CN102331028A - Afterheat steam-water type heat supply system for recycling and absorption type heat pump of thermal power plant - Google Patents
Afterheat steam-water type heat supply system for recycling and absorption type heat pump of thermal power plant Download PDFInfo
- Publication number
- CN102331028A CN102331028A CN201110211960A CN201110211960A CN102331028A CN 102331028 A CN102331028 A CN 102331028A CN 201110211960 A CN201110211960 A CN 201110211960A CN 201110211960 A CN201110211960 A CN 201110211960A CN 102331028 A CN102331028 A CN 102331028A
- Authority
- CN
- China
- Prior art keywords
- heat pump
- water
- absorption heat
- power plant
- cooled condenser
- 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.)
- Granted
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
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/12—Hot water central heating systems using heat pumps
Abstract
The invention relates to an afterheat steam-water type heat supply system for a recycling and absorption type heat pump of a thermal power plant. The system comprises an extraction condensing steam turbine (1), a steam turbine steam extraction tube (3), a first water-cooling condenser (5), a second water-cooling condenser (6), subcoolers (7), a steam and water exchanger (9) and n absorption type heat pumps (XR1, ..., and XRn), wherein backwater of a heat supply network is connected in parallel with the subcoolers (7) of the absorption type heat pumps (XR1, ..., and XRn) and connected in series with the absorption type heat pumps (XR1, ..., and XRn) after entering an absorber of the first absorption type heat pump (XR1) through the second water-cooling condenser (6), gets out of an absorber of the nth absorption type heat pump (XRn) and enters a condenser of the nth absorption type heat pump (XRn), is connected in series with the condensers of the absorption type heat pumps (XR1, ..., and XRn) and is sent out directly or heated and sent out. By the system, much condensing waste heat of the thermal power plant can be recycled, the running efficiency of the heat pumps is improved, and the running of the heat supply network system is more reliable.
Description
Technical field
The present invention relates to a kind of cogeneration heating system, be applicable to that the exhaust steam of cogeneration power plant steam turbine is more energy-conservation, utilize safely and reliably, heat network system more utilizes condensation waste heat.
Background technology
Along with the shortage of the energy and the requirement of energy-saving and emission-reduction improve day by day, the comprehensive utilization technique of the energy is in continuous lifting.Urban planning cogeneration in the north carries out central heating, to substitute original independent boiler central heating, realizes the requirement of energy-saving and emission-reduction.Make full use of steam power plant's used heat, to improve the heat capacity of steam power plant, realize energy-saving and emission-reduction better, guarantee the safe and reliable operation of steam power plant and heat supply network simultaneously again, various new flow processs require study.Realize the more turbine discharge used heat that reclaims in the power plant, the most important condition is that adopting on this basis with the electricity is the source pump of power, or is the absorption type heat pump assembly of power with the heat supply network high-temperature water with the secondary net return water temperature reduction of hot user side.Heat supply network backwater through power plant is confessed carries out refrigeration cool-down, supplies the secondary net to use again as the waste heat source of heat pump, makes the heat supply network return water temperature reduce back telegram in reply factory.Power plant heat supply network backwater is introduced into former plant condenser after getting into power plant, with electric power plant circulating water be blended in heat up in the condenser after, get into absorption heat pump again, see off after in heat pump, heating up.In this system, the temperature that recirculated water goes out heat pump is the keys of heat supply network in many recovery of whole heating season condensation heat, in same outlet temperature, can reclaim more condensation waste heat, and become the another difficult problem of steam power plant's central heating technology with high-grade drawing gas less.
Summary of the invention
The objective of the invention is to overcome above-mentioned deficiency, a kind of condensation waste heat of realizing reclaiming more steam power plants is provided, the operational efficiency of raising heat pump and the heat network system more steam power plant of reliability service reclaim absorption heat pump waste heat carbonated drink formula heating system.
The objective of the invention is to realize like this: a kind of steam power plant reclaims absorption heat pump waste heat carbonated drink formula heating system; Comprise sucking condensing turbine, extracted steam from turbine pipe, first water-cooled condenser, vapor-water heat exchanger and absorption heat pump; Said absorption heat pump has the n platform, and n is >=2 natural number.High steam is extracted the thermal source of part steam as absorption heat pump and vapor-water heat exchanger out in sucking condensing turbine work done generating back.Exhaust steam in steam turbine condenses into water by condenser, and condensation waste heat is recycled.Be characterized in: described absorption heat pump has additional subcooler, in steam power plant, increases by one second water-cooled condenser and the former first water-cooled condenser parallel running.The heat supply network backwater gets into the parallelly connected subcooler that gets into each absorption heat pump after the steam power plant; Outflow gathers the back and gets into second water-cooled condenser; Be introduced into the absorber of first absorption heat pump after heating up once more, get into the absorber of second absorption heat pump again ... Be connected in series successively, until the absorber that gets into n platform absorption heat pump; Go out the condenser that gets into this n platform absorption heat pump behind the absorber of n platform absorption heat pump again; Then from n-1, n-2 ... Be connected in series successively, from the condenser of first absorption heat pump, flow out at last, directly or again behind vapor-water heat exchanger, see off.The cooling circulating water parallel connection or the series connection of said first water-cooled condenser get into the evaporimeter of absorption heat pump and the cooling system of steam power plant.The cooling system of steam power plant can be that air and this first water-cooled condenser go out water direct heat-exchange, also can be that the air and the first water-cooled condenser water outlet indirect exchange enter atmosphere with heat.
Steam power plant of the present invention reclaims absorption heat pump waste heat carbonated drink formula heating system; The cooling circulating water of said first water-cooled condenser go out be divided into behind said first water-cooled condenser two the tunnel: the one tunnel be introduced into n platform absorption heat pump evaporimeter; Return successively then ... Get into the evaporimeter of second, first absorption heat pump, from the evaporimeter of first absorption heat pump, go out at last, return first water-cooled condenser; Another road gets into the cooling system of steam power plant.
Steam power plant of the present invention reclaims absorption heat pump waste heat carbonated drink formula heating system; The cooling circulating water of said first water-cooled condenser goes out the evaporimeter that is introduced into n platform absorption heat pump behind said first water-cooled condenser; Return successively then ... Get into the evaporimeter of second, first absorption heat pump, from the evaporimeter of first absorption heat pump, go out at last, and then get into the cooling system of steam power plant.
Steam power plant of the present invention reclaims absorption heat pump waste heat carbonated drink formula heating system; The subcooler of said each absorption heat pump is merged into a subcooler; The water as refrigerant pipeline parallel connection of each absorption heat pump inserts the subcooler after this merging, and the heat supply network backwater gets into second water-cooled condenser after going out the subcooler after this merging.
Steam power plant of the present invention reclaims absorption heat pump waste heat carbonated drink formula heating system, and the cooling system of said steam power plant is cooling tower, air cooling device or a device for cooling.
Steam power plant of the present invention reclaims absorption heat pump waste heat carbonated drink formula heating system, and described absorption heat pump is a separate unit multisection type absorption heat pump.
This steam power plant reclaims absorption heat pump waste heat carbonated drink formula heating system and also is applicable to an air cooling power plant and a cold power plant.
The invention has the beneficial effects as follows:
Absorption heat pump in steam power plant has increased when subcooler and water-cooled condenser supply heat supply in winter to do heat supply season and has moved.Heat supply network recirculated water and power plant's cool cycles water separation isolated operation.Guaranteed the water quality of hot net water, guaranteed that all kinds of heat transmission equipments can safe and reliable energy-efficient operation.And because cooling circulating water and condensing direct heat transfer, compare with employing cellular-type heat-exchange system and can reclaim used heat more.Adopt heat supply network recirculated water directly to reclaim the COP value that the heat pump waste heat has more effectively improved heat pump.The working steam of heat pump will be practiced thrift more than 8% than original system.Because heat pump has been used high-grade energy less in reclaiming steam power plant's condensation waste heat process; So compare with former heat pump; Under the situation that reclaims same condensation waste heat; The temperature that goes out heat pump is lower than originally, can guarantee that so more heat supply network reclaims condenser heat and realizes maximization when heating demand descends, and is utilizing more exhaust steam in steam turbine to be used for heating in whole heating season.On the other hand, owing to reclaim same condensation heat, the circulating water temperature that goes out heat pump is low, under same outlet temperature situation, and the recyclable more condensation waste heat of heat pump.Through heat supply network recirculated water and cooling circulating water corresponding series flow in absorber, condenser and the evaporimeter of each heat pump, make the performance of heat pump obtain better optimize.The volume of heat pump, weight indicator can descend greatly, and manufacturing cost can descend simultaneously.On the other hand, because the performance optimization of heat pump, each item economic technology economic indicator of steam power plant is further enhanced.
Description of drawings
Fig. 1 (a) directly advances heat pump subcooler and cooling circulating water parallel connection sketch map for the heat supply network backwater that the present invention relates to.
Fig. 1 (b) directly advances heat pump subcooler and cooling circulating water series connection sketch map for the heat supply network backwater that the present invention relates to.
Reference numeral among the figure:
Sucking condensing turbine 1, generator 2, extracted steam from turbine pipe 3, coagulate water pipe 4, first water-cooled condenser 5 (former), second water-cooled condenser 6 (increasing newly), subcooler 7, cool cycles water discharge pipe 8, vapor-water heat exchanger 9, heat supply network return branch 10, cooling tower 11, air cooling device 12, a device for cooling 13, absorption heat pump XR1 ... N.
Heat supply network backwater A1, heat supply network water supply A2, high steam B, exhaust steam in steam turbine C, coagulate water and go out D.
The specific embodiment
Below in conjunction with accompanying drawing the present invention is described further:
Embodiment 1:
Shown in Fig. 1 (a), Fig. 1 (a) directly advances absorption heat pump subcooler and cooling circulating water parallel connection sketch map for the heat supply network backwater that the present invention relates to.Can find out by Fig. 1 (a), steam power plant of the present invention reclaim absorption heat pump waste heat carbonated drink formula heating system by sucking condensing turbine 1, generator 2, extracted steam from turbine pipe 3, coagulate water pipe 4, first water-cooled condenser 5, second water-cooled condenser 6, subcooler 7, cool cycles water discharge pipe 8, vapor-water heat exchanger 9, heat supply network return branch 10, cooling tower 11, air cooling device 12, a device for cooling 13, absorption heat pump XR1 ... Compositions such as n and water pump, valve and connecting line.Said absorption heat pump XR1 ... N has the n platform, and n is >=2 natural number.Parallel connection got into each absorption heat pump XR1 after heat supply network return branch 10 got into power plant ... The subcooler 7 of n; Outflow gathers the back and gets into second water-cooled condenser 6, and the back of heating up once more gets into the absorber of first absorption heat pump XR1, goes out the absorber that gets into second absorption heat pump XR2 behind the absorber of first absorption heat pump XR1; All the other and the like;, go out the absorber that gets into n platform absorption heat pump XRn behind the absorber of n-1 platform absorption heat pump XR2 again, get into the condenser of n platform absorption heat pump XRn again; Get into the condenser of n-1 platform absorption heat pump XR2 then; All the other and the like ..., after the condenser of first absorption heat pump XR1 go out.Just get into the condenser of absorption heat pump XR2 after the minimum absorber from absorption heat pump XR2 of this one road hot net water goes out, go out the condenser that returns absorption heat pump XR1 behind the condenser of absorption heat pump XR2, the condenser from absorption heat pump XR1 goes out at last.This road heat supply network backwater is heated through subcooler 7, second water-cooled condenser 6; Again through first absorption heat pump XR1, second absorption heat pump XR2 ... The absorber of n platform absorption heat pump XRn add gentle n platform absorption heat pump XRn ... The condenser of second absorption heat pump XR2, first absorption heat pump XR1 is heated; The heat supply network return water temperature is raise, directly or again after vapor-water heat exchanger 9 heats up, see off.The heat exchange in subcooler 7 of this one road heat supply network backwater heats up, and has taken away the heat of absorption heat pump condensation water as refrigerant, and the heat of the water as refrigerant that the heat pump generator produces has obtained effective utilization.Because water as refrigerant cooling back gets into evaporimeter; Basically eliminated the liquid state loss that water as refrigerant gets into behind the evaporimeter self flash distillation cooling; Make water as refrigerant can all be used for refrigeration, the COP value of heat pump is improved, reached the effect that one action two gets cooling circulating water.Cool cycles water discharge pipes 8 in first water-cooled condenser 5 of steam power plant be divided into two the tunnel: the one tunnel be introduced into n platform absorption heat pump XRn evaporimeter; Return successively then; Get into the evaporimeter of second absorption heat pump XR2, first absorption heat pump XR1, heat again from returning first water-cooled condenser 5 after the evaporimeter of first absorption heat pump XR1 flows out at last.Another road enters atmosphere to unnecessary heat through cooling tower 11, air cooling device 12 or a device for cooling 13.Direct Air-Cooled power plant second water-cooled condenser 6 links to each other with the admission pipeline of air cooling device, a part of second water-cooled condenser 6 that gets into of exhaust steam in steam turbine, a part of air cooling device that gets into.In this system heat supply network recirculated water and cooling circulating water two at the most the series flow in the platform heat pump make the performance of heat pump obtain optimization, each item technical-economic index of power plant's cogeneration operation is further improved.
Embodiment 2:
Shown in Fig. 1 (b), Fig. 1 (b) directly advances heat pump subcooler and cooling circulating water series connection sketch map for the heat supply network backwater that the present invention relates to.Fig. 1 (b) is the cooling circulating water series circulation with Fig. 1 (a) difference.
Described heat supply network backwater also can carry out heat exchange with a shared subcooler (not drawing among the figure) of many heat pumps.The water as refrigerant pipeline of each heat pump (not drawing among the figure) is connected in parallel with subcooler, through backheat pump after the subcooler heat release.After heating up in subcooler, the heat supply network backwater merges with another road.
Claims (6)
1. a steam power plant reclaims absorption heat pump waste heat carbonated drink formula heating system; Comprise sucking condensing turbine (1), extracted steam from turbine pipe (3), first water-cooled condenser (5), vapor-water heat exchanger (9) and absorption heat pump (XR1 ... N); Said absorption heat pump (XR1 ... N) the n platform is arranged; N is >=2 natural number, it is characterized in that: said absorption heat pump (XR1 ... N) have additional subcooler (7), system's increase has one second water-cooled condenser (6); The parallel connection after getting into steam power plant of heat supply network backwater gets into each absorption heat pump (XR1 ... N) subcooler (7); Outflow gathers the absorber that the back series connection gets into second water-cooled condenser (6) and first absorption heat pump (XR1), gets into the absorber of second absorption heat pump (XR2) again ... Be connected in series successively, until the absorber that gets into n platform absorption heat pump (XRn); Go out the condenser that gets into this n platform absorption heat pump (XRn) behind the absorber of n platform absorption heat pump (XRn) again; Then from n-1, n-2 ... Be connected in series successively, from the condenser of first absorption heat pump (XR1), go out at last, directly or again behind vapor-water heat exchanger (9), see off; The cooling circulating water of first water-cooled condenser (5) goes out the parallel connection of said first water-cooled condenser (5) back or series connection gets into the evaporimeter of absorption heat pump (XRn) and the cooling system of steam power plant.
2. a kind of steam power plant according to claim 1 reclaims absorption heat pump waste heat carbonated drink formula heating system; It is characterized in that: the cooling circulating water of said first water-cooled condenser (5) go out be divided into behind said first water-cooled condenser (5) the two tunnel: the one tunnel be introduced into n platform absorption heat pump (XRn) evaporimeter; Return successively then ... Get into the evaporimeter of second, first absorption heat pump; From the evaporimeter of first absorption heat pump (XR1), go out at last, return first water-cooled condenser (5); Another road gets into the cooling system of steam power plant.
3. a kind of steam power plant according to claim 1 reclaims absorption heat pump waste heat carbonated drink formula heating system; It is characterized in that: the cooling circulating water of said first water-cooled condenser (5) goes out the evaporimeter that is introduced into n platform absorption heat pump (XRn) behind said first water-cooled condenser (5); Return successively then ... Get into the evaporimeter of second, first absorption heat pump, from the evaporimeter of first absorption heat pump (XR1), go out at last, and then get into the cooling system of steam power plant.
4. reclaim absorption heat pump waste heat carbonated drink formula heating system according to claim 1 or 2 or 3 described a kind of steam power plants; It is characterized in that: said each absorption heat pump (XR1 ... N) subcooler (7) is merged into a subcooler; Each absorption heat pump (XR1 ... N) water as refrigerant pipeline parallel connection inserts the subcooler after this merging, and the heat supply network backwater gets into second water-cooled condenser (6) after going out the subcooler after this merging.
5. reclaim absorption heat pump waste heat carbonated drink formula heating system according to claim 1 or 2 or 3 described a kind of steam power plants, it is characterized in that: the cooling system of said steam power plant is cooling tower (11), air cooling device (12) or a device for cooling (13).
6. reclaim absorption heat pump waste heat carbonated drink formula heating system according to claim 1 or 2 or 3 described a kind of steam power plants, it is characterized in that: described absorption heat pump is a separate unit multisection type absorption heat pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201110211960 CN102331028B (en) | 2011-07-27 | 2011-07-27 | Afterheat steam-water type heat supply system for recycling and absorption type heat pump of thermal power plant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201110211960 CN102331028B (en) | 2011-07-27 | 2011-07-27 | Afterheat steam-water type heat supply system for recycling and absorption type heat pump of thermal power plant |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102331028A true CN102331028A (en) | 2012-01-25 |
| CN102331028B CN102331028B (en) | 2013-05-01 |
Family
ID=45482910
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201110211960 Active CN102331028B (en) | 2011-07-27 | 2011-07-27 | Afterheat steam-water type heat supply system for recycling and absorption type heat pump of thermal power plant |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102331028B (en) |
Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2007064047A (en) * | 2005-08-30 | 2007-03-15 | Hitachi Eng Co Ltd | Waste heat recovery facility for steam turbine plant |
| JP2007064050A (en) * | 2005-08-30 | 2007-03-15 | Hitachi Eng Co Ltd | Waste heat utilizing facility for steam turbine plant |
| CN101231004A (en) * | 2008-02-28 | 2008-07-30 | 清华大学 | Large temperature-difference central heating system |
| KR100975276B1 (en) * | 2009-12-01 | 2010-08-12 | 주식회사 코와 | Local heating water feeding system using absorbing type heat pump |
| CN201568088U (en) * | 2009-12-21 | 2010-09-01 | 江苏双良空调设备股份有限公司 | Cogeneration system for directly recycling waste heat of exhaust steam from power station steam turbine with absorption type heat pump |
| CN101943435A (en) * | 2010-09-25 | 2011-01-12 | 北京联合优发能源技术有限公司 | Thermoelectricity co-generation energy-saving device for supplying heat by using waste heat and energy-saving method thereof |
| CN101967999A (en) * | 2010-09-25 | 2011-02-09 | 北京联合优发能源技术有限公司 | Combined heat and power generation energy saving device using afterheat to supply heat and energy saving method |
| CN102022770A (en) * | 2010-10-26 | 2011-04-20 | 北京国电电科院节能技术有限公司 | Heat and power cogeneration energy-saving device and method for supplying heat by using direct waste heat of air-cooling unit |
| CN201884080U (en) * | 2010-11-18 | 2011-06-29 | 清华大学 | Steam exhaust waste heat recycling unit |
| CN202182507U (en) * | 2011-07-27 | 2012-04-04 | 双良节能系统股份有限公司 | Thermal power plant recovery absorption heat pump waste heat steam-water type heat supply system |
-
2011
- 2011-07-27 CN CN 201110211960 patent/CN102331028B/en active Active
Patent Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2007064047A (en) * | 2005-08-30 | 2007-03-15 | Hitachi Eng Co Ltd | Waste heat recovery facility for steam turbine plant |
| JP2007064050A (en) * | 2005-08-30 | 2007-03-15 | Hitachi Eng Co Ltd | Waste heat utilizing facility for steam turbine plant |
| CN101231004A (en) * | 2008-02-28 | 2008-07-30 | 清华大学 | Large temperature-difference central heating system |
| KR100975276B1 (en) * | 2009-12-01 | 2010-08-12 | 주식회사 코와 | Local heating water feeding system using absorbing type heat pump |
| CN201568088U (en) * | 2009-12-21 | 2010-09-01 | 江苏双良空调设备股份有限公司 | Cogeneration system for directly recycling waste heat of exhaust steam from power station steam turbine with absorption type heat pump |
| CN101943435A (en) * | 2010-09-25 | 2011-01-12 | 北京联合优发能源技术有限公司 | Thermoelectricity co-generation energy-saving device for supplying heat by using waste heat and energy-saving method thereof |
| CN101967999A (en) * | 2010-09-25 | 2011-02-09 | 北京联合优发能源技术有限公司 | Combined heat and power generation energy saving device using afterheat to supply heat and energy saving method |
| CN102022770A (en) * | 2010-10-26 | 2011-04-20 | 北京国电电科院节能技术有限公司 | Heat and power cogeneration energy-saving device and method for supplying heat by using direct waste heat of air-cooling unit |
| CN201884080U (en) * | 2010-11-18 | 2011-06-29 | 清华大学 | Steam exhaust waste heat recycling unit |
| CN202182507U (en) * | 2011-07-27 | 2012-04-04 | 双良节能系统股份有限公司 | Thermal power plant recovery absorption heat pump waste heat steam-water type heat supply system |
Also Published As
| Publication number | Publication date |
|---|---|
| CN102331028B (en) | 2013-05-01 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102338408B (en) | Series-type heat supply system of circulating water in thermal power plant | |
| CN102331025B (en) | Steam-waste heat supply system for recycling condensation waste heat of main and auxiliary machines in thermal power plant | |
| CN202118985U (en) | Energy-saving thermoelectric combined heating system | |
| CN102278785B (en) | Energy-saving combined heat and power type heat supply system | |
| CN202221120U (en) | Circulating water parallel-connection type heat supply system of thermal power plant | |
| CN202118984U (en) | Energy-saving heating system of thermal power plant | |
| CN102384515A (en) | Absorption type refrigeration and heat exchange heat and power cogeneration heating system | |
| CN102261694B (en) | Energy-efficient heating system for thermal power plants | |
| CN202182507U (en) | Thermal power plant recovery absorption heat pump waste heat steam-water type heat supply system | |
| CN202182505U (en) | Heat supply network return water serial vapor-water type heat supply system for condensing waste heat of main machine and auxiliary machine in thermal power plant | |
| CN102338412A (en) | Parallel-type heat supply system of circulating water in thermal power plant | |
| CN202141114U (en) | Vapor-water type heating system of thermal power plant | |
| CN202188549U (en) | Heat-net return water serial-connection water type heat supply system used for recovering condensation waste heat of main and auxiliary machine in thermal power plant | |
| CN202216314U (en) | Double-pipe heat supply system for recovering waste condensation heat of auxiliary turbine of thermal power plant | |
| CN202216315U (en) | Circulating-water tandem-type heat supply system for thermal power plant | |
| CN202182506U (en) | Combined heat supply system for recycling condenser heat of main engine and auxiliary engine of thermal power plant | |
| CN102345895B (en) | Steam-water heating system for thermal power plant | |
| CN202221121U (en) | Water-water heat supply system for recovering waste condensation heat of auxiliary steam turbine of thermal power plant | |
| CN102331026B (en) | Heating network return water serial steam-waste heat supply system for recycling condensation waste heat in thermal power plant | |
| CN202182508U (en) | Heating system for empty cold and hot power plant to utilize condensing heat | |
| CN202221122U (en) | Heat supply system directly recycling condensation waste heat of auxiliary machine in thermal power plant | |
| CN102338410B (en) | Double-tube heating system used for recovering auxiliary engine condensing waste heat of thermal power plant | |
| CN202141113U (en) | Circulating water parallel connection type heating system for recovering condensing waste heat of auxiliary machine of thermal power plant | |
| CN102331027B (en) | Backwater and series water type heat supply system for heat supply network for recycling condensing waste heat of main steam turbine and auxiliary steam turbine of thermal power plant | |
| CN202170819U (en) | Thermal power plant recovery main and subsidiary engine condensation waste heat vapor water type heat supply system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |