CN105697076A - Combined heat and power system of large-scale extracting and condensing steam turbine - Google Patents
Combined heat and power system of large-scale extracting and condensing steam turbine Download PDFInfo
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- CN105697076A CN105697076A CN201610199157.0A CN201610199157A CN105697076A CN 105697076 A CN105697076 A CN 105697076A CN 201610199157 A CN201610199157 A CN 201610199157A CN 105697076 A CN105697076 A CN 105697076A
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- cooling water
- heat supply
- supply network
- condenser
- pipe
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
- F01K17/00—Using steam or condensate extracted or exhausted from steam engine plant
- F01K17/02—Using steam or condensate extracted or exhausted from steam engine plant for heating purposes, e.g. industrial, domestic
- F01K17/025—Using steam or condensate extracted or exhausted from steam engine plant for heating purposes, e.g. industrial, domestic in combination with at least one gas turbine, e.g. a combustion gas turbine
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01D—NON-POSITIVE DISPLACEMENT MACHINES OR ENGINES, e.g. STEAM TURBINES
- F01D15/00—Adaptations of machines or engines for special use; Combinations of engines with devices driven thereby
- F01D15/10—Adaptations for driving, or combinations with, electric generators
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01D—NON-POSITIVE DISPLACEMENT MACHINES OR ENGINES, e.g. STEAM TURBINES
- F01D17/00—Regulating or controlling by varying flow
- F01D17/10—Final actuators
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/14—Combined heat and power generation [CHP]
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P80/00—Climate change mitigation technologies for sector-wide applications
- Y02P80/10—Efficient use of energy, e.g. using compressed air or pressurized fluid as energy carrier
- Y02P80/15—On-site combined power, heat or cool generation or distribution, e.g. combined heat and power [CHP] supply
Abstract
The invention provides a combined heat and power system of a large-scale extracting and condensing steam turbine. The combined heat and power system of the large-scale extracting and condensing steam turbine comprises a generating set, a steam condenser, an in-plant heat network and a cooling tower, wherein the in-plant heat network comprises a water inlet pipe of a heat network backwater steam condenser and a water outlet pipe of the heat network backwater steam condenser; the cooling tower communicates with a cooling water inlet pipe and a cooling water outlet pipe; the cooling water inlet pipe and the cooling water outlet pipe are in communication closure in the steam condenser; a circulating cooling water inlet valve is mounted on the cooling water inlet pipe, and a circulating cooling water outlet valve is mounted on the cooling water outlet pipe; the cooling water inlet pipe communicates with the water inlet pipe of the heat network backwater steam condenser in a position between the circulating cooling water inlet valve and the steam condenser; the cooling water outlet pipe communicates with the water outlet pipe of the heat network backwater steam condenser in a position between the circulating cooling water outlet valve and the steam condenser. According to the combined heat and power system of the large-scale extracting and condensing steam turbine, disclosed by the invention, the temperature of a refrigerant in the heat network is increased through the heat generated by the steam emission of the steam condenser, so that the utilizable heat efficiency is improved.
Description
Technical field
The present invention relates to power field, particularly large-scale extraction-condensing steam turbine co-generation unit。
Background technology
The structural long-term surplus of current northern area power supply, the situation that heating heat demand increases,
Large-scale extraction-condensing steam turbine co-generation unit thermal efficiency reason low, that thermal pollution is serious is the exhaust steam after acting to be condensed into water to return boiler producing steam again, and the heat that exhaust steam is contained is wasted, and cools down this exhaust steam and also to consume the energy, therefore the thermal efficiency is low；In condensation process, cooling medium distributes heat in atmosphere again, and environment is caused thermal pollution。Visible, problem it is crucial that find an outlet that can provide utilization for exhaust steam。
Urbanite is provided heating with exhaust steam by this outlet exactly, it not only Shi Lao steam power plant escape the misfortune closed down, also profit gangster is shallow, benefit double。Further, also extract part middle pressure steam, provide industrial heating to industrial user。The remodeling method that condensing bleeder turbine unit improves in prior art back pressure needs to change boiler, rotor, condenser, the shortcoming that there is the cycle length of replacing, expense big (typically requiring 85,000,000 yuan-1.2 hundred million yuan)。
Therefore, in prior art, the utilizable thermal efficiency is low。
Summary of the invention
Present invention aim at providing a kind of large-scale extraction-condensing steam turbine co-generation unit, there is the higher utilizable thermal efficiency。
For reaching above-mentioned advantage, the present invention provides a kind of large-scale extraction-condensing steam turbine co-generation unit, including: heat supply network, cooling tower in generating set, condenser, factory, in described factory, heat supply network includes heat supply network backwater condenser water inlet pipe, heat supply network backwater condenser outlet pipe；
Described cooling tower is communicated with cooling water inlet pipe, cooling water outlet pipe, described cooling water inlet pipe connects Guan Bi with described cooling water outlet pipe in described condenser, described cooling water inlet pipe and be separately installed with recirculated cooling water water intaking valve and recirculated cooling water outlet valve on described cooling water outlet pipe；
Described cooling water inlet pipe position between described recirculated cooling water water intaking valve, described condenser connects with described heat supply network backwater condenser water inlet pipe, and described cooling water outlet pipe position between described recirculated cooling water outlet valve, described condenser connects with described heat supply network backwater condenser outlet pipe。
In one embodiment of the invention, the inlet end of described condenser is provided with atomization water pipe, and described atomization water pipe is for for injecting atomized steam in described condenser。
In one embodiment of the invention, described cooling water inlet pipe is communicated with described heat supply network water pipe, and the position between described heat supply network backwater condenser water inlet pipe and the described condenser of described cooling water inlet pipe connects with described heat supply network water pipe。
In one embodiment of the invention, described generating set includes: the high pressure cylinder of steam turbine, intermediate pressure cylinder, low pressure (LP) cylinder and electromotor。
In one embodiment of the invention, in described factory, heat supply network includes: primary heater, secondary heater。
In one embodiment of the invention, described primary heater all connects with heat supply network backwater condenser outlet pipe with described secondary heater。
In one embodiment of the invention, described heat supply network backwater condenser water inlet pipe, described heat supply network backwater condenser outlet pipe connect with user's heat supply network。
In one embodiment of the invention, described atomization water pipe is provided with atomization water compensating valve。
In one embodiment of the invention, described heat supply network water pipe is provided with heat supply network water compensating valve。
In one embodiment of the invention, it is provided with steam pipe between medium pressure cylinder, described low pressure (LP) cylinder, described steam pipe is provided with steam valve
In the present invention owing to cooling water inlet pipe position between recirculated cooling water water intaking valve, condenser connects with heat supply network backwater condenser water inlet pipe, cooling water outlet pipe position between recirculated cooling water outlet valve, condenser connects with heat supply network backwater condenser outlet pipe。Utilize the temperature of coolant in the heat lift heat supply network of turbine discharge, improve the utilizable thermal efficiency。Utilize turbine low pressure cylinder to enter vapour conduit in the present invention and regulate turning down of valve, reduce to low pressure (LP) cylinder aerofluxus (vapour amount reduce to low pressure (LP) cylinder rotor do not rub, vibrate, the unsafe problems such as air blast time amount), thus reducing low pressure (LP) cylinder acting, increasing thermoelectricity ratio, improving heating pump gas ablity；Simultaneously because the minimizing of low pressure (LP) cylinder steam discharge makes to utilize heating backwater, as condenser cooling water, (cooling-tower circulating water Heating Period cuts off, tower disables), namely the temperature of coolant in the heat lift heat supply network of low pressure (LP) cylinder steam discharge, improves the utilizable thermal efficiency and heating ability。
Accompanying drawing explanation
Fig. 1 show the structural representation of existing large-scale extraction-condensing steam turbine co-generation unit。
Fig. 2 show the structural representation of the large-scale extraction-condensing steam turbine co-generation unit of first embodiment of the invention。
Detailed description of the invention
For further setting forth that the present invention reaches technological means and effect that predetermined goal of the invention is taked, below in conjunction with accompanying drawing and preferred embodiment, to according to the present invention detailed description of the invention, structure, feature and effect thereof proposed, describe in detail as after。
Fig. 1 show the structural representation of existing large-scale extraction-condensing steam turbine co-generation unit。Refer to Fig. 1, existing large-scale extraction-condensing steam turbine co-generation unit, for to outside heat supply network 200 heat supply and generating, existing large-scale extraction-condensing steam turbine co-generation unit includes, heat supply network 30, cooling tower 40 in generating set 10, condenser 20, factory。
Generating set 10, including: the high pressure cylinder 11 of steam turbine, intermediate pressure cylinder 12, low pressure (LP) cylinder 15 and electromotor 17。It is provided with steam pipe 13 between intermediate pressure cylinder 12, low pressure (LP) cylinder 15, steam pipe 13 is provided with steam valve 131。Steam valve 131 can regulate the flow of steam。Effusion meter and pressure transducer (figure does not look) can be installed at steam valve 131 and low pressure (LP) cylinder 15。
Condenser 20, is condensed into a kind of heat exchanger of water by turbine discharge, also known as steam condenser, for being cooled down by steam as cooling water。Connecting with cooling water replenishment pipeline 23 in the steam liquefied water water side of condenser 20, water pipe 23 is provided with benefit water control valve 231。Temperature collecting device is installed in the steam liquefied water water side of condenser 20。
In factory, heat supply network 30 includes heat supply network water return pipeline 30a, heating water compensating valve 32, heating water pump 35, primary heater 37, secondary heater 39。Primary heater 37 extracts the heating agent in the steam heating net water return pipeline 30a of intermediate pressure cylinder 12。Heating agent is sent to outside heat supply network 200 after heating heating agent by primary heater 37, secondary heater 39, flows back to heat supply network 30 in factory through heat supply network water return pipeline 30a after heating agent cooling。Heat supply network water return pipeline 30a connects with heat supply network water pipe 36。
Cooling tower 40, with cooling water inlet pipe 41, cooling water outlet pipe 43 connects, and cools down water inlet pipe 41, and cooling water outlet pipe 43 closes in condenser 20。Cooling water inlet pipe 41, cooling water outlet pipe 43 is separately installed with recirculated cooling water water intaking valve 411, recirculated cooling water outlet valve 431。
Fig. 2 show the structural representation of the large-scale extraction-condensing steam turbine co-generation unit of first embodiment of the invention。Refer to Fig. 2,
Heat supply network water return pipeline 30a is interrupted as heat supply network backwater condenser water inlet pipe 31, heat supply network backwater condenser outlet pipe 33 by the large-scale extraction-condensing steam turbine co-generation unit 100 of the present embodiment, the cooling water inlet pipe 41 position between recirculated cooling water water intaking valve 411, condenser 20 connects with heat supply network backwater condenser water inlet pipe 31, and the cooling water outlet pipe 43 position between recirculated cooling water outlet valve 431, condenser 20 connects with heat supply network backwater condenser outlet pipe 33。
Heat supply network backwater condenser water inlet pipe 31, heat supply network backwater condenser outlet pipe 33 are separately installed with heat supply network backwater condenser water intaking valve 311, heat supply network backwater condenser outlet valve 331。
By closing recirculated cooling water water intaking valve 411, recirculated cooling water outlet valve 431, open heat supply network backwater condenser water intaking valve 311, heat supply network backwater condenser outlet valve 331。The heating agent in heat supply network can be switched and enter condenser 20 and turbine discharge heat-shift。The temperature of the heating agent simultaneously promoted in factory in heat supply network 30。So can improve condenser 20 and cool down the availability of the discharged heat of turbine discharge。
Owing to the temperature of heat supply network backwater expects that temperature is higher, for ensureing the cooling effect of condenser 20, water pipe 23 in condenser 20 steam liquefied water water side is closed or is removed, the inlet end (throat) of condenser 20 newly-increased atomization water pipe 21, atomization water pipe 21 is for for injecting atomization low-temperature steam in condenser 20, to ensure the effect of condenser 20 cooling cooling water。Atomization water pipe 21 is provided with atomization water compensating valve 211.
Heat supply network water pipe 38 connects near the position of condenser 20 with heat supply network backwater condenser water inlet pipe 31。The heat medium temperature making entrance condenser 20 reduces。Heat supply network water pipe 38 is provided with heat supply network water compensating valve。
When returning water shortage of heat supply network backwater, the part in multiple stage cogeneration units can be transformed by first embodiment of the invention by many group cogeneration units according to backwater amount。Such as the repowering equipped with two 300MW grade cogeneration units wherein；Four 300MW grade cogeneration units change two machines, it is achieved exhaust steam heat recovery, increase heating ability with this, improve generatine set heat efficiency, reduce gross coal consumption rate, increase economy of power plant income。
Utilize heating backwater as condenser recirculated cooling water (Heat Supplying with Low Vacuum technology), it is particularly well-suited to 300MW grade extraction condensing type heating or there is the cogeneration units of industrial steam load or the power plant of similar unit simultaneously, for Changchun, the Jilin steam power plant of the cogeneration units equipped with two C350/272-24.2/0.4/566/566, condenser throat fill into cooling water by water spraying atomization form。If rate of water make-up presses 50t/h, temperature 15 DEG C calculating, exhaust temperature can be made to reduce by 0.21 DEG C。Heat supply network moisturizing filled at place before heat supply network backwater enters condenser, improved cooling effect by lowering return water temperature, to reduce turbine discharge temperature further。If rate of water make-up presses 100t/h, temperature 15 DEG C calculating, this method can make exhaust temperature reduce by 0.35 DEG C。
Adopt this method and associated hot Force system is carried out simple transformation respectively can bring following effect: 1, increasing heating 165MW(and In Changchun County can be increased area of heat-supply service 3,000,000 square metres), it is nearly the 1/3 of specified heat capacity, if industrial steam load surplus is big, heating load can be increased more；2, reduce gross coal consumption rate and reduce (because hotspot stress improves, cold source energy greatly reduces) 48 grams/kilowatt. time；3, economic benefit about 40,000,000 yuan/year (if industrial steam load has surplus, namely increase economic well-being of workers and staff up to more than 6,000 ten thousand yuan/year not up to the power plant of rated load) is increased。And improvement expenses less than 8,000,000 yuan of being correlated with (different because each power plant situation is different)。
The operation principle of the present invention is as follows:
Need not to heat supply network hot-water supply time, steam valve 131 is shown in a fully open operation, and opens recirculated cooling water water intaking valve 411, recirculated cooling water outlet valve 431, closes heat supply network backwater condenser water intaking valve 311, heat supply network backwater condenser outlet valve 331, at this moment hotspot stress is low, and generating efficiency is high。
When needing to heat supply network hot-water supply, steam valve 131 is turned down to ensureing low pressure (LP) cylinder minimum safe steam flow, close recirculated cooling water water intaking valve 411, recirculated cooling water outlet valve 431, open heat supply network backwater condenser water intaking valve 311, heat supply network backwater condenser outlet valve 331, at this moment hotspot stress is high, and generating efficiency is high。
Steam valve 131 is turned down to ensureing low pressure (LP) cylinder minimum safe steam flow, and namely the unsafe conditions such as blade air blast, vibration, friction, cylinder body non-homogeneous expansion do not occur。Minimum safe steam flow can be provided by steam turbine manufacturing firm, minimum safe steam flow type and unit capacity and different。Reduce electric power acting, increase heating extraction flow, improve heat capacity by increasing hotspot stress。If extraction steam for factories (high steam) has surplus, then balance acting is down to heating and is drawn gas and can increase heat supply after parameter and draw gas, it is possible to improve heat capacity。
In other embodiments of the invention, by two units wherein turbine discharge increase heat capacity (Heat Supplying with Low Vacuum) making condenser 20 of heating network backwater。Backwater temperature after the latent heat of vaporization that condenser absorbs low pressure (LP) cylinder steam discharge raises 7-8 DEG C, entering back into and being drawn gas the initial station heater heating of heating to heat supply network in heat supply network supply water temperature Zai Qu factory by heating。Owing to not having thermal loss, therefore overall economic benefit reduces, because low-vacuum-operating and low pressure (LP) cylinder vapour amount reduce, the benefit decreasing value done work and bring far above two units。
To sum up, the remodeling method of the large-scale extraction-condensing steam turbine co-generation unit of the present invention
At least have the advantage that
In the present invention owing to cooling water inlet pipe position between recirculated cooling water water intaking valve, condenser connects with heat supply network backwater condenser water inlet pipe, cooling water outlet pipe position between recirculated cooling water outlet valve, condenser connects with heat supply network backwater condenser outlet pipe。Utilize the temperature of coolant in the heat lift heat supply network of turbine discharge, concrete by closing recirculated cooling water water intaking valve, recirculated cooling water outlet valve, open heat supply network backwater condenser water intaking valve, heat supply network backwater condenser outlet valve。The heating agent in heat supply network can be switched and enter condenser and turbine discharge heat-shift。The temperature of the heating agent simultaneously promoted in factory in heat supply network, namely improves the availability of condenser cooling the discharged heat of turbine discharge。
In the present invention, large-scale extraction-condensing steam turbine co-generation unit is safe and reliable to operation, and method of operation switching is simply, conveniently (time is short, does not take off cylinder exchanging rotor)。
In the present invention, the transformation of large-scale extraction-condensing steam turbine co-generation unit is simple, expense is low。The high back pressure transformation general expenses 85,000,000 yuan 1.2 hundred million yuan of exchanging rotor, the inventive method relates to improvement expenses less than 8,000,000 yuan。
In the present invention, the transformation of large-scale extraction-condensing steam turbine co-generation unit adapts at present and power supply is superfluous from now on, and unit utilizes hour trend of reduction；The economic benefit and the heat capacity amplitude that increase are big。
Above, it it is only presently preferred embodiments of the present invention, not the present invention is done any pro forma restriction, although the present invention is disclosed above with preferred embodiment, but it is not limited to the present invention, any those skilled in the art, without departing within the scope of technical solution of the present invention, when the technology contents of available the disclosure above makes a little change or is modified to the Equivalent embodiments of equivalent variations, in every case it is without departing from technical solution of the present invention content, according to any simple modification that above example is made by the technical spirit of the present invention, equivalent variations and modification, all still fall within the scope of technical solution of the present invention。
Claims (10)
1. one kind large-scale extraction-condensing steam turbine co-generation unit (100), including: heat supply network (30), cooling tower (40) in generating set (10), condenser (20), factory, it is characterised in that
In described factory, heat supply network (30) includes heat supply network backwater condenser water inlet pipe (31), heat supply network backwater condenser outlet pipe (33)；
Described cooling tower (40) is communicated with cooling water inlet pipe (41), cooling water outlet pipe (43), described cooling water inlet pipe (41) connects Guan Bi with described cooling water outlet pipe (43) in described condenser (20), and described cooling water inlet pipe (41) and described cooling water outlet pipe (43) are separately installed with recirculated cooling water water intaking valve (411) and recirculated cooling water outlet valve (431)；
The described cooling water inlet pipe (41) position between described recirculated cooling water water intaking valve (411), described condenser (20) connects with described heat supply network backwater condenser water inlet pipe (31), and the described cooling water outlet pipe (43) position between described recirculated cooling water outlet valve (431), described condenser (20) connects with described heat supply network backwater condenser outlet pipe (33)。
2. large-scale extraction-condensing steam turbine co-generation unit (100) according to claim 1, it is characterised in that
The inlet end of described condenser (20) is provided with atomization water pipe (21), and described atomization water pipe (21) is for for injecting atomized steam in described condenser (20)。
3. large-scale extraction-condensing steam turbine co-generation unit (100) according to claim 1, it is characterized in that, described cooling water inlet pipe (41) is communicated with described heat supply network water pipe (38), and the position between described heat supply network backwater condenser water inlet pipe (31) and the described condenser (20) of described cooling water inlet pipe (41) connects with described heat supply network water pipe (38)。
4. large-scale extraction-condensing steam turbine co-generation unit (100) according to claim 1, it is characterised in that described generating set (10) including: the high pressure cylinder (11) of steam turbine, intermediate pressure cylinder (12), low pressure (LP) cylinder (15) and electromotor (17)。
5. large-scale extraction-condensing steam turbine co-generation unit (100) according to claim 1, it is characterised in that in described factory, heat supply network (30) including: primary heater (37), secondary heater (39)。
6. large-scale extraction-condensing steam turbine co-generation unit (100) according to claim 1, it is characterised in that described primary heater (37) all connects with heat supply network backwater condenser outlet pipe (33) with described secondary heater (39)。
7. large-scale extraction-condensing steam turbine co-generation unit (100) according to claim 1, it is characterised in that described heat supply network backwater condenser water inlet pipe (31), described heat supply network backwater condenser outlet pipe (33) connect with user's heat supply network (200)。
8. large-scale extraction-condensing steam turbine co-generation unit (100) according to claim 1, it is characterised in that be provided with atomization water compensating valve (211) on described atomization water pipe (21)。
9. according to the arbitrary described large-scale extraction-condensing steam turbine co-generation unit (100) of claim 1-8, it is characterised in that described heat supply network water pipe (38) is provided with heat supply network water compensating valve。
10. large-scale extraction-condensing steam turbine co-generation unit (100) according to claim 4, it is characterized in that, it is provided with steam pipe (13) between medium pressure cylinder (12), described low pressure (LP) cylinder (15), described steam pipe (13) is provided with steam valve (131)。
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| Application Number | Priority Date | Filing Date | Title |
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| CN201610199157.0A CN105697076A (en) | 2016-04-01 | 2016-04-01 | Combined heat and power system of large-scale extracting and condensing steam turbine |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201610199157.0A CN105697076A (en) | 2016-04-01 | 2016-04-01 | Combined heat and power system of large-scale extracting and condensing steam turbine |
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Application publication date: 20160622 |