CN207621979U - A kind of electric-melting magnesium is dry to put out heat exchange tower smoke and waste steam boiler - Google Patents
A kind of electric-melting magnesium is dry to put out heat exchange tower smoke and waste steam boiler Download PDFInfo
- Publication number
- CN207621979U CN207621979U CN201721420455.4U CN201721420455U CN207621979U CN 207621979 U CN207621979 U CN 207621979U CN 201721420455 U CN201721420455 U CN 201721420455U CN 207621979 U CN207621979 U CN 207621979U
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- Prior art keywords
- heat
- flue
- frame
- electric
- dry
- 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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- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 title claims abstract description 30
- 229910052749 magnesium Inorganic materials 0.000 title claims abstract description 29
- 239000011777 magnesium Substances 0.000 title claims abstract description 29
- 238000002844 melting Methods 0.000 title claims abstract description 28
- 239000000779 smoke Substances 0.000 title claims abstract description 16
- 239000002699 waste material Substances 0.000 title claims abstract description 15
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 34
- 239000003546 flue gas Substances 0.000 claims abstract description 33
- 238000004321 preservation Methods 0.000 claims abstract description 10
- 235000014171 carbonated beverage Nutrition 0.000 claims abstract description 7
- 239000012774 insulation material Substances 0.000 claims description 7
- 238000007599 discharging Methods 0.000 claims description 4
- 239000012528 membrane Substances 0.000 claims description 3
- 230000001815 facial effect Effects 0.000 claims description 2
- 238000004519 manufacturing process Methods 0.000 abstract description 9
- 230000007613 environmental effect Effects 0.000 abstract description 2
- 239000002918 waste heat Substances 0.000 description 10
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 238000002425 crystallisation Methods 0.000 description 3
- 230000008025 crystallization Effects 0.000 description 3
- 238000004064 recycling Methods 0.000 description 3
- 238000001816 cooling Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000001095 magnesium carbonate Substances 0.000 description 2
- 235000014380 magnesium carbonate Nutrition 0.000 description 2
- ZLNQQNXFFQJAID-UHFFFAOYSA-L magnesium carbonate Chemical compound [Mg+2].[O-]C([O-])=O ZLNQQNXFFQJAID-UHFFFAOYSA-L 0.000 description 2
- 229910000021 magnesium carbonate Inorganic materials 0.000 description 2
- 239000000395 magnesium oxide Substances 0.000 description 2
- 235000012245 magnesium oxide Nutrition 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
- 238000009628 steelmaking Methods 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/25—Process efficiency
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- Devices For Medical Bathing And Washing (AREA)
Abstract
Heat exchange tower smoke and waste steam boiler, including flue and modular heat-transfer area bobbin carriage are put out the utility model discloses a kind of electric-melting magnesium is dry；Flue is straight-through shape structure, and flue top is equipped with flue gas input port, and bottom end is equipped with flue gas delivery outlet；In flue steam superheater, evaporator and economizer are equipped with successively from top to bottom along flue gas flow direction；Side above flue is equipped with drum, and drum is connect with steam superheater, evaporator and economizer respectively by piping, and evaporator establishes carbonated drink natural convection loop by tedge, down-comer and drum；Modular heat-transfer area bobbin carriage includes heat-exchange tube group and shell heat preservation frame, and the horizontal shell that is mounted on of conduit saddle that heat-exchange tube group keeps the temperature frame both ends by shell is kept the temperature in frame, and shell heat preservation frame is connected with flue inner wall face.Present application addresses electric-melting magnesium production industry dry the problem of putting out the waste of heat exchange tower smoke heat energy, and can generate the required superheated steam of heat distribution pipe network, to energy-saving and environmental protection, reduce manufacturing cost.
Description
Technical field
The utility model is related to a kind of waste heat boiler, especially a kind of electric-melting magnesium is dry to put out heat exchange tower smoke and waste steam boiler.
Background technology
Fused magnesite crystallization is big, fine and close, is that production steelmaking converter, electric furnace and refining ladle slag line magnesia carbon brick are undesirable
The best body material in generation, wherein low Fe2O3Big crystallization fused magnesite be good fill insulant in electric elements again.
In electric-melting magnesium production process, the high temperature magnesium after melting sticks together and is first cooled to periclase crystal structure temperature, and crystallization, which finishes, sticks together magnesium powder
Feeding is dry after broken puts out heat exchange tower and air heat-exchange, and the dry flue gas part for putting out heat exchange tower discharge is former for preheating magnesium mine
Beginning material, another part are then vented.
The dry heat exchange tower flue-gas temperature of putting out of electric-melting magnesium is distributed in 300~400 DEG C, many thermal energy is still contained in flue gas, if not
It is recycled and is directly discharged into air, not only wasted the valuable energy, but also seriously polluted atmospheric environment.Therefore, it develops
The dry waste heat boiler for putting out heat exchange tower smoke heat energy recycling demand of above-mentioned electric-melting magnesium is adapted to, current electric-melting magnesium production industry is come
It is imperative to say.
Utility model content
The technical problems to be solved in the utility model is that in view of the above shortcomings of the prior art, and it is dry to provide a kind of electric-melting magnesium
Heat exchange tower smoke and waste steam boiler is put out, the electric-melting magnesium is dry to be put out heat exchange tower smoke and waste steam boiler to solve electric-melting magnesium production industry dry
The problem of putting out the waste of heat exchange tower smoke heat energy, and the required superheated steam of heat distribution pipe network can be generated, thus energy-saving and environmental protection,
Reduce manufacturing cost.
In order to solve the above technical problems, the technical solution adopted in the utility model is：
A kind of electric-melting magnesium is dry to put out heat exchange tower smoke and waste steam boiler, including flue and modular heat-transfer area bobbin carriage.
Flue is straight-through shape structure, and flue top is equipped with flue gas input port, and bottom end is equipped with flue gas delivery outlet, flue gas delivery outlet
Bottom surface be equipped with ash-discharging device；In flue steam superheater, evaporator and economizer are equipped with successively from top to bottom along flue gas flow direction；
It is modular heat-transfer area bobbin carriage that steam superheater, evaporator and economizer, which are located at flue inside points,.
Side above flue is equipped with drum, and drum is connected with steam superheater, evaporator and economizer respectively by piping
It connects, evaporator establishes carbonated drink natural convection loop by tedge, down-comer and drum.
Modular heat-transfer area bobbin carriage includes heat-exchange tube group and shell heat preservation frame, and heat-exchange tube group keeps the temperature frame by shell
The conduit saddle at frame both ends is horizontal to be mounted in shell heat preservation frame, and shell heat preservation frame is connected with flue inner wall face.
It includes frame, inner casing, outer casing and thermal insulation material that shell, which keeps the temperature frame, and inner casing is arranged in frame side, outside
Backplate is arranged on the outside of frame, and filled thermal insulation materials are between inner casing and outer casing.
Heat-exchange tube group includes several heat-exchange tube bundles being arranged in in-line or stagger arrangement.
Heat-exchange tube bundle is snakelike light pipe or membrane tube.
With the above structure, dry flue gas of the flue gas through flue for putting out heat exchange tower generation of electric-melting magnesium inputs the utility model
The flue for mouthful entering waste heat boiler, followed by the modular heat-transfer area bobbin carriage in steam superheater, evaporator and economizer, compared with
After the flue gas of high-temperature completes heat exchange cooling by waste heat boiler, foldback returns that electric-melting magnesium is dry puts out hot friendship after circulating fan aspirates
It changes tower and participates in flue gas heat exchange circulation next time.Waste heat boiler water supply enters drum after economizer heats, produced by evaporator
Steam water interface pass through tedge, down-comer and drum and constitute carbonated drink natural convection loop, the saturated vapor generated in drum
Superheated steam is generated after steam superheater further heats, is sent to heat distribution pipe network.
Electric-melting magnesium is dry to put out heat exchange tower flue gas heat to the utility model for recycling, pass through waste heat boiler setting realize it is secondary
Superheated steam is produced, the operation cost of electric-melting magnesium manufacturing enterprise is reduced.The electric-melting magnesium of the utility model is dry to put out heat exchange tower flue gas
Electric-melting magnesium is dry to put out heat exchange tower flue gas heat to waste heat boiler for recycling, and is realized while stability and high efficiency recovered flue gas heat
To the long-effective protection of environment, clean manufacturing and the benign development of electric-melting magnesium industry are promoted, sustainable development war is realized to pushing
Slightly be of great practical significance.
Description of the drawings
Fig. 1 shows a kind of dry structural schematic diagram for putting out heat exchange tower smoke and waste steam boiler of electric-melting magnesium of the utility model.
Fig. 2 shows the cross-sectional view of modular heat-transfer area bobbin carriage.
Wherein have：1. flue；2. modular heat-transfer area bobbin carriage；3. flue gas input port；4. flue gas delivery outlet；5. unloading grey dress
It sets；6. steam superheater；7. evaporator；8. economizer；9. drum；10. piping；11. tedge；12. down-comer；13. heat is handed over
Pipe group is changed, 14. shells keep the temperature frame, 15. conduit saddles, 16. inner casings, 17. frames, 18. outer casings, 19. thermal insulation materials, 20. heat
Exchange tube bank.
Specific implementation mode
The utility model is described in further detail with specific better embodiment below in conjunction with the accompanying drawings.
As depicted in figs. 1 and 2, a kind of electric-melting magnesium is dry puts out heat exchange tower smoke and waste steam boiler, including flue 1 and modular pass
Hot facial canal case 2.
Flue is straight-through shape structure, and flue top is equipped with flue gas input port 3, and bottom end is equipped with flue gas delivery outlet 4, flue gas output
The bottom surface of mouth is equipped with ash-discharging device 5.
In flue steam superheater 6, evaporator 7 and economizer 8 are equipped with successively from top to bottom along flue gas flow direction；Steam superheating
It is modular heat-transfer area bobbin carriage that device, evaporator and economizer, which are located at flue inside points,.
Side above flue is equipped with drum 9, drum by piping 10 respectively with steam superheater, evaporator and economizer
Connection, evaporator establish carbonated drink natural convection loop by tedge, down-comer and drum.
As shown in Fig. 2, modular heat-transfer area bobbin carriage includes heat-exchange tube group 13 and shell heat preservation frame 14, heat-exchange tube group
The horizontal shell that is mounted on of conduit saddle 15 that frame both ends are kept the temperature by shell is kept the temperature in frame, and shell keeps the temperature frame and flue inner wall face
It is connected.
Shell heat preservation frame includes frame 17, inner casing 16, outer casing 18 and thermal insulation material 19, and inner casing is arranged in frame
Inside, outer casing are arranged on the outside of frame, and filled thermal insulation materials are between inner casing and outer casing.
Above-mentioned heat-exchange tube group includes several heat-exchange tube bundles 20 being arranged in in-line or stagger arrangement, and heat-exchange tube bundle is preferably
Snakelike light pipe or membrane tube etc..
Flue gas flow：The dry flue gas for putting out heat exchange tower generation of electric-melting magnesium enters the flue of waste heat boiler through flue gas input port,
Followed by steam superheater 6, evaporator 7 and economizer 8, the dust in flue gas is discharged out of the furnace by ash-discharging device 8, higher temperatures
After the flue gas of degree completes heat exchange cooling by waste heat boiler, foldback Hui Gan is put out under heat exchange tower participation after circulating fan aspirates
Flue gas heat exchange circulation.
Carbonated drink flow：Waste heat boiler water supply enters drum 9 after the heating of economizer 8, steam-water mixing caused by evaporator 7
Object constitutes carbonated drink natural convection loop by tedge 11, down-comer 12 and drum 9, and the saturated vapor generated in drum 9 is through steaming
Vapour superheater 6 generates superheated steam after further heating（Or main steam）, it is sent to heat distribution pipe network, for producing and using.
Preferred embodiments of the present invention described in detail above, still, the utility model are not limited to above-mentioned reality
Apply the detail in mode, in the range of the technology design of the utility model, can to the technical solution of the utility model into
The a variety of equivalents of row, these equivalents belong to the scope of protection of the utility model.
Claims (4)
1. a kind of electric-melting magnesium is dry to put out heat exchange tower smoke and waste steam boiler, it is characterised in that：Including flue and modular heat transfer facial canal
Case；
Flue is straight-through shape structure, and flue top is equipped with flue gas input port, and bottom end is equipped with flue gas delivery outlet, the bottom of flue gas delivery outlet
Face is equipped with ash-discharging device；In flue steam superheater, evaporator and economizer are equipped with successively from top to bottom along flue gas flow direction；Steam
It is modular heat-transfer area bobbin carriage that superheater, evaporator and economizer, which are located at flue inside points,；
Side above flue is equipped with drum, and drum is connect with steam superheater, evaporator and economizer respectively by piping, steams
Hair device establishes carbonated drink natural convection loop by tedge, down-comer and drum；
Modular heat-transfer area bobbin carriage includes heat-exchange tube group and shell heat preservation frame, and heat-exchange tube group keeps the temperature frame two by shell
The conduit saddle at end is horizontal to be mounted in shell heat preservation frame, and shell heat preservation frame is connected with flue inner wall face.
2. electric-melting magnesium according to claim 1 is dry to put out heat exchange tower smoke and waste steam boiler, it is characterised in that：Shell keeps the temperature frame
Frame includes frame, inner casing, outer casing and thermal insulation material, and inner casing is arranged in frame side, and outer casing is arranged on the outside of frame,
Filled thermal insulation materials are between inner casing and outer casing.
3. electric-melting magnesium according to claim 1 is dry to put out heat exchange tower smoke and waste steam boiler, it is characterised in that：Heat-exchange tube group
Including several heat-exchange tube bundles being arranged in in-line or stagger arrangement.
4. electric-melting magnesium according to claim 3 is dry to put out heat exchange tower smoke and waste steam boiler, it is characterised in that：Heat-exchange tube bundle
For snakelike light pipe or membrane tube.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721420455.4U CN207621979U (en) | 2017-10-31 | 2017-10-31 | A kind of electric-melting magnesium is dry to put out heat exchange tower smoke and waste steam boiler |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721420455.4U CN207621979U (en) | 2017-10-31 | 2017-10-31 | A kind of electric-melting magnesium is dry to put out heat exchange tower smoke and waste steam boiler |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207621979U true CN207621979U (en) | 2018-07-17 |
Family
ID=62827163
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721420455.4U Active CN207621979U (en) | 2017-10-31 | 2017-10-31 | A kind of electric-melting magnesium is dry to put out heat exchange tower smoke and waste steam boiler |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207621979U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114317988A (en) * | 2021-12-23 | 2022-04-12 | 太原嘉能动力科技有限公司 | A device and method for sensible heat recovery of magnesium slag |
-
2017
- 2017-10-31 CN CN201721420455.4U patent/CN207621979U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114317988A (en) * | 2021-12-23 | 2022-04-12 | 太原嘉能动力科技有限公司 | A device and method for sensible heat recovery of magnesium slag |
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |