- 240000002853 Nelumbo nucifera Species 0.000 description 1
- 235000006508 Nelumbo nucifera Nutrition 0.000 description 1
- 235000006510 Nelumbo pentapetala Nutrition 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 229910017053 inorganic salt Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 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
- 238000005086 pumping Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 230000001360 synchronised effect Effects 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
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Abstract
一种利用主蒸汽加热的火电厂熔盐蓄热调峰系统，属于火电厂蓄热调峰技术领域。该系统包括主蒸汽调节阀、高压蒸汽—熔盐换热器、再热蒸汽调节阀、高温熔盐罐、高温熔盐泵、低温熔盐罐、低温熔盐泵、节流阀、高压加热器、给水泵、除氧器、锅炉、高压缸、中压缸。在用电负荷降低时充分发挥锅炉的利用率，增加熔盐蓄热系统，将锅炉多余蒸汽的热量通过高压蒸汽—熔盐换热器储存在高温熔盐中，在用电高峰阶段将高温熔盐从熔盐罐中抽出重新送入高压蒸汽—熔盐换热器加热锅炉给水并产生高温高压蒸汽，送入汽轮机中增加汽轮机的发电量并起到对机组的调峰作用。可回收用电负荷较低时锅炉产生的多余蒸汽，提高锅炉的利用率以及运行安全性，达到节能的目的。
The utility model relates to a thermal power plant's molten salt heat storage and peak regulation system heated by main steam, which belongs to the technical field of thermal power plant heat storage and peak regulation. The system includes main steam regulating valve, high pressure steam-molten salt heat exchanger, reheat steam regulating valve, high temperature molten salt tank, high temperature molten salt pump, low temperature molten salt tank, low temperature molten salt pump, throttle valve, high pressure heater , Feed water pump, deaerator, boiler, high pressure cylinder, medium pressure cylinder. When the electricity load is reduced, the utilization rate of the boiler is fully utilized, the molten salt heat storage system is added, and the heat of the excess steam of the boiler is stored in the high-temperature molten salt through the high-pressure steam-molten salt heat exchanger. The salt is extracted from the molten salt tank and sent back to the high pressure steam - the molten salt heat exchanger heats the boiler feed water and generates high temperature and high pressure steam, which is sent to the steam turbine to increase the power generation of the steam turbine and play a role in peak regulation of the unit. The excess steam generated by the boiler when the electricity load is low can be recovered to improve the utilization rate and operation safety of the boiler and achieve the purpose of energy saving.
Description
Technical field:
The utility model provides a kind of thermal power plant's fused salt accumulation of heat peak regulation system heated using main steam, which can be with
The waste heat that power plant generates in electricity consumption underload is stored in the peak regulation for being used for peak times of power consumption unit in high-temperature molten salt, is belonged to
In thermal power plant's accumulation of heat peak regulation technique field.
Background technique:
Due to the adjustment of China's economic structure, electricity consumption composition has changed a lot: Peak power use load increases, low ebb
Electricity consumption largely reduces, and peak-valley difference constantly widens.And as electrical network capacity constantly expands, more and more high parameter large capacity machines
Group is also gradually gone into operation and is run, and causes the contradiction of peak-valley difference further up.In the low power consumption period, it is negative that power plant units are in drop
In the lotus stage, boiler maintains steady combustion load when running cannot be synchronous with steam turbine minimum load, if output power is required to be less than
The steady combustion load of boiler has one to guarantee that the steam production of the safe operation boiler of boiler at this time is greater than the steam consumption of steam turbine
Part main steam will be wasted.
The utility model provides a kind of thermal power plant's fused salt accumulation of heat peak regulation system heated using main steam, in thermal power plant's original
Increase fused salt hold over system in some equipment.Boiler utilization rate is sufficiently improved when power load is lower, is generated using boiler
Excessive main steam heat is by getting up heat storage with fused salt heat exchanging.In peak times of power consumption, high-temperature molten salt heating boiler is utilized
Water supply discharges the heat of storage, generates high temperature and high pressure steam and is sent directly into steam turbine, increases generated energy and plays
Peak Load Adjustment.In this way, can not only greatly improve the utilization rate of equipment, increase power generating capacity, while can also be in peak times of power consumption
Guarantee the consumption for reducing fuel in the case where the operation of boiler normal duty, reduces the environmental pollutions such as haze.Therefore this patent is public
A kind of thermal power plant's fused salt accumulation of heat peak regulation system heated using main steam of cloth is to meet safe and economical boiler operation, raising machine
The effective means of group power output.
Utility model content:
In order to by the heat storage of thermal power plant's excess steam caused by the low power consumption stage get up to be used for unit with
Peak regulation when electric high load capacity, the utility model disclose a kind of thermal power plant's fused salt accumulation of heat peak regulation system heated using main steam.With
Electric load reduce when, by high steam-fused salt heat exchanging device by the heat storage of boiler excess steam in high-temperature molten salt, fill
Divide the excessive main steam heat generated using boiler, improve boiler utilization rate, then utilizes high-temperature molten salt in the peak of power consumption stage
Heating boiler feed water simultaneously generates the generated energy that high temperature and high pressure steam is sent directly into increase unit in steam turbine, and realizes and adjust to unit
Peak effect.
The technical issues of the utility model solves is achieved through the following technical solutions:
A kind of thermal power plant's fused salt accumulation of heat peak regulation system heated using main steam, which includes main steam control valve
(1), high steam-fused salt heat exchanging device (2), reheated steam regulating valve (3), high temperature melting salt cellar (6), high-temperature melting salt pump (7), low
Temperature molten salt tank (10), low-temperature molten salt pump (11), throttle valve (13), the first high-pressure heater (14), the second high-pressure heater (17),
Feed pump (18), oxygen-eliminating device (19), boiler (20), high pressure cylinder (21), intermediate pressure cylinder (22)；
Boiler export is connected with two-way major steam line, all the way main steam line enter steam turbine acting, i.e., respectively with vapour
High pressure cylinder (21), intermediate pressure cylinder (22) connection in turbine, high pressure cylinder (21) and boiler (20) connect into circuit；Another way main steam
Pipeline is successively connect with main steam control valve (1), the steam of main steam control valve (1) and high steam-fused salt heat exchanging device (2)
Side-entrance is connected；High steam-fused salt heat exchanging device (2) steam side outlet by the 5th regulating valve (12), throttle valve (13) with
First high-pressure heater (14) I grade heats water side entrance and is connected；High pressure cylinder (21) exhaust and the first high-pressure heater
(14) I grade steam side entrance is connected；First high-pressure heater (14) I grade heats water side outlet and high-pressure heater (14)
Section II grade heats water side entrance and is connected；First high-pressure heater (14) Section II grade heats water side outlet and oxygen-eliminating device (19) entrance phase
Even；First high-pressure heater (14) Section II grade water supply side entrance is connected by valve with feed pump (18) outlet；First high pressure adds
Hot device (14) Section II grade water supply side outlet is connected with the first high-pressure heater (14) I grade water supply side entrance；First high pressure simultaneously
Heater (14) I grade water supply side outlet is connected by the 7th regulating valve (16) with boiler (20) entrance；First high-pressure heater
(14) I grade water supply side outlet also passes through the 6th regulating valve (15) and high steam-fused salt heat exchanging device (2) steam side outlet phase
Even；High steam-fused salt heat exchanging device (2) steam side outlet successively with the 5th regulating valve (12), throttle valve (13), hyperbaric heating
Device (14) I grade water supply side outlet is connected, so that high steam-fused salt heat exchanging device (2) steam side outlet is successively adjusted with the 5th
Valve (12), throttle valve (13), the first high-pressure heater (14) I grade, the first high-pressure heater (14) Section II grade, feed pump
(18), oxygen-eliminating device (19) is sequentially connected, and forms the heating system at boiler feedwater end.
The steam side-entrance of high steam-fused salt heat exchanging device (2) also passes through in reheated steam regulating valve (3) and steam turbine
Cylinder pressure (22) connection, so that oxygen-eliminating device (19), feed pump (18), high-pressure heater (14), the 6th regulating valve (15), high pressure are steamed
Vapour-fused salt heat exchanging device (2), reheated steam regulating valve (3) and Steam Turbine Through IP Admission (22) are sequentially connected, and form boiler feedwater end
Vapo(u)rization system.
High pressure cylinder (21) exhaust is connected with the second high-pressure heater (17) I grade steam side entrance；Second high pressure adds
Hot device (17) I grade heating water side outlet is connected with high-pressure heater (17) Section II grade heating water side entrance；Second hyperbaric heating
Device (17) Section II grade heating water side outlet is connected with oxygen-eliminating device (19) entrance；Second high-pressure heater (17) Section II grade feedwater side enters
Mouth is connected by valve with feed pump (18) outlet；Second high-pressure heater (17) Section II grade water supply side outlet adds with the second high pressure
Hot device (17) I grade water supply side entrance is connected；Second high-pressure heater (17) I grade water supply side outlet and boiler (20) entrance phase
Even；Above-mentioned oxygen-eliminating device (19), feed pump (18), the Section II grade of the second high-pressure heater (17), I grade and high pressure cylinder (21)
It is sequentially connected, while the I grade of the second high-pressure heater (17) is connect by valve with boiler (20), is transported according to thermal power plant's original
Line mode heating boiler feed water；
Low-temperature molten salt tank (10) passes sequentially through low-temperature molten salt pump (11), the 4th regulating valve (9) is changed with high steam-fused salt
Hot device (2) fused salt side-entrance is connected；High steam-fused salt heat exchanging device (2) fused salt side outlet passes through the second regulating valve (5) and high
Temperature molten salt tank (6) is connected, above-mentioned to be used as hold over system；
High temperature melting salt cellar (6) is passed sequentially through high-temperature melting salt pump (7), the first regulating valve (4) to change with high steam-fused salt
Hot device (2) fused salt side outlet is connected；High steam-fused salt heat exchanging device (2) fused salt side-entrance passes through third regulating valve (8)
It is connected with low-temperature molten salt tank (10)；The steam side-entrance of the high steam-fused salt heat exchanging device (2) is adjusted by reheated steam
Valve (3) is connected with reheaing steam pipe；It is above-mentioned to be used as thermal desorption system；
Heat exchange and exothermic phase in stage regenerator steam and fused salt may be implemented in high steam-fused salt heat exchanging device (2)
The heat exchange of fused salt and boiler feedwater.
The method of operation includes the following:
Timing under power load allows boiler heavy-duty service to generate excessive steam, and a part of main steam is according to power plant's original
Some working methods, which enter in steam turbine, does work, and another part main steam then passes through high steam-fused salt heat exchanging device (2)
It exchanges heat with the fused salt extracted out from low temperature cold salt cellar (10), the high pressure condensed water after heat exchange is through throttle valve (13) expenditure and pressure
After inject the first high-pressure heater (14), completed jointly with high pressure cylinder steam extraction with the heat exchange of water supply；
When power load increases, added with the fused salt in high warm salt cellar (6) by high steam-fused salt heat exchanging device (2)
Boiler feedwater of the heat after the first high-pressure heater (14) are heated, the high temperature and high pressure steam of generation flow through reheated steam regulating valve
(3) it is sent directly into steam turbine after, increases the air inflow of steam turbine, improved generated energy, Peak Load Adjustment is played to unit, after heat exchange
Low-temperature molten salt flow back in low temperature cold salt cellar (10), participate in next round circulation；The original feed water system of boiler of thermal power plant remains former
The method of operation: water supply flows into the second high-pressure heater (17) feeding boiler (20) after high pressure cylinder (21) pumping heating and continues to absorb heat
It evaporates and overheats.
Fused salt used in the accumulation of heat is the molten state of two or more inorganic salt mixt, and operating temperature exists
Between 300~1000 DEG C.
Compared with prior art, the utility model has the following beneficial effects:
(1) utilization rate that can give full play to boiler, improves the economy of boiler operatiopn；
(2) excess steam that boiler generates when recycling power load is lower is used for the peak regulation of peak of power consumption stage Power Plant
It uses, reaches energy-efficient purpose；
(3) due to the presence of hold over system, fired power generating unit flexibility is improved.
Detailed description of the invention:
Fig. 1 is Tthe utility model system structure connection diagram figure
Fig. 2 is hold over system operation schematic diagram.
Fig. 3 is thermal desorption system operation schematic diagram.
In figure: main steam control valve 1, high steam-fused salt heat exchanging device 2, reheated steam regulating valve 3, high temperature melting salt cellar 6,
High-temperature melting salt pump 7, low-temperature molten salt tank 10, low-temperature molten salt pump 11, throttle valve 13, high-pressure heater 14, high-pressure heater 17, water supply
Pump 18, oxygen-eliminating device 19, boiler 20, high pressure cylinder 21, intermediate pressure cylinder 22, the first regulating valve 4, the second regulating valve 5, third regulating valve 8, the
Four regulating valves 9, the 5th regulating valve 12, the 6th regulating valve 15, the 7th regulating valve 16.
Specific embodiment:
The embodiments of the present invention are described in detail with reference to the accompanying drawing, following embodiment is only the utility model
Preferred embodiment, it is all that any modification or equivalent replacement are made in the thought of the utility model not to limit utility model,
It both is within the protection scope of the present invention.
Embodiment 1
Specific component connection, is shown in Fig. 1, accumulation of heat, and Fig. 2 is shown in work, and heat release operation schematic diagram is shown in Fig. 3.
Electricity consumption underload stage regenerator:
As shown in Fig. 2, keeping the operation of boiler full load, timing requires unit to reduce output power under power load, opens
Main steam control valve 1 closes reheated steam regulating valve 3, a part of main steam is made to enter vapour according to the original working method of power plant
It does work in turbine, another part main steam inflow high steam-fused salt heat exchanging device 2, regulating valve of blinding off a line 4,8,15,
It is sent into high steam-fused salt heat exchanging device 2 after fused salt in low temperature cold salt cellar 10 low-temperature molten salt is pumped 11 extractions, fused salt is added
It flow back into high warm salt cellar 6 and is stored after heat；With the high pressure condensed water after fused salt heat exchanging after 13 expenditure and pressure of throttle valve
The water supply come out from oxygen-eliminating device is heated in injection 14 somewhere of high-pressure heater and high pressure cylinder steam extraction jointly；It is heated by high-pressure heater 14
The water supply heated together with the original high-pressure heater 17 of system of water supply be fed together heat absorption in boiler and evaporate and overheat, enter
It does work in steam turbine.
Peak of power consumption exothermic phase:
As shown in figure 3, closing main steam control valve 1 and pipeline regulating valve 5,9,12,16 when peak of power consumption, open again
Hot steam regulating valve 3 keeps unit heavy-duty service.After high-temperature molten salt in high warm salt cellar 6 is extracted out with high-temperature melting salt pump 7
High steam-fused salt heat exchanging device 2 is flowed into, the boiler feedwater a part come out through oxygen-eliminating device 19 is according to original row side of thermal power plant
Formula is sent into boiler after the heating of high-pressure heater 17 absorbs heat, and another part water supply flows into high pressure after the heating of high-pressure heater 14
Exchange heat in steam-fused salt heat exchanging device 2 with high-temperature molten salt, generate high temperature and high pressure steam after by reheated steam regulating valve 3 into
Enter reheaing steam pipe, enters in steam turbine with reheated steam and do work；Low-temperature molten salt after heat exchange cooling flows back to low temperature cold
In salt cellar 10, next round circulation is participated in.
Claims (4)
1. a kind of thermal power plant's fused salt accumulation of heat peak regulation system heated using main steam, which is characterized in that the system includes main steam
Regulating valve (1), high steam-fused salt heat exchanging device (2), reheated steam regulating valve (3), high temperature melting salt cellar (6), high-temperature melting salt pump
(7), low-temperature molten salt tank (10), low-temperature molten salt pump (11), throttle valve (13), the first high-pressure heater (14), the second hyperbaric heating
Device (17), feed pump (18), oxygen-eliminating device (19), boiler (20), high pressure cylinder (21), intermediate pressure cylinder (22)；
Boiler export is connected with two-way major steam line, all the way main steam line enter steam turbine acting, i.e., respectively with steam turbine
In high pressure cylinder (21), intermediate pressure cylinder (22) connection, high pressure cylinder (21) and boiler (20) connect into circuit；Another way main steam line
Successively connect with main steam control valve (1), the steam sides of main steam control valve (1) and high steam-fused salt heat exchanging device (2) into
Mouth is connected；High steam-fused salt heat exchanging device (2) steam side outlet is high by the 5th regulating valve (12), throttle valve (13) and first
Heater (14) I grade heating water side entrance is pressed to be connected；High pressure cylinder (21) exhaust and the first high-pressure heater (14) I grade
Steam side entrance is connected；First high-pressure heater (14) I grade heats water side outlet and high-pressure heater (14) Section II grade heats
Water side entrance is connected；First high-pressure heater (14) Section II grade heating water side outlet is connected with oxygen-eliminating device (19) entrance；First is high
Pressure heater (14) Section II grade water supply side entrance is connected by valve with feed pump (18) outlet；First high-pressure heater (14)
II grades of water supply side outlets are connected with the first high-pressure heater (14) I grade water supply side entrance；First high-pressure heater (14) simultaneously
I grade water supply side outlet is connected by the 7th regulating valve (16) with boiler (20) entrance；First high-pressure heater (14) I grade is given
Water side outlet also passes through the 6th regulating valve (15) and is connected with high steam-fused salt heat exchanging device (2) steam side outlet；High pressure is steamed
Vapour-fused salt heat exchanging device (2) steam side outlet successively with the 5th regulating valve (12), throttle valve (13), high-pressure heater (14) I
Grade water supply side outlet is connected；
The steam side-entrance of high steam-fused salt heat exchanging device (2) also passes through reheated steam regulating valve (3) and Steam Turbine Through IP Admission
(22) it connects；
High pressure cylinder (21) exhaust is connected with the second high-pressure heater (17) I grade steam side entrance；Second high-pressure heater
(17) I grade heating water side outlet is connected with high-pressure heater (17) Section II grade heating water side entrance；Second high-pressure heater
(17) Section II grade heating water side outlet is connected with oxygen-eliminating device (19) entrance；Second high-pressure heater (17) Section II grade water supply side entrance
It is connected by valve with feed pump (18) outlet；Second high-pressure heater (17) Section II grade water supply side outlet and the second hyperbaric heating
Device (17) I grade water supply side entrance is connected；Second high-pressure heater (17) I grade water supply side outlet and boiler (20) entrance phase
Even；
Low-temperature molten salt tank (10) passes sequentially through low-temperature molten salt pump (11), the 4th regulating valve (9) and high steam-fused salt heat exchanging device
(2) fused salt side-entrance is connected；High steam-fused salt heat exchanging device (2) fused salt side outlet passes through the second regulating valve (5) and high temperature melting
Salt cellar (6) is connected, above-mentioned to be used as hold over system；
High temperature melting salt cellar (6) is passed sequentially through into high-temperature melting salt pump (7), the first regulating valve (4) and high steam-fused salt heat exchanging device
(2) fused salt side outlet is connected；High steam-fused salt heat exchanging device (2) fused salt side-entrance by third regulating valve (8) with it is low
Temperature molten salt tank (10) is connected；The steam side-entrance of the high steam-fused salt heat exchanging device (2) passes through reheated steam regulating valve (3)
It is connected with reheaing steam pipe；It is above-mentioned to be used as thermal desorption system.
2. a kind of thermal power plant's fused salt accumulation of heat peak regulation system heated using main steam described in accordance with the claim 1, feature are existed
In, high steam-fused salt heat exchanging device (2) steam side outlet successively with the 5th regulating valve (12), throttle valve (13), the first high pressure
Heater (14) I grade, the first high-pressure heater (14) Section II grade, feed pump (18), oxygen-eliminating device (19) are sequentially connected, and form pot
Heating system of the furnace to water end (W.E.).
3. a kind of thermal power plant's fused salt accumulation of heat peak regulation system heated using main steam described in accordance with the claim 1, feature are existed
In so that oxygen-eliminating device (19), feed pump (18), high-pressure heater (14), the 6th regulating valve (15), high steam-fused salt heat exchanging
Device (2), reheated steam regulating valve (3) and Steam Turbine Through IP Admission (22) are sequentially connected, and form the vapo(u)rization system at boiler feedwater end.
4. a kind of thermal power plant's fused salt accumulation of heat peak regulation system heated using main steam described in accordance with the claim 1, feature are existed
In oxygen-eliminating device (19), feed pump (18), the Section II grade of the second high-pressure heater (17), I grade and high pressure cylinder (21) are successively
Connection, while the I grade of the second high-pressure heater (17) is connect by valve with boiler (20), according to thermal power plant's original method of operation
Heating boiler feed water.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820379152.0U CN208519750U (en) | 2018-03-20 | 2018-03-20 | A kind of thermal power plant's fused salt accumulation of heat peak regulation system heated using main steam |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201820379152.0U CN208519750U (en) | 2018-03-20 | 2018-03-20 | A kind of thermal power plant's fused salt accumulation of heat peak regulation system heated using main steam |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108548168A (en) * | 2018-03-20 | 2018-09-18 | 北京工业大学 | A kind of thermal power plant's fused salt accumulation of heat peak regulation system heated using main steam |
| CN111120995A (en) * | 2019-12-05 | 2020-05-08 | 国网河北省电力有限公司电力科学研究院 | Heat storage system and peak-shaving effect evaluation method for expanding the peak-shaving output range of units |
| CN113586185A (en) * | 2021-09-13 | 2021-11-02 | 西安交通大学 | Coal-fired boiler flue gas and steam combined heat storage deep peak regulation system and operation method |
| CN114876597A (en) * | 2022-05-19 | 2022-08-09 | 西安热工研究院有限公司 | A system and method for coupling molten salt energy storage to realize island operation of thermal power units |
| CN115479266A (en) * | 2022-09-06 | 2022-12-16 | 西安热工研究院有限公司 | A high-parameter industrial steam supply system and method for steam-gas cogeneration |
-
2018
- 2018-03-20 CN CN201820379152.0U patent/CN208519750U/en active Active
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108548168A (en) * | 2018-03-20 | 2018-09-18 | 北京工业大学 | A kind of thermal power plant's fused salt accumulation of heat peak regulation system heated using main steam |
| CN111120995A (en) * | 2019-12-05 | 2020-05-08 | 国网河北省电力有限公司电力科学研究院 | Heat storage system and peak-shaving effect evaluation method for expanding the peak-shaving output range of units |
| CN111120995B (en) * | 2019-12-05 | 2022-04-15 | 国网河北省电力有限公司电力科学研究院 | Heat storage system for expanding peak regulation output range of unit and peak regulation effect evaluation method |
| CN113586185A (en) * | 2021-09-13 | 2021-11-02 | 西安交通大学 | Coal-fired boiler flue gas and steam combined heat storage deep peak regulation system and operation method |
| CN114876597A (en) * | 2022-05-19 | 2022-08-09 | 西安热工研究院有限公司 | A system and method for coupling molten salt energy storage to realize island operation of thermal power units |
| CN114876597B (en) * | 2022-05-19 | 2024-01-23 | 西安热工研究院有限公司 | System and method for realizing island operation of thermal power generating unit by coupling molten salt energy storage |
| CN115479266A (en) * | 2022-09-06 | 2022-12-16 | 西安热工研究院有限公司 | A high-parameter industrial steam supply system and method for steam-gas cogeneration |
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