CN102424867A - Slag granulating and waste heat recovery device - Google Patents
Slag granulating and waste heat recovery device Download PDFInfo
- Publication number
- CN102424867A CN102424867A CN2011104606924A CN201110460692A CN102424867A CN 102424867 A CN102424867 A CN 102424867A CN 2011104606924 A CN2011104606924 A CN 2011104606924A CN 201110460692 A CN201110460692 A CN 201110460692A CN 102424867 A CN102424867 A CN 102424867A
- Authority
- CN
- China
- Prior art keywords
- slag
- waste heat
- cooling air
- ladle
- granulating
- 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.)
- Granted
Links
Images
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
- Y02P10/20—Recycling
-
- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
Landscapes
- Manufacture Of Iron (AREA)
- Curing Cements, Concrete, And Artificial Stone (AREA)
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
Abstract
The invention provides a slag granulating and waste heat recovery device, comprising a slag pot, a slag ladle, a granulating device, a primary cooling fan, a discharge device, a secondary cooling fan, a heat exchange shaft furnace, a cyclone dust collector, a waste heat boiler, a dust collector and a chimney, wherein the slag pot is used for containing slag; a water port is arranged at the lower part of the slag ladle; the granulating device is used for granulating the slag in the slag ladle; the primary cooling fan is used for providing primary cooling air; the discharge device is used for discharging granulated slag; the secondary cooling fan is used for providing secondary cooling air; the heat exchange shaft furnace is used for performing heat exchange between the granulated slag discharged by the discharge device and the secondary cooling air; the cyclone dust collector is used for removing fine particle slag from the primary cooling air and the secondary cooling air; the waste heat boiler is used for generating high-temperature stream; the dust collector is used for collecting dust in the tail gas generated by the waste heat boiler; and the chimney is used for discharging the tail gas after dust collection. By using the slag granulating and waste heat recovery device according to the invention, no new water is consumed in the slag granulating process, the slag waste heat can be effectively recovered for power generation, and the slag vitreous body after treatment can be used as a construction raw material.
Description
Technical field
The present invention relates to a kind of slag granulation and waste-heat recovery device, specifically, relate to a kind of slag dry type granulation and waste-heat recovery device.
Background technology
Metallurgical slag is the by product of steel manufacture process, is mainly derived from ironmaking and steel making working procedure.Blast furnace slag 300～400kg that the pig iron per ton produces, converter slag 80～120kg that steel per ton produces.The treatment process of at present domestic and international blast furnace slag mainly adopts the mode of shrend, promptly with high pressure water the high-temperature liquid state blast furnace slag is washed into the solid granulates shape.The subject matter that the flush slag mode is brought is: (1) takies water resources and consumption of new water in a large number, about the flushing cinder water consumption 10t of liquid blast furnace per ton, about consumption of new water 1t.(2) wasted secondhand energy, the physics heat of high-temperature liquid state blast furnace slag per ton is equivalent to about 60kg mark coal, in the flushing cinder process, all dissipates.And see that with the angle of analyzing the waste heat quality of liquid blast furnace is very high from fire, have utility value.(3) discharging H
2S and SO
x, destroy ecotope, produce a large amount of H in the flush slag process
2S and SO
x, enter in the atmosphere with water vapour, gather the inducement that to a certain degree just becomes acid rain.
In sum, at present general metallurgical slag Water Quenching technology that adopts and metallurgical slag utilize mode, not only wasted a large amount of new water resourcess, and environment caused very serious pollution, also reduced the service efficiency of the energy and resource simultaneously.This method far can not adapt to the Development patterns of new industrialization and recycling economy, and fundamentally change is with discarded.
Summary of the invention
In order to overcome the problems of the prior art, the object of the present invention is to provide a kind of easy to use under hot environment, efficient is higher is used for the device with slag dry type granulation and recovery waste heat.Said device comprises: slag ladle, be used to hold slag, and the inner main material of said slag ladle is a refractory brick, slag ladle diameter 0.5-1.5m, high 1-2m; Cinder ladle is used for buffering, storage slag, and the inner main material of said cinder ladle is a refractory brick, cinder ladle diameter 0.5-1m, and high 1-1.5m, the bottom is provided with the mouth of a river, mouth of a river diameter 50-100mm; Granulating device is used for the slag granulation with said cinder ladle; Discharge device is used to discharge grain slag; A cooling blower is used to provide cooling air one time; The secondary cooling blower is used to provide the secondary cooling air; The heat exchange shaft furnace is used for grain slag and said secondary cooling air that said discharge device is discharged are carried out heat exchange, said heat exchange shaft furnace diameter 3-5m, high 5-10m; Tornado dust collector are used for removing the fine particle slag of said first cooling air and second cooling air, and said tornado dust collector inside is the high strength anti firebrick; Waste heat boiler is used to produce high-temperature steam; Fly-ash separator is used for the tail gas that said waste heat boiler produces is carried out dedusting; Chimney is discharged the tail gas after the said dedusting.
Cinder ladle in the middle of said device also comprises is used to make the slag liquid level to maintain certain altitude, and with control slag liquid dirty speed, middle cinder ladle slag liquid surface height controlling is at 1.4-1.6m, said in the middle of cinder ladle diameter 0.8-1.2m, high 1.5-2.5m.
Cinder ladle comprises the mouth of a river in the middle of said, and the said mouth of a river is provided with stopper and controls slagging speed, carries out granulated processed thereby slag liquid is added said granulating device quantitatively.
Said device also comprises the power pack that links to each other with said waste heat boiler, is used for utilizing said high-temperature steam generating.
Said device also comprises the recirculation blower that links to each other with said fly-ash separator, is used for tail gas after said waste heat boiler provides dedusting.
Said granulating device is the double pair roller pelletizer that is made up of last row's roller and lower roll; Saidly go up the granulation that row's roller carries out slag, lower roll is to whole grain of grain slag and discharge, on arrange the pair roller rotating speed and be controlled at 150-300r/min; Linear resonance surface velocity is not more than 8m/s; Last row is to roller diameter 0.5-1m, and power of motor 70-80kw, following row's power of motor 20-25kw are overlapped in last deploying.
The inner chamber of the said row's of going up roller and said lower roll all is filled with the water coolant of temperature in 0-20 ℃ scope.
The temperature of water coolant is in 0-10 ℃ scope.
The sidewall of said double pair roller pelletizer is provided with bostle pipe and nozzle, with further cooling grain slag.
Said discharge device is a lock gas removal device, is made by high temperature steel, and rotating speed is 25-40r/min, and the revolution withdrawal rate is 40 liters, adopts the variable frequency regulating speed control withdrawal rate, and power of motor is 4kw.
Adopt slag granulation of the present invention and waste-heat recovery device; Make slag treatment not have new water consumption, can reclaim 600-700 ℃ of flue gas, heat recovery efficiency 60-80%; Slag vitreum content after handling simultaneously is greater than 95%, for example can be used as the building materials raw material and is used.
Description of drawings
Through the description of the exemplary embodiment of carrying out below in conjunction with accompanying drawing, these and/or other aspect of the present invention and advantage will become obviously and be easier to and understand, in the accompanying drawing:
Fig. 1 illustrates the synoptic diagram of slag granulation and waste-heat recovery device according to an exemplary embodiment of the present invention.
Fig. 2 is the partial enlarged view of Fig. 1.
The drawing reference numeral explanation:
1 slag ladle, 2 cinder ladles
Cinder ladle 4 nozzles in the middle of 3
5 sizings/6 cooling blowers of slip water
7 granulating devices, 8 discharge devices
9 heat exchange shaft furnaces, 10 secondary cooling blowers
11 tornado dust collector, 12 waste heat boilers
13 power unit, 14 fly-ash separators
15 recirculation blowers, 16 chimneys
Embodiment
See figures.1.and.2, comprise: slag ladle 1, cinder ladle 2, nozzle 4, cooling blower 6, granulating device 7, discharge device 8, heat exchange shaft furnace 9, secondary cooling blower 10, tornado dust collector 11, waste heat boiler 12, fly-ash separator 14, chimney 16 according to slag granulation of the present invention and waste-heat recovery device.
Slag ladle 1 holds the slag that produces in the steel smelting procedure, can slag ladle 1 be transported to the slag treatment place through slag car.Can pour in the cinder ladle 2 through the slag that crane will be contained in the slag ladle 1.The inner main material of slag ladle is a refractory brick, slag ladle diameter 0.5-1.5m, high 1-2m.
The bottom of cinder ladle 2 is provided with mouth of a river (not shown), in granulating device 7, carries out granulated processed with control slag flow, and wherein, the said mouth of a river can be a slide gate nozzle.The inner main material of cinder ladle is a refractory brick, cinder ladle diameter 0.5-1m, high 1-1.5m.
The double pair roller pelletizer that granulating device 7 can be made up of the two rows pair roller.Last row roller carries out the granulation of slag, and lower roll is to whole grain of grain slag and discharge, on arrange the pair roller rotating speed and be controlled at 150-300r/min; Linear resonance surface velocity is not more than 8m/s; Last row is to roller diameter 0.5-1m, and power of motor 70-80kw, following row's power of motor 20-25kw are overlapped in last deploying.It is 0-20 ℃ water coolant that the inner chamber that last row roller and row down roll all is filled with TR.Preferably, the temperature of water coolant is 0-10 ℃.Roll surface temperature through processing under cooling is lower than 300 ℃, crusts fast with the slag that guarantees the roll surface place.The invention is not restricted to this, can also use other dry type granulating devices.
In reference exemplary embodiment of the present invention shown in Figure 1, cinder ladle 3 in the middle of slag granulation and waste-heat recovery device also comprise is so that the slag liquid level maintains certain altitude, with the dirty speed of control slag liquid.The slide gate nozzle control slag flow that is provided with in cinder ladle 2 bottoms is to middle cinder ladle 3.Middle cinder ladle slag liquid surface height controlling is at 1.4-1.6m, slag notch diameter 60-100mm, and tundish diameter 0.8-1.2m, high 1.5-2.5m, slag notch is provided with stopper, control slagging speed.The bottom of middle cinder ladle 3 is provided with sizing/slide gate nozzle 5, carries out granulated processed in the granulating device 7 thereby slag liquid is flowed into quantitatively, and wherein, slide gate nozzle can be realized through stopper.
The sidewall of granulating device 7 is provided with bostle pipe (not shown) and high-velocity nozzle 4, sprays into the cooling air that cooling blower 6 blows out through high-velocity nozzle 4, crusts again thereby make by the grain slag of the band liquid core of granulating device 7 broken shells.In this process, the freezing air temperature raises gradually, and the grain slag temperature descends gradually.Cool off a back cooling air temperature and be about 500 ℃, the grain slag temperature is lower than 750 ℃, has prevented that effectively grain slag from luming again.Cooling blower type selecting parameter: air quantity 70000m
3/ h, blast 4000Pa, wind speed 10-20m/s in the necessary electromotor power 100-120kw, bostle pipe, pipe diameter 1200-1300mm, a wind exhaust duct diameter 2000mm.
Grain slag is through discharge device 8 entering bottom heat exchange shaft furnaces 9.Discharge device 8 can be star-like lock gas removal device, and lock gas removal device adopts high temperature steel to make, and rotating speed is 25-40r/min, and the revolution withdrawal rate is 40 liters, adopts the variable frequency regulating speed control withdrawal rate, and power of motor is 4kw, but the invention is not restricted to this.The secondary cooling air countercurrent flow that high temperature grain slag and secondary cooling blower 10 blow out, the freezing air temperature raises gradually, and the grain slag temperature descends once more gradually.Secondary cooling air temperature rises to about 700 ℃.Finally, grain slag is discharged through the slag discharging device (not shown), and outflow temperature is not higher than 150 ℃.Cooling air and secondary cooling air are collected by the effuser on heat exchange shaft furnace 9 tops and are mixed, and mixed gas is discharged from and gets into tornado dust collector 11 then, thereby removes the fine particle slag.Secondary cooling blower type selecting parameter: air quantity 60000m3/h, blast 20000Pa, necessary electromotor power 500kw.
Gas after the dedusting gets into waste heat boiler 12, produces high temperature and high pressure steam, can be used to the steam that is produced through power pack 13 generatings.Power pack 13 can be the steam turbine power unit.The exhaust temperature that boiler is discharged after the heat exchange is lower than 150 ℃; Introduce fly-ash separator 14 by the induced draft fan (not shown); A part of gas enters chimney 16 after the dedusting, and the circulation of a part of gas through recirculation blower 15 blasts in the ventilation shaft furnace 9 as the secondary cooling air, can reduce heat and dissipate.Wherein, fly-ash separator 14 can be a sack cleaner, but the invention is not restricted to this.The slag of discharging from heat exchange shaft furnace 9 bottoms with the dirt ash of removing by being transported to fixedly stockyard.Heat exchange shaft furnace diameter 3-5m, high 5-10m.
Utilization is according to slag granulation of the present invention and waste-heat recovery device, and no new water consumption in the slag granulating can be reclaimed melting slag waste heat effectively and is used for generating etc. in the slag granulation.In addition, treated slag can also be used as for example building materials raw material.
It will be apparent to those skilled in the art, under the situation that does not break away from the spirit or scope of the present invention, can make various modifications and change the present invention.Therefore, the present invention is intended to cover modification of the present invention and change, as long as these modifications and change drop on the scope of claim and equivalent thereof.
Claims (10)
1. slag granulation and waste-heat recovery device, said device comprises:
Slag ladle is used to hold slag, and the inner main material of said slag ladle is a refractory brick, slag ladle diameter 0.5-1.5m, high 1-2m;
Cinder ladle is used for buffering, storage slag, and the inner main material of said cinder ladle is a refractory brick, cinder ladle diameter 0.5-1m, and high 1-1.5m, the bottom is provided with the mouth of a river, mouth of a river diameter 50-100mm;
Granulating device is used for the slag granulation with said cinder ladle;
Discharge device is used to discharge grain slag;
A cooling blower is used to provide cooling air one time;
The secondary cooling blower is used to provide the secondary cooling air;
The heat exchange shaft furnace is used for grain slag and said secondary cooling air that said discharge device is discharged are carried out heat exchange, said heat exchange shaft furnace diameter 3-5m, high 5-10m;
Tornado dust collector are used for removing the fine particle slag of said first cooling air and second cooling air, and said tornado dust collector inside is the high strength anti firebrick;
Waste heat boiler is used to produce high-temperature steam;
Fly-ash separator is used for the tail gas that said waste heat boiler produces is carried out dedusting;
Chimney is discharged the tail gas after the said dedusting.
2. cinder ladle in the middle of device as claimed in claim 1, said device also comprise is used to make the slag liquid level to maintain certain altitude; With the dirty speed of control slag liquid; Middle cinder ladle slag liquid surface height controlling is at 1.4-1.6m, said in the middle of cinder ladle diameter 0.8-1.2m, high 1.5-2.5m.
3. device as claimed in claim 2, wherein, said middle cinder ladle comprises the mouth of a river, the said mouth of a river is provided with stopper and controls slagging speed, carries out granulated processed thereby slag liquid is added said granulating device quantitatively.
4. according to claim 1 or claim 2 device, said device also comprises the power pack that links to each other with said waste heat boiler, is used for utilizing said high-temperature steam generating.
5. according to claim 1 or claim 2 device, said device also comprises the recirculation blower that links to each other with said fly-ash separator, is used for tail gas after said waste heat boiler provides dedusting.
6. according to claim 1 or claim 2 device, wherein, said granulating device is the double pair roller pelletizer that is made up of last row's roller and lower roll; Saidly go up the granulation that row's roller carries out slag, lower roll is to whole grain of grain slag and discharge, on arrange the pair roller rotating speed and be controlled at 150-300r/min; Linear resonance surface velocity is not more than 8m/s; Last row is to roller diameter 0.5-1m, and power of motor 70-80kw, following row's power of motor 20-25kw are overlapped in last deploying.
7. device as claimed in claim 6, wherein, the inner chamber of the said row's of going up roller and said lower roll all is filled with the water coolant of temperature in 0-20 ℃ scope.
8. device as claimed in claim 7, wherein, the temperature of water coolant is in 0-10 ℃ scope.
9. device as claimed in claim 6, wherein, the sidewall of said double pair roller pelletizer is provided with bostle pipe and nozzle, with further cooling grain slag.
10. according to claim 1 or claim 2 device, wherein, said discharge device is a lock gas removal device, is made by high temperature steel, and rotating speed is 25-40r/min, and the revolution withdrawal rate is 40 liters, adopts the variable frequency regulating speed control withdrawal rate, and power of motor is 4kw.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011104606924A CN102424867B (en) | 2011-12-31 | 2011-12-31 | Slag granulating and waste heat recovery device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011104606924A CN102424867B (en) | 2011-12-31 | 2011-12-31 | Slag granulating and waste heat recovery device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102424867A true CN102424867A (en) | 2012-04-25 |
| CN102424867B CN102424867B (en) | 2013-07-31 |
Family
ID=45958894
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011104606924A Expired - Fee Related CN102424867B (en) | 2011-12-31 | 2011-12-31 | Slag granulating and waste heat recovery device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102424867B (en) |
Cited By (19)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102888473A (en) * | 2012-10-01 | 2013-01-23 | 许征鹏 | Blast furnace slag granulation and waste heat recovery device |
| CN102912044A (en) * | 2012-10-22 | 2013-02-06 | 李玉亮 | Novel efficient and energy-saving dry type granulating system of slag and method thereof |
| CN105132604A (en) * | 2015-08-17 | 2015-12-09 | 北京中冶设备研究设计总院有限公司 | Slag casting heat removing device and method |
| CN105567891A (en) * | 2015-12-28 | 2016-05-11 | 蒋福军 | High-temperature liquid slag heat energy extraction method |
| CN105603135A (en) * | 2016-03-11 | 2016-05-25 | 西安交通大学 | High-temperature liquid-state slag dry type centrifugation and granulation waste heat recycling system and method |
| CN105624346A (en) * | 2016-03-11 | 2016-06-01 | 西安交通大学 | Slag buffering system with flow control function |
| CN105779673A (en) * | 2016-05-09 | 2016-07-20 | 于良富 | Blast furnace slag thermal fracture centrifugal drying method granulation device and method |
| CN105910445A (en) * | 2016-04-22 | 2016-08-31 | 中山市明阳电器有限公司 | Waste heat recovery method for fused calcium carbide |
| CN106636501A (en) * | 2017-02-27 | 2017-05-10 | 安徽工业大学 | Blast furnace slag granulation engine |
| CN106661639A (en) * | 2014-08-08 | 2017-05-10 | 首要金属科技奥地利有限责任公司 | Slag granulation system |
| CN106636502A (en) * | 2017-03-15 | 2017-05-10 | 湖南思为能源环保工程有限公司 | Waste heat recovery device for high-temperature slag wind quenching granulation fluidized bed boiler |
| CN106989608A (en) * | 2017-04-18 | 2017-07-28 | 南京工业大学 | Hot air power type granulating metallurgy liquid slag waste heat recovery system and method |
| WO2017152782A1 (en) * | 2016-03-11 | 2017-09-14 | 西安交通大学 | High-temperature liquid slag granulation and exhaust heat recovery device |
| CN109999721A (en) * | 2019-05-10 | 2019-07-12 | 攀钢集团钒钛资源股份有限公司 | Vanadium slag prilling granulator |
| CN110117164A (en) * | 2019-05-14 | 2019-08-13 | 中冶节能环保有限责任公司 | A kind of device and method of pair of fusion smelting slag glass granulation and waste heat recycling |
| WO2019161639A1 (en) * | 2018-02-26 | 2019-08-29 | 西安交通大学 | Dry type centrifugal granulation and waste heat recycling and utilization system for liquid molten slag |
| CN111170619A (en) * | 2019-12-27 | 2020-05-19 | 黄尚勇 | Glass bead production system and application thereof |
| CN111270027A (en) * | 2020-03-13 | 2020-06-12 | 钢铁研究总院 | High-temperature liquid cooling method |
| CN111351340A (en) * | 2020-03-13 | 2020-06-30 | 钢铁研究总院 | High-temperature liquid cooling device |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| SU1375600A1 (en) * | 1986-02-15 | 1988-02-23 | Всесоюзный Научно-Исследовательский Институт Механизации Труда В Черной Металлургии | Method of granulating glass |
| WO2000030989A1 (en) * | 1998-11-25 | 2000-06-02 | Holderbank Financiere Glarus Ag | Method for crushing and granulating slag |
| CN200943092Y (en) * | 2006-08-25 | 2007-09-05 | 钢铁研究总院 | Blast furnace slag dry-type graining apparatus |
| EP1970455A1 (en) * | 2007-03-10 | 2008-09-17 | Hulek, Anton, Dipl.-Ing. | Process and apparatus for dry treatment of all kinds of slags, from low viscosity to pasty |
| CN101660014A (en) * | 2009-09-24 | 2010-03-03 | 中钢集团鞍山热能研究院有限公司 | Molten blast furnace slag sensible heat recovery method and device |
| CN101850222A (en) * | 2010-04-29 | 2010-10-06 | 江苏百斯特环境工程有限公司 | Mechanical granulation and heat recovery device of liquid slag |
| CN101864504A (en) * | 2010-06-24 | 2010-10-20 | 陈瑞颖 | Method for raising air temperature of hot blast stove by recovering sensible heat of blast furnace slag |
| CN101921884A (en) * | 2009-06-12 | 2010-12-22 | 中国科学院过程工程研究所 | Blast furnace slag dry-type sensible heat recovery system and production process |
-
2011
- 2011-12-31 CN CN2011104606924A patent/CN102424867B/en not_active Expired - Fee Related
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| SU1375600A1 (en) * | 1986-02-15 | 1988-02-23 | Всесоюзный Научно-Исследовательский Институт Механизации Труда В Черной Металлургии | Method of granulating glass |
| WO2000030989A1 (en) * | 1998-11-25 | 2000-06-02 | Holderbank Financiere Glarus Ag | Method for crushing and granulating slag |
| CN200943092Y (en) * | 2006-08-25 | 2007-09-05 | 钢铁研究总院 | Blast furnace slag dry-type graining apparatus |
| EP1970455A1 (en) * | 2007-03-10 | 2008-09-17 | Hulek, Anton, Dipl.-Ing. | Process and apparatus for dry treatment of all kinds of slags, from low viscosity to pasty |
| CN101921884A (en) * | 2009-06-12 | 2010-12-22 | 中国科学院过程工程研究所 | Blast furnace slag dry-type sensible heat recovery system and production process |
| CN101660014A (en) * | 2009-09-24 | 2010-03-03 | 中钢集团鞍山热能研究院有限公司 | Molten blast furnace slag sensible heat recovery method and device |
| CN101850222A (en) * | 2010-04-29 | 2010-10-06 | 江苏百斯特环境工程有限公司 | Mechanical granulation and heat recovery device of liquid slag |
| CN101864504A (en) * | 2010-06-24 | 2010-10-20 | 陈瑞颖 | Method for raising air temperature of hot blast stove by recovering sensible heat of blast furnace slag |
Non-Patent Citations (1)
| Title |
|---|
| 徐永通等: "高炉熔渣干式显热回收技术研究进展", 《中国冶金》 * |
Cited By (26)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102888473B (en) * | 2012-10-01 | 2014-02-19 | 许征鹏 | Blast furnace slag granulation and waste heat recovery device |
| CN102888473A (en) * | 2012-10-01 | 2013-01-23 | 许征鹏 | Blast furnace slag granulation and waste heat recovery device |
| CN102912044A (en) * | 2012-10-22 | 2013-02-06 | 李玉亮 | Novel efficient and energy-saving dry type granulating system of slag and method thereof |
| CN106661639A (en) * | 2014-08-08 | 2017-05-10 | 首要金属科技奥地利有限责任公司 | Slag granulation system |
| CN105132604A (en) * | 2015-08-17 | 2015-12-09 | 北京中冶设备研究设计总院有限公司 | Slag casting heat removing device and method |
| CN105567891A (en) * | 2015-12-28 | 2016-05-11 | 蒋福军 | High-temperature liquid slag heat energy extraction method |
| CN105624346A (en) * | 2016-03-11 | 2016-06-01 | 西安交通大学 | Slag buffering system with flow control function |
| CN105603135A (en) * | 2016-03-11 | 2016-05-25 | 西安交通大学 | High-temperature liquid-state slag dry type centrifugation and granulation waste heat recycling system and method |
| WO2017152784A1 (en) * | 2016-03-11 | 2017-09-14 | 西安交通大学 | System and method for dry centrifugal granulation of high_temperature liquid slag and exhaust heat recovery |
| WO2017152782A1 (en) * | 2016-03-11 | 2017-09-14 | 西安交通大学 | High-temperature liquid slag granulation and exhaust heat recovery device |
| CN105603135B (en) * | 2016-03-11 | 2018-12-07 | 西安交通大学 | A kind of high-temperature liquid state slag dry-type centrifugal granulation residual neat recovering system and method |
| CN105910445A (en) * | 2016-04-22 | 2016-08-31 | 中山市明阳电器有限公司 | Waste heat recovery method for fused calcium carbide |
| CN105779673A (en) * | 2016-05-09 | 2016-07-20 | 于良富 | Blast furnace slag thermal fracture centrifugal drying method granulation device and method |
| CN106636501A (en) * | 2017-02-27 | 2017-05-10 | 安徽工业大学 | Blast furnace slag granulation engine |
| CN106636501B (en) * | 2017-02-27 | 2019-03-05 | 安徽工业大学 | A kind of blast furnace slag granulation engine |
| CN106636502A (en) * | 2017-03-15 | 2017-05-10 | 湖南思为能源环保工程有限公司 | Waste heat recovery device for high-temperature slag wind quenching granulation fluidized bed boiler |
| CN106636502B (en) * | 2017-03-15 | 2019-04-30 | 湖南思为能源环保工程有限公司 | A kind of high temperature furnace slag wind quenching granulation fluidized-bed combustion boiler waste-heat recovery device |
| CN106989608A (en) * | 2017-04-18 | 2017-07-28 | 南京工业大学 | Hot air power type granulating metallurgy liquid slag waste heat recovery system and method |
| CN106989608B (en) * | 2017-04-18 | 2023-04-28 | 南京工业大学 | Hot air power type granulating metallurgical liquid slag waste heat recovery system and method |
| WO2019161639A1 (en) * | 2018-02-26 | 2019-08-29 | 西安交通大学 | Dry type centrifugal granulation and waste heat recycling and utilization system for liquid molten slag |
| CN109999721A (en) * | 2019-05-10 | 2019-07-12 | 攀钢集团钒钛资源股份有限公司 | Vanadium slag prilling granulator |
| CN110117164A (en) * | 2019-05-14 | 2019-08-13 | 中冶节能环保有限责任公司 | A kind of device and method of pair of fusion smelting slag glass granulation and waste heat recycling |
| CN111170619A (en) * | 2019-12-27 | 2020-05-19 | 黄尚勇 | Glass bead production system and application thereof |
| CN111270027A (en) * | 2020-03-13 | 2020-06-12 | 钢铁研究总院 | High-temperature liquid cooling method |
| CN111351340A (en) * | 2020-03-13 | 2020-06-30 | 钢铁研究总院 | High-temperature liquid cooling device |
| CN111270027B (en) * | 2020-03-13 | 2021-05-07 | 钢铁研究总院 | High-temperature liquid cooling method |
Also Published As
| Publication number | Publication date |
|---|---|
| CN102424867B (en) | 2013-07-31 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102424867B (en) | Slag granulating and waste heat recovery device | |
| CN107916312B (en) | Steel slag dry process and waste heat recycling and electricity-generating method | |
| WO2017152784A1 (en) | System and method for dry centrifugal granulation of high_temperature liquid slag and exhaust heat recovery | |
| CN102827969B (en) | Afterheat recovery system and method of dry granulating liquid slag | |
| WO2019161639A1 (en) | Dry type centrifugal granulation and waste heat recycling and utilization system for liquid molten slag | |
| CN102443662B (en) | Treatment device of liquid slag | |
| CN101660014A (en) | Molten blast furnace slag sensible heat recovery method and device | |
| CN101539371B (en) | First flue gas dust removal and waste heat recovery system for electric stove | |
| CN103557711A (en) | Molten slag rapid cooling, granulation and waste heat recovery power generation system and method | |
| CN101539369A (en) | Flue gas waste heat recovery and negative energy consumption dust-removal system for electric stove | |
| WO2021109324A1 (en) | Modularized natural convection boiler system for recovering waste heat of liquid slag | |
| CN103540698B (en) | Steel slag granulating and afterheat recycling device | |
| CN203534229U (en) | Power generating system for quick cooling granulating of molten slag and waste heat recovery | |
| CN105110661A (en) | Melted slag granulating and waste heat recovering device | |
| CN103776045A (en) | Method and system for recycling residual heat of ash and slag of liquid slag-tapping boiler | |
| CN103836948B (en) | A kind of fluidizing reactor of high-carbon molybdenum-nickel ore and system | |
| CN105087946B (en) | Method for recycling arsenic from copper smelting smoke dust | |
| CN104404179A (en) | Liquid high temperature material waste heat recovery unit | |
| CN110117164A (en) | A kind of device and method of pair of fusion smelting slag glass granulation and waste heat recycling | |
| CN202284894U (en) | Energy-saving environment-friendly cupola furnace | |
| CN101539370B (en) | First flue gas dust-removal and waste heat recovery system for electric stove without water cooling flue gas path | |
| CN204265775U (en) | A kind of metallurgical slag granulation and heat-energy recovering apparatus | |
| CN203559060U (en) | Steel slag granulating device | |
| CN214142412U (en) | Slag waste heat recovery system | |
| CN215713243U (en) | System for improving medium-temperature denitration effect of chain grate machine rotary kiln pellets |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Application publication date: 20120425 Assignee: CISRI SHENGHUA ENGINEERING TECHNOLOGY CO., LTD. Assignor: Central Iron & Steel Research Institute Contract record no.: 2014110000038 Denomination of invention: Slag granulating and waste heat recovery device Granted publication date: 20130731 License type: Exclusive License Record date: 20140801 |
|
| LICC | Enforcement, change and cancellation of record of contracts on the licence for exploitation of a patent or utility model | ||
| 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: 20130731 Termination date: 20181231 |