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 PDF

Info

Publication number
CN103484580A
CN103484580A CN201310421159.6A CN201310421159A CN103484580A CN 103484580 A CN103484580 A CN 103484580A CN 201310421159 A CN201310421159 A CN 201310421159A CN 103484580 A CN103484580 A CN 103484580A
Authority
CN
China
Prior art keywords
slag
ditch
air
blast furnace
heat
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
Application number
CN201310421159.6A
Other languages
Chinese (zh)
Other versions
CN103484580B (en
Inventor
张维巍
李霞
赵波
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Ansteel Engineering Technology Corp Ltd
Original Assignee
Ansteel Engineering Technology Corp Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Ansteel Engineering Technology Corp Ltd filed Critical Ansteel Engineering Technology Corp Ltd
Priority to CN201310421159.6A priority Critical patent/CN103484580B/en
Publication of CN103484580A publication Critical patent/CN103484580A/en
Application granted granted Critical
Publication of CN103484580B publication Critical patent/CN103484580B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/25Process efficiency

Landscapes

  • 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。

Figure 201310421159

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.

Figure 201310421159

Description

一种回收熔融高炉渣显热的方法及其装置A method and device for recovering sensible heat from molten blast furnace slag

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 outer slag ditch 1, a ditch body support 2, a ditch body 3 and a ditch cover 4, and the bottom of the cement outer slag ditch 1 is provided with a ditch body support 2. The upper part of the trench body support 2 is provided with a trench body 3 and a trench cover 4 made of refractory materials. The inner surface of the trench cover 4 is provided with a heat storage masonry 5, and a slag is formed between the trench body 3 and the trench cover 4 The flow channel 6, the bottom of the ditch body 3 is provided with a copper stave 7, the copper stave 7 is provided with a cooling water pipe 8, the bottom of the copper stave 7 is provided with a bottom blowing air pipe 9, and the bottom blowing air pipe 9 is provided with a blowing pipe 10 It communicates with the slag runner 6 upwards. The cooling water pipe 8 is connected to the heat exchanger for heat recovery, and the bottom blowing air pipe 9 is connected to the blower. According to the physical characteristics of the molten blast furnace slag: slow heat transfer speed, and the viscosity rises sharply with the decrease of temperature, etc., the blowing pipe 10 should be arranged reasonably Quantity and location, so that the radiant heat of molten blast furnace slag can be absorbed by the regenerator and maintain proper fluidity.

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 blast furnace 11 with a temperature of 1400-1500°C enters the sectioned bottom-blowing composite molten slag ditch 12, and at the same time, the compressed air of 1.5-2.0 MPa is injected at 8 The speed of ~10 m/s is blown from the bottom of the bottom-blown composite molten slag ditch, and the slag is stirred while ensuring the fluidity of the slag, so as to realize the radiant heat absorption of the thermal storage masonry on the top of the bottom-blown composite molten slag ditch. The heating body is heated to 1100-1250°C, and the air blown in from the bottom is also above 900°C at the outlet; 2) Secondly, the slag whose temperature has been lowered to 700-800°C enters the old slag treatment system through the connection unit. The slag is used for follow-up treatment; 3) When the blast furnace stops slag discharge, air is still blown into the bottom of the bottom-blown composite molten slag ditch, and the air is heated to 800-900°C during the process of passing through the regenerator; 4) Finally, the slag The cooling water (about 80°C) of the ditch passes through the heat exchanger 14 to replace the heat for production, while the hot air is dedusted and introduced into the waste heat power generation boiler 15 for power generation. In the figure, the front stage of the waste heat power generation boiler has a dust removal device.

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 blast furnace 11 with a temperature of 1400-1500°C enters the sectioned bottom-blowing composite molten slag ditch 12, and at the same time, the compressed air of 1.5-2.0 MPa is injected at 8 The speed of ~10 m/s is blown from the bottom of the bottom-blown composite molten slag ditch, and the slag is stirred while ensuring the fluidity of the slag, so as to realize the radiant heat absorption of the thermal storage masonry on the top of the bottom-blown composite molten slag ditch. The heating body is heated to 1100-1250°C, and the air blown in from the bottom is also above 900°C at the outlet; 2) Secondly, the slag whose temperature has been lowered to 700-800°C enters the old slag treatment system through the connection unit. The slag is used for follow-up treatment; 3) When the blast furnace stops slag discharge, air is still blown into the bottom of the bottom-blown composite molten slag ditch, and the air is heated to 800-900°C during the process of passing through the regenerator; 4) Finally, the slag The cooling water (about 80°C) of the ditch passes through the heat exchanger 14 to replace the heat for production, and the hot air passes through the dust collector 16 and is used as the combustion-supporting air of the hot blast stove.

Claims (3)

1.一种回收熔融高炉渣显热的方法,其特征在于,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。1. A method for recovering the sensible heat of molten blast furnace slag, characterized in that the flow process is carried out in the following order: 1) Put the blast furnace slag with a temperature of 1400-1500°C into the sectioned bottom-blown composite molten slag ditch, and simultaneously Compressed air of 1.5-2.0 MPa 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 molten slag, and realizing heat storage at 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 ) means that when the blast furnace stops slag discharge, air is still blown into the bottom of the bottom-blown composite molten slag ditch, and the air is heated to 800-900°C in the process of passing through the regenerator; 4) After the hot air is dedusted, it is introduced into the waste heat power generation boiler For power generation, the cooling water of the slag ditch is used for production by displacing heat through a heat exchanger. 2.根据权利要求1所述一种回收熔融高炉渣显热的方法,其特征在于,所述热空气除尘后还可作为热风炉的助燃空气被利用。2. A method for recovering sensible heat from molten blast furnace slag according to claim 1, characterized in that, after the hot air is dedusted, it can also be used as combustion-supporting air of a hot blast stove. 3.权利要求1所述方法中提到的底吹复合熔融渣沟,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。3. The bottom-blowing composite molten slag ditch mentioned in the method of claim 1 is characterized in that it comprises a cement outer slag ditch, a ditch body support, a ditch body and a ditch cover, and the bottom of the cement outer slag ditch is provided with a ditch body support , the upper part of the ditch support is provided with a ditch body and ditch cover made of refractory materials, the inner surface of the ditch cover is provided with heat storage masonry, the slag flow channel is formed between the ditch body and the ditch cover, and the bottom of the ditch body is provided with Copper staves, cooling water pipes are installed inside the copper staves, bottom blowing air pipes are provided at the bottom of the copper staves, and blowing pipes are provided on the bottom blowing air pipes to communicate with the slag flow channel upwards.
CN201310421159.6A 2013-09-13 2013-09-13 Method and device for recovering molten blast furnace slag sensible heat Active CN103484580B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201310421159.6A CN103484580B (en) 2013-09-13 2013-09-13 Method and device for recovering molten blast furnace slag sensible heat

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201310421159.6A CN103484580B (en) 2013-09-13 2013-09-13 Method and device for recovering molten blast furnace slag sensible heat

Publications (2)

Publication Number Publication Date
CN103484580A true CN103484580A (en) 2014-01-01
CN103484580B CN103484580B (en) 2014-12-31

Family

ID=49825169

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201310421159.6A Active CN103484580B (en) 2013-09-13 2013-09-13 Method and device for recovering molten blast furnace slag sensible heat

Country Status (1)

Country Link
CN (1) CN103484580B (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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
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

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4426067A (en) * 1983-01-07 1984-01-17 The Calumite Company Metallic sectional liquid-cooled runners
JPS62156213A (en) * 1985-12-27 1987-07-11 Sumitomo Metal Ind Ltd Gutter structure for hot metal pre-smelting
JPH0379709A (en) * 1989-05-26 1991-04-04 Godo Seitetsu Kk Slag bath type smelting reduction producing apparatus for molten ferrous alloy and method thereof
CN101886149A (en) * 2010-07-08 2010-11-17 无锡市东方环境工程设计研究所有限公司 High temperature liquid slag recovery method

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4426067A (en) * 1983-01-07 1984-01-17 The Calumite Company Metallic sectional liquid-cooled runners
JPS62156213A (en) * 1985-12-27 1987-07-11 Sumitomo Metal Ind Ltd Gutter structure for hot metal pre-smelting
JPH0379709A (en) * 1989-05-26 1991-04-04 Godo Seitetsu Kk Slag bath type smelting reduction producing apparatus for molten ferrous alloy and method thereof
CN101886149A (en) * 2010-07-08 2010-11-17 无锡市东方环境工程设计研究所有限公司 High temperature liquid slag recovery method

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
陈登福 等: "液态高炉渣热量回收利用方法及问题", 《环境污染治理技术与设备》 *

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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

Also Published As

Publication number Publication date
CN103484580B (en) 2014-12-31

Similar Documents

Publication Publication Date Title
CN105112577B (en) Dry granulating blast furnace slag waste heat recovery device and blast furnace slag waste heat recovery method
CN103740939B (en) Method for producing molten iron and recovering zinc by using zinc-containing dust and sludge of steel plant
CN102424868B (en) Blast furnace smelting slag water quenching waste steam waste heat recovery system
CN103484580A (en) Method and device for recovering molten blast furnace slag sensible heat
CN102787874A (en) Device and method for power generation by waste heat of blast furnace slag
CN107022659B (en) High-temperature slag waste heat gradient recycling system
CN201670845U (en) High temperature solid slag sensible heat recovery device
CN109883210A (en) A blast furnace slag waste heat recovery system and method
CN107906971B (en) High, medium and low waste heat recycling system for solidification heat of blast furnace ore slag
CN108277315B (en) A device and method for using converter flue gas reduction pellets to replace scrap steel
CN103882163A (en) Method and device for recovering sensible heat of molten blast furnace slag
CN201621973U (en) A device for recovering waste heat from electric furnace flue gas
CN107990740A (en) The equipment that blast furnace slag wind quenching granulated particles waste heat for supplying is utilized based on flash evaporation technology
CN209322918U (en) A blast furnace slag waste heat recovery power generation system
CN208547260U (en) Steel slag Exposure degree electricity generation system
CN208201018U (en) A kind of device recycling high-temperature slag heat
CN105755189B (en) Blast furnace slag quenching water waste-heat recovery device
CN104152609B (en) blast furnace slag waste heat recycling system
CN203794917U (en) Device for recycling sensible heat of molten blast furnace slag
CN203820804U (en) System for preheating boiler water by washing blast furnace slag water
CN108796155A (en) Energy-saving power generation system and power generation method for sensible heat recovery of slag and molten iron residues in blast furnace casting house
CN217464633U (en) A multi-energy complementary heating system based on waste heat recovery
CN221895037U (en) A device for directly preheating scrap steel by dry recovery of steel slag waste heat
CN220788655U (en) Blast furnace slag sensible heat dual-utilization device
CN203999649U (en) Blast furnace slag waste heat recycling system

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