CN108151545A - A kind of industry kiln stove waste heat recovery system and exhaust heat recovering method - Google Patents
A kind of industry kiln stove waste heat recovery system and exhaust heat recovering method Download PDFInfo
- Publication number
- CN108151545A CN108151545A CN201711410877.8A CN201711410877A CN108151545A CN 108151545 A CN108151545 A CN 108151545A CN 201711410877 A CN201711410877 A CN 201711410877A CN 108151545 A CN108151545 A CN 108151545A
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- China
- Prior art keywords
- waste heat
- heat recovery
- recovery system
- degree
- heat
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Links
- 239000002918 waste heat Substances 0.000 title claims abstract description 55
- 238000011084 recovery Methods 0.000 title claims abstract description 34
- 238000000034 method Methods 0.000 title claims abstract description 10
- 238000010438 heat treatment Methods 0.000 claims abstract description 10
- 239000002351 wastewater Substances 0.000 claims abstract description 5
- 230000003020 moisturizing effect Effects 0.000 claims description 3
- 239000000126 substance Substances 0.000 claims description 2
- 230000005611 electricity Effects 0.000 abstract description 4
- 239000002699 waste material Substances 0.000 abstract description 4
- 239000007789 gas Substances 0.000 abstract description 3
- 230000009286 beneficial effect Effects 0.000 abstract description 2
- 238000010977 unit operation Methods 0.000 abstract description 2
- 238000005516 engineering process Methods 0.000 description 9
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- 239000011344 liquid material Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000008450 motivation Effects 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 230000032258 transport Effects 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
Classifications
-
- F27D17/004—
-
- 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
- Processing Of Solid Wastes (AREA)
Abstract
The invention discloses a kind of industry kiln stove waste heat recovery system and exhaust heat recovering method, which includes residual neat recovering system unit, incubator, bath wastewater and waste heat tank.The beneficial effects of the invention are as follows:Industrial Stoves after the heating can remaining amount of heat, these heats are thrown away by waste in vain.And temperature when similarly waste heat recovery unit discharges again only has 35 degree, 35 subtract 5 degree this mean that 30 degree of thermal energy has been stayed in unit, it is introduced in unit 14 degree or so of heat, 14 degree are equal to 44 degree plus 30 degree, waste heat recovery unit operation cost only needs 4 degree of electricity, more than 75% electricity charge are saved than electrical heating, saving 50% than coal-fired, gas fired-boiler operates above cost.
Description
Technical field
The present invention relates to a kind of industry kiln stove waste heat recovery technology, specifically a kind of industry kiln stove waste heat recovery system and remaining
Heat recovery method belongs to industry kiln stove waste heat recovery technology field.
Background technology
Waste heat refers to the limitation by history, technology, theory etc., in the industrial consumption energy device to have put into operation, original design
The sensible heat and latent heat not being used appropriately, it includes high-temp waste gas waste heat, cooling medium waste heat, waste vapour waste water residual heat, high temperature production
Product and afterheat of slags, chemical reaction waste heat, combustible exhaust gas waste liquid and waste material waste heat etc..According to investigation, the waste heat of every profession and trade always provides
Source accounts for about the 17%~67% of its fuel consumption total amount, and the residual heat resources of recoverable are about the 60% of waste heat total resources.Work
Amateurish heat is by the use of from the waste heat that industrial equipment recycles as the Urban District Heating of heat source.Most energy consumption equipments, it is such as former
The sub-fraction in thermal energy is all only utilized in motivation, heating furnace etc..The industrial exhaust heat that a recycling part was passed into disuse originally carries out
Central heating can save primary energy, increase economic efficiency, and reduce pollution.
Existing industry kiln stove waste heat recovery technology is simultaneously not perfect, this allows for industry kiln stove waste heat recovering effect and is not achieved
Preferably, huge obstruction is brought for the progress of industry kiln stove waste heat recovery technology.
Invention content
In view of the problems of the existing technology, the present invention provides a kind of industry kiln stove waste heat recovery system, the industry kiln
Stove residual neat recovering system includes residual neat recovering system unit, incubator, bath wastewater and waste heat tank.
Preferably, Step 1: Step 2: step 3 and step 4.
Preferably, the step 1 is:By in waste heat centralized collection to waste heat tank, the size of waste heat tank is used according to heat
Flow or maximum use time heat determine.
Preferably, the step 2 is:The waste heat to be got off using pipeline is uniformly flowed into heat recovery system unit, is connect simultaneously
Enter other heats.
Preferably, the step 3 is:Heat exchange, the object contained in heat are proceeded by inside heat recovery system unit
Matter is without exchanging, and only temperature swaps.
Preferably, the step 4 is:Waste heat after thermal energy exchange enters from heat recovery system unit other end outflow waste heat
Residual neat recovering system unit can also carry out continuing moisturizing heating to it after incubator.
The beneficial effects of the invention are as follows:Industrial Stoves after the heating can remaining amount of heat, these heats are by wave in vain
Expense is thrown away.And temperature of same waste heat recovery unit when discharging again only has 3-5 degree, 35 subtract 5 degree this meant that 30 degree
Thermal energy stayed in unit, introduced in unit 14 degree or so of heat, 14 degree plus 30 degree equal to 44 degree, waste heat recovery
Unit operation cost only needs 4 degree of electricity, and more than 75% electricity charge are saved than electrical heating, saves more than 50% than coal-fired, gas fired-boiler and transports
Row cost.
Specific embodiment
The technical solution in the embodiment of the present invention will be clearly and completely described below.Obviously, described implementation
Example is only part of the embodiment of the present invention, instead of all the embodiments.Based on the embodiments of the present invention, this field is common
Technical staff's all other embodiments obtained without making creative work belong to the model that the present invention protects
It encloses.
A kind of industry kiln stove waste heat recovery system, industry kiln stove waste heat recovery system include residual neat recovering system unit, protect
Incubator, bath wastewater and waste heat tank.
Preferably, Step 1: Step 2: step 3 and step 4.
Preferably, step 1 is:By in waste heat centralized collection to waste heat tank, the size of waste heat tank uses flow according to heat
Or maximum use time heat determines.
Preferably, step 2 is:The waste heat to be got off using pipeline is uniformly flowed into heat recovery system unit, while accesses it
His heat.
Preferably, step 3 is:Heat exchange is proceeded by inside heat recovery system unit, the substance contained in heat is not
It swaps, only temperature swaps.
Preferably, step 4 is:Waste heat after thermal energy exchange enters heat preservation from heat recovery system unit other end outflow waste heat
Residual neat recovering system unit can also carry out continuing moisturizing heating to it after case.
Better embodiment of the embodiment provided above for the present invention only is used for facilitating illustrating the present invention, not to this hair
The limitation of bright work in any form, any those of ordinary skill in the art, if putting forward skill not departing from the present invention
In the range of art feature, using the equivalent embodiment for locally changing or modifying made by disclosed technology contents, and
Without departing from the technical feature content of the present invention, in the range of still falling within the technology of the present invention feature.
Claims (6)
1. a kind of industry kiln stove waste heat recovery system, the industry kiln stove waste heat recovery system include residual neat recovering system unit,
Incubator, bath wastewater and waste heat tank.
2. a kind of industry kiln stove waste heat recovery method, which is characterized in that the industry kiln stove waste heat recovery method includes:Step
First, Step 2: step 3 and step 4.
3. a kind of industry kiln stove waste heat recovery system according to claim 1 and exhaust heat recovering method, which is characterized in that institute
Stating step 1 is:By in waste heat centralized collection to waste heat tank, the size of waste heat tank according to heat using flow or it is maximum use when
Section heat determines.
4. a kind of industry kiln stove waste heat recovery system according to claim 1 and exhaust heat recovering method, which is characterized in that institute
Stating step 2 is:The waste heat to be got off using pipeline is uniformly flowed into heat recovery system unit, while accesses other heats.
5. a kind of industry kiln stove waste heat recovery system according to claim 1 and exhaust heat recovering method, which is characterized in that institute
Stating step 3 is:Heat exchange is proceeded by inside heat recovery system unit, the substance contained in heat is without exchanging, only
Temperature swaps.
6. a kind of industry kiln stove waste heat recovery system according to claim 1 and exhaust heat recovering method, which is characterized in that institute
Stating step 4 is:Waste heat after thermal energy exchange enters waste heat recovery after incubator from heat recovery system unit other end outflow waste heat
System unit can also carry out continuing moisturizing heating to it.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201711410877.8A CN108151545A (en) | 2017-12-23 | 2017-12-23 | A kind of industry kiln stove waste heat recovery system and exhaust heat recovering method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201711410877.8A CN108151545A (en) | 2017-12-23 | 2017-12-23 | A kind of industry kiln stove waste heat recovery system and exhaust heat recovering method |
Publications (1)
Publication Number | Publication Date |
---|---|
CN108151545A true CN108151545A (en) | 2018-06-12 |
Family
ID=62465429
Family Applications (1)
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CN201711410877.8A Pending CN108151545A (en) | 2017-12-23 | 2017-12-23 | A kind of industry kiln stove waste heat recovery system and exhaust heat recovering method |
Country Status (1)
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Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2011196615A (en) * | 2010-03-19 | 2011-10-06 | Jfe Steel Corp | Waste heat recovery equipment of heating furnace, and method of utilizing waste heat |
CN202814125U (en) * | 2012-08-31 | 2013-03-20 | 上海宝钢节能技术有限公司 | Waste heat CCHP (Combined Cooling Heating and Power) system of blast furnace cinder flushing water, bled steam and flue gas |
CN204661741U (en) * | 2015-02-12 | 2015-09-23 | 青岛一合节能技术有限公司 | Blast furnace slag quenching water comprehensive utilization system for heat energy |
CN105755189A (en) * | 2016-04-22 | 2016-07-13 | 中冶南方工程技术有限公司 | Waste heat recovery device for blast furnace slag flushing water |
CN107036330A (en) * | 2017-05-02 | 2017-08-11 | 张志国 | A kind of double-source heat pump waste heat recovery unit |
-
2017
- 2017-12-23 CN CN201711410877.8A patent/CN108151545A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2011196615A (en) * | 2010-03-19 | 2011-10-06 | Jfe Steel Corp | Waste heat recovery equipment of heating furnace, and method of utilizing waste heat |
CN202814125U (en) * | 2012-08-31 | 2013-03-20 | 上海宝钢节能技术有限公司 | Waste heat CCHP (Combined Cooling Heating and Power) system of blast furnace cinder flushing water, bled steam and flue gas |
CN204661741U (en) * | 2015-02-12 | 2015-09-23 | 青岛一合节能技术有限公司 | Blast furnace slag quenching water comprehensive utilization system for heat energy |
CN105755189A (en) * | 2016-04-22 | 2016-07-13 | 中冶南方工程技术有限公司 | Waste heat recovery device for blast furnace slag flushing water |
CN107036330A (en) * | 2017-05-02 | 2017-08-11 | 张志国 | A kind of double-source heat pump waste heat recovery unit |
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PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20180612 |
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RJ01 | Rejection of invention patent application after publication |