CN204060826U - Single reheat steam turbine high-temperature steam-extracting cooling system - Google Patents
Single reheat steam turbine high-temperature steam-extracting cooling system Download PDFInfo
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- CN204060826U CN204060826U CN201420384551.8U CN201420384551U CN204060826U CN 204060826 U CN204060826 U CN 204060826U CN 201420384551 U CN201420384551 U CN 201420384551U CN 204060826 U CN204060826 U CN 204060826U
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Abstract
The utility model discloses a kind of high temperature steam-extracting cooling system of single reheat thermodynamic system of steam tur, this single reheat thermodynamic system of steam tur comprises high-pressure cylinder, reheater, intermediate pressure cylinder, low pressure (LP) cylinder, generator, heater and extraction line, at high-pressure cylinder, intermediate pressure cylinder is provided with the one or more extraction openings be connected with extraction line, when thermodynamic system is run, the steam discharge of high-pressure cylinder is directed to after reheater carries out heat temperature raising and enters intermediate pressure cylinder again, the high temperature of drawing from extraction opening draws gas and transfers to heater for heat-setting water and/or feedwater by extraction line, also cooling system is provided with in single reheat thermodynamic system of steam tur, cooling system comprises desuperheater, modulating valve and cooling water piping, desuperheater is via cooling water piping and cooling water fluid communication, desuperheater is arranged so that high temperature draws gas can enter extraction line after reducing temperature again at desuperheater place and cooling water generation heat exchange, modulating valve is located on cooling water piping for regulating attemperation water flow.
Description
Technical field
The utility model relates to single reheat turbine LP rotors, is specifically related to single reheat steam turbine high-temperature steam-extracting cooling system.
Background technique
Adopt the thermal power plant of single reheat technology, its re-heating subsystem is, is drawn by the steam having done part merit and again heats, then lead back steam turbine and continue acting, to improve thermodynamic system efficiency in main steam turbine.
Adopt the firepower electrical plant of single reheat technology, usually also configure heat regenerative system, the heat drawn gas with main steam turbine comes heat-setting water and/or feedwater by heater, is all recovered in working-medium water by the heat drawn gas, reduce the latent heat of vaporization discharge that circulating water is taken away, to improve thermodynamic system efficiency.
For the higher unit of parameter (as main steam and reheat steam temperature more than 620 DEG C, even more than 700 DEG C), certain what extraction temperature is high, need the material rate promoting extraction line, valve, heater, extraction steam pipeline needs to use P91 or P92 even nickel-base material, greatly improve the manufacture cost of pipeline, valve and equipment, poor feasibility.
Accompanying drawing 1 is the schematic diagram of single reheat thermodynamic system of steam tur in prior art.This single reheat thermodynamic system of steam tur comprises high-pressure cylinder 1, intermediate pressure cylinder 2, low pressure (LP) cylinder 3, generator 4, reheater 5, heater 6, oxygen-eliminating device 7 and condenser 8.In normal operation, the steam discharge of steam turbine high-pressure cylinder 1 is directed to after reheater 5 carries out heat temperature raising and enters Steam Turbine Through IP Admission 2 again, steam turbine is provided with one or more extraction opening, the steam of drawing from this extraction opening transfers to heater for heat-setting water and feedwater by extraction line, thus reclaims the latent heat of vaporization to improve efficiency of thermal cycle.But the temperature of drawing gas after reheating is large compared with the high and degree of superheat, and the energy of superheat section is also used to heating water with the latent heat of vaporization, affects efficiency of thermal cycle.For the higher unit of parameter (as main steam and reheat steam temperature more than 620 DEG C, even more than 700 DEG C), certain what extraction temperature is high, need the material rate promoting extraction line, valve, heater, such as use P91 or P92 even nickel-base material, this, by the manufacture cost of riser tubing, valve and equipment greatly, also have impact on the development of high pressure high temperature turbosets.
Model utility content
The purpose of this utility model draws gas to the high temperature of single reheat thermodynamic system of steam tur to lower the temperature, within its temperature is reduced to extraction line that common alloy steel material makes and the heater temperature range of bearing, thus the manufacture cost of pipeline, valve and equipment in reduction system, be beneficial to the development of high pressure high temperature turbosets.
For achieving the above object, the utility model provides a kind of high temperature steam-extracting cooling system of single reheat thermodynamic system of steam tur, this single reheat thermodynamic system of steam tur comprises high-pressure cylinder, reheater, intermediate pressure cylinder, low pressure (LP) cylinder, generator, heater and extraction line, at high-pressure cylinder, intermediate pressure cylinder is provided with the one or more extraction openings be connected with extraction line, when thermodynamic system is run, the steam discharge of high-pressure cylinder is directed to after reheater carries out heat temperature raising and enters intermediate pressure cylinder again, the high temperature of drawing from extraction opening draws gas and transfers to heater for heat-setting water and/or feedwater by extraction line, it is characterized in that, also cooling system is provided with in single reheat thermodynamic system of steam tur, cooling system comprises desuperheater, modulating valve and cooling water piping, desuperheater is via cooling water piping and cooling water fluid communication, wherein, desuperheater is arranged so that high temperature draws gas can enter extraction line after reducing temperature again at desuperheater place and cooling water generation heat exchange, modulating valve is located on cooling water piping for regulating attemperation water flow.
Preferably, this extraction line is provided with high temperature extraction check valve, and desuperheater is arranged on the extraction line after high temperature extraction check valve.
Preferably, a suitable distance after this desuperheater distance high-temperature extraction check valve.
Preferably, cooling water piping is connected with the hydrophobic piping of heater, thus makes hydrophobic from heater of the cooling water in cooling water piping, for the desuperheat that drawn gas by high temperature.
Preferably, lead to the extraction line of the primary heater in described multiple stage heater to be connected with the drain water piping of the previous stage heater of the described primary heater in described multiple stage heater, thus utilize previous stage heater hydrophobic from described primary heater to draw gas to high temperature to carry out desuperheat.
Preferably, the primary heater in described multiple stage heater hydrophobic through several roads cooling water piping respectively with after desuperheater fluid on extraction line corresponding to what heater be communicated with, for the desuperheat that draws gas to corresponding high temperature.
Preferably, this modulating valve for regulate flow hydrophobic in cooling water piping thus the temperature that high temperature is drawn gas reduce to desuperheater after extraction line and the heater temperature range of bearing within.
Preferably, cooling water piping is stated desuperheater fluid and is communicated with, and after making cooling water enter desuperheater, heat absorption vaporization occurs and together enters heater for heat-setting water and/or feedwater with by drawing gas of desuperheat.
Preferably; this cooling system also comprises start and stop or critical cooling water piping; when starting or stop single reheat thermodynamic system of steam tur or when occurring that normal cooling water breaks down; the water supply of these start and stop or critical cooling water piping is used for the desuperheat that high temperature draws gas, the temperature that high temperature is drawn gas be reduced to desuperheater after the temperature range that can bear of relevant device within.
Preferably, also blow-off line is provided with in single reheat thermodynamic system of steam tur, another extraction line is drawn from blow-off line, drawing gas in this another extraction line transfers to heater for heat-setting water and/or feedwater, this another extraction line is provided with desuperheater, and what desuperheater was arranged so that blow-off line draws draw gas can reduce temperature at desuperheater place and cooling water generation heat exchange.
Preferably, the material of the connection desuperheater of heater and extraction line and the part of heater is common alloy steel.
The utility model draws gas for the high temperature of the higher single reheat turbine LP rotors of parameter; desuperheater is provided with after the check valve of high temperature extraction line; start and stop or clutch adopt and come for the cooling of high temperature extraction line to pump tap water; when generator set normally runs; adopt the hydrophobic desuperheat drawn gas for high temperature of prime heater; by the temperature that the desuperheat that draws gas is suitable for common alloy steel; the cost of tubing, external steaming cooler and high-pressure heater after effectively can reducing desuperheater, for the development of more high pressure high temperature turbosets creates conditions.The utility model is very little on the impact of thermodynamic cycle up-time efficiency simultaneously, has good technical and economic feasibility.
Accompanying drawing explanation
Fig. 1 is the schematic diagram of single reheat thermodynamic system of steam tur in prior art;
Fig. 2 is the schematic diagram of the single reheat steam turbine high-temperature steam-extracting cooling system according to the utility model first embodiment;
Fig. 3 is the schematic diagram of the single reheat steam turbine high-temperature steam-extracting cooling system according to the utility model second embodiment; And
Fig. 4 is the schematic diagram of the single reheat steam turbine high-temperature steam-extracting cooling system according to the utility model the 3rd embodiment.
Embodiment
Below with reference to accompanying drawing, preferred embodiment of the present utility model is described in detail, understands the purpose of this utility model, feature and advantage so that clearer.It should be understood that embodiment shown in the drawings is not the restriction to the utility model scope, and the connotation just in order to technical solutions of the utility model are described.
Below, major technique term of the present utility model is described.
Reheating: the steam having done part merit in steam turbine is drawn and again heats, then lead back steam turbine and continue acting.This mode is called reheating.By rational reheating, can exhaust steam moisture be reduced, improve efficiency of thermal cycle.
High temperature draws gas: from the steam that the temperature of the intergrade extraction before turbine discharge is higher, be the main steam of about 600 DEG C for temperature, the temperature that high temperature draws gas is generally about 350 DEG C to about 550 DEG C; For the main steam that temperature is about 700 DEG C, the temperature that high temperature draws gas is generally about 350 DEG C to about 650 DEG C.
Cooling system: the system of the medium that the medium chilling temperature that employing temperature is lower is higher.
Fig. 2 is the schematic diagram of the single reheat steam turbine high-temperature steam-extracting cooling system according to the utility model first embodiment.As shown in Figure 2, single reheat thermodynamic system of steam tur generally includes high-pressure cylinder 1, intermediate pressure cylinder 2, low pressure (LP) cylinder 3, generator 4, reheater 5, heater 6, oxygen-eliminating device 7, vapour condenser 8 and extraction line 12, high-pressure cylinder 1 with intermediate pressure cylinder 2 are provided with the one or more extraction openings be connected with extraction line, when this thermodynamic system is run, the steam discharge of high-pressure cylinder is directed to after reheater carries out heat temperature raising and enters intermediate pressure cylinder again, and the high temperature of drawing from extraction opening draws gas and transfers to heater and oxygen-eliminating device for heat-setting water and/or feedwater by extraction line.But, because the temperature of drawing gas after reheating is compared with high and the degree of superheat is large, for the unit that parameter is higher, certain what extraction temperature is high (as main steam and reheat steam temperature more than 620 DEG C, even more than 700 DEG C), therefore need the material rate promoting extraction line, valve, heater, such as, use P91 or P92 even nickel-base material, this, by the manufacture cost of riser tubing, valve and equipment greatly, also have impact on the development of high pressure high temperature turbosets.Therefore, in the present embodiment, add high temperature steam-extracting cooling system, will draw gas after reducing temperature for drawing gas to high temperature causes heater and oxygen-eliminating device again, heats it.
As shown in Figure 2, single reheat steam turbine high-temperature steam-extracting cooling system comprises desuperheater 9, modulating valve 10, cooling water piping 11 and start and stop or critical cooling water piping (not shown).Desuperheater 9 is arranged on high temperature extraction line, preferably, desuperheater 9 is arranged on the extraction line after high temperature extraction check valve (not shown), this desuperheater is via cooling water piping and cooling water fluid communication, and desuperheater 9 is arranged so that high temperature draws gas again can enter extraction line after reducing temperature at desuperheater 9 place and cooling water generation heat exchange.Modulating valve 10 is located at for regulating attemperation water flow on cooling water piping 11, and cooling water piping 11 one end fluid is communicated in hydrophobic piping 13, and the other end is communicated with desuperheater 9 fluid.
When single reheat thermodynamic system of steam tur normally runs, upper level heater hydrophobic flow to desuperheater 9 by cooling water piping 11 thus with the high-temperature gas generation heat exchange in extraction line 12, the heat that hydrophobic adsorption high temperature draws gas is vaporized and high temperature is drawn gas desuperheat, and drawing gas after the gas that produces afterwards of hydrophobic vaporization and desuperheat together enters next stage heater or oxygen-eliminating device and be used to heated feed water and water of condensation.
Modulating valve 10 is for controlling the hydrophobic flow for next stage gas desuperheat of upper level heater, this uninterrupted makes high temperature draw gas effectively by the temperature that desuperheat is suitable for common alloy steel, thus avoids extraction line to use the high-grade material involved great expense.In addition, the gas produced afterwards due to hydrophobic vaporization together enters next stage heater or oxygen-eliminating device with drawing gas, do not reduce for the total amount of heat of heat-setting water and feedwater in next stage heater or oxygen-eliminating device, the efficiency of utilization that thus high temperature draws gas does not reduce.
When starting or stop single reheat thermodynamic system of steam tur, the water supply that the high temperature of high-pressure cylinder 1 and intermediate pressure cylinder 2 draws gas by start and stop or critical cooling water piping, such as, give the temperature that pump tap water desuperheat can bear to corresponding extraction line and heater or oxygen-eliminating device; When single reheat thermodynamic system of steam tur normally runs, high temperature draws gas by carrying out desuperheat by upper level heater condensate.Fig. 3 is the schematic diagram of the single reheat steam turbine high-temperature steam-extracting cooling system according to the utility model second embodiment.Composition graphs 2 and Fig. 3 can find out, the remarkable difference of the second embodiment and the first embodiment is, the high temperature steam-extracting cooling system of above-described embodiment adopts higher level's heater condensate to spray water step by step to the form of next stage high temperature extraction line, and the high temperature steam-extracting cooling system of the present embodiment adopts the form of the hydrophobic desuperheat that draws gas for what high temperature rear of primary heater.In Fig. 3, hydrophobic all from primary heater of current in cooling water piping 11, modulating valve 10 is according to the hydrophobic flow in each cooling water piping 11 of the desuperheat demand modeling of high temperature extraction line at different levels, thus reaching effective temperature lowering effect, the temperature that high temperature at different levels is drawn gas is within the scope that pipeline that common alloy is made into can bear.Similarly, hydrophobicly flow to desuperheater 9 by cooling water piping 11 and vaporize with the heat absorbing high temperature and draw gas and together enter corresponding heater or oxygen-eliminating device to by drawing gas of desuperheat.
2 tunnels in Fig. 2 and Fig. 3 are a cooling water piping corresponding heater 6 and an oxygen-eliminating device 7 respectively step by step, and heater is the pattern of single-row 1 100% capacity.In fact, according to different extraction temperatures and different desuperheat demands, the quantity of cooling water piping also can be 1 or 3 tunnels or more step by step, and in addition, heater also can adopt the pattern of biserial 2 50% capacity.
Cooling system of the present utility model also can adopt cascaded drain desuperheat and the hydrophobic form combined for what desuperheat rear of prime, such as, more bleedings pipeline is provided with in single reheat thermodynamic system of steam tur, the hydrophobic desuperheat drawn gas for the second level of primary heater, and the desuperheat that second level heater condensate is used for the third level, the fourth stage (or more level) draws gas.
Fig. 4 is the schematic diagram of the single reheat steam turbine high-temperature steam-extracting cooling system according to the utility model the 3rd embodiment.3rd embodiment is similar with the first embodiment as shown in Figure 2, all adopts higher level's heater condensate to spray water step by step to the form of next stage high temperature extraction line.Similar with the second embodiment as shown in Figure 3 according to the single reheat steam turbine high-temperature steam-extracting cooling system of the utility model the 4th embodiment, all adopt prime heater condensate for what high temperature rear to draw gas the form of desuperheat.Unlike, consider for high pressure high temperature turbosets, as extra-supercritical unit, the exhaust temperature of high-pressure cylinder also may be higher, now, also can increase cooling system to blow-off line 12 '.Prime is hydrophobic enters desuperheater by cooling water piping and high temperature draws gas or steam discharge generation heat exchange, high temperature is drawn gas and the temperature of steam discharge is reduced to the temperature that common alloy steel can bear.The utility model draws gas for the high temperature of the higher single reheat turbine LP rotors of parameter; desuperheater is provided with after the check valve of high temperature extraction line; start and stop or clutch adopt and come for the cooling of high temperature extraction line to pump tap water; when generator set normally runs; adopt the hydrophobic desuperheat drawn gas for high temperature of prime heater; by the temperature that the desuperheat that draws gas is suitable for common alloy steel; the cost of tubing, external steaming cooler and high-pressure heater after effectively can reducing desuperheater, for the development of more high pressure high temperature turbosets creates conditions.Meanwhile, for together entering rear class heater or oxygen-eliminating device with drawing gas after the hydrophobic heat absorption vaporization of desuperheat, taking full advantage of high temperature and to draw gas the heat carried.
In high temperature steam-extracting cooling system of the present utility model; cooling water normally can adopt hydrophobic (start and stop or critical cooling water can adopt to pump tap water) of upper level high-pressure heater; or using the hydrophobic cooling water (start and stop or critical cooling water still can adopt to pump tap water) drawn gas as other what high temperature of first order high-pressure heater; by the temperature that extraction temperature desuperheat is suitable for common alloy steel; the cost of tubing, external steaming cooler and high-pressure heater after effectively can reducing desuperheater, for the development of more high pressure high temperature turbosets creates conditions.
Such as, for 1 1000MW, 700 DEG C of single reheat supercritical generating sets, under conventional thermodynamic system schema, thermodynamic system equipment (comprising heater, oxygen-eliminating device, the steaming cooler etc.) needs of each extraction steam pipeline and correspondence adopt expensive high-grade material, such as P91 material, P92 even nickel-base material; But, adopt the utility model single reheat steam turbine high-temperature steam-extracting cooling system, by the temperature that the desuperheat that draws gas is suitable for common alloy steel, the cost of subsequent heat device, external steaming cooler and tubing reduces greatly, makes the investment of thermodynamic system reduce about 5,000 ten thousand compared to conventional main steam turbine thermodynamic system.The utility model is very little on the impact of thermodynamic cycle up-time efficiency simultaneously, has good technical and economic feasibility.
Below described preferred embodiment of the present utility model in detail, but it will be appreciated that, after having read above-mentioned instruction content of the present utility model, those skilled in the art can make various changes or modifications the utility model.These equivalent form of values fall within the application's appended claims limited range equally.
Claims (10)
1. the high temperature steam-extracting cooling system of a single reheat thermodynamic system of steam tur, described single reheat thermodynamic system of steam tur comprises high-pressure cylinder, reheater, intermediate pressure cylinder, low pressure (LP) cylinder, generator, multiple stage heater and extraction line, at described high-pressure cylinder, intermediate pressure cylinder is provided with the one or more extraction openings be connected with described extraction line, when described thermodynamic system is run, the steam discharge of described high-pressure cylinder is directed to after described reheater carries out heat temperature raising and enters described intermediate pressure cylinder again, the high temperature of drawing from described extraction opening draws gas and transfers to described heater for heat-setting water and/or feedwater by described extraction line, it is characterized in that,
In described single reheat thermodynamic system of steam tur, be also provided with cooling system, described cooling system comprises desuperheater, modulating valve and cooling water piping, described desuperheater via described cooling water piping and cooling water fluid communication, wherein,
Described desuperheater is arranged so that described high temperature draws gas can enter extraction line at described desuperheater place and cooling water generation heat exchange after reducing temperature again, and described modulating valve is located on described cooling water piping, for regulating attemperation water flow.
2. high temperature steam-extracting cooling system as claimed in claim 1, it is characterized in that, described extraction line is provided with high temperature extraction check valve, and described desuperheater is arranged on the extraction line after described high temperature extraction check valve.
3. high temperature steam-extracting cooling system as claimed in claim 1, it is characterized in that, described cooling water piping is connected with the hydrophobic piping of described heater, thus makes hydrophobic from described heater of the cooling water in described cooling water piping, for the desuperheat that drawn gas by high temperature.
4. high temperature steam-extracting cooling system as claimed in claim 3, it is characterized in that, lead to the extraction line of the primary heater in described multiple stage heater to be connected with the drain water piping of the previous stage heater of the described primary heater in described multiple stage heater, thus utilize previous stage heater hydrophobic from described primary heater to draw gas to high temperature to carry out desuperheat.
5. high temperature steam-extracting cooling system as claimed in claim 3, it is characterized in that, primary heater in described multiple stage heater hydrophobic through several roads cooling water piping respectively with after desuperheater fluid on extraction line corresponding to what heater be communicated with, for the desuperheat that draws gas to corresponding high temperature.
6. high temperature steam-extracting cooling system as claimed in claim 1, it is characterized in that, described modulating valve is for regulating hydrophobic flow in described cooling water piping thus the temperature enabling described high temperature draw gas reduces within the temperature range that extraction line after described desuperheater and heater bear.
7. high temperature steam-extracting cooling system as claimed in claim 1, it is characterized in that, described cooling water piping is communicated with described desuperheater fluid, and after making described cooling water enter described desuperheater, heat absorption vaporization occurs and together enters described heater for heat-setting water and/or feedwater with by drawing gas of desuperheat.
8. high temperature steam-extracting cooling system as claimed in claim 1; it is characterized in that; described cooling system also comprises start and stop or critical cooling water piping; when starting or stop described single reheat thermodynamic system of steam tur or when occurring that normal cooling water breaks down; the water supply of described start and stop or critical cooling water piping is used for the desuperheat that described high temperature draws gas, and the temperature that described high temperature is drawn gas is reduced within the temperature range that the relevant device after described desuperheater can bear.
9. the high temperature steam-extracting cooling system according to any one of claim 1-8, it is characterized in that, also blow-off line is provided with in described single reheat thermodynamic system of steam tur, another extraction line is drawn from described blow-off line, drawing gas in another extraction line described transfers to described heater for heat-setting water and/or feedwater, another extraction line described is also provided with desuperheater, and what described desuperheater was arranged so that described blow-off line draws draw gas can reduce temperature at described desuperheater place and cooling water generation heat exchange.
10. high temperature steam-extracting cooling system as claimed in claim 1, it is characterized in that, the material of the described desuperheater of connection of described heater and described extraction line and the part of described heater is common alloy steel.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420384551.8U CN204060826U (en) | 2014-07-11 | 2014-07-11 | Single reheat steam turbine high-temperature steam-extracting cooling system |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420384551.8U CN204060826U (en) | 2014-07-11 | 2014-07-11 | Single reheat steam turbine high-temperature steam-extracting cooling system |
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| CN204060826U true CN204060826U (en) | 2014-12-31 |
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| CN201420384551.8U Withdrawn - After Issue CN204060826U (en) | 2014-07-11 | 2014-07-11 | Single reheat steam turbine high-temperature steam-extracting cooling system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104100309A (en) * | 2014-07-11 | 2014-10-15 | 中国电力工程顾问集团华东电力设计院 | High-temperature steam extraction and cooling system for single-reheat steam turbine |
-
2014
- 2014-07-11 CN CN201420384551.8U patent/CN204060826U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104100309A (en) * | 2014-07-11 | 2014-10-15 | 中国电力工程顾问集团华东电力设计院 | High-temperature steam extraction and cooling system for single-reheat steam turbine |
| CN104100309B (en) * | 2014-07-11 | 2016-03-23 | 中国电力工程顾问集团华东电力设计院有限公司 | Single reheat steam turbine high-temperature steam-extracting cooling system |
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Granted publication date: 20141231 Effective date of abandoning: 20160323 |
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