CN104454232A - Fuel gas generator set waste heat utilization device - Google Patents
Fuel gas generator set waste heat utilization device Download PDFInfo
- Publication number
- CN104454232A CN104454232A CN201310431599.XA CN201310431599A CN104454232A CN 104454232 A CN104454232 A CN 104454232A CN 201310431599 A CN201310431599 A CN 201310431599A CN 104454232 A CN104454232 A CN 104454232A
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- China
- Prior art keywords
- generator
- heat exchanger
- lithium
- adsorber
- 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.)
- Pending
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02G—HOT GAS OR COMBUSTION-PRODUCT POSITIVE-DISPLACEMENT ENGINE PLANTS; USE OF WASTE HEAT OF COMBUSTION ENGINES; NOT OTHERWISE PROVIDED FOR
- F02G5/00—Profiting from waste heat of combustion engines, not otherwise provided for
- F02G5/02—Profiting from waste heat of exhaust gases
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H1/00—Water heaters, e.g. boilers, continuous-flow heaters or water-storage heaters
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B15/00—Sorption machines, plants or systems, operating continuously, e.g. absorption type
- F25B15/02—Sorption machines, plants or systems, operating continuously, e.g. absorption type without inert gas
- F25B15/06—Sorption machines, plants or systems, operating continuously, e.g. absorption type without inert gas the refrigerant being water vapour evaporated from a salt solution, e.g. lithium bromide
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B27/00—Machines, plants or systems, using particular sources of energy
- F25B27/02—Machines, plants or systems, using particular sources of energy using waste heat, e.g. from internal-combustion engines
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- 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]
- Y02B30/62—Absorption based systems
- Y02B30/625—Absorption based systems combined with heat or power generation [CHP], e.g. trigeneration
-
- 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
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/12—Improving ICE efficiencies
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Materials Engineering (AREA)
- Sorption Type Refrigeration Machines (AREA)
Abstract
The invention discloses a fuel gas generator set waste heat utilization device which is mainly composed of a heat exchanger (1), a generator (4), a condenser (5), an evaporator (8) and an absorber (12). The heat exchanger is connected with the generator of a lithium-bromide absorption-type refrigeration machine, and a connection pipe of the lithium-bromide absorption-type refrigeration machine is connected with stop vales (2), and an outlet of a high-concentration lithium bromide solution of the generator is communicated with the absorber. The absorber is communicated with the generator through a solution pump (11) to form circulation. The condenser is connected with the evaporator through a pipe, and a connection pipe of the condenser is provided with a throttle valve (7). A water cooling pipe arranged on the absorber is communicated with a water cooling pipe arranged on the condenser, and a water freezing pipe is arranged on the evaporator. The absorber is communicated with the evaporator through a pipe. The evaporator is connected with a water pump (10) so that refrigerant is made to be sprayed circularly in the evaporator. By means of the fuel gas generator set waste heat utilization device, the energy utilization rate is increased, and the purposes of saving energy and lowering consumption are achieved.
Description
Technical field
The present invention relates to a kind of waste heat recovering device technical field, particularly gas electricity generator waste heat recycle method and device.
Background technique
Existing jet dynamic control, the energy of consume fuel only has 30-35% to be converted to useful work, but has the energy of 65-70 to be lost in vain.That is, the energy of the 30-35% that only has an appointment is converted into electric energy by generator set, and the energy of about 30% is discharged with waste gas, and the energy of about 25-30% is taken away by cluster engine cooling water, and the energy of about 10% is dissipated by fuselage.This shows, more than the heat useful work that jet dynamic control waste heat flue gas is discharged and condensed water loses.At present, more ripe technology is not also had to the UTILIZATION OF VESIDUAL HEAT IN of this part loss of jet dynamic control, mostly can only waste, not only cause the waste of resource, but also thermo-pollution can be caused to environment.
Summary of the invention
In order to solve the problems of the technologies described above, the present invention proposes a kind of gas electricity generator waste heat recovery device, by reclaiming fume afterheat in gas electricity generator, reaches UTILIZATION OF VESIDUAL HEAT IN, saves energy and reduce the cost, avoids the object of environmental pollution.
The present invention realizes the technological scheme that above-mentioned purpose takes: a kind of gas electricity generator waste heat recovery device comprises heat exchanger, generator, condenser, vaporizer, adsorber, described heat exchanger is connected with the generator of lithium-bromide absorption-type refrigerating machine, its connecting tube is connected with stop valve, the high concentration lithium-bromide solution outlet of generator is communicated with adsorber, this adsorber is communicated with by solution pump with generator, condenser and vaporizer are connected by pipeline and are provided with throttle valve on its connecting pipelines, the cooling water pipeline that adsorber is arranged is communicated with the cooling water pipeline that condenser is arranged, be provided with chilled water pipeline on an evaporator, described adsorber and vaporizer are by pipeline connection, and vaporizer makes cryogen water spray at vaporizer Inner eycle by water pump.
The present invention is provided with the second heat exchanger and reduction valve further between the outlet of the high concentration lithium-bromide solution of generator and adsorber.
The present invention arranges the 3rd heat exchanger further between described heat exchanger and the generator of lithium-bromide absorption-type refrigerating machine, and is provided with stop valve on its connecting pipeline.
Heat exchanger of the present invention is heat pipe heat exchanger.
High concentration lithium-bromide solution of the present invention is in shape spray inflow absorber.
The present invention is by arranging the device such as heat exchanger and lithium-bromide absorption-type refrigerating machine in the outlet of gas electricity generator high-temperature flue gas, by reclaiming gas electricity generator fume afterheat, utilize the working principle of lithium-bromide absorption-type refrigerating machine, take water as refrigeration agent, take lithium-bromide solution as absorbing agent, according to user need produce domestic hot-water or refrigeration, substantially increase energy utilization rate, serve object that is energy-saving and cost-reducing, that avoid environmental pollution, increase economic efficiency.
accompanying drawing explanation
Fig. 1 is flowage structure schematic diagram of the present invention.
In figure: 1, heat pipe heat exchanger, 2, stop valve, 3, stop valve, 4, generator, 5, condenser, 6, cooling water, 7, throttle valve, 8, vaporizer, 9, chilled water, 10, water pump, 11, solution pump, 12, adsorber, 13, reduction valve, 14, the second heat exchanger, the 15, the 3rd heat exchanger, 16, hot water
By reference to the accompanying drawings, embodiments of the invention are provided as follows:
As shown in Figure 1: the waste heat recycle method of the gas electricity generator described in the present embodiment arranges heat exchanger for heat medium water in the outlet of gas electricity generator high-temperature flue gas, described heat exchanger is known heat-pipe heat exchanger, steam line is connected with the generator of lithium-bromide absorption-type refrigerating machine, it is refrigeration agent with water, take lithium-bromide solution as absorbing agent.The high-temperature steam produced by heat exchanger enters in generator, continues to carry out heat exchange to the lithium-bromide solution in it, makes that the water in the lithium-bromide solution in generator constantly gasifies, concentration constantly raises, and forms refrigerant vapor and high concentration lithium bromide.High concentration lithium-bromide solution enters in the adsorber of lithium-bromide absorption-type refrigerating machine, constantly absorbs refrigerant vapour, and the concentration bromizating lithium solution progressively reduces, then sends generator back to by solution pump, completes whole circulation; Refrigerant vapor then enters in lithium-bromide absorption-type refrigerating machine condenser, and and the cooling water carrying out heat exchange by adsorber again carry out heat exchange, cooling water is dispelled the heat by cooling tower, condensation after water vapour cooling, become liquid water, this liquid water is when entering vaporizer, vaporize due to rapid expansion, and a large amount of absorption enters the heat of 12 DEG C of chilled waters in vaporizer in vaporescence, chilled water is cooled to 7 DEG C and is used to user by Cemented filling, thus reaches the object of cooling refrigeration.Between vaporizer 8 and adsorber 12, be connected with refrigerant vapour pipeline, the refrigerant vapour that vaporizer is produced enters in adsorber 12; The cryogenic fluid pump 10 that vaporizer 8 connects makes cryogen circulated sprinkling in vaporizer 8, makes it fully vaporize.
The present invention also can arrange the second heat exchanger 14 between the generator 4 of lithium-bromide absorption-type refrigerating machine and adsorber 12, the low temperature lithium-bromide solution that the high temperature lithium-bromide solution that generator is flowed out and adsorber flow out carries out heat exchange at this second heat exchanger, heating enters the temperature of the lithium-bromide solution in generator, increases work efficiency.
The present invention also can arrange the 3rd heat exchanger 15 between heat exchanger 1 and the generator 4 of lithium-bromide absorption-type refrigerating machine, when not needing refrigeration, close the stop valve 2 between heat exchanger 1 and generator 4, open the stop valve 3 between heat exchanger 1 and the 3rd heat exchanger 15, produce hot water for life 16 by the 3rd heat exchanger 15.
The device that the present invention realizes said method employing forms primarily of heat exchanger 1, lithium-bromide solution generator 4, condenser 5, vaporizer 8, adsorber 12, second heat exchanger 14 and the 3rd heat exchanger 15, gas-steam type heat pipe heat exchanger 1 is arranged on the smoke outlet pipeline of gas electricity generator, and the steam (vapor) outlet end of this gas-steam type heat pipe heat exchanger 1 is all connected with the generator 4 of lithium-bromide absorption-type refrigerating machine with condensed water entrance point.Lithium-bromide absorption-type refrigerating machine is known products.This gas-steam type heat pipe heat exchanger 1 with the connecting tube of generator 4 being provided with stop valve 2, can closing when not needing refrigeration.The high concentration lithium-bromide solution outlet of generator 4 enters adsorber 12 top of lithium-bromide absorption-type refrigerating machine through the second heat exchanger 14, reduction valve 13, and be in shape spray inflow absorber 12, after carrying out heat exchange with the cooling water 6 entered in it, the concentration bromizating lithium solution progressively reduces, send generator 4 by solution pump 11 back to through the second heat exchanger 14 again, realize recycling of lithium-bromide solution.The high-temperature water vapor outlet of generator 4 is communicated with condenser 5 by pipeline.The entrance point being arranged on condenser 5 inner cooling water pipeline is communicated with the coolant outlet pipeline of adsorber 12 by pipeline, and the outlet end supercooling tower that is connected with cooling tower dispels the heat and recycles.Refrigerant vapour is lowered the temperature after condensation in condenser 5, and become cryogen water, enter in vaporizer 8, vaporizer 8 by throttle valve 7, it is connected with chilled water pipeline 9 and water pump 10, chilled water pipeline 9 the other end is connected with user.Water pump 10 makes cryogen water form circulation in vaporizer 8 by pipeline, and the top namely in vaporizer 8 is provided with cryogen spraying tube, lower end is provided with cryogen water outer pipe, forms circulation by water pump 10.Between vaporizer 8 and adsorber 12, be connected with refrigerant vapour pipeline, the refrigerant vapour that vaporizer is produced enters in adsorber 12.3rd heat exchanger 15 is set between this gas-steam type heat pipe heat exchanger 1 and generator 4 of lithium-bromide absorption-type refrigerating machine, and is provided with stop valve 3 on its connecting pipeline, produce hot water for life 16 by the 3rd heat exchanger 15.
The present embodiment in use, the high-temperature flue gas that gas electricity generator produces is by after heat exchanger 1 heat exchange, lithium-bromide solution is constantly heated by generator 4 by the water vapour produced, the water bromizated in lithium solution is constantly vaporized, lithium bromide water solution concentration constantly raises, and forms high-temperature vapor and high concentration lithium-bromide solution.High-temperature vapor enters condenser 5, and the cooling water 6 be condensed in device 5 condenses after lowering the temperature, and becomes the liquid water of high pressure low temperature; When the water in condenser 5 enters vaporizer 8 by throttle valve 7, rapid expansion and vaporizing, and in vaporescence, heat exchange is carried out with chilled water in vaporizer 9, thus reach the object of cooling refrigeration; In the process, high concentration lithium-bromide solution enters adsorber 12, is absorbed by the lithium bromide water solution in adsorber, and solution concentration is progressively reduced, then sends generator 4 back to by recycle pump 11, completes whole circulation.So move in endless cycles, produce cold continuously.Because bromize lithium dilute solution is cooled in adsorber 12, temperature is lower, in order to save the heat of heating bromize lithium dilute solution, improve the thermal efficiency of whole device, add second heat exchanger 14, the low temperature bromize lithium dilute solution that the high concentration lithium-bromide solution that generator 4 is flowed out and adsorber 12 flow out carries out heat exchange, improves the temperature entering lithium-bromide solution in generator 4.When not needing refrigeration, closing the stop valve 2 between heat exchanger 1 and generator 4, opening the stop valve 3 between heat exchanger and the 3rd heat exchanger 15, produce hot water for life 16 by the 3rd heat exchanger 15.
Claims (5)
1. a jet dynamic control residual heat using device, it is characterized in that: it is primarily of heat exchanger (1), generator (4), condenser (5), vaporizer (8) and adsorber (12) composition, described heat exchanger is connected with the generator of lithium-bromide absorption-type refrigerating machine, its connecting tube is connected with stop valve (2), the high concentration lithium-bromide solution outlet of generator is communicated with adsorber, this adsorber and generator are communicated with to form by solution pump (11) and circulate, condenser and vaporizer are connected by pipeline and on its connecting pipeline, are provided with throttle valve (7), the cooling water pipeline that adsorber is arranged is communicated with the cooling water pipeline arranged on condenser, be provided with chilled water pipeline on an evaporator, described adsorber and vaporizer are by pipeline connection, and vaporizer is connected with water pump (10) makes cryogen spray at vaporizer Inner eycle.
2. the device of jet dynamic control residual-heat utilization method according to claim 5, is characterized in that: between the outlet of high concentration lithium-bromide solution and the adsorber (12) of described generator (4), be provided with the second heat exchanger (14) and reduction valve (13).
3. the device of jet dynamic control residual-heat utilization method according to claim 5, it is characterized in that: the 3rd heat exchanger (15) is set between described heat exchanger (1) and the generator (4) of lithium-bromide absorption-type refrigerating machine, and on its connecting pipeline, is provided with stop valve (3).
4. the device of jet dynamic control residual-heat utilization method according to claim 5, is characterized in that: described heat exchanger (1) is heat pipe heat exchanger.
5. the device of jet dynamic control residual-heat utilization method according to claim 5, is characterized in that: described high concentration lithium-bromide solution is in shape spray inflow absorber (12).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310431599.XA CN104454232A (en) | 2013-09-22 | 2013-09-22 | Fuel gas generator set waste heat utilization device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310431599.XA CN104454232A (en) | 2013-09-22 | 2013-09-22 | Fuel gas generator set waste heat utilization device |
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| Publication Number | Publication Date |
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| CN104454232A true CN104454232A (en) | 2015-03-25 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201310431599.XA Pending CN104454232A (en) | 2013-09-22 | 2013-09-22 | Fuel gas generator set waste heat utilization device |
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| CN (1) | CN104454232A (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108534389A (en) * | 2018-06-09 | 2018-09-14 | 连云港市擎天德邦科技发展有限公司 | Lithium bromide refrigerating heat sink and method in procedure of producing soda under joint alkaline process |
| CN108590779A (en) * | 2018-04-26 | 2018-09-28 | 东莞理工学院 | Geothermal energy cogeneration cooling heating system based on Kalina cycles and lithium bromide refrigerating |
| CN109322748A (en) * | 2018-09-30 | 2019-02-12 | 天津华电北宸分布式能源有限公司 | Combustion engine inlet gas cooling device based on UTILIZATION OF VESIDUAL HEAT IN |
| CN109945547A (en) * | 2019-03-13 | 2019-06-28 | 江苏新能动力科技股份有限公司 | A kind of energy-saving type refrigeration house refrigeration system |
| CN110513999A (en) * | 2019-08-25 | 2019-11-29 | 西北工业大学 | A kind of heat pipe heat exchanging dehumidification device based on absorption heat pump |
| CN113153474A (en) * | 2021-05-17 | 2021-07-23 | 南通理工学院 | Marine diesel engine exhaust gas waste heat recycling system and recycling method thereof |
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| CN1109552A (en) * | 1994-03-31 | 1995-10-04 | 上海精协科技实业公司 | Electric, cold, hot and power synchronously-generating energy resource system |
| JP2000065436A (en) * | 1998-08-18 | 2000-03-03 | Kawasaki Thermal Engineering Co Ltd | Waste heat utilizing absorption type water heater/cooler refrigerating machine with load variation controlling function |
| JP2003329330A (en) * | 2002-05-15 | 2003-11-19 | Meidensha Corp | Absorption refrigerating machine |
| CN1587865A (en) * | 2004-08-05 | 2005-03-02 | 上海交通大学 | Double effect lithium bromide bsorptive refrigerator using smoke waste heat |
| CN203614267U (en) * | 2013-09-22 | 2014-05-28 | 洛阳中懋环保设备有限公司 | Waste heat utilization apparatus of combustion gas generating set |
-
2013
- 2013-09-22 CN CN201310431599.XA patent/CN104454232A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1109552A (en) * | 1994-03-31 | 1995-10-04 | 上海精协科技实业公司 | Electric, cold, hot and power synchronously-generating energy resource system |
| JP2000065436A (en) * | 1998-08-18 | 2000-03-03 | Kawasaki Thermal Engineering Co Ltd | Waste heat utilizing absorption type water heater/cooler refrigerating machine with load variation controlling function |
| JP2003329330A (en) * | 2002-05-15 | 2003-11-19 | Meidensha Corp | Absorption refrigerating machine |
| CN1587865A (en) * | 2004-08-05 | 2005-03-02 | 上海交通大学 | Double effect lithium bromide bsorptive refrigerator using smoke waste heat |
| CN203614267U (en) * | 2013-09-22 | 2014-05-28 | 洛阳中懋环保设备有限公司 | Waste heat utilization apparatus of combustion gas generating set |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108590779A (en) * | 2018-04-26 | 2018-09-28 | 东莞理工学院 | Geothermal energy cogeneration cooling heating system based on Kalina cycles and lithium bromide refrigerating |
| CN108534389A (en) * | 2018-06-09 | 2018-09-14 | 连云港市擎天德邦科技发展有限公司 | Lithium bromide refrigerating heat sink and method in procedure of producing soda under joint alkaline process |
| CN109322748A (en) * | 2018-09-30 | 2019-02-12 | 天津华电北宸分布式能源有限公司 | Combustion engine inlet gas cooling device based on UTILIZATION OF VESIDUAL HEAT IN |
| CN109945547A (en) * | 2019-03-13 | 2019-06-28 | 江苏新能动力科技股份有限公司 | A kind of energy-saving type refrigeration house refrigeration system |
| CN110513999A (en) * | 2019-08-25 | 2019-11-29 | 西北工业大学 | A kind of heat pipe heat exchanging dehumidification device based on absorption heat pump |
| CN113153474A (en) * | 2021-05-17 | 2021-07-23 | 南通理工学院 | Marine diesel engine exhaust gas waste heat recycling system and recycling method thereof |
| CN113153474B (en) * | 2021-05-17 | 2022-04-01 | 南通理工学院 | Marine diesel engine exhaust gas waste heat recycling system and recycling method thereof |
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Application publication date: 20150325 |