CN209540906U - Waste incinerator double cooling systems - Google Patents
Waste incinerator double cooling systems Download PDFInfo
- Publication number
- CN209540906U CN209540906U CN201920089892.5U CN201920089892U CN209540906U CN 209540906 U CN209540906 U CN 209540906U CN 201920089892 U CN201920089892 U CN 201920089892U CN 209540906 U CN209540906 U CN 209540906U
- Authority
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- China
- Prior art keywords
- cooling fluid
- cooling
- pipeline
- water
- waste incinerator
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- Expired - Fee Related
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- 238000001816 cooling Methods 0.000 title claims abstract description 104
- 239000002699 waste material Substances 0.000 title claims abstract description 46
- 239000012809 cooling fluid Substances 0.000 claims abstract description 135
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 84
- 238000003860 storage Methods 0.000 claims abstract description 28
- 238000010612 desalination reaction Methods 0.000 claims description 9
- 230000003020 moisturizing effect Effects 0.000 claims description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 239000012530 fluid Substances 0.000 description 5
- 238000009833 condensation Methods 0.000 description 4
- 230000005494 condensation Effects 0.000 description 4
- 239000000428 dust Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000004781 supercooling Methods 0.000 description 2
- 238000004056 waste incineration Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000003763 carbonization Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000005453 pelletization Methods 0.000 description 1
- 238000007781 pre-processing Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
Abstract
The utility model provides a kind of waste incinerator double cooling systems, wherein the outlet conduit of incinerator cooling device passes through the first pipeline switching switch difference piping connection condensate water discharge road and cooling fluid discharge line, the inlet pipeline difference piping connection cooling fluid discharge line and cooling fluid storage bin of cooling fluid driving device, the outlet conduit of cooling fluid driving device enters pipeline by cooling fluid cooling device piping connection cooling fluid, by the second pipeline switching switch, piping connection condensed water enters pipeline to the inlet pipeline of incinerator cooling device respectively and cooling fluid enters pipeline, industrial colling water inlet line passes through cooling fluid cooling device piping connection industrial colling water return pipeline.The waste incinerator double cooling systems of the utility model can effectively reduce the function of environment heat emission of waste incinerator, improve and burn heat utilization rate, reduce energy waste, ingenious in design, and simple for structure, manufacture is easy, at low cost, be suitable for large-scale promotion application.
Description
Technical field
The utility model relates to technical field of waste treatment, in particular to waste incinerator technical field, in particular to one
Kind waste incinerator double cooling systems.
Background technique
Waste incinerator is the equipment of burning disposal rubbish, and rubbish becomes exhaust gas and enter second-time burning in furnace chamber inner combustion
Room burns completely under the forced burning of burner, enters back into spray type dust separator, be discharged into atmosphere through chimney after dedusting.Rubbish
Incinerator is by rubbish preprocessing system, incineration system, smog biochemistry dust pelletizing system and gas generator (auxiliary firing burning) four
Big system composition, integrates self-feeding, sub-sieve, drying, burning, deashing, dedusting, automation control.
A kind of harmless treatment that waste incinerator is commonly used in terms of medical and life waste product, animal harmless treatment is set
It is standby.Its principle is object to be processed progress high temperature to be destroyed by fire carbonization, using the burning of the fuel such as coal, fuel oil, combustion gas to reach
To the purpose of disinfection treatment.
But that there are function of environment heat emission is serious for existing waste incinerator, burns the low problem of heat utilization rate.
Accordingly, it is desirable to provide a kind of waste incinerator cooling system, the environment that can effectively reduce waste incinerator dissipates
Heat improves and burns heat utilization rate, reduces energy waste.
Utility model content
In order to overcome the disadvantages of the prior art mentioned above, one of the utility model is designed to provide a kind of waste incineration
Furnace double cooling systems can effectively reduce the function of environment heat emission of waste incinerator, improve and burn heat utilization rate, reduce energy wave
Take, is suitable for large-scale promotion application.
The another object of the utility model is to provide a kind of waste incinerator double cooling systems, ingenious in design, structure
Succinctly, manufacture is easy, at low cost, is suitable for large-scale promotion application.
To achieve the above objectives, the utility model provides a kind of waste incinerator double cooling systems, its main feature is that, including burn
Burn furnace cooling device, the first pipeline switching switch, condensate water discharge road, condensed water enter pipeline, cooling fluid discharge line,
Cooling fluid storage bin, cooling fluid driving device, cooling fluid cooling device, cooling fluid enter pipeline, the second pipeline is cut
Change switch, industrial colling water inlet line and industrial colling water return pipeline, in which:
The outlet conduit of the incinerator cooling device is switched described in switch difference piping connection by first pipeline
The inlet pipeline difference pipeline of condensate water discharge road and the cooling fluid discharge line, the cooling fluid driving device connects
The cooling fluid discharge line and the cooling fluid storage bin are connect, the outlet conduit of the cooling fluid driving device passes through
Cooling fluid described in the cooling fluid cooling device piping connection enters pipeline, the inlet pipeline of the incinerator cooling device
Enter pipeline by condensed water described in second pipeline switching switch respectively piping connection and the cooling fluid enter pipeline,
The industrial colling water inlet line passes through industrial colling water return pipeline described in the cooling fluid cooling device piping connection.
Preferably, the incinerator cooling device is fire grate water cooling comb.
Preferably, the first pipeline switching switch and second pipeline switching switch are three-way switch valve.
Preferably, the number of the cooling fluid cooling device is 2,2 cooling fluid cooling device parallel connections are set
It sets.
Preferably, the number of the cooling fluid driving device is 2,2 cooling fluid driving device parallel connections are set
It sets.
Preferably, the cooling fluid discharge line is demineralized water discharge line, the cooling fluid storage bin is desalination
Water storage bin, the cooling fluid driving device are demineralized water driving devices, and the cooling fluid cooling device is desalination water cooling
But device, it is that demineralized water enters pipeline that the cooling fluid, which enters pipeline,.
More preferably, the demineralized water driving device is water circulating pump.
Preferably, the waste incinerator double cooling systems further include cooling fluid supply pipeline, the cooling fluid is mended
The cooling fluid storage bin is connected to conduit line.
More preferably, the cooling fluid supply pipeline is demineralized water moisturizing pipeline, and the cooling fluid storage bin is desalination
Water storage bin.
The beneficial effects of the utility model essentially consist in:
1, the outlet conduit of the incinerator cooling device of the waste incinerator double cooling systems of the utility model passes through first
Pipeline switching switch piping connection condensate water discharge road and cooling fluid discharge line respectively, cooling fluid driving device into
Mouth pipeline difference piping connection cooling fluid discharge line and cooling fluid storage bin, the outlet conduit of cooling fluid driving device
Enter pipeline by cooling fluid cooling device piping connection cooling fluid, the inlet pipeline of incinerator cooling device passes through second
Piping connection condensed water enters pipeline to pipeline switching switch respectively and cooling fluid enters pipeline, and industrial colling water inlet line is logical
Supercooling fluid cooling device piping connection industrial colling water return pipeline, to according to circumstances select condensed water cooling or cold
But fluid is cooling, therefore, can effectively reduce the function of environment heat emission of waste incinerator, improve and burn heat utilization rate, reduce energy
Source waste, is suitable for large-scale promotion application.
2, the outlet conduit of the incinerator cooling device of the waste incinerator double cooling systems of the utility model passes through first
Pipeline switching switch piping connection condensate water discharge road and cooling fluid discharge line respectively, cooling fluid driving device into
Mouth pipeline difference piping connection cooling fluid discharge line and cooling fluid storage bin, the outlet conduit of cooling fluid driving device
Enter pipeline by cooling fluid cooling device piping connection cooling fluid, the inlet pipeline of incinerator cooling device passes through second
Piping connection condensed water enters pipeline to pipeline switching switch respectively and cooling fluid enters pipeline, and industrial colling water inlet line is logical
Supercooling fluid cooling device piping connection industrial colling water return pipeline, to according to circumstances select condensed water cooling or cold
But fluid is cooling, therefore, ingenious in design, simple for structure, and manufacture is easy, at low cost, is suitable for large-scale promotion application.
The these and other objects of the utility model, feature and advantage are wanted by following detailed descriptions, attached drawing and right
It acquires to fully demonstrate, and can be achieved by means, device and the their combination specially pointed out in appended claims.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of a specific embodiment of the waste incinerator double cooling systems of the utility model.
(symbol description)
1 incinerator cooling device；2 first pipelines switching switch；3 condensate water discharge roads；4 condensed waters enter pipeline；5 is cold
But fluid discharge pipe road；6 cooling fluid storage bins；7 cooling fluid driving devices；8 cooling fluid cooling devices；9 cooling fluids
Into pipeline；10 second pipelines switching switch；11 industrial colling water inlet lines；12 industrial colling water return pipelines；13 is cooling
Fluid feeds pipeline.
Specific embodiment
In order to be more clearly understood that the technology contents of the utility model, spy lifts following embodiment and is described in detail.
Shown in Figure 1, in a specific embodiment of the utility model, the waste incinerator of the utility model is double cold
But system include incinerator cooling device 1, the first pipeline switching switch 2, condensate water discharge road 3, condensed water enter pipeline 4,
Cooling fluid discharge line 5, cooling fluid storage bin 6, cooling fluid driving device 7, cooling fluid cooling device 8, cooling stream
Body enters pipeline 9, the second pipeline switching switch 10, industrial colling water inlet line 11 and industrial colling water return pipeline 12,
In:
The outlet conduit of the incinerator cooling device 1 switches switch 2 by first pipeline and distinguishes piping connection institute
State condensate water discharge road 3 and the cooling fluid discharge line 5, the inlet pipeline difference of the cooling fluid driving device 7
Cooling fluid discharge line 5 described in piping connection and the cooling fluid storage bin 6, the cooling fluid driving device 7 go out
Mouth pipeline enters pipeline 9, the cooling dress of the incinerator by cooling fluid described in 8 piping connection of cooling fluid cooling device
1 inlet pipeline is set by second pipeline to switch switch 10 condensed water described in piping connection enters pipeline 4 and described respectively
Cooling fluid enters pipeline 9, and the industrial colling water inlet line 11 passes through the 8 piping connection institute of cooling fluid cooling device
State industrial colling water return pipeline 12.
The incinerator cooling device 1 can be any suitable incinerator cooling device, shown in Figure 1, at this
In one specific embodiment of utility model, the incinerator cooling device 1 is fire grate water cooling comb.
The first pipeline switching switch 2 and second pipeline switching switch 10 can be any suitable pipeline switching
Switch, it is shown in Figure 1, in a specific embodiment of the utility model, first pipeline switching switch 2 and described the
It is three-way switch valve that two pipelines, which switch switch 10,.
The number of the cooling fluid cooling device 8 can according to need determination, shown in Figure 1, practical new at this
In one specific embodiment of type, the number of the cooling fluid cooling device 8 is 2,2 cooling fluid cooling devices 8
It is arranged in parallel.
The number of the cooling fluid driving device 7 can according to need determination, shown in Figure 1, practical new at this
In one specific embodiment of type, the number of the cooling fluid driving device 7 is 2,2 cooling fluid driving devices 7
It is arranged in parallel.
The cooling fluid can be any suitable cooling fluid, preferably, the cooling fluid is demineralized water, at this
In one specific embodiment of utility model, the cooling fluid discharge line 5 is demineralized water discharge line, the cooling fluid storage
Depositing case 6 is desalination water storage bin, and the cooling fluid driving device 7 is demineralized water driving device, the cooling dress of the cooling fluid
Setting 8 is desalination water-cooling apparatus, and it is that demineralized water enters pipeline that the cooling fluid, which enters pipeline 9,.
The demineralized water driving device can be any suitable demineralized water driving device, and one in the utility model is specific
In embodiment, the demineralized water driving device is water circulating pump.
It is shown in Figure 1 for the cooling fluid being replenished in time in the cooling fluid storage bin 6, it is practical new at this
In one specific embodiment of type, the waste incinerator double cooling systems further include cooling fluid supply pipeline 13, the cooling
Fluid feeds cooling fluid storage bin 6 described in 13 piping connection of pipeline.
As described above, the cooling fluid can be any suitable cooling fluid, preferably, the cooling fluid is to remove
Salt water, in a specific embodiment of the utility model, the cooling fluid supply pipeline 13 is demineralized water moisturizing pipeline, described
Cooling fluid storage bin 6 is desalination water storage bin.
In this way, the incinerator cooling device 1, the cooling fluid discharge line 5, the cooling fluid storage bin 6, institute
It states cooling fluid driving device 7, the cooling fluid cooling device 8 and the cooling fluid and enters the composition enclosed cooling of pipeline 9
System, the incinerator cooling device 1, the condensate water discharge road 3 and the condensed water enter pipeline 4 and constitute open type cooling
System, the first pipeline switching switch 2 and second pipeline switching switch 10 constitute apparatus for fast switching.
In use, incinerator cooling device 1 is mounted on waste incinerator, condensed water is entered into pipeline 4 and heating power system
The condensation water out of system is connected, and condensate water discharge road 3 is connected with the condensation water inlet of therrmodynamic system.
Therrmodynamic system Unit Commitment and damage, condensing capacity is few, is not enough to cooling waste incinerator, waste incineration
Furnace is cooling to be cooled down using closed cooling system, switches switch 2 for the outlet of incinerator cooling device 1 by the first pipeline
Road and 5 pipeline connection of cooling fluid discharge line switch switch 10 for the inlet tube of incinerator cooling device 1 by the second pipeline
Road and cooling fluid enter 9 pipeline connection of pipeline, the cooling stream from cooling fluid storage bin 6 and cooling fluid discharge line 5
Body is sent into cooling fluid cooling device 8 by cooling fluid driving device 7 and is cooled down, and heat passes through cooling fluid cooling device
8 are taken away by industrial colling, finally distribute to environment, and cooling fluid after cooling enters incinerator cooling device 1 and obtains heat
To cooling waste incinerator.
When therrmodynamic system operates normally, by the first pipeline switch switch 2 by the outlet conduit of incinerator cooling device 1 and
3 pipeline connection of condensate water discharge road switches switch 10 for the inlet pipeline of incinerator cooling device 1 by the second pipeline and coagulates
It bears water and enters 4 pipeline connection of pipeline, the condensed water of the condensation water out from therrmodynamic system enters the acquisition of incinerator cooling device 1
For heat to cooling waste incinerator, the condensed water after obtaining temperature rise is back to heating power system from the condensation water inlet of therrmodynamic system again
System.
Therefore, using the utility model, while cooling medium required to waste incinerator offer work, by incinerator
It is cooling to bring therrmodynamic system into heat exchange amount, the function of environment heat emission of waste incinerator has been reduced to a great extent, has improved burning thermal energy
Utilization rate.
To sum up, the environment that the waste incinerator double cooling systems of the utility model can effectively reduce waste incinerator dissipates
Heat improves and burns heat utilization rate, reduces energy waste, ingenious in design, and simple for structure, manufacture is easy, at low cost, is suitable for big rule
Mould promotes and applies.
It can be seen that the purpose of this utility model completely and is effectively achieved.The function of the utility model and
Structural principle is shown and is illustrated in embodiment, and under without departing substantially from the principle, embodiment can make any modification.Institute
With the utility model includes all variant embodiments based on claim spirit and scope of the claims.
Claims (9)
1. a kind of waste incinerator double cooling systems, which is characterized in that opened including incinerator cooling device, the switching of the first pipeline
Pass, condensate water discharge road, condensed water enter pipeline, cooling fluid discharge line, cooling fluid storage bin, cooling fluid driving
Device, cooling fluid cooling device, cooling fluid enter pipeline, the second pipeline switching switch, industrial colling water inlet line and
Industrial colling water return pipeline, in which:
The outlet conduit of the incinerator cooling device is switched by first pipeline to be condensed described in switch difference piping connection
The inlet pipeline of water discharge pipe road and the cooling fluid discharge line, the cooling fluid driving device distinguishes piping connection institute
Cooling fluid discharge line and the cooling fluid storage bin are stated, the outlet conduit of the cooling fluid driving device passes through described
Cooling fluid described in cooling fluid cooling device piping connection enters pipeline, and the inlet pipeline of the incinerator cooling device passes through
Condensed water described in piping connection enters pipeline to second pipeline switching switch respectively and the cooling fluid enters pipeline, described
Industrial colling water inlet line passes through industrial colling water return pipeline described in the cooling fluid cooling device piping connection.
2. waste incinerator double cooling systems as described in claim 1, which is characterized in that the incinerator cooling device is furnace
Drain cold comb.
3. waste incinerator double cooling systems as described in claim 1, which is characterized in that first pipeline switching switch and
The second pipeline switching switch is three-way switch valve.
4. waste incinerator double cooling systems as described in claim 1, which is characterized in that the cooling fluid cooling device
Number is 2, and 2 cooling fluid cooling devices are arranged in parallel.
5. waste incinerator double cooling systems as described in claim 1, which is characterized in that the cooling fluid driving device
Number is 2, and 2 cooling fluid driving devices are arranged in parallel.
6. waste incinerator double cooling systems as described in claim 1, which is characterized in that the cooling fluid discharge line is
Demineralized water discharge line, the cooling fluid storage bin are desalination water storage bins, and the cooling fluid driving device is demineralized water
Driving device, the cooling fluid cooling device are desalination water-cooling apparatus, the cooling fluid enter pipeline be demineralized water into
Enter pipeline.
7. waste incinerator double cooling systems as claimed in claim 6, which is characterized in that the demineralized water driving device is to follow
Ring water pump.
8. waste incinerator double cooling systems as described in claim 1, which is characterized in that the double cooling systems of the waste incinerator
System further includes cooling fluid supply pipeline, and the cooling fluid supply conduit line connects the cooling fluid storage bin.
9. waste incinerator double cooling systems as claimed in claim 8, which is characterized in that the cooling fluid, which feeds pipeline, is
Demineralized water moisturizing pipeline, the cooling fluid storage bin are desalination water storage bins.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920089892.5U CN209540906U (en) | 2019-01-18 | 2019-01-18 | Waste incinerator double cooling systems |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920089892.5U CN209540906U (en) | 2019-01-18 | 2019-01-18 | Waste incinerator double cooling systems |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209540906U true CN209540906U (en) | 2019-10-25 |
Family
ID=68270426
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201920089892.5U Expired - Fee Related CN209540906U (en) | 2019-01-18 | 2019-01-18 | Waste incinerator double cooling systems |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209540906U (en) |
-
2019
- 2019-01-18 CN CN201920089892.5U patent/CN209540906U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20191025 |