CN201697153U - Drainage system of steam air heater of power station boiler - Google Patents
Drainage system of steam air heater of power station boiler Download PDFInfo
- Publication number
- CN201697153U CN201697153U CN201020234393XU CN201020234393U CN201697153U CN 201697153 U CN201697153 U CN 201697153U CN 201020234393X U CN201020234393X U CN 201020234393XU CN 201020234393 U CN201020234393 U CN 201020234393U CN 201697153 U CN201697153 U CN 201697153U
- Authority
- CN
- China
- Prior art keywords
- steam
- air heater
- drainage
- steam air
- drainage system
- 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
Images
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
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
The utility model provides a drainage system of a steam air heater of a power station boiler, relates to the drainage system of the steam air heater, and solves the problems of high operating failure rate, heavy maintenance workload, high maintenance cost, incomplete utilization of drainage heat energy, and low unit efficiency of the conventional drainage system of the steam air heater. The drainage system comprises the steam air heater, a drainage pipe, a drainage regulating valve, a steam condenser and a steam supply pipe; an inlet steam header of the steam air heater is communicated with the steam supply pipe, and a drainage header of the steam air heater is communicated with the steam condenser through the drainage pipe; and the drainage regulating valve is arranged on the drainage pipe. The drainage system ensures complete utilization of the drainage heat; and when water flows into the steam condenser at a temperature lower than the exhaust temperature of a steam turbine, the vacuum degree can be well improved and the condensed water amount can be increased, thereby improving the economic performance of the steam turbine unit from many aspects, improving the unit efficiency, and reducing the operating failure rate. The drainage system is applied to power station boilers.
Description
Technical field
The utility model relates to a kind of draining system for steam air heater of utility, is specifically related to a kind of draining system for steam air heater of utility boiler, belongs to thermal power engineering field, power station.
Background technology
In the thermal power plant that the low temperature season area is arranged, for preventing the boiler tail generation cold end corrosion of being heated, boiler fan, primary air fan major part are furnished with steam air heater, the steam air heater thermal source derives from the station-service vapour system, steam air heater adopts high-order the layout usually, arrange drain trap at low level, the hydrophobic flow by gravity that leans on is beaten to oxygen-eliminating device with drainage pump to drain trap again.There is following problem in draining system for steam air heater of utility:
Problem 1: because hydrophobic by flow by gravity, drain temperature is the full temperature of closing of drain trap pressure correspondence, for the closed drain trap, its temperature is all more than 100 ℃, to atmosphere opening formula drain trap (case), its temperature is also all near 100 ℃, and existing system generally is to return oxygen-eliminating device.Hydrophobic like this also have a large amount of heats not obtain utilizing, and, cause the cavitation of water pump because drain temperature is in or near the full state that closes, the drainage pump inlet very easily produces vaporization, thereby can increase operation troubles rate and maintenance workload and expense, and cause the loss of vapour, water and heat.
Problem 2: because existing main force generating set is many more than 300MW, the oxygen-eliminating device leaving water temperature generally will be more than 160 ℃, the evaporation capacity for engine that the steam air heater of lower temperature is hydrophobic also will to increase oxygen-eliminating device after entering adds thermal drain, can reduce unit efficiency like this and exerts oneself.
The utility model content
The purpose of this utility model is big in order to solve operation troubles rate height, maintenance workload that existing draining system for steam air heater of utility exists, maintenance cost height, the problem that hydrophobic heat is utilized and unit efficiency is low, and then a kind of draining system for steam air heater of utility boiler is provided.
The technical solution of the utility model is: a kind of draining system for steam air heater of utility boiler comprises steam air heater, drain pipe, drain regulating valve, condenser and steam supply pipe, the inlet steam header of described steam air heater is communicated with steam supply pipe, the hydrophobic header of described steam air heater is communicated with condenser by drain pipe, and described drain regulating valve is arranged on the drain pipe.
The utility model compared with prior art has following effect: the utility model has been realized the fixed pressure operation of steam air heater, the absolute pressure difference of utilizing interior operating pressure of steam air heater and condenser is with the hydrophobic condenser that directly is discharged to, thereby cancellation drain trap and drainage pump are saved hydrophobic reclaimer and power consumption.The utility model has designed one section hydrophobic cooling section, and directly receive drain pipe on the condenser, on the drain pipe of steam air heater, install drain regulating valve, keep having certain pressure in the steam air heater during operation, pressure differential with steam air heater and condenser enters in the condenser hydrophobic, thereby can cancel drain trap and drainage pump.Be in operation and change the area of hydrophobic cooling section with the hydrophobic liquid level in steam air heater of drain regulating valve control, utilize the heat exchange amount of the different adjustment steam air heater of water and steam exothermic coefficient, thereby adjust steam air heater outlet temperature and exhaust gas temperature, promptly reach the purpose of control air preheater tube wall temperature, also reduced the steam air heater drain temperature simultaneously.Be in operation and guarantee to have certain liquid level all the time in the steam air heater, thereby make drain temperature be lower than the pairing full temperature of closing of steam air heater pressure, realize hydrophobic supercooling, and the exhaust temperature that is lower than steam turbine that can be frequent, so just can guarantee that hydrophobic heat is fully used, when water temperature is lower than steam turbine row temperature, enter condenser and produce better action improving vacuum, and increased condensing capacity, the economy that all helps improving Steam Turbine from many aspects, improve unit efficiency, reduced the operation troubles rate.And directly get back to condenser after the hydrophobic supercooling and can increase the thermal discharge of working medium in steam air heater, reduce the steam air heater steam consumption, for example: by drain temperature is that 30 ℃, former hydrophobic gravity flow drain temperature are 100 ℃ of calculating, can reduce steam air heater consumption vapour more than 10%, by drain temperature is that 30 ℃, former hydrophobic gravity flow drain temperature are 130 ℃ of calculating, can reduce steam air heater consumption vapour more than 15%.The hydrophobic condenser of directly getting back to is compared with the common oxygen-eliminating device of getting back to, and the perfect thermodynamic cycle of this part carbonated drink can improve powergenerationcycleefficiency.The hydrophobic condenser of directly getting back to has utilized the pressure energy of steam and the vacuum of condensing, has cancelled drainage pump and drain trap, minimizing equipment and investment, and maintenance workload is little, and maintenance cost is low, has saved the drainage pump power consumption simultaneously.Steam air heater has realized that band presses operation, can reduce steam superheat, and increases of exerting oneself regulated liquid level in the steam air heater by drain regulating valve and regulated steam air heater and exert oneself, and regulates method that throttle flow adjusting steam air heater exerts oneself flexibility and reliability more than traditional passing through.The utility model is applicable to that the heat exchange area of steam air heater is bigger than hydrophobic gravity flow, and guaranteeing in most cases has certain hydrophobic cooling section in the steam air heater in actual motion.The time generally is to design by boiler peak load, the local lowest temperature for steam air heater in design, and therefore, steam air heater is to work being lower than under its designed capacity in the time of most, guarantees to have enough hydrophobic cooling sections.
Description of drawings
Fig. 1 is an integrally-built front view of the present utility model, and Fig. 2 is the integrally-built front view of embodiment.
The specific embodiment
The specific embodiment one: present embodiment is described in conjunction with Fig. 1, a kind of draining system for steam air heater of utility boiler of present embodiment comprises steam air heater 1, drain pipe 2, drain regulating valve 4, condenser 5 and steam supply pipe 6, the inlet steam header 1-1 of described steam air heater 1 is communicated with steam supply pipe 6, the hydrophobic header 1-2 of described steam air heater 1 is communicated with condenser by drain pipe 2, and described drain regulating valve 4 is arranged on the drain pipe 2.
Described steam air heater 1 is finned steam air heater, rib-type steam air heater or light pipe formula steam air heater, and it is a prior art.
The specific embodiment two: in conjunction with Fig. 1 and Fig. 2 present embodiment is described, the draining system of present embodiment also increases fluid flowmeter 3, and described fluid flowmeter 3 is installed on the drain pipe 2.So be provided with, can monitor the fluid flow in the drain pipe 2.Other composition is identical with the specific embodiment one with annexation.
Embodiment (referring to Fig. 2): the inlet steam header 1-1 of steam air heater 1 is communicated with steam supply pipe 6, the hydrophobic header 1-2 of described steam air heater 1 is communicated with condenser by drain pipe 2, described fluid flowmeter 3 and drain regulating valve 4 are successively set on the drain pipe 2 along the flow direction of water, hydrophobicly directly drain in the condenser 5 by drain pipe 2, fluid flowmeter 3 is used for measuring hydrophobic flow, is used for controlling the deaerator exhaust amount summer.The drain regulating valve of installing is used for regulating the hydrophobic liquid level in the steam air heater 1 on drain pipe 2, changes the heat exchange amount of steam air heater 1 by the variation of liquid level.Draining system maintenance steam air heater 1 in service has certain pressure, the operating pressure of dependence steam air heater 1 and the pressure reduction of condenser 15 are with the hydrophobic condenser 15 that is discharged to, and the liquid level of regulating in the steam air heater 1 by the aperture of drain regulating valve 14 changes the evaporation capacity for engine of steam air heater 1 and exerting oneself of steam air heater 1.The utility model can be united use with steam-supplying system, the steam supply of steam air heater 1 is taken from oxygen-eliminating device 14 steam discharges, installing deaerator exhaust control valve on steam supply pipe 6, be used for regulating the operating pressure of steam air heater, by blast pipe 15 exhausts, the air bleeding valve 12 of installing can be controlled capacity on the blast pipe 15 at steam air heater 1.Auxiliary steam header 9 is injected into steam mixer 7 by air vent pipework 11 with steam, installing auxiliary steam control valve on air vent pipework 11, be used for regulating the auxiliary steam evaporation capacity for engine, oxygen-eliminating device 14 steam discharges and auxiliary steam mix the back by steam mixer 7 and use vapour for steam air heater 1, and exhaust is responsible for 15-1 and is communicated with drain pipe 2.
Claims (2)
1. draining system for steam air heater of utility boiler, it is characterized in that: described draining system comprises steam air heater (1), drain pipe (2), drain regulating valve (4), condenser (5) and steam supply pipe (6), the inlet steam header (1-1) of described steam air heater (1) is communicated with steam supply pipe (6), the hydrophobic header (1-2) of described steam air heater (1) is communicated with condenser by drain pipe (2), and described drain regulating valve (4) is arranged on the drain pipe (2).
2. a kind of draining system for steam air heater of utility boiler according to claim 1 is characterized in that: draining system also comprises fluid flowmeter (3), and described fluid flowmeter (3) is installed on the drain pipe (2).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201020234393XU CN201697153U (en) | 2010-06-23 | 2010-06-23 | Drainage system of steam air heater of power station boiler |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201020234393XU CN201697153U (en) | 2010-06-23 | 2010-06-23 | Drainage system of steam air heater of power station boiler |
Publications (1)
Publication Number | Publication Date |
---|---|
CN201697153U true CN201697153U (en) | 2011-01-05 |
Family
ID=43398399
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201020234393XU Expired - Fee Related CN201697153U (en) | 2010-06-23 | 2010-06-23 | Drainage system of steam air heater of power station boiler |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN201697153U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101846329A (en) * | 2010-06-23 | 2010-09-29 | 魏熙臣 | Draining system for steam air heater of utility boiler |
CN112050248A (en) * | 2020-09-10 | 2020-12-08 | 上海康恒环境股份有限公司 | Steam air preheater for household garbage incineration |
-
2010
- 2010-06-23 CN CN201020234393XU patent/CN201697153U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101846329A (en) * | 2010-06-23 | 2010-09-29 | 魏熙臣 | Draining system for steam air heater of utility boiler |
CN112050248A (en) * | 2020-09-10 | 2020-12-08 | 上海康恒环境股份有限公司 | Steam air preheater for household garbage incineration |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US10968784B2 (en) | Flexible coal-fired power generation system and operation method thereof | |
CN104763485B (en) | A kind of concurrent heating type ultrahigh pressure/subcritical back pressure thermal power plant unit thermodynamic system | |
CN107905897A (en) | Gas turbine cycle flue gas waste heat recovery and inlet gas cooling association system and method | |
CN102734787A (en) | Concurrent recycling system for boiler smoke afterheat | |
CN110726153A (en) | Coal-fired power plant flue gas whitening elimination system and method | |
CN108758584A (en) | A kind of cold and hot storage alliance coal fired power plant air cooling system and its operation regulation and control method of waste heat combination driving | |
CN112050248A (en) | Steam air preheater for household garbage incineration | |
JP2024526396A (en) | Flexible operation system of thermal power generating units based on molten salt thermal storage | |
CN101846329A (en) | Draining system for steam air heater of utility boiler | |
US7827792B2 (en) | Refrigerant cooled main steam condenser binary cycle | |
CN209214399U (en) | Feed forward type hydrophobic side regulation heat exchange control system | |
CN107120713A (en) | A kind of anti-overtemperature cooling system of high back pressure thermal power plant unit condensate | |
CN201697153U (en) | Drainage system of steam air heater of power station boiler | |
CN108180767B (en) | Plate type evaporative condenser applied to direct air cooling unit | |
CN102494329B (en) | Device for utilizing flue gas waste heat of boiler comprehensively | |
CN107816732A (en) | A kind of air preheater cold end wall temperature adjusting means and method | |
CN208154872U (en) | Hot water fall connect direct combustion dual effect type lithium bromide absorption type heat pump unit | |
CN208332748U (en) | Solar air source double-source heat pump unit | |
CN202974001U (en) | Sub-control phase-change heat exchange system based on grading combined heat exchange | |
CN201706526U (en) | Steam supply system of air heater of power station boiler | |
CN209801447U (en) | Stable operation system of ethylbenzene evaporator | |
CN107345656A (en) | A kind of steam raising plant using residual heat from boiler fume | |
CN208186478U (en) | Domestic garbage burning electricity generation low-temperature circulating water heating system | |
CN206831645U (en) | A kind of anti-overtemperature cooling system of high back pressure thermal power plant unit condensate | |
CN208184797U (en) | A kind of solidifying pumping back heating system based on two unit black soy sauce vapour |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110105 Termination date: 20130623 |