CN206582878U - A kind of Horizental showering formula fume afterheat gradient utilization system - Google Patents
A kind of Horizental showering formula fume afterheat gradient utilization system Download PDFInfo
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- CN206582878U CN206582878U CN201621425816.XU CN201621425816U CN206582878U CN 206582878 U CN206582878 U CN 206582878U CN 201621425816 U CN201621425816 U CN 201621425816U CN 206582878 U CN206582878 U CN 206582878U
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- fountain
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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]
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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
Abstract
The utility model is related to flue gas waste heat recovery technical field, more particularly to a kind of Horizental showering formula fume afterheat gradient utilization system.The system includes fountain heat exchange unit, first order fountain waste heat recovery unit, second level fountain waste heat recovery unit and third level fountain waste heat recovery unit, the left end of wherein described fountain heat exchange unit is connected with smoke-intake pipe, the right-hand member of the fountain heat exchange unit is connected with smoke exhaust pipe, and described first order fountain waste heat recovery unit, second level fountain waste heat recovery unit and third level fountain waste heat recovery unit is from left to right connected with the fountain heat exchange unit successively.The system being capable of Mist heat recovering stage by stage, latent heat in effective recovered flue gas, reduce the temperature of smoke evacuation, heat exchange is more abundant, water is directly contacted with flue gas simultaneously, partial impurities that can be in purifying smoke, reduces the pollution discharged fume to environment, the utilization rate of flue gas is improved, is had the advantages that simple in construction, easy to operate.
Description
Technical field
The utility model is related to flue gas waste heat recovery technical field, more particularly to a kind of Horizental showering formula fume afterheat step
Utilize system.
Background technology
The main component of natural gas is methane, and substantial amounts of vapor can be produced after burning, because exhaust gas temperature is general 180
~250 DEG C, part sensible heat and whole latent heat in vapor can be discharged into air together with smoke evacuation, and with fume emission
Also have the pollutant such as nitrogen oxides and fine particulates.In order to reduce energy waste and environmental protection, fume afterheat is carried out
Reclaim and purification is very necessary.
Existing indirect type heat exchange mode is larger due to pipeline thermal resistance, and floor space is big, exchanges heat insufficient, exhaust gas temperature compared with
Most of latent heat in height, flue gas can be still discharged in air with higher exhaust gas temperature, and indirect type heat exchange is prevented pipeline
Rotten Capability Requirement is higher.The condensation heat of the sensible heat of the sufficient recovered flue gas of direct-type heat-energy transducer and most of flue gas.
Utility model content
(1) technical problem to be solved
The purpose of this utility model is to provide a kind of Horizental showering formula fume afterheat gradient utilization system, solves existing waste heat
The heat exchange that way of recycling is present is insufficient, it is impossible to the problem of latent heat in recovered flue gas.
(2) technical scheme
In order to solve the above-mentioned technical problem, the utility model provides a kind of Horizental showering formula fume afterheat cascade utilization system
System, including fountain heat exchange unit, first order fountain waste heat recovery unit, second level fountain waste heat recovery unit and the 3rd
Level fountain waste heat recovery unit, wherein the left end of the fountain heat exchange unit is connected with smoke-intake pipe, the fountain heat exchange
The right-hand member of unit is connected with smoke exhaust pipe, described first order fountain waste heat recovery unit, second level fountain waste heat recovery list
Member and third level fountain waste heat recovery unit are from left to right connected with the fountain heat exchange unit successively.
Further, the first order fountain waste heat recovery unit includes being arranged on outside the fountain heat exchange unit
The first indirect type heat exchanger and the first jet that is arranged on inside the fountain heat exchange unit；
The first indirect type heat exchanger passes through the first spray feed pipe and the first spray return pipe and the spray respectively
Formula heat exchange unit is connected, and the first spray feed pipe is connected with the first jet；
The first indirect type heat exchanger is used by the first heat user water inlet pipe and the first heat user return pipe with heat respectively
Family is connected.
Specifically, first circulation water pump, the first spray return pipe connection are provided with the described first spray feed pipe
In the bottom of the fountain heat exchange unit.
Further, the second level fountain waste heat recovery unit includes being arranged on outside the fountain heat exchange unit
The second indirect type heat exchanger and the second nozzle that is arranged on inside the fountain heat exchange unit；
The second indirect type heat exchanger passes through the second spray feed pipe and the second spray return pipe and the spray respectively
Formula heat exchange unit is connected, and the second spray feed pipe is connected with the second nozzle；
The second indirect type heat exchanger is used by the second heat user water inlet pipe and the second heat user return pipe with heat respectively
Family is connected.
Specifically, second circulation water pump, the second spray return pipe connection are provided with the described second spray feed pipe
In the bottom of the fountain heat exchange unit.
Further, the third level fountain waste heat recovery unit includes being arranged on outside the fountain heat exchange unit
Heat pump and the 3rd nozzle that is arranged on inside the fountain heat exchange unit；
The heat pump passes through the 3rd spray feed pipe and the 3rd spray return pipe and the fountain heat exchange unit phase respectively
Even, the 3rd spray feed pipe is connected with the 3rd nozzle；
The heat pump is connected by the 3rd heat user water inlet pipe and the 3rd heat user return pipe with heat user respectively.
Specifically, the 3rd water circulating pump, the 3rd spray return pipe connection are provided with the described 3rd spray feed pipe
In the bottom of the fountain heat exchange unit.
Further, demister and exhaust blower are separately installed with the smoke exhaust pipe, the demister and exhaust blower are from a left side
It is successively set on to the right side on the smoke exhaust pipe.
Further, two water fenders, two dash are from left to right sequentially provided with the fountain heat exchange unit
The inside of the fountain heat exchange unit is divided into three sections of left, center, right by plate, wherein the first order fountain waste heat recovery list
First left section with the fountain heat exchange unit is connected, and the second level fountain waste heat recovery unit exchanges heat with the fountain
The stage casing of unit is connected, and right section of the third level fountain waste heat recovery unit and the fountain heat exchange unit is connected.
Specifically, the water fender is made up of lower retaining section and upper logical cigarette portion, wherein the upper logical cigarette portion is supplied provided with multiple
The duct of flue gas circulation, the lower retaining section is made up of heat-barrier material.
(3) beneficial effect
Above-mentioned technical proposal of the present utility model has the following advantages that：
The utility model provide Horizental showering formula fume afterheat gradient utilization system, on fountain heat exchange unit according to
The circulating direction of flue gas from left to right sets gradually first order fountain waste heat recovery unit, second level fountain waste heat recovery list
Member and third level fountain waste heat recovery unit, sequentially pass through three-level fountain waste heat by the flue gas of fountain heat exchange unit and return
The recovery that unit carries out fume afterheat is received, hot flue gas has been changed and outdoor is discharged to by smoke exhaust pipe.
The Horizental showering formula fume afterheat gradient utilization system that the utility model is provided, is capable of the remaining of recovered flue gas stage by stage
Latent heat in heat, effective recovered flue gas, reduces the temperature of smoke evacuation, exchanges heat more abundant, while water is directly contacted with flue gas, can
Partial impurities in purifying smoke, reduce pollution of the smoke evacuation to environment, the flue gas after purification by smoke exhaust pipe by demister and
Exhaust blower is discharged, and improves the utilization rate of flue gas, has the advantages that simple in construction, easy to operate.
Brief description of the drawings
Fig. 1 is the structural representation of the utility model embodiment Horizental showering formula fume afterheat gradient utilization system；
Fig. 2 is the structural representation of water fender in the utility model embodiment Horizental showering formula fume afterheat gradient utilization system
Figure.
In figure：1：First indirect type heat exchanger；2：Second indirect type heat exchanger；3：Heat pump； 4：Smoke-intake pipe；5：Fountain
Heat exchange unit；6：Water fender；61：Lower retaining section；62：Upper logical cigarette portion；63：Duct；8：Demister；9：Exhaust blower；10：Smoke evacuation
Pipe；11：First heat user return pipe；12：First heat user water inlet pipe；13：First circulation water pump；14：First spray feed pipe；
15：First jet；16：First spray return pipe；20：Heat user；21：Second heat user return pipe；22：Second heat user is intake
Pipe；23：Second circulation water pump；24：Second spray feed pipe；25：Second nozzle；26：Second spray return pipe；31：3rd heat
User's return pipe；32：3rd heat user water inlet pipe；33：3rd water circulating pump；34：3rd spray feed pipe；35：3rd nozzle；
36：3rd spray return pipe.
Embodiment
It is new below in conjunction with this practicality to make the purpose, technical scheme and advantage of the utility model embodiment clearer
Accompanying drawing in type embodiment, the technical scheme in the utility model embodiment is clearly and completely described, it is clear that retouched
The embodiment stated is a part of embodiment of the present utility model, rather than whole embodiments.Based on the reality in the utility model
Apply example, the every other embodiment that those of ordinary skill in the art are obtained on the premise of creative work is not made, all
Belong to the scope of the utility model protection.
As shown in Figure 1-2, the Horizental showering formula fume afterheat gradient utilization system that the utility model embodiment is provided, including
Fountain heat exchange unit 5, first order fountain waste heat recovery unit, second level fountain waste heat recovery unit and third level spray
Formula waste heat recovery unit, wherein the left end of the fountain heat exchange unit 5 is connected with smoke-intake pipe 4, the fountain heat exchange unit
Right-hand member be connected with smoke exhaust pipe 10, described first order fountain waste heat recovery unit, second level fountain waste heat recovery unit
From left to right it is connected successively with the fountain heat exchange unit with third level fountain waste heat recovery unit.
The Horizental showering formula fume afterheat gradient utilization system that the utility model embodiment is provided, is entered by smoke-intake pipe 4
To the flue gas in the fountain waste heat recovery unit 5, sprayed first with the first order fountain waste heat recovery unit compared with
The water of high temperature is exchanged heat, and flue-gas temperature has declined after heat exchange, is sprayed afterwards with the second level fountain waste heat recovery unit
The middle warm water gone out is exchanged heat, and temperature declines again after heat exchange, is finally sprayed with the third level fountain waste heat recovery unit
Water at low temperature exchanged heat, flue-gas temperature reaches minimum temperature after heat exchange, now again discharges flue gas by the smoke exhaust pipe 10,
So as to reach the purpose of fume afterheat classification recycling.
Furthermore, it is understood that the first order fountain waste heat recovery unit includes being arranged on the fountain heat exchange unit 5
The first outside indirect type heat exchanger 1 and the first jet 15 being arranged on inside the fountain heat exchange unit 5.Between described first
Connect formula heat exchanger 1 and return pipe 16 and the phase of fountain heat exchange unit 5 are sprayed by the first spray feed pipe 14 and first respectively
Even, the first spray feed pipe 14 is connected with the first jet 15.The first indirect type heat exchanger 1 passes through first respectively
The heat user return pipe 11 of heat user water inlet pipe 12 and first is connected with heat user 20.Set on the described first spray feed pipe 14
There is first circulation water pump 13, the first spray return pipe 16 is connected to the bottom of the fountain heat exchange unit 5.
First order heat transfer process is in the utility model embodiment：The first indirect type heat exchanger 1 passes through the first spray
Water temperature is raised after shower water and flue gas heat exchange that feed pipe 14 is provided to the fountain heat exchange unit 5, the height after temperature rise
Warm shower water is back in the first indirect type heat exchanger 1 by the first spray return pipe 16, because spray coolant-temperature gage now is higher,
The current that heat user 20 is flowed into the first indirect type heat exchanger 1 by the first heat user return pipe 11 exchange heat with high temperature shower water
Water temperature is raised afterwards, then is back to by the first heat user water inlet pipe 12 on heat user 20 and is used for heat supply, now shower water heat quilt
Partially absorb, temperature reduction in the presence of first circulation water pump 13, is sprayed through the first shower water feed pipe 14 by first jet 15
Continue to exchange heat after going out, move in circles.It is that the waste heat of flue gas is passed through into the first indirect type heat exchanger 1 in first order heat transfer process
It is supplied to heat user 20 to be used for heat supply after Gas heated reforming.
Furthermore, it is understood that the second level fountain waste heat recovery unit includes being arranged on the fountain heat exchange unit 5
Outside the second indirect type heat exchanger 2 and the second nozzle 25 being arranged on inside the fountain heat exchange unit 5.Described
Two indirect type heat exchangers 2 spray return pipe 26 and the fountain heat exchange unit by the second spray feed pipe 24 and second respectively
5 are connected, and the second spray feed pipe 24 is connected with the second nozzle 25.The second indirect type heat exchanger 2 passes through respectively
Second heat user water inlet pipe 22 and the second heat user return pipe 21 are connected with heat user 20.On the described second spray feed pipe 24
Provided with second circulation water pump 23, the second spray return pipe 26 is connected to the bottom of the fountain heat exchange unit 5.
Second level heat transfer process is in the utility model embodiment：The second indirect type heat exchanger 2 passes through the second spray
Water temperature is raised after shower water and flue gas heat exchange that feed pipe 24 is provided to the fountain heat exchange unit 5, the height after temperature rise
Warm shower water is back in the second indirect type heat exchanger 2 by the second spray return pipe 26, because spray coolant-temperature gage now is compared with the
Spray coolant-temperature gage in one-level heat transfer process decreases, but now remains to reclaim most latent heat and supplied for heat user 20
Heat, namely the current that heat user 20 is flowed into the second indirect type heat exchanger 2 by the second heat user return pipe 21 spray with high temperature
Water temperature is raised after water drenching heat exchange, then is back to by the second heat user water inlet pipe 22 on heat user 20 for heat supply, is now sprayed
Hydro-thermal amount is partially absorbed, temperature reduction, in the presence of second circulation water pump 23, through the second shower water feed pipe 24 by second
Nozzle 25 continues to exchange heat after spraying, and moves in circles.It is that the waste heat of flue gas is passed through into the second indirect type in the heat transfer process of the second level
It is supplied to heat user 20 to be used for heat supply after the Gas heated reforming of heat exchanger 2.
Furthermore, it is understood that the third level fountain waste heat recovery unit includes being arranged on the fountain heat exchange unit 5
Outside heat pump 3 and the 3rd nozzle 35 being arranged on inside the fountain heat exchange unit 5.The heat pump 3 passes through the 3rd respectively
The spray spray return pipe 36 of feed pipe 34 and the 3rd is connected with the fountain heat exchange unit 5, the 3rd spray feed pipe 34
It is connected with the 3rd nozzle 35.The heat pump 3 passes through the 3rd heat user water inlet pipe 32 and the 3rd heat user return pipe 31 respectively
It is connected with heat user 20.The 3rd water circulating pump 33, the 3rd spray return pipe are provided with the described 3rd spray feed pipe 34
36 are connected to the bottom of the fountain heat exchange unit 5.
Third level heat transfer process is in the utility model embodiment：The heat pump 3 sprays feed pipe 34 to institute by the 3rd
State water temperature after the shower water and flue gas heat exchange of the offer of fountain heat exchange unit 5 to raise, the high temperature shower water after temperature rise is by the
Three spray return pipes 36 are back in the heat pump 3, and due to flue gas, temperature is relatively low after the heat exchange of preceding two-stage, therefore by heat exchange
Spray coolant-temperature gage afterwards is relatively low, then needs to make water temperature be increased to heat user usable temp by the heating of heat pump 3, now heat user
Water temperature liter after high temperature shower water heat exchange after 20 current being flowed into by the 3rd heat user return pipe 31 in heat pump 3 and heating
Height, then by the 3rd heat user water inlet pipe 32 be back on heat user 20 be used for heat supply, now shower water heat be partially absorbed,
Temperature reduce, in the presence of the 3rd water circulating pump 33, through the 3rd shower water feed pipe 34 by the 3rd nozzle 35 spray after continue
Heat exchange, moves in circles.It is that heat exchange is supplied to hot use after the waste heat of flue gas is heated up by heat pump 3 in third level heat transfer process
Family 20 is used for heat supply.
Specifically, demister 8 and exhaust blower 9, the demister 8 and exhaust blower are separately installed with the smoke exhaust pipe 10
9 are from left to right successively set on the smoke exhaust pipe 10.Namely demister 8 needs to be arranged on before exhaust blower 9, flue gas is first passed through
Cross demister 8 and pass through blower fan 9 again, the purpose is to the flue gas for ensureing cleaning by blower fan, extend the life-span of blower fan.
Specifically, needed by the flue gas in the fountain waste heat recovery unit 5 by three-level waste heat recovery, and
The temperature of shower water is different after being sprayed during waste heat recoveries at different levels, therefore, from a left side in the fountain heat exchange unit 5
Be sequentially provided with two water fenders 6 to the right side, two water fenders 6 by the inside of the fountain heat exchange unit 5 be divided into it is left,
In, right three sections, wherein left section of the first order fountain waste heat recovery unit and the fountain heat exchange unit 5 is connected, institute
The stage casing that second level fountain waste heat recovery unit is stated with the fountain heat exchange unit 5 is connected, more than the third level fountain
Right section of heat recovery units and the fountain heat exchange unit 5 is connected.
As shown in Fig. 2 the water fender 6 is made up of lower retaining section 61 and upper logical cigarette portion 62, wherein the upper logical cigarette portion 62
Provided with multiple confession flue gases circulate duct 63, be easy to flue gas by duct 63 smoothly circulate, reduce flue gas pass through water fender 6 when
Resistance.Have no duct and gap on the lower retaining section 61, for preventing the flowing between liquid, while in order to prevent the temperature difference
Caused heat transfer, the lower retaining section 61 is made of heat-barrier material.
In addition, the corrosion in order to reduce pipeline, all connecting pipes in the utility model are strong using corrosion resistance
Tubing.
In summary, the Horizental showering formula fume afterheat gradient utilization system described in the utility model embodiment, by setting
Put three-level fountain waste heat recovery unit and carry out step Mist heat recovering by stages, it is to avoid in boiler runs at full capacity and portion
Requirement during point load operation to exhaust smoke level, some stage therein can be selectively opened or closed by the difference of exhaust smoke level
Or certain two stage.The system takes into account the purification of flue gas while more Mist heat recovering amount, and with simple in construction,
Easy to operate, fume afterheat utilizes sufficient advantage.
, it is necessary to illustrate in description of the present utility model, unless otherwise clearly defined and limited, term " phase
Even ", " connection " should be interpreted broadly, for example, it may be being fixedly connected or being detachably connected, or be integrally connected；Can
To be mechanical connection or electrical connection；Can be joined directly together, can also be indirectly connected to by intermediary.For this
For the those of ordinary skill in field, concrete meaning of the above-mentioned term in the utility model can be understood with concrete condition.
In description of the present utility model, unless otherwise indicated, " multiple " are meant that two or more；Term
The orientation or position relationship of the instruction such as " on ", " under ", "left", "right", " interior ", " outer " are based on orientation shown in the drawings or position
Relation, is for only for ease of description the utility model and simplifies description, rather than indicate or imply that the machine or element of meaning are necessary
With specific orientation, with specific azimuth configuration and operation, therefore it is not intended that to limitation of the present utility model.
Finally it should be noted that：Above example is only to illustrate the technical solution of the utility model, rather than its limitations；
Although the utility model is described in detail with reference to the foregoing embodiments, it will be understood by those within the art that：
It can still modify to the technical scheme described in foregoing embodiments, or which part technical characteristic is carried out etc.
With replacement；And these modifications or replacement, the essence of appropriate technical solution is departed from each embodiment technology of the utility model
The spirit and scope of scheme.
Claims (10)
1. a kind of Horizental showering formula fume afterheat gradient utilization system, it is characterised in that：Including fountain heat exchange unit (5),
One-level fountain waste heat recovery unit, second level fountain waste heat recovery unit and third level fountain waste heat recovery unit, its
Described in the left end of fountain heat exchange unit (5) be connected with smoke-intake pipe (4), the right-hand member of the fountain heat exchange unit is connected with row
Smoke pipe (10), described first order fountain waste heat recovery unit, second level fountain waste heat recovery unit and third level spray
Formula waste heat recovery unit is from left to right connected with the fountain heat exchange unit successively.
2. Horizental showering formula fume afterheat gradient utilization system according to claim 1, it is characterised in that：The first order
Fountain waste heat recovery unit include being arranged on the first outside indirect type heat exchanger (1) of the fountain heat exchange unit (5) and
It is arranged on the internal first jet (15) of the fountain heat exchange unit (5)；
The first indirect type heat exchanger (1) passes through the first spray feed pipe (14) and the first spray return pipe (16) and institute respectively
State fountain heat exchange unit (5) to be connected, the first spray feed pipe (14) is connected with the first jet (15)；
The first indirect type heat exchanger (1) passes through the first heat user water inlet pipe (12) and the first heat user return pipe (11) respectively
It is connected with heat user (20).
3. Horizental showering formula fume afterheat gradient utilization system according to claim 2, it is characterised in that：Described first
Spray feed pipe (14) and be provided with first circulation water pump (13), the first spray return pipe (16) is connected to the fountain and changed
The bottom of hot cell (5).
4. Horizental showering formula fume afterheat gradient utilization system according to claim 1, it is characterised in that：The second level
Fountain waste heat recovery unit include being arranged on the second outside indirect type heat exchanger (2) of the fountain heat exchange unit (5) and
It is arranged on the internal second nozzle (25) of the fountain heat exchange unit (5)；
The second indirect type heat exchanger (2) passes through the second spray feed pipe (24) and the second spray return pipe (26) and institute respectively
State fountain heat exchange unit (5) to be connected, the second spray feed pipe (24) is connected with the second nozzle (25)；
The second indirect type heat exchanger (2) passes through the second heat user water inlet pipe (22) and the second heat user return pipe (21) respectively
It is connected with heat user (20).
5. Horizental showering formula fume afterheat gradient utilization system according to claim 4, it is characterised in that：Described second
Spray feed pipe (24) and be provided with second circulation water pump (23), the second spray return pipe (26) is connected to the fountain and changed
The bottom of hot cell (5).
6. Horizental showering formula fume afterheat gradient utilization system according to claim 1, it is characterised in that：The third level
Fountain waste heat recovery unit includes being arranged on the outside heat pump (3) of the fountain heat exchange unit (5) and is arranged on the spray
The 3rd internal nozzle (35) of pouring formula heat exchange unit (5)；
The heat pump (3) is exchanged heat by the 3rd spray feed pipe (34) and the 3rd spray return pipe (36) with the fountain respectively
Unit (5) is connected, and the 3rd spray feed pipe (34) is connected with the 3rd nozzle (35)；
The heat pump (3) passes through the 3rd heat user water inlet pipe (32) and the 3rd heat user return pipe (31) and heat user (20) respectively
It is connected.
7. Horizental showering formula fume afterheat gradient utilization system according to claim 6, it is characterised in that：The described 3rd
Spray feed pipe (34) and be provided with the 3rd water circulating pump (33), the 3rd spray return pipe (36) is connected to the fountain and changed
The bottom of hot cell (5).
8. Horizental showering formula fume afterheat gradient utilization system according to claim 1, it is characterised in that：The smoke exhaust pipe
(10) demister (8) and exhaust blower (9) are separately installed with, the demister (8) and exhaust blower (9) are from left to right set gradually
On the smoke exhaust pipe (10).
9. Horizental showering formula fume afterheat gradient utilization system according to claim 1, it is characterised in that：The fountain
Two water fenders (6) are from left to right sequentially provided with heat exchange unit (5), two water fenders (6) exchange heat the fountain
The inside of unit (5) is divided into three sections of left, center, right, wherein the first order fountain waste heat recovery unit and the fountain
Left section of heat exchange unit (5) is connected, in the second level fountain waste heat recovery unit and the fountain heat exchange unit (5)
Duan Xianglian, right section of the third level fountain waste heat recovery unit and the fountain heat exchange unit (5) is connected.
10. Horizental showering formula fume afterheat gradient utilization system according to claim 9, it is characterised in that：The dash
Plate (6) is made up of lower retaining section (61) and upper logical cigarette portion (62), wherein the upper logical cigarette portion (62) is circulated provided with multiple confession flue gases
Duct (63), the lower retaining section (61) is made up of heat-barrier material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621425816.XU CN206582878U (en) | 2016-12-23 | 2016-12-23 | A kind of Horizental showering formula fume afterheat gradient utilization system |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621425816.XU CN206582878U (en) | 2016-12-23 | 2016-12-23 | A kind of Horizental showering formula fume afterheat gradient utilization system |
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| CN206582878U true CN206582878U (en) | 2017-10-24 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106765253A (en) * | 2016-12-23 | 2017-05-31 | 北京建筑大学 | A kind of Horizental showering formula fume afterheat gradient utilization system |
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2016
- 2016-12-23 CN CN201621425816.XU patent/CN206582878U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106765253A (en) * | 2016-12-23 | 2017-05-31 | 北京建筑大学 | A kind of Horizental showering formula fume afterheat gradient utilization system |
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