CN202024865U - On-line detection device for air leakage quantity of vacuum system of steam turbine generator unit - Google Patents
On-line detection device for air leakage quantity of vacuum system of steam turbine generator unit Download PDFInfo
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- CN202024865U CN202024865U CN2011201267280U CN201120126728U CN202024865U CN 202024865 U CN202024865 U CN 202024865U CN 2011201267280 U CN2011201267280 U CN 2011201267280U CN 201120126728 U CN201120126728 U CN 201120126728U CN 202024865 U CN202024865 U CN 202024865U
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- 238000004364 calculation method Methods 0.000 abstract description 3
- 230000009286 beneficial effect Effects 0.000 abstract description 2
- 238000009434 installation Methods 0.000 abstract description 2
- 238000005086 pumping Methods 0.000 abstract 2
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- 229920006395 saturated elastomer Polymers 0.000 description 13
- 238000005259 measurement Methods 0.000 description 7
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- 238000001816 cooling Methods 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 230000000740 bleeding effect Effects 0.000 description 5
- 238000000605 extraction Methods 0.000 description 3
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- 238000002474 experimental method Methods 0.000 description 2
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- 238000005516 engineering process Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000000691 measurement method Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000000523 sample Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000004781 supercooling Methods 0.000 description 1
- PICXIOQBANWBIZ-UHFFFAOYSA-N zinc;1-oxidopyridine-2-thione Chemical class [Zn+2].[O-]N1C=CC=CC1=S.[O-]N1C=CC=CC1=S PICXIOQBANWBIZ-UHFFFAOYSA-N 0.000 description 1
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Abstract
The utility model relates to an on-line detection device for air leakage quantity of a vacuum system of a steam turbine generator unit, which can be used for on-line detection on the air leakage rate of a condenser adopting a water-ring vacuum pump for vacuum pumping. The on-line detection device has a concrete arrangement that a temperature sensor, a pressure sensor, an air flow rate sensor and an absolute humidity sensor are additionally installed behind the water-ring vacuum pump, through the parameters, the mass and the flow rate of water vapor in an air pumping pipeline under a specific work condition can be determined, and finally, the mass and the flow rate of the pumped air (i.e. the sum of the air leakage rate of each negative pressure part of the whole vacuum system) can be obtained through calculation according to a thermodynamic formulae. The on-line detection device has the beneficial effects that the measuring principle is clear and accurate, a measuring mechanism is simple, the installation is convenient, the air leakage quantity of the condenser can be measured on line in real time, the reliable parameter basis is provided for the vacuum system of the steam turbine generator unit to maintain a higher vacuum level, and the assurance is provided for the safe and economic production of power plants.
Description
Technical field
The utility model relates to a kind of METHOD FOR TURBOGENERATOR SET vacuum system air leakage on-line measuring device.
Background technology
The vacuum system of Turbo-generator Set comprises: condenser vapour side, exhaust system and other negative pressure position, its effect are to make steam can change heat content into the kinetic energy of steam turbine to greatest extent, and finally are converted into electric energy.Condenser vacuum is bigger to the influence of unit economic benefit, and the every raising of condenser vacuum value 1kPa will reduce the about 3g/kWh of net coal consumption rate, so keep the economy that the higher vacuum of Turbo-generator Set can significantly improve power plant.
In addition, consider, keep the vacuum of Turbo-generator Set, also be absolutely necessary from the angle of safety in production:
1, the bleed air of condenser raises except making exhaust steam pressure and temperature, reduces outside the economy of steam turbine, and turbine low pressure cylinder is out of shape because of vapor (steam) temperature is high, causes unit vibration.
2, because the partial pressure of air increases, increase the solubleness of air in water, aggravated the corrosion of low pressure pipeline and low-pressure heater, increased the burden of oxygen-eliminating device, unfavorable to unit safety.
3, air accumulation is around water pipe, and making changes the resistance to heat increase, and commentaries on classics hot junction difference increases, vacuum descends; The increase of air partial pressure also makes the burden of condensate undercooling increasing and increase air ejector or the like adverse effect.
As can be seen, in the actual production, the air leakage of online detection condenser promptly and accurately so that can keep the higher vacuum of unit, all is of great importance for the economy of power plant and safety in production.
China still based on fired power generating unit, became under the high situation in energy shortage, generating in long period of time from now on, and condenser vacuum research is a very urgent and long-term job.Change condenser and air-extractor Effect on Performance degree in order to understand the unit vacuum tightness, be necessary qualitative, quantitative relationship between unit vacuum tightness and the gas leakage flow are studied, the gas leakage flow size of grasp under the tight degree of certain vacuum, and the unit vacuum tightness is with the variation relation of gas leakage flow.
Traditional measurement method:
Lot of documents is consulted demonstration, measures the condenser air leakage at present and has only a kind of round-about way, isolates out vacuum means postpone, measures its rate of vacuum drop and air leakage by repeatedly put into air in condenser, and its principle as shown in Figure 1.
Open air intake valve, the control air rate of bleeding is the Δ G on the horizontal ordinate
1Kilogram/per hour measures rate of vacuum drop under this operating mode and is the V on the ordinate
H1, changing the air rate of bleeding then is Δ G
2Kilogram/per hour, measure new rate of vacuum drop V
H2, in like manner, just can draw out the relation curve v that replenishes between air capacity and the vacuum decline rate
H=f (Δ G), curve and horizontal ordinate intersection point Δ G
-1Be exactly when not replenishing air, the air capacity of the vacuum system of bleeding.
As can be seen, this method need be through repeatedly measuring, and the very important person be in condenser, put into air, bigger to the destruction of vacuum, unfavorable to keeping the safety in production.This patent proposes a kind of method of can direct-on-line measuring the condenser air leakage.
Summary of the invention
The method of existing measurement Turbo-generator Set vacuum system air leakage is a kind of round-about way, need be through repeatedly measuring, and the very important person be in condenser, put into air, bigger to the destruction of vacuum, unfavorable to keeping the safety in production.In order to overcome the drawback of existing measuring method, the utility model provides a kind of new direct measuring method, can be in real time, on-line measurement Turbo-generator Set vacuum system air leakage.Method is simple and reliable, utilizes power plant safety, economical operation.
The utility model also provides a kind of Turbo-generator Set vacuum system air leakage on-line measuring device.
The technical scheme that its technical matters that solves the utility model adopts is:
A kind of Turbo-generator Set vacuum system air leakage online test method, step is as follows:
(1) at first on the condenser air hose, adopts vacuum pump that the vacuum system of unit is vacuumized, make most of water vapor condense and dredge out;
(2) after vacuum pump, install and measure the instrument of flow, humidity, temperature and pressure, the above-mentioned parameter that obtains surveying utilizes formula
The computing system air capacity of bleeding
In the formula, v, x, t, p are respectively flow, humidity, humidity and the pressure of real side, p
sBe the pressure of saturated vapour corresponding under the t temperature, S is the cross-sectional area of pump-line, and R is a universal gas constant.
Use as further expansion, in step (2) afterwards,, carry out repeatedly simulated experiment, air leakage is fitted to and temperature t, pressure p, empirical correlation formula G that humidity x is relevant with flow v by changing parameters of temperature t, pressure p, humidity x and/or flow v
Dry air=f (t, p, x, v).
At said method, the utility model provides a kind of Turbo-generator Set vacuum system air leakage on-line measuring device, on condenser exhaust pipeline, connect a vacuum pump, add flow sensor, humidity sensor, temperature sensor and pressure transducer on the pipeline behind the vacuum pump.
Further, described temperature sensor, pressure transducer, flow sensor and humidity sensor link to each other successively.
Further, described vacuum pump is a water-ring vacuum pump.
Further, on the pipeline of described flow sensor, humidity sensor, temperature sensor and pressure transducer back, be provided with stop valve.
Technical scheme general introduction: on condenser exhaust pipeline, adopt water-ring vacuum pump that the vacuum system of unit is vacuumized, the vapour gas mixture is after passing through water-ring vacuum pump in the pipeline, wherein most of water vapor is cooled, condense and dredge out, reduced the partial pressure and the relative content of steam in the pipeline, after water-ring vacuum pump, install measuring shunt mechanism additional, comprising the thermal resistance type temperature sensor---measure the temperature of residue mixed gas, the piezoelectric type pressure unit---measure the pressure of residue mixed gas, the hot-wire gas meter---measure the flow of residue mixed gas, hygristor formula humidity sensor---measure the humidity of residue mixed gas, by these parameters, just can determine under a certain specific operation, water vapour relative content in the pipeline, and finally calculate the air capacity of extraction, each negative pressure part leaked-in air amount sum of promptly whole vacuum system.
The beneficial effects of the utility model are, measuring principle is clear, accurate, measuring mechanism is simple, easy for installation, can real-time online measuring condenser air leakage, keep higher vacuum level for the Steam Turbine vacuum system reliable parameter foundation is provided, for power plant safety, economic production are given security.
Description of drawings
Fig. 1 is a schematic diagram of measuring condenser air leakage conventional method at present;
Fig. 2 is the structural representation of the utility model METHOD FOR TURBOGENERATOR SET vacuum system air leakage online test method schematic diagram and the utility model device.
Among the figure, 1. low pressure (LP) cylinder, 2. condenser, 3. condensate pump, 4. water-ring vacuum pump, 5. temperature sensor, 6. pressure transducer, 7. flow sensor, 8. humidity sensor, 9. stop valve.
Embodiment
Below in conjunction with drawings and Examples the utility model is further specified.
See also Fig. 2, a kind of Turbo-generator Set vacuum system air leakage online test method, step is as follows:
(1) at first on the condenser air hose, adopts water-ring vacuum pump that the vacuum system of unit is vacuumized, make most of water vapor condense and dredge out;
Before water-ring vacuum pump 4, the temperature of mixed gas, pressure are respectively t in the extraction line
1, p
1, gas componant is wet saturated steam and AIR MIXTURES, as shown in Equation (1):
t
1, p
1Under the operating mode: G
Mixed gas=G
Wet saturated steam+ G
Air(1)
Formula (1) just illustrates the composition of mixed gas qualitatively, is not to be used for calculating air quality.At this moment most of in the mixed gas is wet saturated steam (accounting for 80%), and air only accounts for 20%, we can't determine air quality for the mixed gas of this ratio, head and shoulders above the measurement range of humidity sensor 8, so we expect at first reducing the amount of water vapour, reaching major part all is air, water vapour accounts for a fraction of situation (for example as the gas in the room, air is a lot, water vapour seldom), so what we expected in the past is to install cooling device additional, allow most wet saturated steam condensation dredge out earlier, reach a kind of state: air is a lot, and steam is less, so that measure moisture in the potpourri, and finally determine air capacity with humidity sensor 8.
Water-ring vacuum pump 4 plays here bleeds and two effects of cooling and mixing gas, it is very essential cooling off this effect, have only through supercooling, could allow a large amount of wet saturated steams freeze-outs in the mixed gas, purpose is to reduce the content of water vapour in the mixed gas, improve the relative content of air, because the moisture that we will utilize humidity sensor 8 to measure in the soft air next step, if adopt other vacuum pumps can only play a part to vacuumize.G in this formula and the following formula all refers to mass rate.
Dredging water outlet (condensate water) has incorporated in the working water of water-ring vacuum pump 4 and has taken away, so gas remaining in the pipeline is a spot of water vapour and most air, at this moment just can utilize moisture probe to measure moisture mass percent in the mixed gas mass percent of air (thereby obtain).Such as after originally the cooling of the water vapour of the overwhelming majority was taken away, mixed gas composition was the air of only remaining 2% water vapour+98%, so just can utilize hygrometer to measure the moisture in the mixed gas.
(2) after water-ring vacuum pump, install and measure the instrument of flow, humidity, temperature and pressure, at first obtain the above-mentioned parameter of surveying.
After process water-ring vacuum pump 4, because the cooling effect of working water in the vacuum pump, the mixed gas temperature is reduced to t
2Owing to the boosting of pump, mixture pressure raises and is p simultaneously
2, the process that such cooling is boosted causes in the mixed gas a large amount of wet saturated steams to condense into water, taken out of by the working water in the water-ring vacuum pump 4, and saturated vapour that residue is not condensed and air formation soft air, the mass balance equation of this process is as follows:
t
2, p
2Under the operating mode: G
Mixed gas=G
Dredge water outlet+ G
Saturated vapour+ G
Air=G
Dredge water outlet+ G
Soft air(2)
As mentioned above, soft air composition in the formula (2) should be t in theory
2Saturated vapour+air under the temperature, but in the actual production, may be in the pipeline after water-ring vacuum pump 4 owing to the low reason of pipe temperature, also having very a spot of steam is condensed on the inside pipe wall, cause water vapour to reach a kind of unsaturation state, therefore, the gas componant in the exhaust pipe after the water-ring vacuum pump 4, as the formula (3)
G
Soft air=G
Water vapour+ G
Air(3)
In the formula (3),
G
Soft air, total mass rate (kg/s) in the pump-line,
G
Water vapourThe mass rate of water vapour (kg/s) in the pump-line, following footnote " water vapour " comprises the unsaturated steam state (the hygrometer indicating value is the numerical value between 0～1 during on-line measurement) of desirable saturated-vapor state (the hygrometer indicating value is 1 during on-line measurement) or real process, be referred to as water vapour at this, to not influence of subsequent calculations.
G
Air, the mass rate of air (kg/s) in the pump-line,
Above three mass rates can utilize separately molar flow to multiply by amount of substance to obtain, at this, we only are concerned about MAF.
After the water-ring vacuum pump, the pump-line internal pressure can be similar to and regard ideal gas as a little more than 1 atmospheric pressure.Utilize temperature, pressure, and the volumetric flow rate of perfect gas equation substitution air, just can calculate the molar flow of air, as shown in Equation (4):
p·V＝n·R(t+273.15) (4)
In the formula,
P---gaseous tension, kpa,
V---gas flow rate, (m/s),
N---gas molar flow, (mol/s),
R---universal gas constant, 8.314J/ (molK)
If utilize following formula to calculate the molar flow of air, must to know the partial pressure of air, for the calculating of air partial pressure: suppose t
2The saturated vapour pressure p of correspondence under the temperature
s, the rh value that hygrometer measures is x, then the partial pressure of water vapor under this operating mode is: xp
s, the air partial pressure is: p
2-xp
s, can obtain the mass flow calculation formula of air thus:
In the formula (5),
V
Air---volume of air flow (m
3/ s), its value equates with the volumetric flow rate of soft air in the pump-line, calculate by formula (6),
V
Soft air=v * S (6)
In the formula,
V---gas flow rate (m/s) is obtained by the on-line measurement of gas flow rate meter,
Cross-sectional area (the m of S---pump-line
2), obtain by the pump-line mechanical drawing;
Finally, utilize formula
The computing system air capacity of bleeding
In the formula, v, x, t, p are respectively flow, humidity, humidity and the pressure of real side, p
sBe the pressure of saturated vapour corresponding under the t temperature, S is the cross-sectional area of pump-line, and R is a universal gas constant.
Use as further expansion of the present utility model, in step (2) afterwards, by changing parameters of temperature t
2, pressure p
2, humidity x and/or flow v, carry out repeatedly simulated experiment, air leakage is fitted to and temperature t
2, pressure p
2, empirical correlation formula G that humidity x is relevant with flow v
Dry air=f (t
2, p
2, x, v).
Calculated examples:
On-line measurement obtains parameter: temperature t
2: 35 ℃, pressure p
2: 106kpa, relative humidity: 50%, gas flow rate: 1.5m/s, the caliber 0.05m of pump-line obtains cross-sectional area S=3.14 * 0.05
2=0.0079m
2,
Obtain V by formula (6)
Air=V
Soft air=v * S=1.5m/s * 0.0079m
2=0.0119m
3/ s,
Find the saturated vapour pressure p in the time of 35 ℃ by the saturated vapour chart
sBe 5.626kpa, with last planar survey, the parameter substitution formula (5) that calculates:
G
Air=29 * (106kpa-50% * 5.626kpa) * 0.0119m
3/ s ÷ [8.314J/ (molK) * (35+273.15)]=0.0139kg/s=0.0139 * 3600kg/h=50.0378kg/h
Figure 2 shows that a kind of Turbo-generator Set vacuum system air leakage on-line measuring device provided by the utility model, it connects a water-ring vacuum pump 4 on condenser 2 exhaust pipelines, add temperature sensor 5, pressure transducer 6, flow sensor 7 and humidity sensor 8 on the pipeline behind the water-ring vacuum pump successively, temperature sensor 5, pressure transducer 6, flow sensor 7 and humidity sensor 8 and erection sequence no requirement (NR) are provided with stop valve 9 on the pipeline of described flow sensor 7, humidity sensor 8, temperature sensor 5 and pressure transducer 6 back.
On condenser exhaust pipeline, adopt the vacuum system of 4 pairs of units of water-ring vacuum pump to vacuumize, the vapour gas mixture is after passing through water-ring vacuum pump 4 in the pipeline, wherein most of water vapor is cooled, condense and dredge out, reduced the partial pressure and the relative content of steam in the pipeline, after water-ring vacuum pump 4, install measuring shunt mechanism additional, comprising the thermal resistance type temperature sensor---measure the temperature of residue mixed gas, the piezoelectric type pressure unit---measure the pressure of residue mixed gas, the hot-wire gas meter---measure the flow of residue mixed gas, hygristor formula humidity sensor---measure the humidity of residue mixed gas, by these parameters, just can determine under a certain specific operation, water vapour relative content in the pipeline, and finally calculate the air capacity of extraction, each negative pressure part leaked-in air amount sum of promptly whole vacuum system.
Claims (4)
1. Turbo-generator Set vacuum system air leakage on-line measuring device, it is characterized in that: on condenser exhaust pipeline, connect a vacuum pump, add flow sensor, humidity sensor, temperature sensor and pressure transducer on the pipeline behind the vacuum pump.
2. a kind of Turbo-generator Set vacuum system air leakage on-line measuring device according to claim 1, it is characterized in that: described temperature sensor, pressure transducer, flow sensor and humidity sensor link to each other successively.
3. a kind of Turbo-generator Set vacuum system air leakage on-line measuring device according to claim 1, it is characterized in that: described vacuum pump is a water-ring vacuum pump.
4. a kind of Turbo-generator Set vacuum system air leakage on-line measuring device according to claim 1 and 2 is characterized in that: be provided with stop valve on the pipeline of described flow sensor, humidity sensor, temperature sensor and pressure transducer back.
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102252808A (en) * | 2011-04-26 | 2011-11-23 | 山东电力研究院 | Online detecting method and device for air leakage quantity of vacuum system of turbo generator unit |
| CN102494895A (en) * | 2011-11-29 | 2012-06-13 | 河北省电力建设调整试验所 | Analyzing method for energy saving and optimization of steam turbine set of power station |
| CN104296942A (en) * | 2014-09-05 | 2015-01-21 | 西安亨特电力科技有限公司 | Leak detection processing method for vacuum system of thermal generating unit |
| CN105241667A (en) * | 2015-10-23 | 2016-01-13 | 上海电力学院 | Condenser vacuum state identification method based on k-M model |
| CN108061624A (en) * | 2017-11-21 | 2018-05-22 | 四川成发普睿玛机械工业制造有限责任公司 | The air mass flow of aerial motor spare part and seal tightness test platform and test method |
| CN111140507A (en) * | 2019-12-05 | 2020-05-12 | 国网河北省电力有限公司电力科学研究院 | Method for measuring air suction amount of water-ring vacuum pump and terminal equipment |
| CN111175450A (en) * | 2020-01-10 | 2020-05-19 | 中铁十四局集团大盾构工程有限公司 | Real-time detection device for harmful gas in excavation bin of large-diameter slurry shield machine |
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2011
- 2011-04-26 CN CN2011201267280U patent/CN202024865U/en not_active Expired - Lifetime
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102252808A (en) * | 2011-04-26 | 2011-11-23 | 山东电力研究院 | Online detecting method and device for air leakage quantity of vacuum system of turbo generator unit |
| CN102494895A (en) * | 2011-11-29 | 2012-06-13 | 河北省电力建设调整试验所 | Analyzing method for energy saving and optimization of steam turbine set of power station |
| CN102494895B (en) * | 2011-11-29 | 2014-12-10 | 河北省电力建设调整试验所 | Analyzing method for energy saving and optimization of steam turbine set of power station |
| CN104296942A (en) * | 2014-09-05 | 2015-01-21 | 西安亨特电力科技有限公司 | Leak detection processing method for vacuum system of thermal generating unit |
| CN104296942B (en) * | 2014-09-05 | 2015-11-11 | 西安亨特电力科技有限公司 | A kind of thermal power generation unit vacuum system Leak Detection disposal route |
| CN105241667A (en) * | 2015-10-23 | 2016-01-13 | 上海电力学院 | Condenser vacuum state identification method based on k-M model |
| CN108061624A (en) * | 2017-11-21 | 2018-05-22 | 四川成发普睿玛机械工业制造有限责任公司 | The air mass flow of aerial motor spare part and seal tightness test platform and test method |
| CN108061624B (en) * | 2017-11-21 | 2019-08-02 | 四川成发普睿玛机械工业制造有限责任公司 | The air mass flow and seal tightness test platform and test method of aerial motor spare part |
| CN111140507A (en) * | 2019-12-05 | 2020-05-12 | 国网河北省电力有限公司电力科学研究院 | Method for measuring air suction amount of water-ring vacuum pump and terminal equipment |
| CN111175450A (en) * | 2020-01-10 | 2020-05-19 | 中铁十四局集团大盾构工程有限公司 | Real-time detection device for harmful gas in excavation bin of large-diameter slurry shield machine |
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Owner name: STATE ELECTRIC NET CROP. Effective date: 20130326 |
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Effective date of registration: 20130326 Address after: 250002 Ji'nan City Central District, Shandong, No. 2 South Road, No. 500 Patentee after: Shandong Research Inst. of Electric Power Patentee after: State Grid Corporation of China Address before: 250002 Ji'nan City Central District, Shandong, No. 2 South Road, No. 500 Patentee before: Shandong Research Inst. of Electric Power |
|
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Address after: 250003 No. 2000, Wang Yue Road, Shizhong District, Ji'nan, Shandong Patentee after: Shandong Electric Power Research Institute Patentee after: State Grid Corporation of China Address before: 250002, No. 500, South Second Ring Road, Shizhong District, Shandong, Ji'nan Patentee before: Shandong Electric Power Research Institute Patentee before: State Grid Corporation of China |
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| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20111102 |