CN107339687B - It is a kind of to utilize gas compressor waste heat for station area's heating technique - Google Patents
It is a kind of to utilize gas compressor waste heat for station area's heating technique Download PDFInfo
- Publication number
- CN107339687B CN107339687B CN201611265107.4A CN201611265107A CN107339687B CN 107339687 B CN107339687 B CN 107339687B CN 201611265107 A CN201611265107 A CN 201611265107A CN 107339687 B CN107339687 B CN 107339687B
- Authority
- CN
- China
- Prior art keywords
- heat exchanger
- gas compressor
- station area
- pipeline
- heating
- 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 title claims abstract description 79
- 238000010438 heat treatment Methods 0.000 title claims abstract description 58
- 238000000034 method Methods 0.000 title claims abstract description 39
- 239000002918 waste heat Substances 0.000 title claims abstract description 35
- 239000000779 smoke Substances 0.000 claims abstract description 50
- 238000009833 condensation Methods 0.000 claims abstract description 45
- 230000005494 condensation Effects 0.000 claims abstract description 45
- 238000001816 cooling Methods 0.000 claims abstract description 35
- 239000007788 liquid Substances 0.000 claims abstract description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 23
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 15
- 239000003546 flue gas Substances 0.000 claims description 15
- 239000000567 combustion gas Substances 0.000 claims description 3
- 235000019504 cigarettes Nutrition 0.000 claims 2
- 238000004064 recycling Methods 0.000 abstract description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 24
- 239000003345 natural gas Substances 0.000 description 12
- 239000000446 fuel Substances 0.000 description 7
- 238000004519 manufacturing process Methods 0.000 description 4
- 238000002485 combustion reaction Methods 0.000 description 3
- 239000003517 fume Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000006392 deoxygenation reaction Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 230000001932 seasonal effect Effects 0.000 description 1
- 239000008234 soft water Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22D—PREHEATING, OR ACCUMULATING PREHEATED, FEED-WATER FOR STEAM GENERATION; FEED-WATER SUPPLY FOR STEAM GENERATION; CONTROLLING WATER LEVEL FOR STEAM GENERATION; AUXILIARY DEVICES FOR PROMOTING WATER CIRCULATION WITHIN STEAM BOILERS
- F22D1/00—Feed-water heaters, i.e. economisers or like preheaters
- F22D1/50—Feed-water heaters, i.e. economisers or like preheaters incorporating thermal de-aeration of feed-water
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
- F24D3/00—Hot-water central heating systems
- F24D3/02—Hot-water central heating systems with forced circulation, e.g. by pumps
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
- F24D2200/00—Heat sources or energy sources
- F24D2200/16—Waste heat
- F24D2200/18—Flue gas recuperation
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
- F24D2220/00—Components of central heating installations excluding heat sources
- F24D2220/06—Heat exchangers
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Engine Equipment That Uses Special Cycles (AREA)
- Air Supply (AREA)
Abstract
It is station area's heating technique that the present invention provides a kind of using gas compressor waste heat, belongs to the technical field of using energy source.It is a kind of using gas compressor waste heat be station area's heating technique include gas compressor, cooling heat exchanger, boiler system, smoke condensation device and heat load；Cooling heat exchanger is arranged in the present invention in the cooling system of gas compressor, and cooling heat exchanger is connect with boiler system, realizes the recycling for discarding the energy to gas compressor part, improves boiler feed temperature, more energy saving；The smoke evacuation of gas compressor tail portion is connect by three-way control valve with smoke condensation device, heat exchange is more able to achieve while improving safety；Smoke condensation device is connect with station area's heating system and heat exchanger, guarantees in winter for the heating of station area, is that Produced Liquid or wet crude heat in summer, energy utilization rate is higher；By the way that valve is arranged, controllability and safety are improved.
Description
Technical field
The present invention relates to the technical field of using energy source, it is specifically related to a kind of adopt using gas compressor waste heat for station area
Warm technique.
Background technique
Gas compressor is the capital equipment at natural gas processing station, is consumed energy larger, heat loss is also larger, fuel availability
It is low.The energy utilization rate for how improving gas compressor is the main problem that the energy conservation of natural gas processing station faces.
Current gas compressor both domestic and external is mostly developed on the basis of gasoline engine or diesel engine, and fuel is (natural
Gas) chemical energy be converted into the mechanical energy of compressor in such a way that hot merit converts, for by technique natural gas compressing.At this
Technique natural gas compressing boosts and heats up in the process, the high-temperature flue gas row Xiang great Qi generated after fuel natural gas burning.
Technique natural gas needs just to can enter next process flow after cooling down, and scene is dropped frequently with air-cooled cooler
Temperature, this partial heat have been discharged into environment in vain by air, have not been utilized.The high-temperature flue gas of gas compressor is discharged fume
Temperature is directly discharged to atmosphere generally between 380~420 DEG C, and energy loss is serious, and also creates thermal pollution and other
The discharge of pollutant.
If the two main heat loss can be utilized, the exhaust gas temperature of gas compressor is reduced to 130 DEG C
Or condensation point is hereinafter, the heat recovery and utilization for simultaneously being discharged natural gas cooling using cold source, so that it may by natural gas energy resource benefit
It is improved with rate to 70% or more, it is big that waste heat recycles potentiality.
Mainly there are winter heating, production to be heated with heat and steam boiler water supply with hot spot and cold source in standing, wherein heating is
Seasonal heating load；Production is heating Produced Liquid and wet crude with heat, is perennial thermic load；At present by combustion and steam pot
Furnace provides, and fuel consumption is big.Steam boiler water supply heating is also perennial load, is not heated at present, after softened and deoxygenation
It is sent directly into steam boiler, increases steam boiler fuel consumption.
Summary of the invention
For the above-mentioned problems in the prior art, be now intended to provide it is a kind of using gas compressor waste heat for station area adopt
Warm technique is realized by the way that cooling heat exchanger is arranged on the cooling system of gas compressor and carries out heat exchange with boiler feedwater, return
The heat of skill of knocking off natural gas cooling release；Smoke condensation device is set in the tail portion of gas compressor, by smoke condensation device
It is connect with the heat exchanger on station area's heating system and Produced Liquid or wet crude pipeline to recycle high-temperature flue gas waste heat, and control is set
Valve processed switches circulation path；The utilization rate of waste heat that gas compressor can be improved reduces the thermic load of gas-steam boiler, section
About resource reduces the discharge of thermal pollution and other pollutants.
Specific technical solution is as follows:
It is a kind of to utilize gas compressor waste heat for station area's heating technique, it has the feature that, comprising: be set to gas pressure
Cooling heat exchanger on contracting machine cooling system, and the entrance and exit of cooling heat exchanger passes through pipeline respectively and in boiler system
Demineralizer is connected with oxygen-eliminating device, and the tail portion smoke evacuation of gas compressor is connect by pipeline with smoke condensation device, and flue gas condensing
Device is connect by pipeline with station area's heating system and the heat exchanger being set on Produced Liquid or wet crude pipeline, and in pipeline
The opening and closing of upper several valve control pipelines of setting.
A kind of above-mentioned utilization gas compressor waste heat is station area's heating technique, wherein is discharged fume the tail portion of gas compressor
Place is provided with three-way control valve, and three interfaces of three-way control valve are discharged fume with the tail gas of gas compressor respectively, flue gas condensing
Device is arranged to the connection of the flue of atmosphere.
A kind of above-mentioned utilization gas compressor waste heat is station area's heating technique, wherein smoke condensation device includes sensible heat
Heat exchanger and latent heat exchanger, and sensible heat exchanger and latent heat exchanger are integral type setting.
A kind of above-mentioned utilization gas compressor waste heat is station area's heating technique, wherein smoke condensation device further includes cold
Condensation tank, and condensation water tank is set to smoke condensation device bottom.
It is a kind of using gas compressor waste heat be stand area's heating technique it is above-mentioned it is a kind of using gas compressor waste heat be station
Area's heating technique, wherein the entrance and exit of sensible heat exchanger respectively with station area's heating system and be set to Produced Liquid or aqueous
The outlet of heat exchanger on crude oil pipeline is connected with entrance.
It is above-mentioned it is a kind of using gas compressor waste heat be station area's heating technique, wherein the entrance of latent heat exchanger and go out
Mouth respectively by pipeline in boiler system demineralizer and oxygen-eliminating device connect, and the outlet of latent heat exchanger is also and sensible heat transfer
The pipeline connection that the area Qi Yuzhan heating system is connected with the heat exchanger being set on Produced Liquid or wet crude pipeline.
It is above-mentioned it is a kind of using gas compressor waste heat be station area's heating technique, wherein sensible heat exchanger and the heating of station area
Booster pump is provided on the pipeline that system is connected with the heat exchanger being set on Produced Liquid or wet crude pipeline.
A kind of above-mentioned utilization gas compressor waste heat is station area's heating technique, wherein in the exhaust of smoke condensation device
Air-introduced machine is provided on mouthful.
It is above-mentioned it is a kind of using gas compressor waste heat be station area's heating technique, wherein demineralizer in boiler system and
By-pass line is provided between oxygen-eliminating device.
A kind of above-mentioned utilization gas compressor waste heat is station area's heating technique, wherein latent heat exchanger and sensible heat transfer
Device is one or more combinations of finned tube or other extended surface heat exchanger tubes.
It is above-mentioned it is a kind of using gas compressor waste heat be station area's heating technique, wherein valve is manually, electrically or pneumatic
One of or a variety of combinations.
The good effect of above-mentioned technical proposal is: 1, by the way that cooling heat transferring is arranged on the cooling system of gas compressor
Boiler soft water in device, with boiler system carries out heat exchange, realizes to the cooling release of gas compressor technique natural gas
The recycling of heat improves the temperature of boiler feedwater, reduces the fuel consumption of boiler；2, the tail portion smoke evacuation of gas compressor is logical
Piping is connect with smoke condensation device, and heating system and being set to is adopted by the sensible heat exchanger of smoke condensation device and in standing
Heat exchanger connection on liquid or wet crude pipeline out, can reduce exhaust gas temperature, and the sensible heat of recovered flue gas mitigates steam boiler
Thermic load；3, high-temperature flue gas and be softened water with the sensible heat exchanger intermediate medium of hot spot heat transfer is realized, the area Shi Zhan
Steam heating is changed to hot water heating, Produced Liquid or wet crude part heat load and is changed to hot water heating, avoids using steam mistake
Danger in journey, substantially increases the safety of system, and reduces the waste of high-grade steam；4, it is situated between among sensible heat exchanger
Matter softens water circulation use, saves water resource, while being convenient to be supplemented with steam boiler water supply, so that system is simple, cost
It is low；5, the latent heat exchanger of smoke condensation device directly heats steam boiler water supply, further decreases exhaust gas temperature, recovered flue gas
In latent heat, energy recovery is more thorough；6, three-way control valve is set between tail portion smoke discharging pipe and smoke condensation device, improves
Safety and flexibility；7, it is provided with air-introduced machine on the exhaust outlet of smoke condensation device, newly-increased system can be overcome to hinder well
Power keeps smoke evacuation more smooth；8, flexible structure, the energy regenerating that can be suitable for more gas compressors simultaneously utilize, adaptability is good,
It is at low cost.
Detailed description of the invention
Fig. 1 is a kind of artwork using the embodiment that gas compressor waste heat is station area's heating technique of the invention；
In attached drawing: 1, gas compressor；2, demineralizer；3, oxygen-eliminating device；4, cooling heat exchanger；5, air-cooled cooler；6, three
Logical control valve；7, smoke condensation device；71, sensible heat exchanger；72, latent heat exchanger；73, condensation water tank；74, air-introduced machine；8,
It stands area's heating system；9, Produced Liquid or wet crude pipeline；10, heat exchanger；11, booster pump.
Specific embodiment
It is real below in order to be easy to understand the technical means, the creative features, the aims and the efficiencies achieved by the present invention
It applies example combination attached drawing 1 to be specifically addressed technical solution provided by the invention, but the following contents is not as the limitation of the invention.
Fig. 1 is a kind of artwork using the embodiment that gas compressor waste heat is station area's heating technique of the invention.Such as
Shown in Fig. 1, it includes: combustion that the waste heat provided in this embodiment using gas compressor, which provides station area's heating and the technique of production heat,
Air compressor 1, demineralizer 2, oxygen-eliminating device 3, cooling heat exchanger 4, air-cooled cooler 5, three-way control valve 6, smoke condensation device 7,
Sensible heat exchanger 71, latent heat exchanger 72, condensation water tank 73, air-introduced machine 74, stand area's heating system 8, Produced Liquid or wet crude
Pipeline 9, heat exchanger 10 and booster pump 11.
Specifically, cooling heat exchanger 4 is arranged in the cooling system of gas compressor 1, and cooling heat exchanger 4 is connected to combustion gas
It is also connect with boiler (not shown) system while 1 cooling system of compressor, i.e. an entrance and boiler system for cooling heat exchanger 4
Demineralizer 2 outlet by pipeline connect, cooling heat exchanger 4 one outlet is connect with the import of the oxygen-eliminating device 3 of boiler system,
Ensure that the water energy in boiler (not shown) system enter in cooling heat exchanger 4 in the cooling system of gas compressor 1 with
High temperature coolant after technique heat exchange gas carries out heat exchange, realizes the recycling of the heat of technique natural gas cooling release,
Steam boiler feed temperature can also be improved, the fuel consumption of boiler (not shown) is effectively reduced.
Specifically, (not shown) is connect by pipeline with smoke condensation device 7 at the tail portion smoke evacuation of gas compressor 1,
The high-temperature flue gas that ensure that gas compressor 1 is discharged can smoothly enter into smoke condensation device 7, be realized by smoke condensation device 7
The recycling of waste heat, the utilization of resources are more reasonable.
(not shown) is additionally provided with three-way control valve 6 at the tail portion smoke evacuation of gas compressor 1, and three-way control valve 6 is set
Be placed in front of smoke condensation device 7, i.e., the three of three-way control valve 6 interface respectively with the tail gas of gas compressor smoke evacuation, flue gas
Condensing unit is arranged to the connection of the flue of atmosphere, and the passage path of three-way control valve 6, safety can be converted according to on-site actual situations
Property is higher.
Specifically, smoke condensation device 7 includes sensible heat exchanger 71 and latent heat exchanger 72, sensible heat exchanger 71 and station area
Heating system 8 and heat exchanger 10 connect, and heat exchanger 10 is set on Produced Liquid or wet crude pipeline 9, ensure that gas pressure
The high-temperature flue gas of contracting machine 1 enters 71 area Zhong Yuzhan heating system 8 of sensible heat exchanger by (not shown) at the smoke evacuation of tail portion and changes
Hot device 10 carries out heat exchange, realize to the heating of station area and in Produced Liquid or wet crude pipeline 9 Produced Liquid or aqueous original
Oil is heated, and exhaust gas temperature is reduced, and recovered flue gas sensible heat rationally utilizes energy.
Latent heat exchanger 72 is directly connect with boiler (not shown) system, i.e. the entrance and exit difference of latent heat exchanger 72
By pipeline in boiler (not shown) system demineralizer 2 and oxygen-eliminating device 3 connect, directly with steam boiler (not shown) water supply
Heat exchange is carried out, exhaust gas temperature, recovered flue gas latent heat are further decreased, waste heat recycles more thorough.
More specifically, it is additionally provided with condensation water tank 73 on smoke condensation device 7, and to be set to flue gas cold for condensation water tank 73
The bottom of solidifying device 7 is discharged after processing reaches requirement convenient for condensed water；And smoke condensation device is set on condensation water tank 73
7 exhaust outlet (not shown).
More specifically, it is provided with by-pass line between the demineralizer 2 and oxygen-eliminating device 3 in boiler (not shown) system,
Softened water can be directly entered oxygen-eliminating device when gas compressor 1 or cooling heat exchanger 4 do not come into operation, and ensure that boiler (not shown) supplies water
Continuity, improve the applicability and reliability of system.
More specifically, it is arranged on the pipeline that station area's heating system 8 and heat exchanger 10 are connect with smoke condensation device 7
There is booster pump 11, overcome pipe resistance, guarantees that heat exchange is gone on smoothly.
More specifically, it is provided with air-introduced machine 74 in the exhaust outlet (not shown) of smoke condensation device 7, can overcome well
Newly-increased device resistance, keeps smoke evacuation more smooth.
More specifically, it is provided with several valves on pipeline, the opening and closing of pipeline is controlled by the valve of pipeline, is effectively mentioned
High safety and flexibility.
As preferred embodiment, sensible heat exchanger 71 and latent heat exchanger 72 are arranged in integral type, so that device is tight
It gathers, occupies little space.
As preferred embodiment, latent heat exchanger 72 and sensible heat exchanger 71 are finned tube, increase heat-transfer surface
Product, keeps heat transfer effect more preferable, energy utilization rate is higher.
As further preferred embodiment, valve is electronic, it can be achieved that automatically controlling, and then realizes long-range control,
Mitigate work load.
As further preferred embodiment, can there are more gas compressors 1 and a smoke condensation device 7 to connect
It connects, the cooling heat exchanger 4 in the cooling system of each gas compressor 1 is connect with boiler (not shown) system, combustion gas compression
(not shown) passes through three-way control valve 6 and connect with smoke condensation device 7 at the tail portion smoke evacuation of machine 1, enhances applicability, effectively full
The various operating conditions of more gas compressors of foot, reduce equipment investment.
Waste heat provided in this embodiment using gas compressor provides the technique of station area's heating and production heat, including combustion
Air compressor 1, cooling heat exchanger 4, boiler (not shown) system, smoke condensation device 7 and heat load (area's heating system 8 of standing
And heat exchanger 10), structure setting is reasonable, compact layout；By the way that cooling heat transferring is arranged in the cooling system of gas compressor 1
Device 4, and cooling heat exchanger 4 is connect with boiler (not shown) system, it realizes and the discarded energy in 1 part of gas compressor is returned
It receives, improves the initial temperature of boiler (not shown) water supply, it is more energy saving；It (will not be marked at the tail portion smoke evacuation of gas compressor 1
It is connect out) by three-way control valve 6 with smoke condensation device 7, heat exchange is more able to achieve while improving safety, and will
Smoke condensation device 7 is connect with station area's heating system 8 and heat exchanger 10, it is ensured that is in winter the heating of station area, is in summer
Produced Liquid or wet crude heating, energy utilization rate are higher；By the way that valve is arranged, controllability and safety are effectively increased.
The above is only preferred embodiments of the present invention, are not intended to limit the implementation manners and the protection scope of the present invention, right
For those skilled in the art, it should can appreciate that and all replace with being equal made by description of the invention and diagramatic content
It changes and obviously changes obtained scheme, should all be included within the scope of the present invention.
Claims (8)
1. a kind of utilize gas compressor waste heat for station area's heating technique characterized by comprising it is cold to be set to gas compressor
But the cooling heat exchanger in system, and the entrance and exit of the cooling heat exchanger by pipeline respectively with it is soft in boiler system
Change device to connect with oxygen-eliminating device, the tail portion smoke evacuation of the gas compressor is connect by pipeline with smoke condensation device, and the cigarette
Gas condensing unit is connect by pipeline with station area's heating system and the heat exchanger being set on Produced Liquid or wet crude pipeline, and
The opening and closing of several valve control pipelines is set on pipeline；The smoke condensation device includes sensible heat exchanger and latent heat heat exchange
Device, and the sensible heat exchanger and the latent heat exchanger are integral type setting；The entrance and exit of the sensible heat exchanger point
Not with it is described station area's heating system and the heat exchanger being set on the Produced Liquid or wet crude pipeline outlet and enter
Mouth connection；The entrance and exit of the latent heat exchanger passes through the demineralizer and institute in pipeline and the boiler system respectively
State oxygen-eliminating device connection, and the outlet of the latent heat exchanger also with the sensible heat exchanger and station area's heating system and setting
In the pipeline connection of the heat exchanger connection on the Produced Liquid or wet crude pipeline.
2. according to claim 1 utilize gas compressor waste heat for station area's heating technique, which is characterized in that the combustion gas
Be provided with three-way control valve at the tail portion smoke evacuation of compressor, and three interfaces of the three-way control valve respectively with the gas pressure
The tail gas smoke evacuation of contracting machine, is arranged to the connection of the flue of atmosphere the smoke condensation device.
3. according to claim 1 utilize gas compressor waste heat for station area's heating technique, which is characterized in that the flue gas
Condensing unit further includes condensation water tank, and the condensation water tank is set to the smoke condensation device bottom.
4. according to claim 1 utilize gas compressor waste heat for station area's heating technique, which is characterized in that the sensible heat
Heat exchanger is connect with station area's heating system and the heat exchanger being set on the Produced Liquid or wet crude pipeline
Booster pump is provided on pipeline.
5. according to claim 1 utilize gas compressor waste heat for station area's heating technique, which is characterized in that in the cigarette
Air-introduced machine is provided on the exhaust outlet of gas condensing unit.
6. according to claim 1 utilize gas compressor waste heat for station area's heating technique, which is characterized in that the boiler
By-pass line is provided between the demineralizer and the oxygen-eliminating device in system.
7. according to claim 1 utilize gas compressor waste heat for station area's heating technique, which is characterized in that the latent heat
Heat exchanger and the sensible heat exchanger are one or more combinations of finned tube or other extended surface heat exchanger tubes.
8. according to claim 1 utilize gas compressor waste heat for station area's heating technique, which is characterized in that the valve
For one of manual, electric or pneumatic or a variety of combination.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611265107.4A CN107339687B (en) | 2016-12-30 | 2016-12-30 | It is a kind of to utilize gas compressor waste heat for station area's heating technique |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611265107.4A CN107339687B (en) | 2016-12-30 | 2016-12-30 | It is a kind of to utilize gas compressor waste heat for station area's heating technique |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN107339687A CN107339687A (en) | 2017-11-10 |
| CN107339687B true CN107339687B (en) | 2019-09-06 |
Family
ID=60222378
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201611265107.4A Expired - Fee Related CN107339687B (en) | 2016-12-30 | 2016-12-30 | It is a kind of to utilize gas compressor waste heat for station area's heating technique |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107339687B (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108561939B (en) * | 2018-06-26 | 2023-05-26 | 克拉玛依市科力节能环保技术有限公司 | Waste heat utilization device based on phase change heat exchange technology |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1536293A (en) * | 2003-04-11 | 2004-10-13 | 清华大学 | A dual heat pump combined heat and power system powered by a gas turbine |
| CN202613843U (en) * | 2012-02-24 | 2012-12-19 | 东南大学 | Alternating current and gas engine parallel connection dual-drive heat pump device |
| CN103335445A (en) * | 2013-07-05 | 2013-10-02 | 中国石油集团工程设计有限责任公司 | System and method for utilizing gas-driven compressor waste heat |
| CN205532794U (en) * | 2016-01-20 | 2016-08-31 | 四川村田机械制造有限公司 | Combustion engine system based on improve boiler life -span |
| CN205561332U (en) * | 2016-03-16 | 2016-09-07 | 碧海舟（北京）节能环保装备有限公司 | Refrigerating system is carried to natural gas compressor |
| CN106257158A (en) * | 2016-07-29 | 2016-12-28 | 东南大学 | A kind of hybrid-power combustion-gas thermal pump water-heater system and control method thereof |
-
2016
- 2016-12-30 CN CN201611265107.4A patent/CN107339687B/en not_active Expired - Fee Related
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1536293A (en) * | 2003-04-11 | 2004-10-13 | 清华大学 | A dual heat pump combined heat and power system powered by a gas turbine |
| CN202613843U (en) * | 2012-02-24 | 2012-12-19 | 东南大学 | Alternating current and gas engine parallel connection dual-drive heat pump device |
| CN103335445A (en) * | 2013-07-05 | 2013-10-02 | 中国石油集团工程设计有限责任公司 | System and method for utilizing gas-driven compressor waste heat |
| CN205532794U (en) * | 2016-01-20 | 2016-08-31 | 四川村田机械制造有限公司 | Combustion engine system based on improve boiler life -span |
| CN205561332U (en) * | 2016-03-16 | 2016-09-07 | 碧海舟（北京）节能环保装备有限公司 | Refrigerating system is carried to natural gas compressor |
| CN106257158A (en) * | 2016-07-29 | 2016-12-28 | 东南大学 | A kind of hybrid-power combustion-gas thermal pump water-heater system and control method thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| CN107339687A (en) | 2017-11-10 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101900347B (en) | System for high-grade recycling waste heat of smoke discharged from boiler of power station | |
| CN101769594B (en) | Flue gas total-heat recovery device of gas boiler | |
| CN107120714B (en) | A year-round comprehensive utilization energy-saving system | |
| CN201662226U (en) | Condensing gas heating water heater | |
| CN109737440B (en) | Boiler flue gas deep waste heat recovery system and method | |
| CN104481611A (en) | Dead steam waste heat recovery system based on large temperature difference heat exchange technology | |
| CN104913294B (en) | A kind of power plant boiler smoke waste heat recovery system | |
| CN201779684U (en) | High-grade recycling system for exhaust heat of power station boiler | |
| CN201637072U (en) | Pulsating heat pipe condensing gas water heater | |
| CN203744519U (en) | Multifunctional phase-change cooler | |
| CN107345656A (en) | A kind of steam raising plant using residual heat from boiler fume | |
| CN107339687B (en) | It is a kind of to utilize gas compressor waste heat for station area's heating technique | |
| CN103954039B (en) | Device and method for recycling smoke condensate heat energy of gas boiler in heat pumping mode | |
| CN211502980U (en) | Heating device capable of cooling reaction liquid and recycling waste heat | |
| CN204756887U (en) | High -efficient hot media water system of circulating fluidized bed boiler | |
| CN202501626U (en) | Heat transfer oil furnace internal circulation waste heat recovery device with thermostat | |
| CN216790153U (en) | Flue gas waste heat utilization system that many operation modes switch | |
| CN206755129U (en) | A kind of steam raising plant using residual heat from boiler fume | |
| CN201488165U (en) | Solar central air conditioner | |
| CN212778764U (en) | Single-air-duct heat pipe heat recovery device | |
| CN205537195U (en) | Straight touch heat exchange device | |
| CN204214136U (en) | Heat conducting oil boiler waste heat recovery device | |
| CN202494216U (en) | Heat-recovery steam-heating air treatment unit | |
| CN2791495Y (en) | Boiler chimney residual heat recovery device | |
| CN100520268C (en) | Fume-fume hot pipe heater exchanger for fume desulphurization in heat-engine plant |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| 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: 20190906 |