CN201836849U - Recovery unit for waste heat of high-temperature industrial slag - Google Patents
Recovery unit for waste heat of high-temperature industrial slag Download PDFInfo
- Publication number
- CN201836849U CN201836849U CN2010205240282U CN201020524028U CN201836849U CN 201836849 U CN201836849 U CN 201836849U CN 2010205240282 U CN2010205240282 U CN 2010205240282U CN 201020524028 U CN201020524028 U CN 201020524028U CN 201836849 U CN201836849 U CN 201836849U
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- membrane wall
- casing
- waste heat
- drum
- waste
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- 239000002918 waste heat Substances 0.000 title claims abstract description 49
- 239000002893 slag Substances 0.000 title claims abstract description 41
- 238000011084 recovery Methods 0.000 title claims abstract description 29
- 239000012528 membrane Substances 0.000 claims abstract description 58
- 238000004519 manufacturing process Methods 0.000 abstract description 10
- 239000000428 dust Substances 0.000 abstract description 4
- 239000000843 powder Substances 0.000 abstract description 2
- 230000001174 ascending effect Effects 0.000 abstract 2
- 238000005265 energy consumption Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 36
- 238000007670 refining Methods 0.000 description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 11
- 238000003723 Smelting Methods 0.000 description 10
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 6
- 229910000861 Mg alloy Inorganic materials 0.000 description 6
- 229910052749 magnesium Inorganic materials 0.000 description 6
- 239000011777 magnesium Substances 0.000 description 6
- 239000002994 raw material Substances 0.000 description 6
- 239000003638 chemical reducing agent Substances 0.000 description 5
- 239000002699 waste material Substances 0.000 description 4
- 241000196324 Embryophyta Species 0.000 description 3
- 229910000519 Ferrosilicon Inorganic materials 0.000 description 3
- 229910000831 Steel Inorganic materials 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000010959 steel Substances 0.000 description 3
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 2
- 235000003283 Pachira macrocarpa Nutrition 0.000 description 2
- 241001083492 Trapa Species 0.000 description 2
- 235000014364 Trapa natans Nutrition 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 239000000571 coke Substances 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 238000009413 insulation Methods 0.000 description 2
- 239000012774 insulation material Substances 0.000 description 2
- 238000010926 purge Methods 0.000 description 2
- 235000009165 saligot Nutrition 0.000 description 2
- 239000002912 waste gas Substances 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 238000003466 welding Methods 0.000 description 2
- 229910000851 Alloy steel Inorganic materials 0.000 description 1
- 239000005997 Calcium carbide Substances 0.000 description 1
- 229910001570 bauxite Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- WUKWITHWXAAZEY-UHFFFAOYSA-L calcium difluoride Chemical compound [F-].[F-].[Ca+2] WUKWITHWXAAZEY-UHFFFAOYSA-L 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 239000003818 cinder Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000010459 dolomite Substances 0.000 description 1
- 229910000514 dolomite Inorganic materials 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 239000010436 fluorite Substances 0.000 description 1
- 238000013467 fragmentation Methods 0.000 description 1
- 238000006062 fragmentation reaction Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 238000005065 mining Methods 0.000 description 1
- 239000002006 petroleum coke Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- CLZWAWBPWVRRGI-UHFFFAOYSA-N tert-butyl 2-[2-[2-[2-[bis[2-[(2-methylpropan-2-yl)oxy]-2-oxoethyl]amino]-5-bromophenoxy]ethoxy]-4-methyl-n-[2-[(2-methylpropan-2-yl)oxy]-2-oxoethyl]anilino]acetate Chemical compound CC1=CC=C(N(CC(=O)OC(C)(C)C)CC(=O)OC(C)(C)C)C(OCCOC=2C(=CC=C(Br)C=2)N(CC(=O)OC(C)(C)C)CC(=O)OC(C)(C)C)=C1 CLZWAWBPWVRRGI-UHFFFAOYSA-N 0.000 description 1
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- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
Abstract
The utility model discloses a recovery unit for waste heat of high-temperature industrial slag, relating to the field of waste heat recovery. A waste heat boiler box assembly is arranged at the upper part of a support, the main body of the box assembly is a box with a membrane wall, the inner row of cabins of the tubular membrane wall are arranged in the tubular membrane wall at intervals, the inner row of cabin of each tubular membrane wall is through up and down, and the lowermost part of the box with a membrane wall is connected with a rotary slagging device. A steam pocket body is arranged at the upper part of the waste heat boiler box assembly, a steam pocket ascending pipe at the side part of the steam pocket body is connected with an upper collection box of box with a membrane wall, a steam pocket descending pipe at the lower part of the steam pocket body is connected with a lower collection box of the box with a membrane wall, and both the steam pocket ascending pipe and the steam pocket descending pipe are communicated with the interior of the steam pocket body by pipes. The recovery unit solves the problems in the prior art that spherical slag can not be crushed into powder along with temperature reduction, and waste heat is hard to recycle; furthermore, an additional dust collecting device is not needed, energy consumption and equipment investment are reduced, and energy-saving and environment-friendly production is facilitated.
Description
Technical field
The utility model relates to the heat recovery field, relates in particular to a kind of device that the heat that should distribute of hot industry slag is reclaimed.
Background technology
At present, because the requirement in ore deposit increases suddenly, can not satisfy the demand in the ore deposit that fused salt electrolysis process refining ore deposit produces, usually use a kind of mining and metallurgy smelting method that at high temperature oxide ore is reduced into metallic ore at each tame iron-smelter, steel mill in the process of smelting with reducing agent, this method is referred to as reducing process, also claim thermal reduction, thermal reduction refining ore deposit method has Pidgeon process refining ore deposit method, semicontinuous smelting silicothermic process ore deposit method, bohr Zha Nuofa refining ore deposit method, carbothermy refining ore deposit and the hot method refining of carbide ore deposit method etc., and characteristics are as described below separately for it:
1. Pidgeon process refining ore deposit method is raw material with the dolime, and ferrosilicon is a reducing agent, adds fluorite, and material is loaded in the heat-resisting alloy steel reduction jar through grinding briquetting, and metallic ore is produced in reduction under 1473K temperature, 1～10Pa vacuum;
2. semicontinuous smelting silicothermic process ore deposit method adopts continuously and regularly feeds in raw material, periodically ore removal is slagged tap, so be called semicontinuous ferrosilicon process.This method is a raw material with dolomite, bauxite, and ferrosilicon is a reducing agent, goes back the original production metallic ore in the single-phase vacuum electric furnace under 1773～1873K, 3400～4000Pa vacuum;
3. bohr Zha Nuofa refining ore deposit method is improving one's methods of Pidgeon process refining ore deposit, adopts vertical electric internal thermal reducing furnace.Carbothermy refining ore deposit is a raw material with ore deposit, water chestnut ore deposit, and coke or petroleum coke are reducing agent, after briquetting, reduces operating mine in three-phawse arc furnace under 2273～2573K temperature;
4. the hot method refining of carbide ore deposit method is a raw material with ore deposit, water chestnut ore deposit, and calcium carbide is reducing agent, and its production method is similar to Pidgeon process refining ore deposit basically.
Be applicable to relatively that wherein industry refining ore deposit is three kinds of Pidgeon process refining ore deposit method, semicontinuous smelting silicothermic process ore deposit method and bohr Zha Nuofa refining ore deposit methods etc.
And in the process in above-mentioned various reducing process refinings ore deposit, the hot industry slag that must have a large amount of temperature to be about 1200 ℃ is discharged, in order to utilize this part energy, conventional method is as the high temperature chamotte in the manufacture of cement, adopt air-cooled method that heat is cemented out from grog, make cold wind become hot blast, produce steam by waste heat boiler again, be used for generating electricity or heat supply.But this method is difficult to be applied to the heat recovery field of hot industry slag, wear into and suppress balling-up again after powder mixes because slag is various raw materials, most of still spherical under the condition of high temperature after smelting, but along with decrease of temperature, spherical slag fragmentation, become powdery again, be mixed in and add dust arrester in the hot blast and could discharge, very likely will consume more energy and a large amount of investments in order to save this part energy.
Application number 200610200646.X, Chinese patent, a kind of magnesium and the magnesium alloy resource cyclic utilization system of on 06 30th, 2006 applying date.The formation of this system comprises the smeltery that magnesium and magnesium alloy are produced, Mg-slag brick factory, calcium carbonate factory, coal water mixture plant that waste residue, waste water, the waste gas that produces in magnesium and the magnesium alloy production process is utilized again, and waste heat steam boiler, life office heating circulating cooling system; The smeltery comprises the rotary kiln workshop that mainly comprises magnesium and magnesium alloy production process, reduction plant, magnesium refining plant, magnesium alloy smelting shop; This system also carries out purified treatment to finally discharged gas, makes the gas of discharging meet the discharge standard that low temperature hangs down dirt.
The a large amount of industrial residues that produce in the smelting production process of this patent utilization magnesium and magnesium alloy, industrial wastewater and industrial waste gas carry out recyclingly, have reduced these waste residues of business processes, and the expense of waste water and waste gas can reduce the pollution to environment.Yet the present application surface of this patent is narrower, and has the same problem with the method for high-temperature coke CDQ waste heat recovery, that is, the equipment manufacturing cost costliness is so be difficult to promote in the enterprise of middle-size and small-size refining ore deposit.
In sum, owing to can't effectively get up the waste heat Btu utilization of this part hot industry slag, cause a large amount of wastes of energy, and, in order to reduce the temperature of this part high temperature cinder, be convenient to landfill and processing, must consume a large amount of water under a lot of situations and make its cooling, cause the great amount of water resources waste virtually again.So now press for a kind of novel slag waste-heat recovery device, not only can solve and under the prior art spherical slag is broken into Powderedly along with temperature reduces, waste heat is difficult to recycle, and needs the problem of extra dedusting, and needs simple in structurely, is easy to promote.
The utility model content
In order to solve the waste heat energy that is difficult to recycle the hot industry slag under the prior art, the utility model provides a kind of waste-heat recovery device of hot industry slag, and its concrete structure is as described below:
A kind of waste-heat recovery device of hot industry slag comprises support, it is characterized in that:
The top of described support is provided with a waste heat boiler box assembly, being connected with a drum assembly again of this waste heat boiler box assembly.
Waste-heat recovery device according to a kind of hot industry slag of the present utility model, it is characterized in that, described waste heat boiler box assembly, the membrane wall casing that comprises the membrane wall form, the casing upper collecting chamber, casing next part case, row's bin and rotary slagging coutrol device in the tubulose membrane wall of membrane wall form, its main body that is specially the waste heat boiler box assembly is the membrane wall casing, the casing upper collecting chamber is arranged at the top of casing, casing next part case then is arranged at the bottom of casing, and the inside of this casing is spaced and is formed by row's bin in the tubulose membrane wall, and row's bin is got through up and down in each tubulose membrane wall, connects at the foot of membrane wall casing a rotary slagging coutrol device is set.
The waste-heat recovery device of hot industry slag of the present utility model, row's bin has all adopted the membrane wall form in the membrane wall casing of its waste heat boiler box assembly and the tubulose membrane wall, compare with traditional heavy boiler setting, the furnace wall of the boiler of membrane wall form is in blocks with pipe and fin welding, have simple, save advantage such as steel, insulation is just passable as long as lay the silicate insulation material outside stove, need not build refractory brickwork, expand evenly, have the higher thermal efficiency.
During work, the high temperature slag is poured the interior interior row of the tubulose membrane wall bin of membrane wall casing of waste heat boiler box assembly into, and the big I of body of row's bin is selected according to the big freedom in minor affairs of slag in this tubulose membrane wall, note during installation being spaced getting final product, slag dwell phase in bin is the heat recovery stage, because bin is for being spaced composition, promptly equal to have increased heat-transfer surface, improved heat exchange efficiency, in the tubulose membrane wall, arrange time of staying in the bin in order to control slag, reclaim used heat how more economically, connect at the foot of membrane wall casing a rotary slagging coutrol device is set, control bed drain purge by the rotating speed of controlling this rotary slagging coutrol device.
Waste-heat recovery device according to a kind of hot industry slag of the present utility model, it is characterized in that, described drum assembly, comprise drum body, drum tedge and drum down-comer, it is specially the membrane wall casing top that the drum body is arranged at the waste heat boiler box assembly, the drum tedge of drum body sidepiece is connected with the casing upper collecting chamber of membrane wall casing, and the drum down-comer of drum body bottom is connected with the casing next part case of membrane wall casing, and drum tedge and drum down-comer all are connected with the drum body interior by pipeline.
Be arranged at the drum body on membrane wall casing top, set up the water circulation in the heat-transfer surface, the upper and lower heat-collecting box of the casing of membrane wall casing is connected with the drum down-comer with the drum tedge of the drum body that is located at membrane wall casing top respectively, utilizes the cold water and the gravitational difference of heat absorption back hot water to finish the Natural Circulation of the water in the membrane wall.
Use the waste-heat recovery device of hot industry slag of the present utility model, obtain following beneficial effect:
1. the waste-heat recovery device of hot industry slag of the present utility model is simple in structure, and cost is lower, is applicable to middle-size and small-size smelting ore deposit enterprise, also can be applied to relatively large smelting ore deposit enterprise after its structure is enlarged in proportion;
2. the waste-heat recovery device of hot industry slag of the present utility model has solved under the prior art Powdered along with the temperature reduction is broken into to spherical slag, the problem that waste heat is difficult to recycle;
3. the waste-heat recovery device of hot industry slag of the present utility model need not extra dust arrester, has directly reduced energy resource consumption and equipment investment, helps energy-conserving and environment-protective production.
Description of drawings
Fig. 1 is the concrete structure front view of the waste-heat recovery device of a kind of hot industry slag of the present utility model;
Fig. 2 is the concrete structure side view of the waste-heat recovery device of a kind of hot industry slag of the present utility model.
Among the figure: 1-support, A-waste heat boiler box assembly, A1-membrane wall casing, A11-casing upper collecting chamber, row's bin in the A12-casing next part case, A2-tubulose membrane wall, A3-rotary slagging coutrol device, B-drum assembly, B1-drum body, B2-drum tedge, B3-drum down-comer.
The specific embodiment
Be described further below in conjunction with the waste-heat recovery device of drawings and Examples hot industry slag of the present utility model.
As depicted in figs. 1 and 2, that step is set is as follows in the concrete installation of the waste-heat recovery device of hot industry slag of the present utility model:
The waste heat boiler box assembly A that the amount of handling according to required slag adopts a size to be fit to, it is mounted on the support 1, it adopts the membrane wall casing A1 of membrane wall form, compare with traditional heavy boiler setting, the furnace wall of the boiler of membrane wall form is in blocks with pipe and fin welding, has simply, saves advantages such as steel, insulation is just passable as long as lay the silicate insulation material outside stove, need not build refractory brickwork, expand evenly, have the higher thermal efficiency.
Then the inside of this membrane wall casing A1 by the tubulose membrane wall in row's bin A2 be spaced and form, and row's bin is got through up and down in each tubulose membrane wall, during work, the high temperature slag is poured the interior interior row of the tubulose membrane wall bin of membrane wall casing of waste heat boiler box assembly into, slag dwell phase in bin is the heat recovery stage, because bin is for being spaced composition, promptly equal to have increased heat-transfer surface, improved heat exchange efficiency, in the tubulose membrane wall, arrange time of staying in the bin in order to control slag, reclaim used heat how more economically, foot connection at the membrane wall casing is provided with a rotary slagging coutrol device A3, by bed drain purge is controlled in the control of this rotary slagging coutrol device rotary speed.
Then the drum body 1 of a drum assembly B is arranged at the membrane wall casing A1 top of waste heat boiler box assembly A, set up the water circulation in the heat-transfer surface, the drum tedge B2 of drum body sidepiece is connected with the casing upper collecting chamber A11 of membrane wall casing, and the drum down-comer B3 of drum body bottom is connected with the casing next part case A12 of membrane wall casing, and drum tedge and drum down-comer all are connected with the drum body interior by pipeline, utilize the cold water and the gravitational difference of heat absorption back hot water to finish the Natural Circulation of the water in the membrane wall.
The waste-heat recovery device of hot industry slag so far of the present utility model can use, the utility model is simple in structure, cost is lower, solved and be difficult under the prior art be broken into Powdered along with temperature reduces spherical slag, the problem that waste heat is difficult to recycle, and need not extra dust arrester, directly reduced energy resource consumption and equipment investment, help energy-conserving and environment-protective production, be applicable to the heat recovery field.
Claims (3)
1. the waste-heat recovery device of a hot industry slag comprises support (1), it is characterized in that:
The top of described support (1) is provided with a waste heat boiler box assembly (A), being connected with a drum assembly (B) again of this waste heat boiler box assembly.
2. the waste-heat recovery device of a kind of hot industry slag as claimed in claim 1, it is characterized in that, described waste heat boiler box assembly (A), the membrane wall casing (A1) that comprises the membrane wall form, casing upper collecting chamber (A11), casing next part case (A12), row's bin (A2) and rotary slagging coutrol device (A3) in the tubulose membrane wall of membrane wall form, its main body that is specially the waste heat boiler box assembly is the membrane wall casing, the casing upper collecting chamber is arranged at the top of casing, casing next part case then is arranged at the bottom of casing, and the inside of this casing is spaced and is formed by row's bin in the tubulose membrane wall, and row's bin is got through up and down in each tubulose membrane wall, connects at the foot of membrane wall casing a rotary slagging coutrol device is set.
3. the waste-heat recovery device of a kind of hot industry slag as claimed in claim 1, it is characterized in that, described drum assembly (B), comprise drum body (B1), drum tedge (B2) and drum down-comer (B3), it is specially membrane wall casing (A1) top that the drum body is arranged at waste heat boiler box assembly (A), the drum tedge of drum body sidepiece is connected with the casing upper collecting chamber (A11) of membrane wall casing, and the drum down-comer of drum body bottom is connected with the casing next part case (A12) of membrane wall casing, and drum tedge and drum down-comer all are connected with the drum body interior by pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205240282U CN201836849U (en) | 2010-09-09 | 2010-09-09 | Recovery unit for waste heat of high-temperature industrial slag |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205240282U CN201836849U (en) | 2010-09-09 | 2010-09-09 | Recovery unit for waste heat of high-temperature industrial slag |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201836849U true CN201836849U (en) | 2011-05-18 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN2010205240282U Expired - Fee Related CN201836849U (en) | 2010-09-09 | 2010-09-09 | Recovery unit for waste heat of high-temperature industrial slag |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102966935A (en) * | 2012-12-04 | 2013-03-13 | 中国科学院电工研究所 | A molten salt steam generator |
| CN103123205A (en) * | 2013-03-07 | 2013-05-29 | 浙江大学 | Fluidization moving series arrangement steam drying system and technology |
| CN103574567A (en) * | 2012-08-04 | 2014-02-12 | 回红 | Device for reclaiming heat energy from hot dregs |
| CN103644745A (en) * | 2013-12-27 | 2014-03-19 | 济宁华德环保能源科技有限责任公司 | Slag cooler for calcinator |
| CN115493444A (en) * | 2022-10-26 | 2022-12-20 | 中国建筑西北设计研究院有限公司 | A device and method for utilizing waste heat of magnesium slag |
-
2010
- 2010-09-09 CN CN2010205240282U patent/CN201836849U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103574567A (en) * | 2012-08-04 | 2014-02-12 | 回红 | Device for reclaiming heat energy from hot dregs |
| CN102966935A (en) * | 2012-12-04 | 2013-03-13 | 中国科学院电工研究所 | A molten salt steam generator |
| CN102966935B (en) * | 2012-12-04 | 2014-12-03 | 中国科学院电工研究所 | Molten salt steam generator |
| CN103123205A (en) * | 2013-03-07 | 2013-05-29 | 浙江大学 | Fluidization moving series arrangement steam drying system and technology |
| CN103644745A (en) * | 2013-12-27 | 2014-03-19 | 济宁华德环保能源科技有限责任公司 | Slag cooler for calcinator |
| CN115493444A (en) * | 2022-10-26 | 2022-12-20 | 中国建筑西北设计研究院有限公司 | A device and method for utilizing waste heat of magnesium slag |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
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Granted publication date: 20110518 Termination date: 20160909 |