CN107062192B - Deaerator bay - Google Patents
Deaerator bay Download PDFInfo
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- CN107062192B CN107062192B CN201710262172.XA CN201710262172A CN107062192B CN 107062192 B CN107062192 B CN 107062192B CN 201710262172 A CN201710262172 A CN 201710262172A CN 107062192 B CN107062192 B CN 107062192B
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22D—PREHEATING, OR ACCUMULATING PREHEATED, FEED-WATER FOR STEAM GENERATION; FEED-WATER SUPPLY FOR STEAM GENERATION; CONTROLLING WATER LEVEL FOR STEAM GENERATION; AUXILIARY DEVICES FOR PROMOTING WATER CIRCULATION WITHIN STEAM BOILERS
- F22D1/00—Feed-water heaters, i.e. economisers or like preheaters
- F22D1/32—Feed-water heaters, i.e. economisers or like preheaters arranged to be heated by steam, e.g. bled from turbines
- F22D1/325—Schematic arrangements or control devices therefor
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22D—PREHEATING, OR ACCUMULATING PREHEATED, FEED-WATER FOR STEAM GENERATION; FEED-WATER SUPPLY FOR STEAM GENERATION; CONTROLLING WATER LEVEL FOR STEAM GENERATION; AUXILIARY DEVICES FOR PROMOTING WATER CIRCULATION WITHIN STEAM BOILERS
- F22D1/00—Feed-water heaters, i.e. economisers or like preheaters
- F22D1/50—Feed-water heaters, i.e. economisers or like preheaters incorporating thermal de-aeration of feed-water
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- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Control Of Steam Boilers And Waste-Gas Boilers (AREA)
- Separation By Low-Temperature Treatments (AREA)
Abstract
The present invention relates to a kind of deaerator bays.The deaerator bay is for arranging heat regenerative system, the heat regenerative system, including No.1 high-pressure heater, No. two high-pressure heaters, No. three high-pressure heaters, No. four high-pressure heaters, oxygen-eliminating device, No. six low-pressure heaters, No. seven low-pressure heaters, No. eight low-pressure heaters, No. nine low-pressure heaters, No. ten low-pressure heaters, condenser, condensate pump, drainage pump, feed pump, the first externally arranged steam cooler and the second externally arranged steam cooler, poor, blocked drain caused by reducing because of difference between grade between reduction grade.Deaerator bay is from top to bottom disposed with except oxygen layer, interlayer, operating layer, middle layer and zero meter of layer, No. eight low-pressure heaters are arranged in middle layer, No. seven low-pressure heaters setting is in operating floor, No. six low-pressure heaters setting is in interlayer or operating floor, widen the vertical drop between low-pressure heater, low plus hydrophobic is unsmooth when can overcome the problems, such as underload completely using difference in height, reduces hydrophobic heat loss, increases generated energy.
Description
Technical field
The present invention relates to technical field of power generation, disclose a kind of deaerator bay for arranging heat regenerative system.
Background technique
The major parameter for influencing water supply backheat heating economics is backheat heating distribution, corresponding optimum feed temperature and returns
Thermal level number.Power industry such as generally uses at the temperature rises method, rises the enthalpy of every primary heater equal.Traditional heat regenerative system steam extraction
Temperature is very big, and corresponding bleeder heater heat transfer temperature difference increases, and irreversible loss caused by the temperature difference exchanges heat increases, and UTILIZATION OF VESIDUAL HEAT IN
Rate is lower.
Traditional deaerator bay is often chronically at low load condition when reducing using hourage.When encountering underload, such as
Under 30%HTA operating condition, it may appear that the pressure difference between low-pressure heater is inadequate, and often the water column pressure difference of 5m does not all have, normal to dredge
Water often blocked drain.Power plant will open emergent drain to condenser, recyclable hydrophobic heat be wasted, when causing underload
Heat consumption increases, and reduces unit economy.By primary Calculation, the hydrophobic of every 1t/h is not recycled, and heat consumption increases 0.25KJ/kw.h,
Annual coal consumption increases, and annual gene-ration revenue is reduced.
Summary of the invention
The present invention provides when can overcome the problems, such as underload using difference in height that low plus hydrophobic is unsmooth, reduces hydrophobic heat waste
It loses, reduces coal consumption, increase the deaerator bay of generated energy.
Deaerator bay, for arranging heat regenerative system, the heat regenerative system, including No.1 high-pressure heater, No. two hyperbaric heatings
Device, No. three high-pressure heaters, No. four high-pressure heaters, oxygen-eliminating device, No. six low-pressure heaters, No. seven low-pressure heaters, No. eight it is low
Press heater, No. nine low-pressure heaters, No. ten low-pressure heaters, condenser, condensate pump, drainage pump, feed pump, first external
Formula steam condenser and the second externally arranged steam cooler；
The No.1 high-pressure heater, No. two high-pressure heaters, No. three high-pressure heaters, No. four high-pressure heaters, deoxygenations
Device, No. six low-pressure heaters, No. seven low-pressure heaters, No. eight low-pressure heaters, No. nine low-pressure heaters, No. ten low-pressure heaters
Interior pressure successively reduces and is used to connect with extract system；The condenser, condensate pump, No. ten low-pressure heaters, nine
Number low-pressure heater, No. eight low-pressure heaters, No. seven low-pressure heaters, No. six low-pressure heaters, oxygen-eliminating devices are in turn connected to form
Condensate system；The oxygen-eliminating device, feed pump, No. four high-pressure heaters, No. three high-pressure heaters, No. two high-pressure heaters and one
Number high-pressure heater is in turn connected to form water supply system, the drainage pump both ends hydrophobic cooling with No. eight low-pressure heaters respectively
Section is connected with No. seven low-pressure heaters；First externally arranged steam cooler is connect with No. three high-pressure heaters, and described second
Externally arranged steam cooler is connect with No. four high-pressure heaters；
Deaerator bay is from top to bottom disposed with except oxygen layer, interlayer, operating layer, middle layer and zero meter of layer, and described No. eight low
Press heater setting in middle layer, No. seven low-pressure heaters setting exists in operating floor, No. six low-pressure heaters setting
Interlayer or operating layer；In except oxygen layer, second external steams for first externally arranged steam cooler and oxygen-eliminating device setting
Vapour cooler and the setting of No.1 high-pressure heater are in interlayer, and No. four high-pressure heaters setting is in operating floor, No. three height
Press heater setting in interlayer or operating layer, No. two high-pressure heaters, No. nine low-pressure heaters, No. ten low-pressure heaters are set
It sets in middle layer, the drainage pump is arranged in zero meter of layer.
No. six low-pressure heaters, No. seven low-pressure heaters and No. eight low-pressure heaters are arranged in different marks above-mentioned deaerator bay
Height widens the vertical drop between low-pressure heater, and low plus hydrophobic is unsmooth when can overcome underload completely using difference in height
The problem of, hydrophobic heat loss is reduced, coal consumption is reduced, increases generated energy.By the way that each heater is separately positioned on each of deaerator bay
Layer can be good at the space using deaerator bay, avoid using excessive space in use process；First external steam is cold
But device, the second externally arranged steam cooler are separately positioned on above No. three high-pressure heaters and No. four high-pressure heaters, convenient for making
With；No. three high-pressure heaters can be arranged in interlayer or operating floor according to space size, meet different space requirements.Above-mentioned time
Hot systems, level Four high-pressure heater, level-one oxygen-eliminating device, Pyatyi low-pressure heater with the use of increasing high-pressure heater and low
The use for pressing heater, can reduce stage head, reduce because stage head not enough due to caused by blocked drain, while reduce because
Crisis situations are directly hydrophobic to condenser, efficiently use hydrophobic heat, improve economy；Drainage pump both ends respectively with No. eight low pressure
The hydrophobic cooling section of heater and No. seven low-pressure heater connections, can be hydrophobic by the water of No. eight hydrophobic cooling sections of low-pressure heater
To No. seven low-pressure heaters, the water in No. eight hydrophobic cooling sections of low-pressure heater can be recycled, improve the use effect of heat
Rate；Steam superheat is big in use for No. three high-pressure heaters and No. four high-pressure heaters simultaneously, by being arranged outside first
It sets formula steam condenser and the second externally arranged steam cooler makes full use of steam superheat, irreversible heat exchange damage can be reduced
It loses, while feed temperature can be improved to a certain degree under various load conditions, reduce heat consumption.
The hydrophobic cooling section of No. six low-pressure heaters and No. seven low-pressure heaters connect in one of the embodiments,
It connects, the hydrophobic cooling section of No. seven low-pressure heaters is connect with No. eight low-pressure heaters.No. six low-pressure heaters, No. seven low pressure
Heater, No. eight low-pressure heaters are successively hydrophobic, and the water in No. eight hydrophobic cooling sections of low-pressure heater is hydrophobic by drainage pump
To No. seven low-pressure heaters, pass through this connection type, No. six low-pressure heaters, No. seven low-pressure heaters and No. eight low-pressure heaters
Circulation is formed, it, can be by the heat in water by this circulation since the water temperature in No. eight hydrophobic cooling sections of low-pressure heating is higher
It makes full use of, avoids the heat waste in hydrophobic process.
The hydrophobic cooling section of No. nine low-pressure heaters and No. ten low-pressure heaters connect in one of the embodiments,
It connects, the hydrophobic cooling section of described No. ten low-pressure heaters is connect with condenser.No. nine low-pressure heaters, No. ten low-pressure heaters according to
Secondary hydrophobic to condenser, water is delivered to No. ten heaters by condensate pump by condenser again, can be very well using in water
Heat, while water being made full use of, reduce the dosage of water.
The hydrophobic cooling section of the No.1 high-pressure heater and No. two high-pressure heaters connect in one of the embodiments,
It connects, the hydrophobic cooling section of No. two high-pressure heaters is connect with No. three high-pressure heaters, and No. three high-pressure heaters are dredged
Water cooling section is connect with No. four high-pressure heaters, and the hydrophobic cooling section of No. four high-pressure heaters is connect with oxygen-eliminating device.No.1
High-pressure heater, No. two high-pressure heaters, No. three high-pressure heaters, No. four high-pressure heaters and oxygen-eliminating device are successively hydrophobic, finally
Hydrophobic water in oxygen-eliminating device is delivered to No. four high-pressure heaters by feed pump to oxygen-eliminating device, forms circulation, in this manner
Heat in water can be made full use of, while reduce the dosage of water.
The high-pressure heater is single-row horizontal high pressure heater in one of the embodiments,.Single-row horizontal high-pressure adds
Hot device has the advantages that structure is simple, connection and reasonable arrangement, repair and maintenance are convenient and hydrophobic capacious, solves along setting standing heater
Heat-transfer pipe internal water accumulation can not be discharged and core pulling inconvenience；The inversion hydrophobic volume of standing heater is smaller, and water level control is more difficult
Problem.
The larynx of condenser is arranged in No. nine low-pressure heaters and No. ten low-pressure heaters in one of the embodiments,
Portion.Condenser throat, which is arranged in, in No. nine low-pressure heaters and No. ten low-pressure heaters can reduce the resistance damage of extraction line
It loses, saves space, reduce installation difficulty.
In one of the embodiments, the No.1 high-pressure heater respectively with the first externally arranged steam cooler and second
Externally arranged steam cooler connection, first externally arranged steam cooler, the second externally arranged steam cooler is used for and boiler
Economizer connection, the No.1 high-pressure heater with boiler economizer for connecting.Heat regenerative system disclosed by the invention is last
Two externally arranged steam coolers are set before two-stage high-pressure heater, by utilizing No. three high-pressure heaters and No. four high pressures
The degree of superheat of heater improves final feed temperature, and whole cycle efficieny can be made to improve.
The condenser lower end is arranged in zero meter of layer in one of the embodiments, and the throat of the condenser extends to
The throat of condenser is arranged in middle layer, No. nine low-pressure heaters and No. ten low-pressure heaters.By the way that No. nine low pressure are added
The throat that condenser is arranged in hot device and No. ten low-pressure heaters can be good at utilizing space, while condenser, No. nine low pressure
Heater and No. ten low-pressure heaters fit together, easy for installation.
Detailed description of the invention
Fig. 1 is heat regenerative system schematic diagram；
Fig. 2 is condenser cross-sectional view；
Fig. 3 is 1 layout drawing of embodiment of deaerator bay；
Fig. 4 is 2 layout drawing of embodiment of deaerator bay.
The reference numerals are as follows:
1. No.1 high-pressure heater, 2. No. two high-pressure heaters, 3. No. three high-pressure heaters, 4. No. four high-pressure heaters,
5. oxygen-eliminating device, 6. No. six low-pressure heaters, 7. No. seven low-pressure heaters, 8. No. eight low-pressure heaters, 9. No. nine low-pressure heaters,
10. No. ten low-pressure heaters, 11. condensers, 12. condensate pumps, 13. drainage pumps, 14. feed pumps, 15. first external steam
Cooler, 16. second externally arranged steam coolers；
101. oxygen layer is removed, 102. interlayers, 103. operating layers, 104. middle layers, 105. 0 meters of layers.
Specific embodiment
The present invention will be further described in detail in the following with reference to the drawings and specific embodiments.
Referring to Fig.1, a kind of heat regenerative system, including No.1 high-pressure heater 1, two are disclosed in one embodiment of the present of invention
Number high-pressure heater 3, four of high-pressure heater 2, three high-pressure heater 4, the low-pressure heater 6, seven of oxygen-eliminating device 5, six are low
Press the low-pressure heater 8, nine of heater 7, eight low-pressure heater 9, No. ten low-pressure heaters 10, condensers 11, condensate pump
12, drainage pump 13, feed pump 14, the first externally arranged steam cooler 15 and the second externally arranged steam cooler 16；
3, No. four high-pressure heaters 4 of the high-pressure heater of high-pressure heater 2, three of the No.1 high-pressure heater 1, two,
The low-pressure heater 8, nine low-pressure heater 9, ten of low-pressure heater 7, eight of low-pressure heater 6, seven of oxygen-eliminating device 5, six
Pressure in low-pressure heater 10 successively reduces and is used to connect with extract system；
The condenser 11,9, No. eight low-pressure heatings of low-pressure heater of low-pressure heater 10, nine of condensate pump 12, ten
Device 8, seven low-pressure heater 7, six low-pressure heater 6, oxygen-eliminating device 5 are in turn connected to form condensate system；
The oxygen-eliminating device 5,3, No. two high-pressure heaters 2 of high-pressure heater of high-pressure heater 4, three of feed pump 14, four
Be in turn connected to form water supply system with No.1 high-pressure heater 1,13 both ends of drainage pump respectively with No. eight low-pressure heaters 8
Hydrophobic cooling section and No. seven low-pressure heaters 7 connect；
First externally arranged steam cooler 15 is connect with No. three high-pressure heaters 3, and the second external steam is cold
But device 16 is connect with No. four high-pressure heaters 4.
Above-mentioned heat regenerative system, level Four high-pressure heater, level-one oxygen-eliminating device, being used cooperatively for Pyatyi low-pressure heater increase
The use of high-pressure heater and low-pressure heater can reduce stage head, hydrophobic caused by reducing due to stage head is inadequate
It is unsmooth, while reducing because crisis situations are directly hydrophobic to condenser 11, hydrophobic heat is efficiently used, economy is improved；Drainage pump
13 both ends are connect with the hydrophobic cooling section of No. eight low-pressure heaters 8 and No. seven low-pressure heaters 7 respectively, No. eight low pressure can be added
Hydrophobic to No. seven low-pressure heaters 7 of water of the hydrophobic cooling section of hot device 8, can be recycled the hydrophobic cooling of No. eight low-pressure heaters 8
Water in section, improves the service efficiency of heat；While No. three high-pressure heaters 3 and No. four high-pressure heaters 4 are in use
Steam superheat is big, makes full use of steaming by the first externally arranged steam cooler 15 of setting and the second externally arranged steam cooler 16
The vapour degree of superheat can reduce irreversible heat exchange loss, while can improve feed temperature to a certain degree under various load conditions,
Reduce heat consumption.
Referring to Fig.1, optionally, the hydrophobic cooling section of No. six low-pressure heaters 6 is connect with No. seven low-pressure heaters 7,
The hydrophobic cooling section of No. seven low-pressure heaters 7 is connect with No. eight low-pressure heaters 8.6, No. seven low pressure of No. six low-pressure heaters
7, No. eight low-pressure heaters 8 of heater are successively hydrophobic, and the water in No. eight hydrophobic cooling sections of low-pressure heater 8 passes through drainage pump 13
Hydrophobic to No. seven low-pressure heaters 7, by this connection type, 6, No. seven low-pressure heaters 7 of No. six low-pressure heaters and No. eight it is low
Heater 8 is pressed to form circulation, it, can by this circulation since the water temperature in the hydrophobic cooling section of No. eight low-pressure heaters 8 is higher
To make full use of the heat in water, the heat waste in hydrophobic process is avoided.
Referring to Fig.1, optionally, the hydrophobic cooling section of No. nine low-pressure heaters 9 is connect with No. ten low-pressure heaters 10,
The hydrophobic cooling section of described No. ten low-pressure heaters 10 is connect with condenser 11.9, No. ten low-pressure heaters of No. nine low-pressure heaters
10 is successively hydrophobic to condenser 11, and water is delivered to No. ten heaters by condensate pump 12 by condenser 11 again, can be fine
It is made full use of using the heat in water, while by water, reduces the dosage of water.
Referring to Fig.1, optionally, the hydrophobic cooling section of the No.1 high-pressure heater 1 is connect with No. two high-pressure heaters 2,
The hydrophobic cooling section of No. two high-pressure heaters 2 is connect with No. three high-pressure heaters 3, and No. three high-pressure heaters 3 are dredged
Water cooling section is connect with No. four high-pressure heaters 4, and the hydrophobic cooling section of No. four high-pressure heaters 4 is connect with oxygen-eliminating device 5.One
Number 3, No. four high-pressure heaters 4 of the high-pressure heater of high-pressure heater 2, three of high-pressure heater 1, two and oxygen-eliminating device 5 are successively dredged
Water, final hydrophobic to oxygen-eliminating device 5, the water in oxygen-eliminating device 5 is delivered to No. four high-pressure heaters 4 by feed pump 14, forms circulation,
The heat in water can be made full use of in this manner, while reduce the dosage of water.
Referring to Fig.1, optionally, the high-pressure heater is single-row horizontal high pressure heater.Single-row horizontal high pressure heater
Have the advantages that structure is simple, connection and reasonable arrangement, repair and maintenance are convenient and hydrophobic capacious, solves suitable standing heater of setting and conduct heat
Pipe internal water accumulation can not be discharged and core pulling inconvenience；It is smaller to be inverted the hydrophobic volume of standing heater, the more difficult problem of water level control.
Referring to Fig. 2, optionally, condenser 11 is arranged in No. nine low-pressure heaters 9 and No. ten low-pressure heaters 10
Throat.11 throat of condenser, which is arranged in, in No. nine low-pressure heaters 9 and No. ten low-pressure heaters 10 can reduce extraction line
Drag losses save space, reduce installation difficulty.
Referring to Fig.1, optionally, No.1 high-pressure heater 1 is external with the first externally arranged steam cooler 15 and second respectively
Formula steam condenser 16 connects, and first externally arranged steam cooler 15, the second externally arranged steam cooler 16 are used for and pot
The connection of furnace economizer, the No.1 high-pressure heater 1 with boiler economizer for connecting.Heat regenerative system disclosed by the invention is most
Two externally arranged steam coolers are set before two-stage high-pressure heater afterwards, by utilizing No. three high-pressure heaters 3 and No. four
The degree of superheat of high-pressure heater 4 improves final feed temperature, and whole cycle efficieny can be made to improve.
Referring to Fig. 3 and Fig. 4, a kind of deaerator bay is disclosed in one embodiment of the present of invention, for arranging above-mentioned backheat system
System, deaerator bay are from top to bottom disposed with except oxygen layer 101, interlayer 102, operating layer 103, middle layer 104 and zero meter of layer 105,
No. eight low-pressure heaters 8 setting is in middle layer 104, and No. seven low-pressure heaters 7 setting is in operating floor 103, and described six
The setting of number low-pressure heater 6 is in interlayer 102 or operating floor 103.
6, No. seven low-pressure heaters 7 of No. six low-pressure heaters and No. eight low-pressure heaters 8 are arranged not above-mentioned deaerator bay
Same absolute altitude widens the vertical drop between low-pressure heater, low plus hydrophobic when can overcome underload completely using difference in height
Unsmooth problem reduces hydrophobic heat loss, reduces coal consumption, increases generated energy.
Referring to Fig. 3 and Fig. 4, optionally, the first externally arranged steam cooler 15 and the setting of oxygen-eliminating device 5 are being removed in oxygen layer 101,
Second externally arranged steam cooler 16 and No.1 high-pressure heater 1 are arranged in interlayer 102, No. four high-pressure heaters 4
Setting is in operating layer 103, and No. three high-pressure heaters 3 setting is in interlayer 102 or operating floor 103, No. two hyperbaric heatings
The setting of the low-pressure heater 10 of low-pressure heater 9, ten of device 2, nine is arranged in middle layer 104, the drainage pump 13 in zero meter of layer
105.It can be good at the space using deaerator bay by each layer that each heater is separately positioned on deaerator bay, avoid using
Excessive space is used in journey；First externally arranged steam cooler 15, the second externally arranged steam cooler 16 are separately positioned on
No. three high-pressure heaters 3 and No. four 4 tops of high-pressure heater, are easy to use；No. three high-pressure heaters 3 can be according to space size
Setting meets different space requirements in interlayer 102 or operating layer 103.
Referring to Fig. 2, optionally, 11 lower end of the condenser setting extends in zero meter of layer 105, the throat of the condenser 11
To middle layer 104, the throat of condenser 11 is arranged in No. nine low-pressure heaters 9 and No. ten low-pressure heaters 10.Passing through will
The throat that condenser 11 is arranged in No. nine low-pressure heaters 9 and No. ten low-pressure heaters 10 can be good at using space, simultaneously
11, No. nine low-pressure heaters 9 of condenser and No. ten low-pressure heaters 10 fit together, easy for installation.
Each technical characteristic of embodiment described above can be combined arbitrarily, for simplicity of description, not to above-mentioned reality
It applies all possible combination of each technical characteristic in example to be all described, as long as however, the combination of these technical characteristics is not deposited
In contradiction, all should be considered as described in this specification.
The embodiments described above only express several embodiments of the present invention, and the description thereof is more specific and detailed, but simultaneously
It cannot therefore be construed as limiting the scope of the patent.It should be pointed out that coming for those of ordinary skill in the art
It says, without departing from the inventive concept of the premise, various modifications and improvements can be made, these belong to protection of the invention
Range.Therefore, the scope of protection of the patent of the invention shall be subject to the appended claims.
Claims (8)
1. deaerator bay, which is characterized in that for arranging that heat regenerative system, the heat regenerative system include No.1 high-pressure heater, No. two
High-pressure heater, No. three high-pressure heaters, No. four high-pressure heaters, oxygen-eliminating device, No. six low-pressure heaters, No. seven low-pressure heatings
Device, No. eight low-pressure heaters, No. nine low-pressure heaters, No. ten low-pressure heaters, condenser, condensate pump, drainage pump, water supply
Pump, the first externally arranged steam cooler and the second externally arranged steam cooler；
The No.1 high-pressure heater, No. two high-pressure heaters, No. three high-pressure heaters, No. four high-pressure heaters, oxygen-eliminating device, six
Number low-pressure heater, No. seven low-pressure heaters, No. eight low-pressure heaters, No. nine low-pressure heaters, in No. ten low-pressure heaters
Pressure successively reduces and is used to connect with extract system；
The condenser, condensate pump, No. ten low-pressure heaters, No. nine low-pressure heaters, No. eight low-pressure heaters, No. seven low pressure
Heater, No. six low-pressure heaters, oxygen-eliminating devices are in turn connected to form condensate system；
The oxygen-eliminating device, feed pump, No. four high-pressure heaters, No. three high-pressure heaters, No. two high-pressure heaters and No.1 high pressure
Heater is in turn connected to form water supply system, the drainage pump both ends hydrophobic cooling section and seven with No. eight low-pressure heaters respectively
The connection of number low-pressure heater；
First externally arranged steam cooler is connect with No. three high-pressure heaters, second externally arranged steam cooler and four
The connection of number high-pressure heater；
Deaerator bay is from top to bottom disposed with except oxygen layer, interlayer, operating layer, middle layer and zero meter of layer, No. eight low pressure add
Hot device setting is in middle layer, and in operating floor, No. six low-pressure heaters are arranged in interlayer for No. seven low-pressure heaters setting
Or operating layer, in except oxygen layer, the second external steam is cold for first externally arranged steam cooler and oxygen-eliminating device setting
But device and the setting of No.1 high-pressure heater are in interlayer, and in operating floor, No. three high pressures add for No. four high-pressure heaters setting
Hot device setting exists in interlayer or operating layer, No. two high-pressure heaters, No. nine low-pressure heaters, No. ten low-pressure heater settings
Middle layer, the drainage pump are arranged in zero meter of layer.
2. deaerator bay according to claim 1, which is characterized in that the hydrophobic cooling section and seven of No. six low-pressure heaters
The connection of number low-pressure heater, the hydrophobic cooling section of No. seven low-pressure heaters are connect with No. eight low-pressure heaters.
3. deaerator bay according to claim 2, which is characterized in that the hydrophobic cooling section and ten of No. nine low-pressure heaters
The connection of number low-pressure heater, the hydrophobic cooling section of described No. ten low-pressure heaters are connect with condenser.
4. deaerator bay according to claim 1, which is characterized in that the hydrophobic cooling section and two of the No.1 high-pressure heater
The connection of number high-pressure heater, the hydrophobic cooling section of No. two high-pressure heaters are connect with No. three high-pressure heaters, and described No. three
The hydrophobic cooling section of high-pressure heater is connect with No. four high-pressure heaters, the hydrophobic cooling section of No. four high-pressure heaters with remove
The connection of oxygen device.
5. deaerator bay according to claim 1, which is characterized in that the high-pressure heater is the heating of single-row horizontal high-pressure
Device.
6. deaerator bay according to claim 1, which is characterized in that No. nine low-pressure heaters and No. ten low-pressure heaters
The throat of condenser is set.
7. deaerator bay according to claim 1, which is characterized in that the No.1 high-pressure heater respectively with the first external
Steam condenser and the connection of the second externally arranged steam cooler, first externally arranged steam cooler, the second external steam
Cooler with boiler economizer for connecting, and the No.1 high-pressure heater with boiler economizer for connecting.
8. deaerator bay according to claim 1, which is characterized in that condenser lower end setting is described solidifying in zero meter of layer
The throat of vapour device extends to middle layer, and the throat of condenser is arranged in No. nine low-pressure heaters and No. ten low-pressure heaters.
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| CN201710262172.XA CN107062192B (en) | 2017-04-20 | 2017-04-20 | Deaerator bay |
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| CN201710262172.XA CN107062192B (en) | 2017-04-20 | 2017-04-20 | Deaerator bay |
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| CN107062192B true CN107062192B (en) | 2019-03-12 |
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| CN108167806B (en) * | 2017-12-26 | 2019-08-09 | 中国能源建设集团江苏省电力设计院有限公司 | Million unit high-pressure heater system structure of double reheat and its application method |
| CN108533012B (en) * | 2018-05-24 | 2023-11-14 | 中国电力工程顾问集团西北电力设计院有限公司 | Lateral arrangement structure of 660 MW-level unit steam turbine generator unit of thermal power plant |
| CN112594919B (en) * | 2020-12-16 | 2022-05-03 | 安庆船用电器有限责任公司 | Vertical explosion-proof type marine heater convenient to installation |
| CN113107621A (en) * | 2021-05-28 | 2021-07-13 | 西安热工研究院有限公司 | 650 ℃ high-efficiency supercritical (super-supercritical) coal-fired power generation system |
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| JPH0267402A (en) * | 1988-09-02 | 1990-03-07 | Toshiba Corp | Turbine building |
| JP3628201B2 (en) * | 1999-01-28 | 2005-03-09 | 株式会社日立製作所 | Thermal power plant |
| CN101270675A (en) * | 2008-04-24 | 2008-09-24 | 华北电力大学 | Solar energy and coal-burning unit combined thermal power generation system |
| CN102352696B (en) * | 2011-06-23 | 2013-09-18 | 中国电力工程顾问集团西北电力设计院 | Lateral structure and arranging method of steam turbine generator unit of 1000MW-grade set in thermal power plant |
| CN203478195U (en) * | 2013-10-11 | 2014-03-12 | 山东电力工程咨询院有限公司 | External parallel-connection type steam cooler in fed water heating system of thermal power plant |
| CN204663057U (en) * | 2015-04-30 | 2015-09-23 | 中国能源建设集团广东省电力设计研究院有限公司 | Steam power station main building arrangement structure |
| CN205857838U (en) * | 2016-08-04 | 2017-01-04 | 中国电力工程顾问集团西北电力设计院有限公司 | Thermal power plant heater island arrangement |
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