CN208887391U - Temperature wave ejector half electric heating fusion apparatus waste heat recycling system - Google Patents
Temperature wave ejector half electric heating fusion apparatus waste heat recycling system Download PDFInfo
- Publication number
- CN208887391U CN208887391U CN201821026925.3U CN201821026925U CN208887391U CN 208887391 U CN208887391 U CN 208887391U CN 201821026925 U CN201821026925 U CN 201821026925U CN 208887391 U CN208887391 U CN 208887391U
- Authority
- CN
- China
- Prior art keywords
- heat
- flue
- high temperature
- flue gas
- phase
- 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
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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/25—Process efficiency
Landscapes
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
Abstract
The utility model discloses a kind of temperature wave ejector half electric heating fusion apparatus waste heat recycling system, comprising: smelting furnace, at least two high temperature Heat Rooms in parallel being connected respectively by the first rank flue with the smoke discharging pipe of smelting furnace, at least two phase-change heat-exchangers being correspondingly connected with respectively by second-order flue and at least two high temperature Heat Rooms and at least two waste-heat recovery devices being correspondingly connected with respectively by third rank flue and at least two phase-change heat-exchangers.Phase-change heat-exchanger includes heat exchanger body, the hot fume entrance for being set to heat exchanger body roof, several phase change material devices being set in heat exchanger body and the secondary flue gas for being set to heat exchanger body bottom wall outlet, hot fume entrance is connected by second-order flue with an exhanst gas outlet of high temperature Heat Room, and second-order valve is provided on second-order flue.
Description
Technical field
The utility model relates to a kind of heat energy recycling system more particularly to a kind of flue gas step recycling systems.
Background technique
Electric furnace generally fluctuates between 200~1000 DEG C in the fume afterheat temperature generated in purified steel class process, output
Flue-gas temperature it is unstable, waste heat boiler mainly used to the recycling of its waste heat at present, however waste heat boiler is to entering cigarette in it
The temperature range requirements of gas are narrow, and 200~1000 DEG C of electric furnace flue gas of temperature fluctuation is excessive, it will cause waste heat boiler non-
It operates normally, also results in the unstable of steam production, influence subsequent quality of steam requirement.
Therefore it is made it stable to need to be adjusted the flue-gas temperature of output using the fume afterheat of electric furnace smelting,
This just needs corresponding a set of equipment or other technologies to make up the temperature difference.And it there are no corresponding technical solution in the prior art
Report.
A kind of electrolytic aluminium factory waste heat step recovering system as disclosed in Chinese patent application the 201711021181.6th and
Recovery method, including water resource heat pump, high temperature compressed air heat exchanger, high temperature oil heat exchanger and the height being sequentially connected in series by pipeline
Warm flue gas heat-exchange unit, water resource heat pump input tap water at normal temperature by water pump, and the outlet output of high-temperature flue gas heat exchanger is connected to storage
Water tank；The cooling water system of the air compressor of water resource heat pump and electrolytic aluminium factory carries out heat exchange connection, high temperature compressed air heat exchange
Device and air compressor house high temperature compressed air pipeline carry out heat exchange connection, the high temperature oil pipe line of high temperature oil heat exchanger and dry computer room into
The high temperature flue gas pipeline of row heat exchange connection, high-temperature flue gas heat exchanger and Tan Su subsidiary factory hot Media Oven carries out heat exchange connection.However, this is specially
The excessive flue gas of the electrolytic aluminium factory waste heat step recovering system and unresolved temperature fluctuation that benefit application discloses, it will cause system non-
The problem of normal operation.
A kind of for another example side for smelting iron exhaust heat stepped recycling of Chinese patent application the 201210337277.4th announcement
Method, step recycling and classified utilization process including different low-grade ironmaking waste heats, comprising: successively by the raw coke oven gas from blast furnace
The dedusting of dry method action of low-voltage pulse is carried out by coal gas dry method dust-remover, then becomes blast furnace gas after the power generation of waste pressure turbine machine, finally
Cold water is set to enter coal gas afterheat heat exchanger recovery waste heat；By dedusting wind successively after dedusting wind deduster dedusting, cold water, which enters, to be removed
Dirt wind afterheat heat exchanger recovery waste heat；After gas chamber, enter Combustion of Hot Air Furnace generation hot wind all the way makes blast furnace gas for blast furnace
With another way enters waste heat boiler afterburning, and the high temperature and high pressure steam of generation does work through compressing expansion machine drives electrical power generators；It will
Blast furnace cinder is first granulated into grain slag through bath granulator bath, then after slag separation device separates slag, into sedimentation basin,
Grain slag waste heat flash vessel is set above sedimentation basin, and warm water is heated through sedimentation basin, subsequently into grain slag waste heat flash vessel evaporative condenser
For high temperature water；Hot-blast stove fume is entered into low-temperature flue gas heat exchanger after coal gas heat exchange of heat pipe, further heating comes from water
The high temperature water of slag waste heat flash vessel；In dedusting cover inner surface, dust excluding hood afterheat heat exchanger is set.However, the patent application discloses
The exhaust heat stepped recycling of ironmaking method and the excessive flue gas of unresolved temperature fluctuation, it will lead to system abnormal running
The problem of.
For another example the off-gas recovery processing of a kind of Aluminum smelting furnace of Chinese patent application the 201720225831.8th announcement
Device is related to Aluminum smelting equipment field, including smelting furnace, water tank, dust collecting box, pernicious gas processing pond and white lime pond, melts
Cooling water pipe is wound on furnace outer wall, smelting furnace top is connected with flue, and flue passes through water tank, water tank rear
Flue bottom end is communicated with a cavity, and empty lumenal levels are separated with filter screen, and cavity is connected to by hose with smelting furnace, You Haiqi
Body processing pond and white lime pond are inside and outside double-layer structure, are connected with hot water between the cavity in water tank and pernicious gas processing pond
Pipe, is equipped with communicating pipe between pernicious gas processing pond and the cavity in white lime pond, the cavity in white lime pond and cooling water pipe into
Cold water pipe is communicated between the mouth of a river.However, the off-gas recovery processing unit for the Aluminum smelting furnace that the patent application discloses fails to fill
Divide the thermal energy of the high-temperature flue gas generated using aluminium melting, it is larger to environmental thermal pollution.
Therefore it provides one kind can overcome the shortcomings of the prior art, provide a kind of structure it is simple, it is easy to use, have
The electric heating fusion apparatus flue gas step that the temperature difference for making up and adjusting temperature fluctuation flue gas, the operational safety of effect are stable recycles
System becomes urgent problem in the industry.
Summary of the invention
It is simple, easy to use that the purpose of the utility model is to provide a kind of structures, effectively makes up and adjust the temperature of flue gas
Difference makes the flue gas step recycling system that residual heat system operational safety is stable.
To achieve the goals above, the utility model provides a kind of temperature wave ejector half electric heating fusion apparatus waste heat recycling
Utilize system, comprising: smelting furnace, smelting furnace include: to enter including burner hearth, the feed inlet for the end wall for being set to burner hearth and air
Mouthful, at least two groups electric heater from one end wall of burner hearth to the inner cavity of burner hearth that extend from, set on burner hearth another end wall discharge port,
And the high-temperature flue gas outlet of the roof set on burner hearth, high-temperature flue gas outlet are connected with smoke discharging pipe.The temperature of the utility model
Wave type electric heating fusion apparatus waste heat recycling system further includes the row for passing through the first rank flue and smelting furnace respectively
At least two high temperature Heat Rooms in parallel that smoke pipeline is connected are changed by second-order flue and at least two high temperature respectively
At least two phase-change heat-exchangers and pass through third rank flue and at least two phase-change heat-exchanges respectively that hot cell is correspondingly connected with
At least two waste-heat recovery devices that device is correspondingly connected with；Wherein, high temperature Heat Room includes: high temperature Heat Room ontology, is set to height
The high-temperature flue gas entry of warm Heat Room ontology roof and an exhanst gas outlet for being set to high temperature Heat Room ontology bottom wall are high
Heat transferring medium is filled in the inner cavity of warm Heat Room ontology, the high-temperature flue gas entry of high temperature Heat Room passes through the first rank flue
It is connected with the high-temperature flue gas outlet of smelting furnace the high-temperature flue gas in smelting furnace to be delivered in high temperature Heat Room and is situated between with heat exchange
Matter exchanges heat, and the first rank valve is provided on the first rank flue；Phase-change heat-exchanger includes heat exchanger body, is set to and changes
The hot fume entrance of hot device ontology roof, several phase change material devices being set in heat exchanger body and being set to change
The secondary flue gas of hot device ontology bottom wall exports, and hot fume entrance passes through a flue gas of second-order flue and high temperature Heat Room
Outlet is connected so that exchange heat through high temperature Heat Room flue gas to be delivered in phase-change heat-exchanger and carries out secondary heat exchange, second-order
Second-order valve is provided on flue；Waste-heat recovery device includes: furnace body, is formed in the intracorporal flue of furnace and setting
Coil heat exchanger in flue, the both ends of flue are respectively formed as smoke inlet three times and three times exhanst gas outlet, waste heat recycling
The smoke inlet three times of device is connected by the secondary flue gas outlet of third rank flue and phase-change heat-exchanger with will be through two
The flue gas of secondary heat exchange is introduced into waste-heat recovery device to be exchanged heat three times, and third rank valve is provided on third rank flue.
It selectively, further include set on the smoke distributing chamber between high temperature Heat Room and phase-change heat-exchanger, smoke distributing chamber
Including at least three into cigarette entrance and at least three smoke evacuation outlet, an exhanst gas outlet of at least two high temperature Heat Rooms respectively with
Smoke distributing chamber is connected into cigarette entrance by fourth order flue, the hot fume entrance point of at least two phase-change heat-exchangers
It does not export with the smoke evacuation of smoke distributing chamber and is connected by second-order flue, wherein fourth order flue is equipped with the
Quadravalence valve.
It selectively, further comprise the bypass flue pipe being connected with the smoke discharging pipe of smelting furnace and smoke distributing chamber
Road, bypass flue pipeline are equipped with bypath valve.
Selectively, high temperature exchange heat indoor heat transferring medium loading be high temperature Heat Room volume 80%~
90%, heat transferring medium is the porous ceramic ball that surface is coated with sodium sulphate.
Selectively, several phase change material devices are respectively set to the inner wall of heat exchanger body, phase change material device
It is set as the circular tube shaped metal bar that outer surface is equipped with several heat exchange fins, the inside of the circular tube shaped metal bar of phase change material device is filled out
Filled with phase-change thermal storage medium.
Preferably, every group of electric heater group in smelting furnace includes at least five electric heaters, and the length of electric heater is
2nd/5th to three/8ths of smelting furnace longitudinal length.
Selectively, phase-change thermal storage medium is the alloy that phase transition temperature is 500~650 DEG C, it is preferable that phase-change thermal storage medium
It may be set to silico-aluminum.
Preferably, if the inner wall of phase-change heat-exchanger is equipped with the alternate dry flue gas directing plate being arranged at random and makes phase-change heat-exchanger
The flue gas inside flowed through is uniformly contacted with phase change material device.
Preferably, which further comprises being set to phase transformation
At least two heat-exchanging chambers between heat exchanger and waste-heat recovery device, heat-exchanging chamber include being set in heat-exchanging chamber roof
Warm smoke inlet, the low-temperature flue gas outlet for being set to heat-exchanging chamber bottom wall and the heat exchange being filled in inside heat-exchanging chamber are situated between
Matter, the secondary flue gas outlet of medium temperature smoke inlet and phase-change heat-exchanger are connected by the 5th rank flue with by secondary flue gas
It is delivered in heat-exchanging chamber and exchanges heat, low-temperature flue gas outlet and the smoke inlet three times of waste-heat recovery device pass through third rank cigarette
Feed channel is connected, wherein the 5th rank flue is equipped with the 5th rank valve.
Selectively, the loading for the heat exchange medium filled in heat-exchanging chamber be the volume of heat-exchanging chamber 80%~
90%, heat exchange medium is the porous ceramic ball that surface coats sodium nitrate.
Selectively, which further comprises for drying
To the drying room of smelting material, drying room, which is exported by flue gas branch pipe with a smoke evacuation in smoke distributing chamber, to be connected with by portion
Dividing flue gas to be delivered in drying room, heating is to smelting material, and flue gas branch pipe is equipped with branch pipe valve.
Preferably, drying room includes the wet feed entrance for being set to drying room locular wall, drier outlet, is connected with flue gas branch pipe
Logical drying smoke inlet and smoke outlet, wherein the drier outlet of drying room passes through the feed inlet phase of conveying pipeline and smelting furnace
Connection is delivered in smelting furnace with the dried material for obtaining drying smelts.
Selectively, hydrated salt is equipped in coil heat exchanger, the both ends of coil heat exchanger are respectively formed as hydrated salt and enter
Mouthful and the outlet of dehydration salt, the smoke inlet three times of waste-heat recovery device it is secondary by third rank flue and phase-change heat-exchanger
Exhanst gas outlet connection closes salt heat exchange with flowing water in coil heat exchanger will be introduced into flue through the flue gas of secondary heat exchange, goes
Except the crystallization water therein becomes dehydration salt.
Selectively, it is five hydrated sulfuric acid sodium (Na that flowing water, which closes salt, in the coil heat exchanger of waste-heat recovery device2SO4·
5H2O)。
Wherein, the high-temperature flue-gas generated in smelting furnace is fluctuated in 200~1000 degree celsius temperature sections, when in smelting furnace
The high-temperature flue-gas of generation opens at least two high temperature Heat Rooms and smelting furnace connects in 500~1000 degree celsius temperature section
The first rank valve being arranged on the first logical rank flue, closes the bypath valve on bypass flue pipeline, and high-temperature flue gas is logical
After crossing the flue gas that high temperature Heat Room carries out 500 degrees centigrades of primary heat exchange formation, enter phase-change thermal storage dress through smoke distributing chamber
It sets, partial heat is stored in the phase-change thermal storage medium in phase-change heat-exchanger.When the high-temperature flue-gas generated in smelting furnace
In 200~500 degree celsius temperature section, the bypath valve on bypass flue pipeline is opened, closes at least two high temperature Heat Rooms
The first rank valve being arranged on the first rank flue being connected to smelting furnace, high-temperature flue gas by bypass flue pipeline directly into
Enter in smoke distributing chamber, flue gas will be heated by entering back into phase-change heat-exchanger, make up the flue gas temperature difference, make the temperature into waste-heat recovery device
It spends constant.
Selectively, into phase-change heat-exchanger flue gas with become about 300 Celsius after phase-change thermal storage medium secondary heat exchange
The secondary flue gas of degree.
Selectively, secondary flue gas enters heat-exchanging chamber through the 5th rank flue, exchanges heat with heat exchange medium therein
Become 150~180 degrees Celsius of flue gas afterwards, then waste heat recycling dress is entered through third rank flue by low-temperature flue gas outlet
It sets.
Selectively, the hydrated salt in 150~180 degrees Celsius of flue gas and coil heat exchanger in waste-heat recovery device changes
After heat, temperature is down to 50~80 degree of flue gas, through chimney discharge system.
Selectively, waste-heat recovery device can also be steam boiler, and the both ends of coil heat exchanger are respectively formed hot water and enter
Mouth and steam (vapor) outlet, the hot water temperature that the hot water inlet of waste-heat recovery device enters waste-heat recovery device is 92~96 degrees Celsius,
Hot water becomes 110~120 DEG C water steam with flue gas heat exchange in waste-heat recovery device and transfers out outside system from steam (vapor) outlet
Portion.
Selectively, waste-heat recovery device can also be the boiler for being currently used for recovery waste heat.
Preferably, the material smelted in smelting furnace, which is set as the smog discharge temperatures such as metal or ore, can generate larger fluctuation
Fuel, the metal smelted in smelting furnace is one or more of steel, lead, copper or nickel alloy.
Selectively, pass through method between each component of the temperature wave ejector half electric heating fusion apparatus waste heat recycling system
Orchid connection.
The beneficial effects of the utility model are: being provided with the heat exchanger for adjusting flue-gas temperature on (1), fume pipe, work as flue gas
Partial heat is stored in the phase-change thermal storage medium of heat exchanger when temperature is high, when flue-gas temperature is low, heat exchanger is by cigarette
Gas heating, makes up the temperature difference of flue gas, it is excessive to overcome the shortcomings of that smelting furnace smog discharge temperature fluctuates；(2), the cigarette of the utility model
Gas step recycling system can realize that structure is simple based on the boiler for being currently used for recovery waste heat, and heat exchange efficiency is high, maintenance and
Installation does not influence the normal operation of whole system；(3), the flue gas step recycling system of the utility model both absorbs smelting
Pernicious gas, carbon dioxide and the dust of furnace discharge, and the high temperature heat of flue gas is made full use of, final waste-heat recovery device row
Flue-gas temperature out is 50~80 degrees Celsius, and very big limit reduces the thermal pollution to environment；(4), the flue gas step of utility model
Recycling system can in members failure or repair procedures continual normal operation.
Detailed description of the invention
Fig. 1 is the schematic diagram of the temperature wave ejector half electric heating fusion apparatus waste heat recycling system of the utility model.
Fig. 2 is the schematic diagram of another embodiment of the utility model.
Specific embodiment
The embodiments of the present invention are described below in detail, examples of the embodiments are shown in the accompanying drawings, wherein from beginning
Same or similar element or element with the same or similar functions are indicated to same or similar label eventually.Below by ginseng
The embodiment for examining attached drawing description is exemplary, it is intended to for explaining the utility model, and should not be understood as to the utility model
Limitation.
Fig. 1 is please referred to, as a kind of non-limiting embodiment, the temperature wave ejector half electric heating melting of the utility model is set
Standby waste heat recycling system, comprising: the phase-change heat-exchanger 400 and two of high temperature Heat Room 200, two of smelting furnace 100, two
A waste-heat recovery device 600.
Wherein, smelting furnace 100 includes burner hearth 110, is set to the feed inlet 120 of 110 1 end wall of burner hearth, is set to burner hearth
The air intake 130 of 110 1 end walls, from 110 1 end wall of burner hearth to two groups of electric heater groups 140 of 100 internal stretch of smelting furnace,
The high-temperature flue gas outlet 160 of discharge port 150 set on another end wall of burner hearth 110 and the roof set on burner hearth 110.Every group
Electric heater group 140 includes five electric heaters, and the length of electric heater is 5/8ths of 100 longitudinal length of smelting furnace, high
Warm exhanst gas outlet 160 is connected with smoke discharging pipe P.
Two high temperature Heat Rooms 200 are in parallel relationship, pass through the smoke evacuation of the first rank flue L1 and smelting furnace 100 respectively
Pipeline P is connected, and the first rank valve V1 is provided on the first rank flue L1.As shown in Figure 1, high temperature Heat Room 200 includes
High temperature Heat Room ontology 210, the high-temperature flue gas entry 220 for being set to 210 roof of high temperature Heat Room ontology and it is set to heat exchange
Exhanst gas outlet 230 of 210 bottom wall of room ontology is filled with heat transferring medium 240 in the inner cavity of high temperature Heat Room ontology 210,
In, heat transferring medium 240 is the porous ceramic ball that surface coats sodium sulphate, and the loading of heat transferring medium 240 is high temperature Heat Room 200
Volume 85 percent, the high-temperature flue gas as a result, from smelting furnace 100 enter in high temperature Heat Room 200 with heat exchange be situated between
Matter 240 carries out heat exchange.
Phase-change heat-exchanger 400 includes heat exchanger body 410, three phase-change thermal storages being set in heat exchanger body 410 dress
420 are set, the hot fume entrance 430 of 410 roof of heat exchanger body is set to and is set to the two of 410 bottom wall of heat exchanger body
Secondary exhanst gas outlet 440.Three phase change material devices 420 are alternate to be set to inside heat exchanger body 410, each phase-change thermal storage dress
Set the 420 circular tube shaped metal bars that several heat exchange fins 421 are equipped with for outer surface, the circular tube shaped metal bar of phase change material device 421
Inside be filled with phase-change thermal storage medium 422.
Waste-heat recovery device 600 includes furnace body 610, is formed in the intracorporal flue 620 of furnace and is set in flue 620
Coil heat exchanger 630, the both ends of flue 620 are respectively formed smoke inlet 621 and three times exhanst gas outlet 622 three times, and coil pipe changes
Hydrated salt is equipped in hot device 630, the both ends of coil heat exchanger 630 are respectively formed hydrated salt entrance 631 and the outlet of dehydration salt
632, waste-heat recovery device 600 is by closing salt heating for flowing water in coil heat exchanger 630 with the flue gas heat exchange in flue 620
Removing the crystallization water therein becomes dehydration salt, and the exhanst gas outlet three times 622 of waste-heat recovery device 600 is then connected to chimney and will exchange heat
Low-temperature flue gas discharge system afterwards.
It further include smoke distributing chamber 300 and two heat-exchanging chambers 500 as a kind of alternative embodiments, in system.
Wherein, smoke distributing chamber 300 is set between high temperature Heat Room 200 and phase-change heat-exchanger 400, as shown in Figure 1, flue gas
Distributor chamber 300 includes into cigarette entrance 310 and smoke evacuation outlet 320, an exhanst gas outlet 230 difference of two high temperature Heat Rooms 200
With being connected into cigarette entrance 310 by fourth order flue L4 for smoke distributing chamber 300, fourth order flue L4 is equipped with
Fourth order valve V4, the hot fume entrance 430 of two phase-change heat-exchangers 400 export 320 with the smoke evacuation of smoke distributing chamber 300 respectively
It is connected by second-order flue L2, second-order flue L2 is equipped with second-order valve V2.
In the non-limiting embodiment, it is additionally provided with and 300 phase of the smoke discharging pipe P of smelting furnace 100 and smoke distributing chamber
The bypass flue pipeline LP of connection, bypass flue pipeline are equipped with bypath valve VP.
Heat-exchanging chamber 500 includes: the medium temperature smoke inlet 510 for being set to 500 roof of heat-exchanging chamber, is set to heat-exchanging chamber
The heat exchange medium 530 that the low-temperature flue gas of 500 bottom walls exports 520 and is filled in inside heat-exchanging chamber 500, in the embodiment party
In formula, the loading of heat exchange medium 530 is the 85% of the volume of heat-exchanging chamber, and heat exchange medium is that surface coats sodium nitrate
Porous ceramic ball.The secondary flue gas of medium temperature smoke inlet 510 and phase-change heat-exchanger 400 outlet 410 passes through the 5th rank flue
L5 is connected, and exchanges heat so that secondary flue gas is delivered in heat-exchanging chamber 500, and low-temperature flue gas outlet 520 is recycled with waste heat
The smoke inlet three times 621 of device 600 is connected by third rank flue L3, wherein is set on the 5th rank flue L5
There are the 5th rank valve V5, third rank flue L3 to be equipped with third valve V3.
As another alternative embodiments, system is additionally provided with for drying the drying room 700 to smelting material, is dried
Room 700 is connected by flue gas branch pipe LB with second-order flue L2, and flue gas branch pipe LB is equipped with branch pipe valve VB.
In the non-limiting embodiment, drying room 700 include be set to 700 locular wall of drying room wet feed entrance 710,
Drier outlet 720, with the flue gas branch pipe LB drying smoke inlet 730 being connected to and smoke outlet 740, wherein drying room 700 it is dry
Material outlet 720 is connected by conveying pipeline (not shown) with the feed inlet 120 of smelting furnace 100, thus the drying that drying is obtained
Material, which is delivered in smelting furnace 100, to be smelted.
It should be noted that in the non-limiting embodiment, the phase change material device 420 of phase-change heat-exchanger 400 is
Outer surface is equipped with the circular tube shaped metal bar of several heat exchange fins, but is not limited thereto system, the phase-change thermal storage of phase-change heat-exchanger 400
Device 420 can also be equipped with the hollow metal plate of several heat exchange fins for outer surface.
A kind of non-limiting embodiment according to the present utility model, in the process of running, the temperature from smelting furnace 100
For the biggish flue gas of 200~1000 degrees Celsius of temperature fluctuations, two high temperature Heat Rooms 200 are initially entered, when flue-gas temperature is
At 500 degrees Celsius or more, high temperature Heat Room 200 absorbs flue gas heat accumulation of heat, high when flue-gas temperature is 500 degrees Celsius or less
Warm Heat Room 200 is to flue gas heat release, so that the flue-gas temperature flowed out from high temperature Heat Room 200 is constant to maintain 500 degrees Celsius of left sides
It is right.When one of damage of two high temperature Heat Rooms 200, one of high temperature Heat Room 200 can be only used, to another
A carry out repair and replacement, the operation without influencing whole system.When two high temperature Heat Rooms 200 break down, valve is closed
Door V1, Open valve VP, so that flue gas be made to flow into smoke distributing chamber 300 through bypass flue pipeline LP.In a kind of non-limiting reality
It applies in mode, the utility model uses two groups of phase-change heat-exchangers 400, heat-exchanging chamber 500 and waste-heat recovery device 600, when wherein
When one group of phase-change heat-exchanger 400, heat-exchanging chamber 500 and waste-heat recovery device 600 are in accumulation of heat working condition, another group of phase inversion
Hot device 400, heat-exchanging chamber 500 and waste-heat recovery device 600 are then in heat release working condition.Pass through opening for control respective valves
It closes, the respective valves V2 as closed the one group of phase-change heat-exchanger 400 in left side, heat-exchanging chamber 500 and waste-heat recovery device 600 in Fig. 1
And V8, V3, V5, VB are opened, simultaneously close off the one group of phase-change heat-exchanger 400 in right side in Fig. 1, heat-exchanging chamber 500 and waste heat recycling dress
Set 600 respective valves V8, VB and open V2, V5, V3 so that two groups of equipment accumulation of heat working condition and heat release working condition it
Between exchange-column shift.To which the high-temperature flue gas of 500 degrees centigrades from smoke distributing chamber 300 is followed by accumulation of heat work
Make one group of phase-change heat-exchanger 400, heat-exchanging chamber 500 and the waste-heat recovery device 600 of state, flue gas carries out respectively with heat storage medium
Become about 60 degrees Celsius of low-temperature flue gas after heat exchange and is emitted into chimney (not shown).Cold air from blower (not shown) is then
Another group of waste-heat recovery device 600, heat-exchanging chamber 500 and the phase of heat release state are in by cool air inlet 810
Become heat exchanger 400, the high temperature air that cold air and heat storage medium carry out becoming after heat exchange respectively about 400 degrees Celsius is delivered to baking
For drying ore in dry chamber 700.
According to a kind of alternative embodiments, cancel flue gas branch pipe LB and two groups of phase-change heat-exchangers 400, heat-exchanging chambers
500 and waste-heat recovery device 600, directly adopt waste heat boiler, waste heat boiler includes Heat Room and set on indoor change that exchange heat
Hot coil.High-temperature flue gas entry is arranged in one end of Heat Room, and the other end is arranged low-temperature flue gas and exports, and high-temperature flue gas entry passes through pipe
Line is connected to the smoke evacuation of smoke distributing chamber 300 outlet 320, and low-temperature flue gas outlet is connected to chimney.One end of heat exchange coil is formed
Cold water inlet, the other end form steam (vapor) outlet.So as to use waste heat boiler to provide steam using fume afterheat for user.
Fig. 2 is another embodiment of the present invention, in addition to not using heat-exchanging chamber 500 and waste-heat recovery device 600, remaining
It constructs roughly the same with the embodiment of Fig. 1.
Although preferred embodiments of the present invention have been described in detail herein, it is to be understood that the utility model is not
It is confined to the specific structure be described in detail and shown here and step, without departing from the spirit and scope of the present invention may be used
Other modifications and variant are realized by those skilled in the art.In addition, the parameters such as volume, temperature in the utility model can be with
It is suitably chosen in range disclosed in the utility model according to concrete application conditions.
Claims (6)
1. a kind of temperature wave ejector half electric heating fusion apparatus waste heat recycling system, comprising:
Smelting furnace, the smelting furnace include: burner hearth, be set to the burner hearth an end wall feed inlet and air intake, from institute
State at least two groups electric heater group that one end wall of burner hearth extends to the inner cavity of the burner hearth, another end wall set on the burner hearth
The high-temperature flue gas outlet of discharge port and the roof set on the burner hearth, the high-temperature flue gas outlet are connected with smoke discharging pipe；
It is characterized in that, further including being connected respectively by the first rank flue with the smoke discharging pipe of the smelting furnace
At least two high temperature Heat Rooms in parallel and pass through second-order flue and at least two high temperature Heat Rooms pair respectively
At least two phase-change heat-exchangers that should be connected；Wherein, the high temperature Heat Room include: high temperature Heat Room ontology, be set to it is described
The high-temperature flue gas entry of high temperature Heat Room ontology roof and a flue gas for being set to the high temperature Heat Room ontology bottom wall go out
Mouthful, heat transferring medium is filled in the inner cavity of the high temperature Heat Room ontology, the high-temperature flue gas entry of the high temperature Heat Room passes through
The first rank flue is connected with the high-temperature flue gas outlet of the smelting furnace, sets on the first rank flue
It is equipped with the first rank valve；The phase-change heat-exchanger includes heat exchanger body, the hot fume for being set to the heat exchanger body roof
Entrance, several phase change material devices being set in the heat exchanger body and it is set to the heat exchanger body bottom wall
Secondary flue gas outlet, the hot fume entrance passes through a flue gas of the second-order flue and the high temperature Heat Room
Outlet is connected, and is provided with second-order valve on the second-order flue.
2. temperature wave ejector half electric heating fusion apparatus waste heat recycling system as described in claim 1, which is characterized in that also
Including the smoke distributing chamber being set between the high temperature Heat Room and the phase-change heat-exchanger, the smoke distributing chamber includes at least
Three into cigarette entrance and at least two smoke evacuations outlet, an exhanst gas outlet of at least two high temperature Heat Rooms respectively with it is described
Smoke distributing chamber is connected into cigarette entrance by fourth order flue, and the hot fume of at least two phase-change heat-exchangers enters
Mouth is exported with the smoke evacuation of the smoke distributing chamber respectively to be connected by the second-order flue, wherein the fourth order
Flue is equipped with fourth order valve.
3. temperature wave ejector half electric heating fusion apparatus waste heat recycling system as claimed in claim 2, which is characterized in that into
One step includes being connected with one of them of the smoke discharging pipe of the smelting furnace and the smoke distributing chamber into cigarette entrance
Bypass flue pipeline, the bypass flue pipeline are equipped with bypath valve.
4. temperature wave ejector half electric heating fusion apparatus waste heat recycling system according to any one of claims 1 to 3,
Be characterized in that, the high temperature exchange heat the indoor heat transferring medium loading be the high temperature Heat Room volume 80%~
90%, the heat transferring medium is the porous ceramic ball that surface is coated with sodium sulphate.
5. temperature wave ejector half electric heating fusion apparatus waste heat recycling system according to any one of claims 1 to 3,
It is characterized in that, several described phase change material devices are respectively set to the inner wall of the heat exchanger body, the phase-change thermal storage
Device is set as the circular tube shaped metal bar that outer surface is equipped with several heat exchange fins, the circular tube shaped metal bar of the phase change material device
Inside be filled with phase-change thermal storage medium.
6. temperature wave ejector half electric heating fusion apparatus waste heat recycling system according to any one of claims 1 to 3,
It is characterized in that, further comprises for drying the drying room to smelting material, the drying room passes through flue gas branch pipe and described the
Second order flue is connected, and the flue gas branch pipe is equipped with branch pipe valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821026925.3U CN208887391U (en) | 2018-07-01 | 2018-07-01 | Temperature wave ejector half electric heating fusion apparatus waste heat recycling system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821026925.3U CN208887391U (en) | 2018-07-01 | 2018-07-01 | Temperature wave ejector half electric heating fusion apparatus waste heat recycling system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208887391U true CN208887391U (en) | 2019-05-21 |
Family
ID=66506055
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821026925.3U Expired - Fee Related CN208887391U (en) | 2018-07-01 | 2018-07-01 | Temperature wave ejector half electric heating fusion apparatus waste heat recycling system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208887391U (en) |
-
2018
- 2018-07-01 CN CN201821026925.3U patent/CN208887391U/en not_active Expired - Fee Related
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN109141042A (en) | Temperature wave ejector half electric heating fusion apparatus flue gas step recycling system | |
| CN102062534B (en) | Method and device for heat supply of rotary hearth furnace | |
| CN201203263Y (en) | Tube arranging type hot-air stove | |
| CN102607010B (en) | Composite phase-change heat exchange system | |
| CN107525090B (en) | Come into operation the coal-fired power station boiler device and its application method of denitrating system when a kind of igniting | |
| CN208606602U (en) | Electric heating fusion apparatus flue gas step recycling system | |
| CN106969638A (en) | Rotary hearth furnace fume afterheat gradient utilization system and application method | |
| CN105135468B (en) | Smoke waste heat utilization system | |
| CN205316352U (en) | RTO system with tail gas waste heat recovery function | |
| CN101979951B (en) | Dry dedusting and sensible heat recovery system for electric furnace flue gas | |
| CN202691996U (en) | Pure medium temperature heat recovery boiler at cement kiln back end | |
| CN101261008B (en) | Liquid phase intermediate medium heat exchanging type heat exchanger | |
| CN103063044B (en) | Rotary hearth furnace smoke waste heat utilization system and rotary hearth furnace fume afterheat Application way | |
| CN208887391U (en) | Temperature wave ejector half electric heating fusion apparatus waste heat recycling system | |
| CN108823352A (en) | A kind of converter gas dry type waste heat recycling dust-extraction unit and method | |
| CN117190722A (en) | System and method for recycling waste heat of high-temperature steel billet based on phase change heat storage | |
| CN110860378A (en) | Hot air blowing system for electric dust remover | |
| CN201206829Y (en) | Liquid phase intermediate medium heat exchanging type heat exchanger | |
| CN110822928A (en) | Heat accumulating type waste heat utilization device and system for carbon single furnace and control method | |
| CN202660525U (en) | Composite phase-change heat exchange system | |
| CN205223311U (en) | Collection device to cast iron pipe annealing kiln gas | |
| CN204901732U (en) | Modular waste heat of boiler flue gas recovery system | |
| CN105318735B (en) | A kind of utilization sintering low temperature waste heat cools down the device of circulation water of blast furnace | |
| CN112097287B (en) | Boiler energy-saving and flue gas whitening system, process and application | |
| CN206724722U (en) | Rotary hearth furnace fume afterheat gradient utilization system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20190521 Termination date: 20210701 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |