CN103484580A - Method and device for recovering molten blast furnace slag sensible heat - Google Patents
Method and device for recovering molten blast furnace slag sensible heat Download PDFInfo
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- 239000002893 slag Substances 0.000 title claims abstract description 108
- 238000000034 method Methods 0.000 title claims abstract description 32
- 239000002131 composite material Substances 0.000 claims abstract description 24
- 238000007664 blowing Methods 0.000 claims abstract description 18
- 238000004519 manufacturing process Methods 0.000 claims abstract description 10
- 239000000498 cooling water Substances 0.000 claims abstract description 9
- 238000010248 power generation Methods 0.000 claims abstract description 9
- 238000005338 heat storage Methods 0.000 claims abstract description 7
- 239000002918 waste heat Substances 0.000 claims abstract description 7
- 229910052802 copper Inorganic materials 0.000 claims description 10
- 239000010949 copper Substances 0.000 claims description 10
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 9
- 239000004568 cement Substances 0.000 claims description 7
- 239000011819 refractory material Substances 0.000 claims description 3
- 238000003756 stirring Methods 0.000 claims description 2
- 238000011084 recovery Methods 0.000 abstract description 6
- 230000009286 beneficial effect Effects 0.000 abstract description 2
- 230000005611 electricity Effects 0.000 abstract description 2
- 230000009466 transformation Effects 0.000 abstract description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 12
- 229910000831 Steel Inorganic materials 0.000 description 8
- 239000010959 steel Substances 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 229910052742 iron Inorganic materials 0.000 description 6
- 238000010586 diagram Methods 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 3
- 239000000428 dust Substances 0.000 description 3
- 238000005265 energy consumption Methods 0.000 description 3
- 238000011010 flushing procedure Methods 0.000 description 3
- 229910001341 Crude steel Inorganic materials 0.000 description 2
- 229910000805 Pig iron Inorganic materials 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 239000002910 solid waste Substances 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- 238000003723 Smelting Methods 0.000 description 1
- 238000004364 calculation method Methods 0.000 description 1
- 238000004939 coking Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000002407 reforming Methods 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000009865 steel metallurgy Methods 0.000 description 1
- 238000009628 steelmaking Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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- 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
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- 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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- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
Abstract
本发明属于能源回收技术领域,特别涉及一种回收熔融高炉渣显热的方法及其装置,其流程按顺序如下进行:1)高炉熔渣进入分段的底吹复合熔融渣沟,同时将压缩空气从底吹复合熔融渣沟底部吹入,这时蓄热体被加热到1100~1250℃;2)是温度被降到700~800℃的熔渣通过连接单元进入旧有渣处理系统,对炉渣作后续处理;3)是当高炉停止出渣时,底吹复合熔融渣沟底部依旧吹入空气,在通过蓄热体的过程中空气被加热到800~900℃;4)将热空气除尘后用于发电,冷却水置换热量用于生产。与现有技术相比,本发明的有益效果是:通过改造实现既能高效回收热能又能提高热风炉助燃空气温度,还可用于余热发电,达到能源再利用的目的。
The invention belongs to the technical field of energy recovery, and particularly relates to a method and device for recovering the sensible heat of molten blast furnace slag. The air is blown in from the bottom of the bottom-blowing composite molten slag ditch, and the regenerator is heated to 1100-1250°C at this time; 2) The slag whose temperature has been lowered to 700-800°C enters the old slag treatment system through the connecting unit. The slag is used for subsequent treatment; 3) When the blast furnace stops slag discharge, the bottom of the bottom-blown composite molten slag ditch is still blown into air, and the air is heated to 800-900°C during the process of passing through the heat storage body; 4) The hot air is dedusted After that, it is used to generate electricity, and the cooling water replaces heat for production. Compared with the prior art, the beneficial effect of the present invention is: through the transformation, the heat energy can be efficiently recovered and the temperature of the combustion-supporting air of the hot blast stove can be increased, and the waste heat can also be used for power generation to achieve the purpose of energy reuse.
Description
技术领域technical field
本发明属于钢铁冶金节能减排、二次能源回收技术领域,特别涉及一种回收熔融高炉渣显热的方法及其装置。The invention belongs to the technical field of iron and steel metallurgy energy saving and emission reduction and secondary energy recovery, and in particular relates to a method and a device for recovering sensible heat of molten blast furnace slag.
背景技术Background technique
钢铁工业是我国国民经济的重要基础产业,从20世纪90年代以来我国的钢铁工业快速发展,2012年粗钢产量达到7.2亿吨、其中高炉生铁(即长流程粗钢生产)产量接近6.59亿吨,随着钢铁产量的增长,钢铁工业产生固体废弃物的总量越来越多,在固体废弃物中,高炉渣又占了很大的比例。高炉渣的排放量随矿石品位和冶炼方法的不同而变化。一般来说,炉料品位达到60%~66%时,每炼成1吨生铁将产渣250~300公斤,按此计算,我国每年的高炉渣产量也在1.65~1.98亿吨左右。The iron and steel industry is an important basic industry of my country's national economy. Since the 1990s, my country's iron and steel industry has developed rapidly. In 2012, the output of crude steel reached 720 million tons, of which the output of blast furnace pig iron (that is, long-process crude steel production) was close to 659 million tons. , with the growth of iron and steel production, the total amount of solid waste produced by the iron and steel industry is increasing. Among the solid waste, blast furnace slag accounts for a large proportion. Blast furnace slag emissions vary with ore grade and smelting method. Generally speaking, when the charge grade reaches 60% to 66%, 250 to 300 kilograms of slag will be produced for every ton of pig iron smelted. Based on this calculation, the annual blast furnace slag output in my country is also about 165 to 198 million tons.
同时钢铁工业的能源消耗又占到全国总能耗的10%~15%,目前主要的钢铁生产流程为长流程,即包括炼焦工序、烧结工序、高炉炼铁工序、转炉炼钢工序和轧钢工序,而高炉炼铁工序的资源与能量消耗都是最大的,又约占整个钢铁生产工序的77%左右。高炉渣的出炉温度一般在1400℃~1500℃,即1吨高炉渣所含有的热量相当于64kg标准煤,这样计算下来我国每年因高炉渣带走热量相当于1056~1267.2吨标准煤。At the same time, the energy consumption of the steel industry accounts for 10% to 15% of the country's total energy consumption. At present, the main steel production process is a long process, including coking process, sintering process, blast furnace ironmaking process, converter steelmaking process and steel rolling process. , while the resource and energy consumption of the blast furnace ironmaking process is the largest, accounting for about 77% of the entire iron and steel production process. The temperature of blast furnace slag is generally 1400℃~1500℃, that is, the heat contained in 1 ton of blast furnace slag is equivalent to 64kg of standard coal. In this way, the heat taken away by blast furnace slag in my country is equivalent to 1056~1267.2 tons of standard coal every year.
目前我国高炉渣显热利用率极低,而且大多数企业都采用水渣处理工艺,并且所谓的利用就是北方企业冬季用高炉冲渣水取暖,由于受到供热区域、流量等条件的限制,以及冲渣水含有大量碱性物质对泵及管道腐蚀等因素,渣热能利用率极低,而且春、夏、秋三个季节不能适应,大量热水、蒸汽影响生产。因此高炉渣的显热回收是十分重要的课题,迫切需要解决。At present, the sensible heat utilization rate of blast furnace slag in my country is extremely low, and most enterprises adopt water slag treatment process, and the so-called utilization means that northern enterprises use blast furnace slag flushing water for heating in winter, due to the limitation of heating area, flow rate and other conditions, and The slag flushing water contains a large amount of alkaline substances, which will cause corrosion of pumps and pipelines. The utilization rate of slag heat energy is extremely low, and it cannot adapt to the three seasons of spring, summer, and autumn. A large amount of hot water and steam affect production. Therefore, the recovery of sensible heat from blast furnace slag is a very important issue and needs to be solved urgently.
发明内容Contents of the invention
本发明的目的是提供一种回收熔融高炉渣显热的方法及其装置,在不改变现有大部分高炉水冲渣工艺的前提下,通过对熔融渣沟的改造达到回收高炉渣的显热、能源再利用的目的。The purpose of the present invention is to provide a method and device for recovering the sensible heat of molten blast furnace slag. Under the premise of not changing most of the existing blast furnace water slag flushing process, the sensible heat of blast furnace slag can be recovered by reforming the molten slag ditch , The purpose of energy reuse.
为解决上述技术问题,本发明的技术方案是:In order to solve the problems of the technologies described above, the technical solution of the present invention is:
一种回收熔融高炉渣显热的方法,其流程按顺序如下进行:1)将温度达1400~1500℃的高炉熔渣进入分段的底吹复合熔融渣沟,同时将1.5~2.0MPa的压缩空气以8~10米/秒的速度从底吹复合熔融渣沟底部吹入,在保证熔渣流动性的同时搅拌熔渣,实现底吹复合熔融渣沟顶部蓄热砌体的辐射热吸收,这时蓄热体被加热到1100~1250℃;2)是温度被降到700~800℃的熔渣通过连接单元进入旧有渣处理系统,对炉渣作后续处理;3)是当高炉停止出渣时,底吹复合熔融渣沟底部依旧吹入空气,在通过蓄热体的过程中空气被加热到800~900℃;4)将热空气除尘后引入余热发电锅炉用于发电,渣沟的冷却水通过换热器置换热量用于生产。A method for recovering the sensible heat of molten blast furnace slag, the process of which is carried out in sequence as follows: 1) Blast furnace slag with a temperature of 1400-1500 °C enters the sectioned bottom-blown composite molten slag ditch, and simultaneously compresses 1.5-2.0 MPa The air is blown in from the bottom of the bottom-blown composite molten slag ditch at a speed of 8-10 m/s, stirring the slag while ensuring the fluidity of the slag, realizing the radiant heat absorption of the regenerative masonry on the top of the bottom-blown composite molten slag ditch, At this time, the regenerator is heated to 1100-1250°C; 2) The slag whose temperature has been lowered to 700-800°C enters the old slag treatment system through the connection unit for subsequent treatment of the slag; 3) When the blast furnace stops discharging When slag is slag, the bottom of the bottom-blown composite molten slag ditch is still blown into air, and the air is heated to 800-900°C during the process of passing through the heat storage body; 4) After the hot air is dedusted, it is introduced into the waste heat power generation boiler for power generation. Cooling water is used for production by displacing heat through a heat exchanger.
所述热空气除尘后还可作为热风炉的助燃空气被利用。After the hot air is dedusted, it can also be used as the combustion-supporting air of the hot stove.
所述底吹复合熔融渣沟,其特征在于,包括水泥外渣沟、沟体支撑、沟体及沟盖,水泥外渣沟的底部设有沟体支撑,沟体支撑的上部设有耐火材料制成的沟体和沟盖,沟盖的内表面设有蓄热砌体,沟体与沟盖之间围成熔渣流道,沟体底部设有铜冷却壁,铜冷却壁内设冷却水管,铜冷却壁的底部设有底吹空气管,底吹空气管上设有喷吹管向上与熔渣流道相通。The bottom-blown composite molten slag ditch is characterized in that it includes a cement outer slag ditch, a ditch body support, a ditch body and a ditch cover, the bottom of the cement outer slag ditch is provided with a ditch body support, and the upper part of the ditch body support is provided with a refractory material The ditch body and ditch cover are made, the inner surface of the ditch cover is provided with heat storage masonry, the slag flow channel is surrounded between the ditch body and the ditch cover, the bottom of the ditch body is provided with a copper stave, and the copper stave is equipped with a cooling The bottom of the copper stave is provided with a bottom blowing air pipe, and the bottom blowing air pipe is provided with a blowing pipe to communicate with the slag flow channel upwards.
与现有技术相比,本发明的有益效果是:Compared with prior art, the beneficial effect of the present invention is:
本方法不仅可以有效回收熔融高炉渣显热,并且能够充分利用现有的渣处理系统,通过高炉出铁场的局部改造实现既能高效回收热能又能提高热风炉助燃空气温度,还可用于余热发电,达到能源再利用的目的。This method can not only effectively recover the sensible heat of molten blast furnace slag, but also can make full use of the existing slag treatment system. Through the partial transformation of the blast furnace casthouse, it can not only recover heat energy efficiently but also increase the temperature of the combustion air of the hot blast stove, and can also be used for waste heat. Generate electricity to achieve the purpose of energy reuse.
附图说明Description of drawings
图1是本发明底吹复合熔融渣沟实施例结构示意图;Fig. 1 is a schematic structural view of an embodiment of a bottom-blown composite molten slag ditch of the present invention;
图2是本发明实施流程之一的示意图;Fig. 2 is a schematic diagram of one of the implementation processes of the present invention;
图3是本发明实施流程之二的示意图。Fig. 3 is a schematic diagram of the second implementation process of the present invention.
图中:1-水泥外渣沟 2-沟体支撑 3-沟体 4-沟盖 5-蓄热砌体 6-熔渣流道 7-铜冷却壁 8-冷却水管 9-底吹空气管 10-喷吹管 11-高炉 12-底吹复合熔融渣沟 13-连接单元 14-换热器 15-余热发电锅炉 16-除尘器In the figure: 1-cement outer slag ditch 2-ditch body support 3-ditch body 4-ditch cover 5-heat storage masonry 6-slag runner 7-copper stave 8-cooling water pipe 9-bottom blowing air pipe 10 -Injection pipe 11-Blast furnace 12-Bottom blowing compound molten slag ditch 13-Connection unit 14-Heat exchanger 15-Waste heat power generation boiler 16-Dust collector
具体实施方式Detailed ways
下面结合附图对本发明的具体实施方式作进一步说明:The specific embodiment of the present invention will be further described below in conjunction with accompanying drawing:
见图1,是本发明底吹复合熔融渣沟实施例结构示意图,包括水泥外渣沟1、沟体支撑2、沟体3及沟盖4,水泥外渣沟1的底部设有沟体支撑2,沟体支撑2的上部设有耐火材料制成的沟体3和沟盖4,沟盖4的内表面设有蓄热砌体5,沟体3与沟盖4之间围成熔渣流道6,沟体3底部设有铜冷却壁7,铜冷却壁7内设冷却水管8,铜冷却壁7的底部设有底吹空气管9,底吹空气管9上设有喷吹管10向上与熔渣流道6相通。冷却水管8接换热器进行热能回收,底吹空气管9与鼓风机相连,根据熔融高炉渣的物理特性:换热速度慢,粘度随着温度降低急剧升高等特点,应合理布置喷吹管10的数量和位置,使熔融高炉渣的辐射热既能被蓄热体吸收又能保持适当的流动性。See Fig. 1, which is a structural schematic diagram of an embodiment of the bottom-blowing composite molten slag ditch of the present invention, including a cement
见图2,是本发明一种回收熔融高炉渣显热的方法实施流程之一的示意图,通过底吹复合熔融渣沟对熔融高炉渣的辐射热进行吸收,热量交换产生热空气和热水,实现高炉渣显热回收的目的,1)首先将高炉11排出的温度达1400~1500℃的高炉熔渣进入分段的底吹复合熔融渣沟12,同时将1.5~2.0MPa的压缩空气以8~10米/秒的速度从底吹复合熔融渣沟底部吹入,在保证熔渣流动性的同时搅拌熔渣,实现底吹复合熔融渣沟顶部蓄热砌体的辐射热吸收,这时蓄热体被加热到1100~1250℃,而底部吹入的空气在出口处也有900℃以上;2)其次是温度被降到700~800℃的熔渣通过连接单元进入旧有渣处理系统,对炉渣作后续处理;3)再次是当高炉停止出渣时,底吹复合熔融渣沟底部依旧吹入空气,在通过蓄热体的过程中空气被加热到800~900℃;4)最后是渣沟的冷却水(约80℃)通过换热器14将热量置换出来用于生产,而热空气除尘后引入余热发电锅炉15用于发电,图中余热发电锅炉前级自带除尘装置。See Figure 2, which is a schematic diagram of one of the implementation processes of a method for recovering the sensible heat of molten blast furnace slag according to the present invention. The radiant heat of molten blast furnace slag is absorbed through the bottom-blown composite molten slag ditch, and heat exchange generates hot air and hot water. To achieve the purpose of recovery of sensible heat from blast furnace slag, 1) First, the blast furnace slag discharged from the
见图3,是本发明一种回收熔融高炉渣显热的方法实施流程之二的示意图,通过底吹复合熔融渣沟对熔融高炉渣的辐射热进行吸收,热量交换产生热空气和热水,实现高炉渣显热回收的目的,1)首先将高炉11排出的温度达1400~1500℃的高炉熔渣进入分段的底吹复合熔融渣沟12,同时将1.5~2.0MPa的压缩空气以8~10米/秒的速度从底吹复合熔融渣沟底部吹入,在保证熔渣流动性的同时搅拌熔渣,实现底吹复合熔融渣沟顶部蓄热砌体的辐射热吸收,这时蓄热体被加热到1100~1250℃,而底部吹入的空气在出口处也有900℃以上;2)其次是温度被降到700~800℃的熔渣通过连接单元进入旧有渣处理系统,对炉渣作后续处理;3)再次是当高炉停止出渣时,底吹复合熔融渣沟底部依旧吹入空气,在通过蓄热体的过程中空气被加热到800~900℃;4)最后是渣沟的冷却水(约80℃)通过换热器14将热量置换出来用于生产,热空气经除尘器16后作为热风炉的助燃空气被利用。See Figure 3, which is a schematic diagram of the second implementation process of a method for recovering sensible heat from molten blast furnace slag according to the present invention. The radiant heat of molten blast furnace slag is absorbed through the bottom-blown composite molten slag ditch, and heat exchange generates hot air and hot water. To achieve the purpose of recovery of sensible heat from blast furnace slag, 1) First, the blast furnace slag discharged from the
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Cited By (5)
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---|---|---|---|---|
CN105400918A (en) * | 2015-12-30 | 2016-03-16 | 中冶南方工程技术有限公司 | Cover plate for slag-iron runner of blast furnace |
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CN111637776A (en) * | 2020-06-12 | 2020-09-08 | 东北大学 | A multi-stage secondary phase change recovery and storage device for metallurgical high-temperature slag waste heat |
CN114774603A (en) * | 2022-04-29 | 2022-07-22 | 马鞍山钢铁股份有限公司 | A recycling system for high temperature radiant heat in blast furnace tap ditch |
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Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
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CN105400918A (en) * | 2015-12-30 | 2016-03-16 | 中冶南方工程技术有限公司 | Cover plate for slag-iron runner of blast furnace |
CN108278904A (en) * | 2017-01-05 | 2018-07-13 | 北京金熔节能环保科技有限公司 | A kind of pyrolytic semlting slag waste-heat recovery device and method |
CN108278904B (en) * | 2017-01-05 | 2020-10-30 | 北京金熔节能环保科技有限公司 | High-temperature smelting slag waste heat recovery device and method |
CN108870350A (en) * | 2018-07-19 | 2018-11-23 | 北京金熔节能环保科技有限公司 | A kind of tunnel type high temperature sludge waste heat Dry recovery device and method |
CN111637776A (en) * | 2020-06-12 | 2020-09-08 | 东北大学 | A multi-stage secondary phase change recovery and storage device for metallurgical high-temperature slag waste heat |
CN114774603A (en) * | 2022-04-29 | 2022-07-22 | 马鞍山钢铁股份有限公司 | A recycling system for high temperature radiant heat in blast furnace tap ditch |
CN114774603B (en) * | 2022-04-29 | 2024-01-30 | 马鞍山钢铁股份有限公司 | A recycling and utilization system for high-temperature radiant heat in the blast furnace tap trough |
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