CN206463745U - A kind of device based on hollow ceramic membranes recovered flue gas moisture and waste heat - Google Patents
A kind of device based on hollow ceramic membranes recovered flue gas moisture and waste heat Download PDFInfo
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- CN206463745U CN206463745U CN201621369690.9U CN201621369690U CN206463745U CN 206463745 U CN206463745 U CN 206463745U CN 201621369690 U CN201621369690 U CN 201621369690U CN 206463745 U CN206463745 U CN 206463745U
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- Prior art keywords
- hollow ceramic
- vacuum
- pipe
- heat exchange
- flue
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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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/30—Technologies for a more efficient combustion or heat usage
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- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model belongs to a kind of device based on hollow ceramic membranes recovered flue gas moisture and waste heat in energy saving for power plants field.The device is formed by connecting by hollow ceramic membrane module, vacuum system and heat exchange condenser system by valve, pipeline;It is staggered in arrangement by many hollow ceramic membranes in rectangular flue, constitutes hollow ceramic membrane module, hollow ceramic membranes upper and lower side is fixed on the flue left and right sides;It is connected on the upside of flue with vacuum reducing pipe, reducing pipe is connected by vacuum pipe with heat exchange condenser system;Heat exchange condensation pipe system has heat exchange pipeline, vavuum pump and drainage pipeline;Vavuum pump makes to form vacuum outside ceramic membrane, and by adjusting valve regulation vacuum so that vapor is formed inside and outside earthenware to be recovered outside proper pressure differential, vapor permeation outlet pipe.The utility model has good spontaneity, and high-efficiency environment friendly, recyclable thermal power plant's smoke evacuation moisture, the rate of recovery is up to 55%.Thermal power plant's water saving purpose is reached, while Mist heat recovering, is energy saving for power plants.
Description
Technical field
The utility model is related to a kind of device based on hollow ceramic membranes recovered flue gas moisture and waste heat, is particularly suitable for use in back
Vapor and waste heat in power plant boiler smoke evacuation are received, belongs to the energy-conserving and emission-cutting technology field in thermal power plant.
Background technology
Coal-burning boiler smoke evacuation moisture average value about 10%, gas fired-boiler discharges fume moisture average value more than 15%.By 2013
Year statistics, about 10.1 hundred million tons/year of total emission volumn of China's fired power generating unit flue gas moisture year, and thermoelectricity water total amount about 84.4 hundred million
Ton/year, about 3.9255 hundred million tons/year of wastewater emission amount.As can be seen here, there is great lot of water resources in China with coal steam-electric plant smoke every year
It is discharged into air, is used if adopting an effective measure and reclaiming this part water resource electric power supply plant, then energy-conservation aspect is received every year for power plant
Benefit is considerable.
Have a large amount of on being reduced using heat exchanger below flue-gas temperature to dew-point temperature so as to recovered flue gas both at home and abroad
The research of waste heat and condensate.As a kind of new " green technology ", membrane separating method also grades neck in dehumidification and recycle-water
Domain obtains more and more widely paying close attention to.But the membrane separating and trapping moisture studied at present focus mostly in the research of organic film.Have
There are high water vapor infiltration coefficient and preferable vapor and nitrogen separation machine film more.But all in all, the infiltration of organic film
Flux is much lower than inoranic membrane.For in-situ processing big flow gas, inoranic membrane has bigger application potential.Porous ceramics
Film belongs to inoranic membrane, and it shows the stability of height under high temperature and acid or alkali environment and microbial attack environment.It is this steady
It is qualitative to cause it to possess very strong applicability under this complex environment of power-plant flue gas.
Domestic applied there is presently no hollow ceramic membrane technology is furtherd investigate in the recovery of coal steam-electric plant smoke moisture.
Utility model content
The purpose of this utility model is to provide a kind of device based on hollow ceramic membranes recovered flue gas moisture and waste heat, and it is special
Levy and be:The device by hollow ceramic membrane module, vacuum system and heat exchange condenser system, and by valve, vacuum breaker,
Vacuum pipe, heat exchange pipeline, drainage pipeline etc. are formed by connecting;It is staggered in arrangement by many hollow ceramic membranes in rectangular flue, group
Into hollow ceramic membrane module, hollow ceramic membranes upper and lower side is fixed on the flue left and right sides respectively, and contact surface uses high temperature resistant rubber
Plug is sealed;It is connected on the upside of flue with vacuum reducing pipe, reducing pipe passes through vacuum pipe and heat exchange condenser system phase
Even;Heat exchange condensation pipe system has heat exchange pipeline, band regulating valve vavuum pump and with valve drainage pipeline;Vavuum pump makes hollow pottery
Vacuum is formed outside porcelain film, and passes through vacuum conditions valve regulation vacuum size so that vapor is formed inside and outside hollow ceramic pipe
Suitable pressure difference, vapor is recovered by being permeated in pipe outside outlet pipe.
The device based on empty ceramic membrane recovered flue gas moisture and waste heat, it is characterised in that:Flue gas flows through rectangular flue,
Into in hollow ceramic pipe;Vavuum pump is started working simultaneously, and by using vacuum breaker in whole rectangular flue (i.e. institute
Have on the outside of hollow ceramic pipe) cause suitable vacuum so that and hollow ceramic pipe is inside and outside to have pressure differential;Vapor is in pressure in flue gas
Hollow ceramic membranes are passed through in the presence of difference, due to control pressure difference maintain have compared with fractional value and ceramic membrane it is stronger hydrophilic
Other components in property, flue gas are more difficult to pass through hollow ceramic membranes;Vapor into reducing pipe is in the presence of pressure differential, from true
Dead end flows to heat exchange condenser system;Vapor is condensed into aqueous water and into heat-exchange system in heat exchange condenser system
Cold end discharges latent heat;Moisture and its latent heat are recycled in last flue gas.
The beneficial effects of the utility model are:The recyclable thermal power plant's smoke evacuation moisture of the utility model, the rate of recovery is reached as high as
55%.Thermal power plant's water saving purpose is reached, while recovery section fume afterheat resource, is energy saving for power plants.
Brief description of the drawings
Fig. 1 is the flue gas moisture waste-heat recovery device structural representation of hollow ceramic membranes;
Fig. 2 is assembling schematic diagram of the hollow ceramic membrane module in flue;
Fig. 3 is that schematic diagram is fixed at hollow ceramic membranes two ends.
Number explanation:1 is hollow ceramic membranes, and 2 be hollow ceramic membrane module, 3 reducing pipes, and 4 be vacuum pipe, and 5 be heat friendship
Condenser system is changed, 6 be vavuum pump, and 7 be regulating valve, and 8 be valve, and 9 be drainage pipeline, and 10 be heat exchange pipeline, and 11 be that high temperature resistant is close
Seal.
Embodiment
The utility model provides a kind of device based on hollow ceramic membranes recovered flue gas moisture and waste heat, with reference to attached
Figure and embodiment are described further to the utility model.
Fig. 1 show the flue gas moisture waste-heat recovery device structural representation of hollow ceramic membranes.The device is by hollow ceramic
Membrane module, vacuum system and heat exchange condenser system, and pass through valve, vacuum breaker, vacuum pipe, heat exchange pipeline, draining
Pipeline is constituted;It is staggered in arrangement by many hollow ceramic membranes 1 in rectangular flue, composition hollow ceramic membrane module 2, hollow ceramic
Film upper and lower side is fixed on the flue left and right sides respectively, and contact surface is sealed using high-temperature resistant rubber plug 11;On the upside of flue with
Reducing pipe 3 is connected, and reducing pipe 3 is connected by vacuum pipe 4 with heat exchange condenser system 5;Heat exchange condensation pipe system 5 is changed
Hot channel 10, the band vavuum pump 6 of regulating valve 7 and with the drainage pipeline 9 of valve 8;Vavuum pump 6 makes the outside of hollow ceramic membranes 1 form vacuum,
And vacuum size is adjusted by vacuum breaker 7 so that vapor manages the inside and outside suitable pressure difference of formation, water in hollow ceramic membranes 1
Steam is recovered by being permeated in pipe outside outlet pipe.
In Fig. 1, flue gas flows through rectangular flue, is managed into hollow ceramic membranes 1 interior;Vavuum pump 6 is started working simultaneously, and is led to
Cross and cause suitable vacuum (on the outside of i.e. all pipes of hollow ceramic membranes 1) in whole rectangular flue using vacuum breaker 7 so that in
Empty ceramic membrane 1 is managed inside and outside with pressure differential;Vapor passes through hollow ceramic membranes 1 in the presence of pressure differential in flue gas, due to control
Pressing pressure difference is maintained compared with fractional value and ceramic membrane has the other components in stronger hydrophily, flue gas are more difficult to pass through hollow pottery
Porcelain film 1;Vapor into reducing pipe 3 flows to heat exchange condenser system 5 in the presence of pressure differential from vacuum end;Vapor
Aqueous water is condensed into heat exchange condenser system 5 and latent heat is discharged to the cold end of heat-exchange system 5;Moisture in last flue gas
And its latent heat is recycled.
Claims (1)
1. a kind of device based on hollow ceramic membranes recovered flue gas moisture and waste heat, it is characterised in that:The device is by hollow ceramic
Membrane module, vacuum system and heat exchange condenser system, and pass through valve, vacuum breaker, vacuum pipe, heat exchange pipeline, draining
Pipeline is formed by connecting;Many hollow ceramic membranes are staggered in arrangement in rectangular flue, constitute hollow ceramic membrane module, hollow ceramic membranes
Upper and lower side is fixed on the flue left and right sides respectively, and contact surface fills in capable sealing using high-temperature resistant rubber;Flue upside and vacuum
Reducing pipe is connected, and reducing pipe is connected by vacuum pipe with heat exchange condenser system;Heat exchange condensation pipe system has heat exchanger tube
Road, band regulating valve vavuum pump and with valve drainage pipeline;Vavuum pump makes to form vacuum outside hollow ceramic membranes, and is adjusted by vacuum
Save valve regulation vacuum size so that vapor forms suitable pressure difference inside and outside hollow ceramic pipe, and vapor in pipe by permeating
Outlet pipe is recovered outside.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621369690.9U CN206463745U (en) | 2016-12-14 | 2016-12-14 | A kind of device based on hollow ceramic membranes recovered flue gas moisture and waste heat |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621369690.9U CN206463745U (en) | 2016-12-14 | 2016-12-14 | A kind of device based on hollow ceramic membranes recovered flue gas moisture and waste heat |
Publications (1)
Publication Number | Publication Date |
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CN206463745U true CN206463745U (en) | 2017-09-05 |
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ID=59712692
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CN201621369690.9U Expired - Fee Related CN206463745U (en) | 2016-12-14 | 2016-12-14 | A kind of device based on hollow ceramic membranes recovered flue gas moisture and waste heat |
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CN (1) | CN206463745U (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106512668A (en) * | 2016-12-14 | 2017-03-22 | 华北电力大学 | Device and method for recovering moisture and waste heat of flue gas on basis of hollow ceramic membranes |
CN107631290A (en) * | 2017-09-14 | 2018-01-26 | 北京建筑大学 | A kind of flue gas waste heat recovery system absorbed based on film |
CN111821802A (en) * | 2019-04-23 | 2020-10-27 | 青岛达能环保设备股份有限公司 | Wet desulphurization white plume and wastewater reduction cooperative treatment system |
-
2016
- 2016-12-14 CN CN201621369690.9U patent/CN206463745U/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106512668A (en) * | 2016-12-14 | 2017-03-22 | 华北电力大学 | Device and method for recovering moisture and waste heat of flue gas on basis of hollow ceramic membranes |
CN107631290A (en) * | 2017-09-14 | 2018-01-26 | 北京建筑大学 | A kind of flue gas waste heat recovery system absorbed based on film |
CN107631290B (en) * | 2017-09-14 | 2019-01-25 | 北京建筑大学 | A kind of flue gas waste heat recovery system absorbed based on film |
CN111821802A (en) * | 2019-04-23 | 2020-10-27 | 青岛达能环保设备股份有限公司 | Wet desulphurization white plume and wastewater reduction cooperative treatment system |
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Date | Code | Title | Description |
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GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170905 Termination date: 20181214 |
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CF01 | Termination of patent right due to non-payment of annual fee |