CN205505820U - Waste gas waste heat recovery device of boiler - Google Patents
Waste gas waste heat recovery device of boiler Download PDFInfo
- Publication number
- CN205505820U CN205505820U CN201620284597.1U CN201620284597U CN205505820U CN 205505820 U CN205505820 U CN 205505820U CN 201620284597 U CN201620284597 U CN 201620284597U CN 205505820 U CN205505820 U CN 205505820U
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- CN
- China
- Prior art keywords
- heat
- heat room
- room
- chamber
- air chamber
- 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.)
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Classifications
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/56—Heat recovery units
Abstract
The utility model discloses a waste gas waste heat recovery device of boiler, the device is including first heat transfer room, second heat transfer room and third heat transfer room, reservoir chamber and air chamber are all split into through the division board to the inner chamber of the inner chamber of first heat transfer room, the inner chamber of second heat transfer room and third heat transfer room, and install the heat transfer fin on the division board, and the both ends of heat transfer fin place respectively in reservoir chamber gentleness indoor, an air compressor is connected to the left end of the air chamber of first heat transfer room, and the 2nd gas compressor is connected to the right -hand member of the air chamber of first heat transfer room, this device is through setting up multi - stage heat exchange device, make exhaust gas of boiler carry out the heat transfer with cold water step by step, can fall to exhaust gas of boiler's final temperature very lowly, and the cold water of heat transfer is unnecessary the flow very fast also, and can get rid of at the harmful substance during the in -process of recovery waste heat is with exhaust gas of boiler, avoid exhaust gas of boiler air pollution, the present invention has higher practical value.
Description
Technical field
This utility model relates to boiler waste gas processing technology field, is specially a kind of boiler waste gas waste heat recovery
Device.
Background technology
Thermal power plant is carrying out thermal power generation when, and the waste gas heat loss of boiler accounts for the percentage of boiler heat loss
70 to percent eight ten, and along with the lengthening of boiler operation time, EGT will be than design
Temperature high ten to percent 2 percent 30, China is thermoelectricity big country, also exist large quantity of exhaust gas temperature high,
The fired power generating unit of making time length, boiler waste gas temperature reaches as high as about 200 degree, newly comes into operation
Coal steam-electric plant smoke also at about 130 degree, is therefore processed by boiler waste gas temperature, can not only
Reduce discharge, reduce matchmaker's consumption, additionally it is possible to be greatly improved energy utilization efficiency, but existing boiler afterheat returns
The most all there is an identical problem in receiving apparatus, that is, uses single-stage heat-exchanger rig heat exchange so that with
The elongated of heat-exchange time, the temperature fall of gas gradually tends to the liquid for heat exchange or the temperature of gas,
If the flow rate being used for the liquid of heat exchange or gas is relatively low, then it is poor to deposit heat energy power, flue-gas temperature
Cannot effectively be lowered, substantial amounts of heat losses, if flow rate is relatively big, need again to provide a large amount of
The colder heat exchanging liquid of temperature or gas, increase substantial amounts of Financial cost, therefore final heat transfer effect is all
Undesirable, and boiler waste gas all contains a large amount of pollutant, existing waste-heat recovery device all can not be right
Boiler waste gas purifies, if it is possible to invention one uses multi-stage heat exchanger mode to carry out heat exchange and in heat exchange
During the novel waste heat retracting device that boiler waste gas can also be purified just can solve the problem that problems,
A kind of device for recovering afterheat of waste gas in boiler is we provided for this.
Utility model content
The purpose of this utility model is to provide a kind of device for recovering afterheat of waste gas in boiler, to solve the above-mentioned back of the body
The problem proposed in scape technology.
For achieving the above object, this utility model provides following technical scheme: a kind of boiler waste gas waste heat returns
Receiving apparatus, described device includes the first Heat Room, the second Heat Room and the 3rd Heat Room, and described first changes
The inner chamber of the inner chamber in hot cell, the inner chamber of the second Heat Room and the 3rd Heat Room is all divided into storage by division board
On hydroecium and air chamber, and division board, heat exchange fin is installed, and the two ends of heat exchange fin are respectively placed in storage
The gentle indoor of hydroecium, the left end of the air chamber of described first Heat Room connects the first air compressor, and first
The right-hand member of the air chamber of Heat Room connects the second gas compressor, and the port of export of described second gas compressor is even
Connect the air chamber of the second Heat Room, and the right-hand member of the air chamber of the second Heat Room connects the 3rd gas compressor, institute
The port of export stating the 3rd gas compressor connects the air chamber of the 3rd Heat Room, the air chamber of described 3rd Heat Room
Right-hand member connect and have on exhaustor, and exhaustor air bleeding valve is installed, described first Heat Room, second change
Hot cell and the 3rd Heat Room are all provided with gas temperature detection sensor, and the at the lower wall of respective air chamber
One Heat Room, the second Heat Room and the 3rd Heat Room are all provided with water temperature inspection at the upper wall of respective reservoir chamber
Surveying sensor, the left end of the reservoir chamber of described first Heat Room connects to have on drain pipe, and drain pipe to be installed
Having drain valve, the right-hand member of the reservoir chamber of described first Heat Room connects the port of export of the second water pump, and second
The entrance point of water pump connects the reservoir chamber of the second Heat Room, and the right-hand member of the reservoir chamber of described second Heat Room is even
Connect the water side of the first water pump, and the entrance point of the first water pump connects the reservoir chamber of the 3rd Heat Room, described
The right-hand member of the reservoir chamber of the 3rd Heat Room connects water inlet pipe, and the lower wall of the air chamber of described first Heat Room is installed
In having monitoring harmful gases device and pressure transducer, and the air chamber of the first Heat Room, catalytic reaction is installed
Device, the lower wall of the air chamber of described second Heat Room is provided with dust investigating and waste sludge discharge valve, and
The upper end of the second Heat Room is provided with controller, and the internally installed of air chamber of described second Heat Room has absorption
Device, described controller is electrically connected with the first gas compressor, gas temperature detection sensor, is harmful to
Gas controlling device, pressure transducer, catalyst reaction device, the second gas compressor, adsorbent equipment,
Waste sludge discharge valve, dust investigating, the 3rd gas compressor, air bleeding valve, the first water pump, the second water
Pump, water temperature detection sensor and drain valve.
Preferably, described adsorbent equipment is electrostatic adsorption device.
Preferably, described division board is heat-conducting metal or thermal conductive ceramic plate.
Preferably, described heat exchange fin is copper coin.
Compared with prior art, the beneficial effects of the utility model are: this utility model is multistage by arranging
Heat-exchanger rig, makes boiler waste gas carry out heat exchange with cold water step by step, it is possible to the final temperature of boiler waste gas dropped
To the lowest, and the cold water of heat exchange also need not flow quickly, and can during recovery waste heat incite somebody to action
Harmful substance in boiler waste gas is removed, it is to avoid boiler waste gas atmosphere pollution, therefore has the highest practicality
It is worth.
Accompanying drawing explanation
Fig. 1 is this utility model structural representation.
In figure: 1 first gas compressor, 2 first Heat Rooms, 3 gas temperatures detection sensors, 4 have
Evil gas controlling device, 5 pressure transducers, 6 catalyst reaction devices, 7 second gas compressors, 8 the
Two Heat Rooms, 9 adsorbent equipments, 10 waste sludge discharge valves, 11 dust investigatings, 12 the 3rd gas compressions
Machine, 13 the 3rd Heat Rooms, 14 exhaustors, 15 air bleeding valves, 16 water inlet pipes, 17 first water pumps, 18
Two water pumps, 19 water temperatures detection sensors, 20 reservoir chambers, 21 drain valves, 22 drain pipies, 23 division boards,
24 heat exchange fins, 25 air chambers, 26 controllers.
Detailed description of the invention
Below in conjunction with the accompanying drawing in this utility model embodiment, to the technology in this utility model embodiment
Scheme is clearly and completely described, it is clear that described embodiment is only this utility model one
Divide embodiment rather than whole embodiments.Based on the embodiment in this utility model, this area is common
The every other embodiment that technical staff is obtained under not making creative work premise, broadly falls into this
The scope of utility model protection.
Referring to Fig. 1, this utility model provides a kind of technical scheme: a kind of device for recovering afterheat of waste gas in boiler,
Device includes the first Heat Room the 2, second Heat Room 8 and the 3rd Heat Room 13, the first Heat Room 2 interior
The inner chamber of chamber, the inner chamber of the second Heat Room 8 and the 3rd Heat Room 13 is all divided into storage by division board 23
On hydroecium 20 and air chamber 25, and division board 23, heat exchange fin 24, and the two of heat exchange fin 24 are installed
End is respectively placed in reservoir chamber 20 and air chamber 25, and the left end of the air chamber 25 of the first Heat Room 2 connects the
One air compressor 1, and the right-hand member of the air chamber 25 of the first Heat Room 2 connects the second gas compressor 7,
The port of export of the second gas compressor 7 connects the air chamber 25 of the second Heat Room 8, and the second Heat Room 8
The right-hand member of air chamber 25 connects the 3rd gas compressor 12, and the port of export of the 3rd gas compressor 12 connects the
The air chamber 25 of three Heat Rooms 13, the right-hand member of the air chamber 25 of the 3rd Heat Room 13 connects exhaustor 14,
And air bleeding valve 15, the first Heat Room the 2, second Heat Room 8 and the 3rd Heat Room are installed on exhaustor 14
13 all the lower wall of respective air chamber 25 be provided with gas temperature detection sensor 3, and the first Heat Room 2,
Second Heat Room 8 and the 3rd Heat Room 13 are all provided with water temperature detection at the upper wall of respective reservoir chamber 20
Sensor 19, the left end of the reservoir chamber 20 of the first Heat Room 2 connects drain pipe 22, and drain pipe 22
On drain valve 21 is installed, the right-hand member of the reservoir chamber 20 of the first Heat Room 2 connects going out of the second water pump 18
Mouthful end, and the entrance point of the second water pump 18 connects the reservoir chamber 20 of the second Heat Room 8, the second Heat Room 8
The right-hand member of reservoir chamber 20 connect the water side of the first water pump 17, and the entrance point of the first water pump 17 connects
The reservoir chamber 20 of the 3rd Heat Room 13, the right-hand member of the reservoir chamber 20 of the 3rd Heat Room 13 connects water inlet pipe
16, the lower wall of the air chamber 25 of the first Heat Room 2 is provided with monitoring harmful gases device 4 and pressure transducer
Catalyst reaction device 6, the air chamber of the second Heat Room 8 are installed in 5, and the air chamber 25 of the first Heat Room 2
The lower wall of 25 is provided with dust investigating 11 and waste sludge discharge valve 10, and the upper end of the second Heat Room 8
Being provided with controller 26, the internally installed of the air chamber 25 of the second Heat Room 8 has adsorbent equipment 9, absorption dress
Putting 9 is electrostatic adsorption device, and division board 23 is heat-conducting metal or thermal conductive ceramic plate, heat exchange fin 24
For copper coin, controller 26 is electrically connected with the first gas compressor 1, gas temperature detects sensor 3,
Monitoring harmful gases device 4, pressure transducer 5, catalyst reaction device the 6, second gas compressor 7,
Adsorbent equipment 9, waste sludge discharge valve 10, dust investigating the 11, the 3rd gas compressor 12, air bleeding valve
15, first water pump the 17, second water pump 18, water temperature detection sensor 19 and drain valve 21, this device exists
The when of work, boiler waste gas is pressed into Heat Room at different levels by each gas compressor the most successively,
Current then enter each reservoir chamber from opposite direction, owing in one-level Heat Room every during whole, temperature is relatively
Low waste gas can carry out heat exchange with the current lower than its temperature all the time, therefore, it is possible to by boiler waste gas
Waste heat recovery more thorough, and also can be by the dust in boiler waste gas with have during heat exchange
Evil gas removes, it is possible to is substantially reduced the pollution to air, therefore has the highest practical value.
Embodiment the most of the present utility model, for the ordinary skill people of this area
For Yuan, it is possible to understand that can be real to these in the case of without departing from principle of the present utility model and spirit
Executing example to carry out multiple change, revise, replace and modification, scope of the present utility model is by claims
And equivalent limits.
Claims (4)
1. a device for recovering afterheat of waste gas in boiler, described device includes the first Heat Room (2), the second heat exchange
Room (8) and the 3rd Heat Room (13), it is characterised in that: the inner chamber of described first Heat Room (2),
The inner chamber of two Heat Rooms (8) and the inner chamber of the 3rd Heat Room (13) are all divided into by division board (23)
On reservoir chamber (20) and air chamber (25), and division board (23), heat exchange fin (24) is installed, and changes
The two ends of hot fin (24) are respectively placed in reservoir chamber (20) and air chamber (25), and described first changes
The left end of the air chamber (25) in hot cell (2) connects the first air compressor (1), and the first Heat Room (2)
The right-hand member of air chamber (25) connect the second gas compressor (7), described second gas compressor (7)
The port of export connects the air chamber (25) of the second Heat Room (8), and the air chamber (25) of the second Heat Room (8)
Right-hand member connect the 3rd gas compressor (12), the port of export of described 3rd gas compressor (12) connects
The air chamber (25) of the 3rd Heat Room (13), the right-hand member of the air chamber (25) of described 3rd Heat Room (13)
Connect to have on exhaustor (14), and exhaustor (14) and air bleeding valve (15) is installed, described first heat exchange
Room (2), the second Heat Room (8) and the 3rd Heat Room (13) are all at the lower wall of respective air chamber (25)
Gas temperature detection sensor (3), and the first Heat Room (2), the second Heat Room (8) and the are installed
Three Heat Rooms (13) are all provided with water temperature detection sensor (19) at the upper wall of respective reservoir chamber (20),
The left end of the reservoir chamber (20) of described first Heat Room (2) connects drain pipe (22), and drain pipe
(22) drain valve (21), the right-hand member of the reservoir chamber (20) of described first Heat Room (2) are installed on
Connect the port of export of the second water pump (18), and the entrance point of the second water pump (18) connects the second Heat Room
(8) reservoir chamber (20), the right-hand member of the reservoir chamber (20) of described second Heat Room (8) connects first
The water side of water pump (17), and entrance point connection the 3rd Heat Room (13) of the first water pump (17)
Reservoir chamber (20), the right-hand member of the reservoir chamber (20) of described 3rd Heat Room (13) connects water inlet pipe (16),
The lower wall of the air chamber (25) of described first Heat Room (2) be provided with monitoring harmful gases device (4) and
Catalyst reaction device (6) is installed in pressure transducer (5), and the air chamber (25) of the first Heat Room (2),
The lower wall of the air chamber (25) of described second Heat Room (8) is provided with dust investigating (11) and waste residue
Drain valve (10), and the upper end of the second Heat Room (8) is provided with controller (26), described second heat exchange
The internally installed of the air chamber (25) of room (8) has adsorbent equipment (9), and described controller (26) electrically connects
Be connected to the first gas compressor (1), gas temperature detection sensor (3), monitoring harmful gases device (4),
Pressure transducer (5), catalyst reaction device (6), the second gas compressor (7), adsorbent equipment (9),
Waste sludge discharge valve (10), dust investigating (11), the 3rd gas compressor (12), air bleeding valve (15),
First water pump (17), the second water pump (18), water temperature detection sensor (19) and drain valve (21).
A kind of device for recovering afterheat of waste gas in boiler the most according to claim 1, it is characterised in that: institute
Stating adsorbent equipment (9) is electrostatic adsorption device.
A kind of device for recovering afterheat of waste gas in boiler the most according to claim 1, it is characterised in that: institute
Stating division board (23) is heat-conducting metal or thermal conductive ceramic plate.
A kind of device for recovering afterheat of waste gas in boiler the most according to claim 1, it is characterised in that: institute
Stating heat exchange fin (24) is copper coin.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620284597.1U CN205505820U (en) | 2016-04-07 | 2016-04-07 | Waste gas waste heat recovery device of boiler |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620284597.1U CN205505820U (en) | 2016-04-07 | 2016-04-07 | Waste gas waste heat recovery device of boiler |
Publications (1)
Publication Number | Publication Date |
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CN205505820U true CN205505820U (en) | 2016-08-24 |
Family
ID=56736944
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201620284597.1U Expired - Fee Related CN205505820U (en) | 2016-04-07 | 2016-04-07 | Waste gas waste heat recovery device of boiler |
Country Status (1)
Country | Link |
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CN (1) | CN205505820U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106765259A (en) * | 2016-11-23 | 2017-05-31 | 广东东燃热能科技有限公司 | A kind of method of boiler residual heat recovery energy-saving |
CN112361314A (en) * | 2020-11-04 | 2021-02-12 | 余书同 | Steel plant waste gas treatment and utilization equipment and use method thereof |
-
2016
- 2016-04-07 CN CN201620284597.1U patent/CN205505820U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106765259A (en) * | 2016-11-23 | 2017-05-31 | 广东东燃热能科技有限公司 | A kind of method of boiler residual heat recovery energy-saving |
CN112361314A (en) * | 2020-11-04 | 2021-02-12 | 余书同 | Steel plant waste gas treatment and utilization equipment and use method thereof |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160824 Termination date: 20200407 |
|
CF01 | Termination of patent right due to non-payment of annual fee |