CN208222484U - A kind of pair is dragged electric pump back pressure turbine comprehensive utilization device - Google Patents
A kind of pair is dragged electric pump back pressure turbine comprehensive utilization device Download PDFInfo
- Publication number
- CN208222484U CN208222484U CN201820480873.0U CN201820480873U CN208222484U CN 208222484 U CN208222484 U CN 208222484U CN 201820480873 U CN201820480873 U CN 201820480873U CN 208222484 U CN208222484 U CN 208222484U
- Authority
- CN
- China
- Prior art keywords
- low
- back pressure
- gas
- air
- pressure turbine
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 239000007789 gas Substances 0.000 claims abstract description 79
- 230000003009 desulfurizing effect Effects 0.000 claims abstract description 23
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 56
- 238000010612 desalination reaction Methods 0.000 claims description 39
- 230000008676 import Effects 0.000 claims description 18
- 238000010248 power generation Methods 0.000 claims description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims 1
- 239000001301 oxygen Substances 0.000 claims 1
- 229910052760 oxygen Inorganic materials 0.000 claims 1
- 230000007797 corrosion Effects 0.000 abstract description 10
- 238000005260 corrosion Methods 0.000 abstract description 10
- 230000002209 hydrophobic effect Effects 0.000 abstract description 6
- 239000003517 fume Substances 0.000 abstract description 5
- 238000010438 heat treatment Methods 0.000 description 10
- 239000003245 coal Substances 0.000 description 9
- 239000000779 smoke Substances 0.000 description 6
- 230000007812 deficiency Effects 0.000 description 5
- 239000000428 dust Substances 0.000 description 5
- 239000000463 material Substances 0.000 description 5
- 239000004810 polytetrafluoroethylene Substances 0.000 description 5
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 5
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 4
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- 238000005265 energy consumption Methods 0.000 description 4
- 239000003546 flue gas Substances 0.000 description 4
- 230000005611 electricity Effects 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 230000001105 regulatory effect Effects 0.000 description 3
- 238000013475 authorization Methods 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000006392 deoxygenation reaction Methods 0.000 description 2
- 238000006477 desulfuration reaction Methods 0.000 description 2
- 230000023556 desulfurization Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000004134 energy conservation Methods 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 239000003595 mist Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 238000010025 steaming Methods 0.000 description 2
- 238000013517 stratification Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000003628 erosive effect Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
Classifications
-
- 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
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
Landscapes
- Engine Equipment That Uses Special Cycles (AREA)
Abstract
The utility model discloses a kind of pair to drag electric pump back pressure turbine comprehensive utilization device, including feed pump, back pressure turbine, timing gear roller box, generator, warm pocket, pressure fan, air preheater, boiler, bag filter, air-introduced machine, low low-level (stack-gas) economizer, oxygen-eliminating device, desulfurizing tower, chimney.The utility model is structurally reasonable, using back pressure turbine steam discharge as warm pocket gas source, solves the problems, such as the stifled ash of boiler air preheater low-temperature corrosion, and the use of low low-level (stack-gas) economizer solves the problems, such as warm empty bring high fume temperature, warm pocket is hydrophobic is again introduced into boiler system further through low low-level (stack-gas) economizer, substantially increases generatine set heat efficiency and resource utilization.
Description
Technical field
The utility model relates to cogeneration units high efficient energy sources to utilize, energy-conserving and emission-cutting technology field, and in particular to a kind of
It is double to drag electric pump back pressure turbine comprehensive utilization device.
Background technique
Coal fired thermal power plant is the main enterprises of China's power generation, has 78% electricity from Coal-fired Thermal Power in national electricity consumption
Factory.AND ENERGY RESOURCES CONSUMPTION IN CHINA will exploit the non-renewable energy of nearly 2,000,000,000 tons of standard coals based on coal every year, convert into RMB about 1
The industrial output value of trillion yuan, wherein nearly half is burnt up by power plant boiler.Therefore, coal-burning power plant advocates section comprehensively at this stage
It can be transformed, coal consumption for power generation is greatly reduced and improve energy utilization rate, energy-saving and emission-reduction reach power industry with this and clean, efficiently
Change development.
Power plant watering cycle can use feed pump, and power plant generally uses Steam Turbine Driven feed pump, i.e. steam turbine at present
Axis one end drive feed pump, master be to solve the power-consuming problem of feed pump.For relatively economical performance, more more options
Back pressure turbine is as feed-water pump turbine.But in order to meet unit in summer long period oepration at full load, back pressure turbine
Nominal output it is usually bigger than the nominal output of feed pump, therefore the nominal output of steam turbine has a larger allowance, generally 20% with
On.In addition, the steam exhaust temperature of steam turbine is higher in power station, generally access condenser, but feed pump turbine steam exhaust pressure one
As be higher than condenser pressure, when actual motion, manufactured and designed by feed pump turbine and mounting process level limited, especially given
When water pump operation performance is poor, this difference is bigger, on the one hand causes wasting for feed pump turbine exhaust steam residual heat, another
Aspect also makes condenser duty higher, influences unit vacuum, and unit net coal consumption rate increases.More than this sub-load allowance and steam exhaust
Heat cannot such as make full use of, and will lead to equipment and energy utilization rate is low, deficiency in economic performance.Therefore, how this portion of recycling and reusing
Divide load margin and exhaust steam residual heat, is that those skilled in the art need urgently to solve the problems, such as.
As Chinese patent Authorization Notice No. CN204002945U discloses a kind of feed pump small turbine Driven by Coaxial power generation
Device.Described device includes: feed pump, small turbine, constant rotational speed output gear case and generator；The feed pump and described
Small turbine is connected；The input terminal of the constant rotational speed output gear case is connected with the small turbine；The generator
Connect the output end of the constant rotational speed output gear case.The feed pump small turbine Driven by Coaxial power generator, can be realized
Effective use to the small turbine extra margin (load) can effectively avoid driving the process of feed pump in small turbine
In caused by load waste the problem of.Shortcoming is that the exhaust steam residual heat of steam turbine is not utilized effectively.
For another example Chinese patent Authorization Notice No. CN206160094U discloses a kind of feed pump turbine exhaust steam residual heat utilization
System, including steam jet ejector, intermediate pressure cylinder, low-pressure heater and forward type heat exchangers for district heating, the steam jet pressure
The first entrance of contracting device is connected with feed pump turbine, the second entrance of the steam jet ejector and the row of medium pressure cylinder
Vapour end is connected, and another exhaust steam end of medium pressure cylinder is connected with heat exchangers for district heating shell-side, the outlet of the steam jet ejector
It is connected with the shell-side of forward type heat exchangers for district heating, the outlet of the steam jet ejector is also connected with low-pressure heater, described
Steam jet ejector aspirates the steam exhaust of feed pump turbine using the part steam discharge steam extraction of intermediate pressure cylinder as driving vapour source, will
The relatively high intermediate pressure cylinder steam discharge of temperature, pressure carries out temperature, pressure with the relatively low feed pump turbine steam exhaust of temperature, pressure
Power matching, and the steam after matching is used for low-pressure heater and forward type heat exchangers for district heating.Shortcoming is exhaust steam residual heat
Utilization rate is not high, and the load margin of steam turbine is not utilized effectively.
In addition, boiler air preheater enters the combustion air in furnace using the smoke discharging residual heat preheating of boiler, it can not only
Improve the thermal efficiency of boiler, moreover it is possible to mitigate the pollution to environment.SO is generated after sulphur content burning in fuel2And SO3, and and flue gas
In steam interaction, generate sulfuric acid vapor.When heated surface at the end of boiler wall temperature is lower than flue gas acid dew point, just moisture condensation cohesion
In on the wall surface, since liquid sulfuric acid corrosivity is strong, the metal erosion of low temperature heating surface, frequently referred to boiler low-temperature heating surface are caused
Corrosion.Boiler is easiest to along the final stage air preheater of flue gas flow direction by low-temperature corrosion.While low-temperature corrosion occurs,
Incident is exactly the dust stratification of air preheater, they mutually promote, and forms vicious circle, destroys the normal operation of boiler.
The low-temperature corrosion of heated surface at the end of boiler influences station boiler economy and normal work very big, it is necessary to take measures to prevent low
Temperature corrosion and dust stratification.The common approach is that adding warm pocket, being heated using steam, shortcoming is waste vast resources,
Increase energy consumption.
Summary of the invention
The purpose of the utility model is to overcome the deficiencies in the prior art, provide a kind of structurally reasonable, energy utilization rate height, peace
The double of loopful guarantor drag electric pump back pressure turbine comprehensive utilization device.
One kind that in order to achieve the above purposes, the technical solution adopted by the utility model is: is double to drag electric pump back pressure turbine comprehensive
Utilize device, including feed pump, back pressure turbine, timing gear roller box, generator, warm pocket, pressure fan, air preheater, boiler, cloth
Bag dust collector, air-introduced machine, low low-level (stack-gas) economizer, oxygen-eliminating device, desulfurizing tower, chimney, the first output shaft of the back pressure turbine with
The input shaft of the feed pump is connected, the second output shaft and the input shaft phase of the timing gear roller box of the back pressure turbine
Even, the output shaft of the timing gear roller box is connected with the input shaft of the generator, the steam drain of the back pressure turbine and institute
The steam inlet for stating warm pocket is connected, and the water outlet of the warm pocket is connected with the desalination water inlet of the low low-level (stack-gas) economizer,
The desalination water out of the low low-level (stack-gas) economizer is connect with the desalination water inlet of the oxygen-eliminating device, and the demineralized water of the oxygen-eliminating device goes out
Mouth is connected with the desalination water inlet of the feed pump, and the desalination water out of the feed pump and the desalination water inlet of the boiler connect
It connects, the air outlet of the pressure fan is connected with the air inlet of the warm pocket, the air outlet and the air preheater of the warm pocket
Air inlet be connected, the air outlet of the air preheater is connected with the air inlet of the boiler, the exhaust pass of the boiler and institute
The gas inlet connection of air preheater is stated, the exhanst gas outlet of the air preheater is connected with the gas inlet of the bag filter, institute
The exhanst gas outlet for stating bag filter is connected with the import of the air-introduced machine, and the outlet of the air-introduced machine and the low temperature save coal
The gas inlet of device is connected, and the exhanst gas outlet of the low low-level (stack-gas) economizer is connected with the import of the desulfurizing tower, the desulfurizing tower
Outlet connect with the import of the chimney.
As preferred embodiments of the present invention, the back pressure turbine is additionally provided with steam inlet pipe, the steaming
It is provided on vapor inlet pipe into steam control valve, accurately to control steam flow.
As preferred embodiments of the present invention, the low low-level (stack-gas) economizer preferably includes at least one set of U-shaped heat exchange
Pipe.
In order to reduce low-temperature corrosion and equipment attrition, device security is improved, it is described in the utility model U-shaped to change
Heat pipe material is preferably PTFE.
To the resistance of boiler smoke flowing when in order to reduce warm air system maintenance, energy conservation and consumption reduction effects are further increased, are made
For preferred embodiments of the present invention, the warm pocket is preferably that drawable type warms up pocket.
The double of the utility model drag electric pump back pressure turbine comprehensive utilization device, in order to overcome warm pocket to improve boiler smoke
Gas exhaust gas temperature reduces the deficiency of generatine set heat efficiency, and low low-level (stack-gas) economizer, low low temperature are arranged between air-introduced machine and desulfurizing tower
The application of economizer is not only utilized by condensing boiler smoke temperature hydrophobic, and that warm pocket is raised after warm pocket heating air
It significantly reduces, Mist heat recovering, improves desalination coolant-temperature gage, enhance boiler overall utilization rate.The utility model overcomes low
Warm economizer by boiler smoke temperature drop it is low after, the problem of leading to desulfurizing tower disrupted water balance, saves coal so as to avoid low temperature is reduced
Device uses the defect of flow.Pocket is warmed up in the utility model and the cooperation of low low-level (stack-gas) economizer not only solves high fume temperature
Problem also improves the utilization efficiency of low low-level (stack-gas) economizer.The double of the utility model drag electric pump back pressure turbine comprehensive utilization dress
It sets, greatly reduces energy loss, improve equipment and energy utilization rate, increase economic benefit.
Double actings for dragging electric pump back pressure turbine comprehensive utilization device that can give full play to back pressure turbine of the utility model
Ability, steam discharge can be used for boiler air preheater and warm pocket gas source, not only improve utilization rate of equipment and installations, but also solve air preheater low temperature
The problem of ash is blocked up in corrosion.
Compared with prior art, the utility model has the advantages that
1, the utility model improves the utilization efficiency of back pressure turbine to greatest extent, not only double using back pressure turbine
Feed pump and generator are dragged, and low using the stifled ash of its steam discharge solution boiler air preheater low-temperature corrosion and winter boiler inlet temperature
The problem of, improve boiler thermal efficiency.
2, the utility model is used using the low low-level (stack-gas) economizer of warm pocket collocation, is not only utilized empty by warm pocket heating
What is condensed after gas is hydrophobic, and the boiler smoke temperature that warm pocket is raised significantly reduces, and Mist heat recovering improves desalination coolant-temperature gage,
Enhance boiler overall utilization rate.
3, PTFE can be used in the U heat exchange material of low low-level (stack-gas) economizer used in the utility model, reduces low temperature
Corrosion and equipment attrition, improve device security.
4, the utility model overcome the prior art warm up pocket because it is hydrophobic into oxygen-eliminating device due to add the equipment such as drainage pump
Deficiency, at the same also overcome because drain tank be reduce hydrophobic pump intake cavitation phenomenons also to keep certain height generate pressure
Head, and drainage pump progress frequent start-stop is caused to control the high failure rate of cumbersome and drainage pump for the limit of drain tank height
The low low-level (stack-gas) economizer of the hydrophobic entrance of warm pocket is saved the equipment such as drainage pump, has saved energy consumption, improved by deficiency, the utility model
Security reliability.
5, the utility model warms up pocket using drawable type, and when warm air system maintenance, drawable type warms up pocket and can reduce to pot
Kiln gas flow resistance has obvious energy conservation and consumption reduction effects.
Detailed description of the invention
Fig. 1 is double flow diagrams for dragging electric pump back pressure turbine comprehensive utilization device of the utility model.
In figure, feed pump 1, back pressure turbine 2, timing gear roller box 3, generator 4, warm pocket 5, air preheater 6, boiler 7, cloth
Bag dust collector 8, air-introduced machine 9, low low-level (stack-gas) economizer 10, desulfurizing tower 11, chimney 12, pressure fan 13, oxygen-eliminating device 14, into steam control valve
15。
Specific embodiment
As shown in Figure 1, the double of the utility model drag electric pump back pressure turbine comprehensive utilization device, including feed pump 1, back pressure
Steam turbine 2, timing gear roller box 3, generator 4, warm pocket 5, pressure fan 13, air preheater 6, boiler 7, bag filter 8, air-introduced machine
9, low low-level (stack-gas) economizer 10, oxygen-eliminating device 14, desulfurizing tower 11, chimney 12, the first output shaft and the feed pump 1 of back pressure turbine 2
Input shaft is connected, and the second output shaft of back pressure turbine 2 is connected with the input shaft of timing gear roller box 3, the output of timing gear roller box 3
Axis is connected with the input shaft of generator 4, and the steam drain of back pressure turbine 2 is connected with the steam inlet of warm pocket 5, warms up pocket 5
Water outlet is connected with the desalination water inlet of low low-level (stack-gas) economizer 10, desalination water out and the oxygen-eliminating device 14 of low low-level (stack-gas) economizer 10
The connection of desalination water inlet, the desalination water out of oxygen-eliminating device 14 are connected with the desalination water inlet of feed pump 2, the demineralized water of feed pump 2
Outlet is connect with the desalination water inlet of boiler 7, and the air outlet of pressure fan 13 is connected with the air inlet of warm pocket 5, warms up going out for pocket 5
Air port is connected with the air inlet of air preheater 6, and the air outlet of air preheater 6 is connected with the air inlet of boiler 7, the exhaust pass of boiler 7
It is connect with the gas inlet of air preheater 6, the exhanst gas outlet of air preheater 6 is connected with the gas inlet of bag filter 8, bag-type dust
The exhanst gas outlet of device 8 is connected with the import of air-introduced machine 9, and the outlet of air-introduced machine 9 is connected with the gas inlet of low low-level (stack-gas) economizer 10,
The exhanst gas outlet of low low-level (stack-gas) economizer 10 is connected with the import of desulfurizing tower 11, and the outlet of desulfurizing tower 11 and the import of chimney 12 connect
It connects.Back pressure turbine 2 is additionally provided with steam inlet pipe, is provided on steam inlet pipe into steam control valve 15, with accurate control steaming
Steam flow amount.
The double of the utility model drag electric pump back pressure turbine comprehensive utilization device workflow are as follows: are discharged from main steam turbine
Low-pressure steam is done work by entering back pressure turbine 2 after adjusting flow into steam control valve 15, and back pressure turbine 2 drives water supply on one side
Pump 1, while driving generator 4 to generate electricity by timing gear roller box 3, the steam exhaust being discharged from back pressure turbine 2 enters warm pocket 5, with
Condense into demineralized water after the heat exchange of the cold air of pressure fan 13 into low low-level (stack-gas) economizer 10, in low low-level (stack-gas) economizer 10 with
Enter 14 deoxygenation of oxygen-eliminating device after the heat exchange heating of the hot fume of air-introduced machine 9, the demineralized water after deoxygenation pressurizes laggard through feed pump 1
Enter the water supply system of boiler 7.Enter air preheater 6 after heat exchange heating in warm pocket 5 from the cold air of pressure fan 13, in sky
Enter boiler 7 in pre- device 6 after hot fume further increases temperature and participates in burning.The hot fume that boiler 7 is discharged after burning is successively
Through the cooling of air preheater 6, after 8 dedusting of bag filter, enter under the traction of air-introduced machine 9 low low-level (stack-gas) economizer 10 with from warm pocket
Enter 11 desulfurization of desulfurizing tower after 5 condensed water heat exchange cooling, the flue gas after desulfurization is through 12 qualified discharge of chimney.
Below in conjunction with drawings and the specific embodiments, the utility model is described in further detail.But the utility model
It is not limited in the embodiment described.
Embodiment 1
A kind of pair is dragged electric pump back pressure turbine comprehensive utilization device, including feed pump 1, back pressure turbine 2, timing gear roller box
3, generator 4, warm pocket 5 (drawable type), pressure fan 13, air preheater 6, boiler 7, bag filter 8, air-introduced machine 9, low temperature save
Coal device 10 (U heat exchange for being PTFE including one group of material), oxygen-eliminating device 14, desulfurizing tower 11, chimney 12, back pressure turbine 2
First output shaft is connected with the input shaft of feed pump 1, the second output shaft of back pressure turbine 2 and the input shaft of timing gear roller box 3
It is connected, the output shaft of timing gear roller box 3 is connected with the input shaft of generator 4, the steam drain of back pressure turbine 2 and warm pocket 5
Steam inlet is connected, and the water outlet of warm pocket 5 is connected with the desalination water inlet of low low-level (stack-gas) economizer 10, low low-level (stack-gas) economizer 10
Desalination water out is connect with the desalination water inlet of oxygen-eliminating device 14, the demineralized water of the desalination water out of oxygen-eliminating device 14 and feed pump 2 into
Mouth is connected, and the desalination water out of feed pump 2 is connect with the desalination water inlet of boiler 7, the air outlet of pressure fan 13 and warm pocket 5
Air inlet is connected, and the air outlet of warm pocket 5 is connected with the air inlet of air preheater 6, the air outlet of air preheater 6 and the air inlet of boiler 7
Mouth is connected, and the exhaust pass of boiler 7 is connect with the gas inlet of air preheater 6, the exhanst gas outlet and bag filter 8 of air preheater 6
Gas inlet be connected, the exhanst gas outlet of bag filter 8 is connected with the import of air-introduced machine 9, the outlet of air-introduced machine 9 and low temperature
The gas inlet of economizer 10 is connected, and the exhanst gas outlet of low low-level (stack-gas) economizer 10 is connected with the import of desulfurizing tower 11, desulfurizing tower 11
Outlet connect with the import of chimney 12.Back pressure turbine 2 is additionally provided with steam inlet pipe, is provided on steam inlet pipe into vapour
Regulating valve 15, accurately to control steam flow.
Embodiment 2
A kind of pair is dragged electric pump back pressure turbine comprehensive utilization device, including feed pump 1, back pressure turbine 2, timing gear roller box
3, generator 4, warm pocket 5 (drawable type), pressure fan 13, air preheater 6, boiler 7, bag filter 8, air-introduced machine 9, low temperature save
Coal device 10 (U heat exchange for being PTFE including three groups of materials), oxygen-eliminating device 14, desulfurizing tower 11, chimney 12, back pressure turbine 2
First output shaft is connected with the input shaft of feed pump 1, the second output shaft of back pressure turbine 2 and the input shaft of timing gear roller box 3
It is connected, the output shaft of timing gear roller box 3 is connected with the input shaft of generator 4, the steam drain of back pressure turbine 2 and warm pocket 5
Steam inlet is connected, and the water outlet of warm pocket 5 is connected with the desalination water inlet of low low-level (stack-gas) economizer 10, low low-level (stack-gas) economizer 10
Desalination water out is connect with the desalination water inlet of oxygen-eliminating device 14, the demineralized water of the desalination water out of oxygen-eliminating device 14 and feed pump 2 into
Mouth is connected, and the desalination water out of feed pump 2 is connect with the desalination water inlet of boiler 7, the air outlet of pressure fan 13 and warm pocket 5
Air inlet is connected, and the air outlet of warm pocket 5 is connected with the air inlet of air preheater 6, the air outlet of air preheater 6 and the air inlet of boiler 7
Mouth is connected, and the exhaust pass of boiler 7 is connect with the gas inlet of air preheater 6, the exhanst gas outlet and bag filter 8 of air preheater 6
Gas inlet be connected, the exhanst gas outlet of bag filter 8 is connected with the import of air-introduced machine 9, the outlet of air-introduced machine 9 and low temperature
The gas inlet of economizer 10 is connected, and the exhanst gas outlet of low low-level (stack-gas) economizer 10 is connected with the import of desulfurizing tower 11, desulfurizing tower 11
Outlet connect with the import of chimney 12.Back pressure turbine 2 is additionally provided with steam inlet pipe, is provided on steam inlet pipe into vapour
Regulating valve 15, accurately to control steam flow.
Embodiment 3
A kind of pair is dragged electric pump back pressure turbine comprehensive utilization device, including feed pump 1, back pressure turbine 2, timing gear roller box
3, generator 4, warm pocket 5 (drawable type), pressure fan 13, air preheater 6, boiler 7, bag filter 8, air-introduced machine 9, low temperature save
Coal device 10 (U heat exchange for being PTFE including five groups of materials), oxygen-eliminating device 14, desulfurizing tower 11, chimney 12, back pressure turbine 2
First output shaft is connected with the input shaft of feed pump 1, the second output shaft of back pressure turbine 2 and the input shaft of timing gear roller box 3
It is connected, the output shaft of timing gear roller box 3 is connected with the input shaft of generator 4, the steam drain of back pressure turbine 2 and warm pocket 5
Steam inlet is connected, and the water outlet of warm pocket 5 is connected with the desalination water inlet of low low-level (stack-gas) economizer 10, low low-level (stack-gas) economizer 10
Desalination water out is connect with the desalination water inlet of oxygen-eliminating device 14, the demineralized water of the desalination water out of oxygen-eliminating device 14 and feed pump 2 into
Mouth is connected, and the desalination water out of feed pump 2 is connect with the desalination water inlet of boiler 7, the air outlet of pressure fan 13 and warm pocket 5
Air inlet is connected, and the air outlet of warm pocket 5 is connected with the air inlet of air preheater 6, the air outlet of air preheater 6 and the air inlet of boiler 7
Mouth is connected, and the exhaust pass of boiler 7 is connect with the gas inlet of air preheater 6, the exhanst gas outlet and bag filter 8 of air preheater 6
Gas inlet be connected, the exhanst gas outlet of bag filter 8 is connected with the import of air-introduced machine 9, the outlet of air-introduced machine 9 and low temperature
The gas inlet of economizer 10 is connected, and the exhanst gas outlet of low low-level (stack-gas) economizer 10 is connected with the import of desulfurizing tower 11, desulfurizing tower 11
Outlet connect with the import of chimney 12.Back pressure turbine 2 is additionally provided with steam inlet pipe, is provided on steam inlet pipe into vapour
Regulating valve 15, accurately to control steam flow.
Claims (4)
1. a kind of pair is dragged electric pump back pressure turbine comprehensive utilization device, including feed pump, back pressure turbine, timing gear roller box, hair
Motor, warm pocket, pressure fan, air preheater, boiler, bag filter, air-introduced machine, low low-level (stack-gas) economizer, oxygen-eliminating device, desulfurizing tower,
Chimney, which is characterized in that the first output shaft of the back pressure turbine is connected with the input shaft of the feed pump, the back pressure steam
Second output shaft of turbine is connected with the input shaft of the timing gear roller box, the output shaft of the timing gear roller box and the power generation
The input shaft of machine is connected, and the steam drain of the back pressure turbine is connected with the steam inlet of the warm pocket, the warm pocket
Water outlet is connected with the desalination water inlet of the low low-level (stack-gas) economizer, and the desalination water out of the low low-level (stack-gas) economizer is removed with described
The desalination water inlet of oxygen device connects, and the desalination water out of the oxygen-eliminating device is connected with the desalination water inlet of the feed pump, described
The desalination water out of feed pump is connect with the desalination water inlet of the boiler, the air outlet of the pressure fan and the warm pocket
Air inlet is connected, and the air outlet of the warm pocket is connected with the air inlet of the air preheater, the air outlet of the air preheater and institute
The air inlet for stating boiler is connected, and the exhaust pass of the boiler is connect with the gas inlet of the air preheater, the air preheater
Exhanst gas outlet is connected with the gas inlet of the bag filter, the exhanst gas outlet of the bag filter and the air-introduced machine
Import is connected, and the outlet of the air-introduced machine is connected with the gas inlet of the low low-level (stack-gas) economizer, the low low-level (stack-gas) economizer
Exhanst gas outlet is connected with the import of the desulfurizing tower, and the outlet of the desulfurizing tower is connect with the import of the chimney.
2. according to claim 1 pair is dragged electric pump back pressure turbine comprehensive utilization device, which is characterized in that the back pressure steam
Turbine is additionally provided with steam inlet pipe, is provided on the steam inlet pipe into steam control valve.
3. according to claim 1 pair is dragged electric pump back pressure turbine comprehensive utilization device, which is characterized in that the low temperature
Economizer includes at least one set of U heat exchange.
4. according to claim 1 pair is dragged electric pump back pressure turbine comprehensive utilization device, which is characterized in that the warm pocket
Pocket is warmed up for drawable type.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820480873.0U CN208222484U (en) | 2018-04-04 | 2018-04-04 | A kind of pair is dragged electric pump back pressure turbine comprehensive utilization device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820480873.0U CN208222484U (en) | 2018-04-04 | 2018-04-04 | A kind of pair is dragged electric pump back pressure turbine comprehensive utilization device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208222484U true CN208222484U (en) | 2018-12-11 |
Family
ID=64514055
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820480873.0U Expired - Fee Related CN208222484U (en) | 2018-04-04 | 2018-04-04 | A kind of pair is dragged electric pump back pressure turbine comprehensive utilization device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208222484U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108469017A (en) * | 2018-04-04 | 2018-08-31 | 浙江巨化热电有限公司 | A kind of pair is dragged electric pump back pressure turbine comprehensive utilization device and its method |
-
2018
- 2018-04-04 CN CN201820480873.0U patent/CN208222484U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108469017A (en) * | 2018-04-04 | 2018-08-31 | 浙江巨化热电有限公司 | A kind of pair is dragged electric pump back pressure turbine comprehensive utilization device and its method |
| CN108469017B (en) * | 2018-04-04 | 2023-09-15 | 浙江巨化热电有限公司 | Comprehensive utilization device and method for back pressure steam turbine of double-drag electric pump |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103062754B (en) | Power station machine furnace integrated cold end comprehensive optimization system | |
| CN102454980B (en) | Method for recycling flue gas waste heat of thermal power plant boiler | |
| CN202177093U (en) | Multi-level efficient displacement type fume waste-heat utilization system | |
| CN102767821B (en) | Smoke waste heat deep utilization system of power station boiler for heating supplied water at high pressure | |
| CN202973061U (en) | Power station engine and boiler integrated cold end comprehensive optimization system | |
| CN111396913A (en) | System and method for recovering flue gas waste heat and moisture of coal-fired unit | |
| CN205383589U (en) | Novel energy -efficient application system of afterbody flue gas heat energy set | |
| CN109668165A (en) | Hot Secondary Air and smoke waste heat utilization system and thermal power generation unit | |
| CN112128732B (en) | Waste steam and flue gas waste heat energy quality coupling and improving system | |
| CN101639211A (en) | Float glass melting furnace parallel connection waste heat power generation system | |
| CN203731368U (en) | Device for deep recovery of smoke discharge waste heat of waste heat boiler | |
| CN205137624U (en) | Boiler waste heat heating system economizer | |
| CN205332168U (en) | Waste heat comprehensive recovery utilization system of thermal power factory | |
| CN201884079U (en) | Heat regenerative system of steam turbine generator unit capable of utilizing waste heat of heat conducting oil furnace in calcination plant | |
| CN212057351U (en) | Recovery system of residual heat of flue gas and moisture of coal-fired unit | |
| CN208222484U (en) | A kind of pair is dragged electric pump back pressure turbine comprehensive utilization device | |
| CN203036658U (en) | Boiler flue gas waste heat multipurpose utilization system | |
| CN202813417U (en) | Energy-saving system for preheating air by utilizing exhaust steam of small steam turbine in power plant | |
| CN205638587U (en) | Tail gas afterheat recycling device of thermal power factory | |
| CN205383640U (en) | Novel circulating water afterheat system is retrieved to fan heater | |
| CN202125937U (en) | System for comprehensively recycling boiler energy in tobacco industry | |
| CN202203970U (en) | Secondary energy saving and utilizing device for furnace exhaust gas waste heat | |
| CN202733874U (en) | Device utilizing waste heat of low-grade flue gas | |
| CN108469017A (en) | A kind of pair is dragged electric pump back pressure turbine comprehensive utilization device and its method | |
| CN211011316U (en) | Steam turbine boiler waste heat utilization system for coal-fired power plant |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20181211 |