CN201406440Y - Blast furnace gas dry dust removal heat pipe heating and cooling device - Google Patents
Blast furnace gas dry dust removal heat pipe heating and cooling device Download PDFInfo
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- CN201406440Y CN201406440Y CN200920106930XU CN200920106930U CN201406440Y CN 201406440 Y CN201406440 Y CN 201406440Y CN 200920106930X U CN200920106930X U CN 200920106930XU CN 200920106930 U CN200920106930 U CN 200920106930U CN 201406440 Y CN201406440 Y CN 201406440Y
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- 238000001816 cooling Methods 0.000 title claims abstract description 23
- 238000010438 heat treatment Methods 0.000 title abstract description 17
- 239000000428 dust Substances 0.000 title abstract description 12
- 239000008234 soft water Substances 0.000 claims abstract description 45
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 25
- 238000009833 condensation Methods 0.000 claims description 6
- 230000005494 condensation Effects 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 6
- 238000005507 spraying Methods 0.000 claims description 5
- 230000000737 periodic effect Effects 0.000 claims description 3
- 229910018487 Ni—Cr Inorganic materials 0.000 claims description 2
- VNNRSPGTAMTISX-UHFFFAOYSA-N chromium nickel Chemical compound [Cr].[Ni] VNNRSPGTAMTISX-UHFFFAOYSA-N 0.000 claims description 2
- 239000003082 abrasive agent Substances 0.000 claims 1
- 238000010410 dusting Methods 0.000 claims 1
- 210000003516 pericardium Anatomy 0.000 claims 1
- 238000004064 recycling Methods 0.000 claims 1
- 238000005476 soldering Methods 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 4
- 239000010865 sewage Substances 0.000 abstract description 4
- 206010015137 Eructation Diseases 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 37
- 238000005516 engineering process Methods 0.000 description 5
- 229920006395 saturated elastomer Polymers 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 238000003723 Smelting Methods 0.000 description 1
- 238000005219 brazing Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 230000008646 thermal stress Effects 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
一种高炉煤气干法除尘热管升、降温装置,装置包括:热交换器本体、热管、换热器中心蒸汽或软水包、换热器上部的软水或蒸汽包、定期排污管、连续排污管、安全阀、放散阀、疏水阀、冷凝水箱、冷凝水过滤器、冷凝水泵、止回阀、截止阀。换热器内中心蒸汽或软水包上有很多水平放置的热管进行传热;换热器中心蒸汽或软水包上方与换热器上部的软水或蒸汽包相连;下方与冷凝水箱、冷凝水泵及过滤器相连,管路配有疏水阀、止回阀、截止阀,冷凝水管路与高炉水泵房软水系统相连。优点在于,换热器的煤气升、降温功能合二而一,设备体积小、投资省、效果好,适用于高炉煤气干法除尘。
A heating and cooling device for blast furnace gas dry dust removal heat pipe, the device includes: heat exchanger body, heat pipe, steam or soft water bag in the center of heat exchanger, soft water or steam bag on the upper part of heat exchanger, regular sewage discharge pipe, continuous sewage discharge pipe, Safety valves, relief valves, steam traps, condensate tanks, condensate filters, condensate pumps, check valves, globe valves. There are many heat pipes placed horizontally on the central steam or soft water bag in the heat exchanger for heat transfer; the upper part of the central steam or soft water bag of the heat exchanger is connected to the soft water or steam bag on the upper part of the heat exchanger; the lower part is connected to the condensate tank, condensate pump and filter The pipeline is equipped with traps, check valves and stop valves, and the condensate pipeline is connected to the soft water system of the blast furnace water pump room. The advantage is that the functions of gas raising and cooling of the heat exchanger are combined into one, the equipment is small in size, low in investment and good in effect, and is suitable for dry dust removal of blast furnace gas.
Description
技术领域 technical field
本实用新型属于钢铁工业高炉炼铁技术领域,提供了一种高炉煤气干法除尘热管升、降温装置;适用于高炉煤气干法除尘技术煤气升温、降温技术。The utility model belongs to the technical field of blast furnace ironmaking in the iron and steel industry, and provides a blast furnace gas dry dust removal heat pipe heating and cooling device, which is suitable for the gas heating and cooling technology of the blast furnace gas dry dust removal technology.
背景技术 Background technique
高炉煤气干法除尘是一项煤气除尘的新技术。原理是采用高温滤料以过滤的方法净化煤气,有别于传统的湿法除尘。Blast furnace gas dry dedusting is a new technology of gas dedusting. The principle is to use high-temperature filter material to purify gas by filtering, which is different from traditional wet dust removal.
干法除尘具有净化质量好、节能、节水、环保、占地少、投资与生产费用低等优点,因此具有良好的发展前景。Dry dust removal has the advantages of good purification quality, energy saving, water saving, environmental protection, less land occupation, low investment and production costs, etc., so it has a good development prospect.
高温滤料有一定的温度要求,目前几种滤料适用温度为100~220℃,最高不超过260~280℃,温度过高应适当控制,否则影响滤袋性能,使寿命降低。High-temperature filter materials have certain temperature requirements. At present, the applicable temperature of several filter materials is 100-220°C, and the maximum temperature does not exceed 260-280°C. If the temperature is too high, it should be properly controlled, otherwise it will affect the performance of the filter bag and reduce the service life.
低温时容易结露,易使滤袋糊住,影响操作。开炉初期由于煤气水分多,炉顶温度低,影响尤为严重,这些问题湿法除尘是不存在的。It is easy to condense at low temperature, and it is easy to stick the filter bag and affect the operation. In the early stage of furnace start-up, due to the high moisture in the gas and the low furnace top temperature, the impact is particularly serious. These problems do not exist in wet dust removal.
高炉炉顶温度一般在150℃~250℃范围,但是由于冶炼情况多变,温度过高过低是常有的事,比如炉况不顺,有时会升高到500~600℃以上;炉况顺行又经常温度偏低,有时只有100℃左右,因此使用干法除尘必须对煤气温度进行控制才好。The top temperature of blast furnace is generally in the range of 150-250°C, but due to the changeable smelting conditions, it is common for the temperature to be too high or too low. And the temperature is often on the low side, sometimes only about 100°C, so it is necessary to control the gas temperature when using dry dust removal.
从操作上煤气温度不太容易控制。高温除炉顶喷水降温外,还可以在进入布袋前用换热器进一步降温。目前降温换热器有两种类型:一种是列管换热器,即利用无缝钢管组作为降温设备,管内通过热煤气自然散热降温;一种是热管换热器,利用热管原理传热降温。而升温至今缺乏手段,曾经使用热烟气加热方法升温,即煤气通过排管,外部烧高炉煤气加热升温,有一定效果。其他方案虽多却难于实践,即使可行也相当复杂,此外增加升温装置使系统庞大、占地多、投资也大幅增加。Operationally, the gas temperature is not easy to control. In addition to spraying water on the top of the furnace to cool down the high temperature, the heat exchanger can be used to further cool down before entering the cloth bag. At present, there are two types of cooling heat exchangers: one is the tube heat exchanger, that is, the seamless steel pipe group is used as the cooling equipment, and the hot gas is naturally radiated and cooled in the tube; the other is the heat pipe heat exchanger, which uses the heat pipe principle to transfer heat cool down. However, there is no way to raise the temperature. The hot flue gas heating method was used to raise the temperature, that is, the gas passes through the exhaust pipe, and the blast furnace gas is burned externally to heat the temperature, which has a certain effect. Although there are many other schemes, it is difficult to practice, and even if it is feasible, it is quite complicated. In addition, adding a heating device will make the system huge, take up a lot of land, and the investment will also increase significantly.
其实无论温度升高或降低各有50℃即可,如果采用一套设备既可以升温又可以降温,两项功能集于一身,将使干法除尘技术更为先进与适用。本实用新型就是利用热管传热原理完成既能加热也能降温的温度调节装置。In fact, whether the temperature rises or falls by 50°C, if a set of equipment can be used to heat up and cool down, the combination of the two functions will make the dry dust removal technology more advanced and applicable. The utility model utilizes the heat transfer principle of a heat pipe to complete a temperature regulating device capable of both heating and cooling.
发明内容 Contents of the invention
本实用新型的目的在于提供一种高炉煤气干法除尘热管升、降温装置,特别适用于高炉煤气干法除尘。装置主体是换热器,煤气升、降温功能合二而一,体积小、投资省。The purpose of the utility model is to provide a blast furnace gas dry dust removal heat pipe heating and cooling device, which is especially suitable for blast furnace gas dry dust removal. The main body of the device is a heat exchanger, which combines the functions of gas raising and cooling into one, with small size and low investment.
本实用新型包括:热交换器本体、热管、换热器中心蒸汽或软水包、换热器上部的软水或蒸汽包、疏水阀、冷凝水箱、冷凝水过滤器、冷凝水泵、止回阀、截止阀、定期排污管、连续排污管、安全阀、放散阀。主体是换热器,内设中心蒸汽或软水包以及包上为数众多的水平热管。换热器中心蒸汽或软水包上与换热器上部的软水或蒸汽包相连;换热器中心蒸汽或软水包下与冷凝水箱、冷凝水泵及过滤器相连,管路设疏水阀、止回阀、截止阀,冷凝水管路与高炉水泵站软水系统相连;利用热管传热原理进行煤气加热升温或冷却降温。The utility model comprises: a heat exchanger body, a heat pipe, a steam or soft water bag in the center of the heat exchanger, a soft water or steam bag on the upper part of the heat exchanger, a steam trap, a condensed water tank, a condensed water filter, a condensed water pump, a check valve, and a cut-off valve. Valves, periodic blowdown pipes, continuous blowdown pipes, safety valves, relief valves. The main body is a heat exchanger with a central steam or soft water bag and a large number of horizontal heat pipes on the bag. The steam or soft water bag in the center of the heat exchanger is connected to the soft water or steam bag on the upper part of the heat exchanger; the steam or soft water bag in the center of the heat exchanger is connected to the condensate tank, condensate pump and filter, and the pipeline is equipped with a drain valve and a check valve , Stop valve, condensed water pipeline is connected to the soft water system of the blast furnace water pump station; use the heat pipe heat transfer principle to heat up or cool down the gas.
热管焊在换热器中心蒸汽或软水包壳体上,水平放置;在换热器中心蒸汽或软水包外煤气流动一侧的热管表面焊有纵向翅片以加大热管传热面积,热管表面钎焊或喷涂镍铬质耐磨材料。The heat pipe is welded on the shell of the steam or soft water bag in the center of the heat exchanger and placed horizontally; the surface of the heat pipe on the side where the steam or soft water flows outside the center of the heat exchanger is welded with longitudinal fins to increase the heat transfer area of the heat pipe. Brazing or spraying nickel-chromium wear-resistant material.
换热器中心蒸汽或软水包与换热器上部的软水或蒸汽包充满软水并联通时,完成煤气散热降温任务;换热器中心蒸汽或软水包改通饱和蒸汽时,与下部软水回收系统一起完成煤气加热升温任务。一台设备可以具有升温和降温两种功能。When the steam or soft water bag in the center of the heat exchanger is filled with soft water and communicated with the soft water or steam bag in the upper part of the heat exchanger, the task of heat dissipation and cooling of gas is completed; Complete the gas heating and heating up task. One device can have both heating and cooling functions.
此煤气温控装置需要升温时,有饱和蒸汽供应管和冷凝水回收设施如:冷凝水箱、冷凝水泵、阀门等与之配套;当煤气需要冷却时,有补水管路、上方蒸汽包和蒸汽放散装置来实现煤气降温。When the gas temperature control device needs to be heated up, there are saturated steam supply pipes and condensate recovery facilities such as: condensate tanks, condensate pumps, valves, etc.; when the gas needs to be cooled, there are water supply pipelines, upper steam drums and steam release device to achieve gas cooling.
本实用新型原理是:利用热管技术来实现升、降温。换热器是一个套管结构,外环走煤气;中心包通蒸汽或软水,内外两层之间利用焊在中心包壳体上的热管传递热量。The principle of the utility model is: use heat pipe technology to realize temperature rise and fall. The heat exchanger is a casing structure, the outer ring is fed with gas; the center pack is passed through steam or soft water, and the heat is transferred between the inner and outer layers by the heat pipe welded on the center pack shell.
煤气加热升温时,中心包内通饱和蒸汽。密排的热管将蒸汽热量传递给外环煤气,使其加热升温。传热过程主要是利用了相变热原理:一是蒸汽冷凝过程放出大量凝结热来加热煤气,二是热管利用了相变原理传导热量,传热量大、热效率高。When the gas is heated and the temperature rises, the center bag is filled with saturated steam. Closely arranged heat pipes transfer the steam heat to the outer ring gas to heat it up. The heat transfer process mainly uses the principle of phase change heat: one is that the steam condensation process releases a large amount of condensation heat to heat the gas, and the other is that the heat pipe uses the phase change principle to conduct heat, with large heat transfer and high thermal efficiency.
冷却原理是利用同一套设备、同一组热管进行热交换,只是中心包从通蒸汽改成软水作为冷却介质。高温煤气通过热管将热量传到水中,加热使水汽化带走热量完成煤气降温。The cooling principle is to use the same set of equipment and the same set of heat pipes for heat exchange, but the center bag is changed from steam to soft water as the cooling medium. The high-temperature gas transfers heat to the water through the heat pipe, and the heating causes the water to vaporize and take away the heat to complete the cooling of the gas.
双功能热管换热器关键是热管需要水平放置,无论是加热还是冷却都能迅速传递热量。不同功能中心包内介质不同:煤气加热时通饱和蒸汽;冷却时改为软水,按要求进行转换。The key to the dual-function heat pipe heat exchanger is that the heat pipe needs to be placed horizontally, so that it can transfer heat quickly whether it is heating or cooling. The medium in the center bag of different functions is different: when the gas is heated, it is saturated steam; when it is cooled, it is changed to soft water, and the conversion is performed as required.
为了加大煤气与热管之间的换热面积,换热器中心蒸汽或软水包外煤气流动一侧的热管表面焊有纵向翅片。为防止含尘煤气造成的磨损,热管外表面喷涂或钎焊一定厚度的硬质耐磨材料。In order to increase the heat exchange area between the gas and the heat pipe, longitudinal fins are welded on the surface of the heat pipe on the side where the gas flows outside the steam or soft water bag in the center of the heat exchanger. In order to prevent wear and tear caused by dusty gas, the outer surface of the heat pipe is sprayed or brazed with a certain thickness of hard wear-resistant material.
换热器按压力容器设计。煤气进出口有波纹膨胀器,中心包的连接管件有一定弯曲,用以消除热应力。The heat exchanger is designed as a pressure vessel. There is a corrugated expander at the gas inlet and outlet, and the connecting pipe fittings of the center package have a certain bend to eliminate thermal stress.
因为加热或冷却均为间断使用,所以换热器设在干法袋式除尘器入口之前并联管路上,根据需要可以接入或切除。Because heating or cooling is used intermittently, the heat exchanger is installed on the parallel pipeline before the inlet of the dry bag filter, and can be connected or removed as needed.
热管传热效率很高,又是双功能,体积不大,因此非常具有特色。The heat transfer efficiency of the heat pipe is very high, and it has dual functions, and the volume is small, so it is very distinctive.
本发明的优点在于:The advantages of the present invention are:
无论是升温还是降温,都是利用热管传热,且都是利用了相变热进行热交换,传热量大,热效率高,因此比管式表面换热器传热面积小很多,升温或降温效果更好。设备寿命长、占地小、投资只相当或略高于现有的降温装置费用。有完善的供汽和给排水装置,保障了系统正常工作。Whether it is heating up or cooling down, heat pipes are used to transfer heat, and phase change heat is used for heat exchange. The heat transfer is large and the thermal efficiency is high. Therefore, the heat transfer area is much smaller than that of the tubular surface heat exchanger, and the heating or cooling effect better. The equipment has a long service life, occupies a small area, and the investment is only equivalent to or slightly higher than that of the existing cooling device. There are complete steam supply and water supply and drainage devices to ensure the normal operation of the system.
附图说明 Description of drawings
图1为热管加热与冷却装置图。其中,热交换器本体1、热管2、换热器中心蒸汽或软水包包3、换热器上部的软水或蒸汽包4、疏水阀5、冷凝水箱6、冷凝水过滤器7、冷凝水泵8、止回阀9、截止阀10、定期排污管11、连续排污管12、安全阀13、放散阀14。Figure 1 is a diagram of a heat pipe heating and cooling device. Among them, the heat exchanger body 1, the heat pipe 2, the steam or soft water bag in the center of the heat exchanger 3, the soft water or steam bag on the upper part of the heat exchanger 4, the steam trap 5, the condensate tank 6, the condensate filter 7, the condensate pump 8 , Check valve 9, stop valve 10, regular blowdown pipe 11, continuous blowdown pipe 12, safety valve 13, release valve 14.
具体实施方式 Detailed ways
换热器中心蒸汽或软水包包3与换热器上部的蒸汽或软水包4通过管道连接;下部与冷凝水箱6连接。中心包与蒸汽管和软水管路连接,既可通饱和蒸汽,又可以通以软水。The steam or soft water bag 3 in the center of the heat exchanger is connected to the steam or soft water bag 4 on the upper part of the heat exchanger through pipelines; the lower part is connected to the condensed water tank 6 . The center bag is connected with the steam pipe and the soft water pipeline, which can pass through both saturated steam and soft water.
换热器壳体内有一定厚度的喷涂层起绝热和防止磨损作用。在壳体上、下设有检修用人孔。There is a spray coating with a certain thickness in the heat exchanger shell to insulate heat and prevent wear. There are manholes for maintenance on the top and bottom of the shell.
热管换热器本体1和内置换热器中心蒸汽或软水包包3均为压力容器,换热器中心蒸汽或软水包包3壳体上安有数千根水平放置的热管2。当煤气需要升温时中心包内通入饱和蒸汽,热管将蒸汽热量传递给外侧荒煤气,使之加热升温。蒸汽传热后成为冷凝水,经疏水器5,冷凝水箱6,过滤器7,冷凝水泵8及止回阀9、截止阀10进行回收。煤气需要降温时换热器中心包中蒸汽改换为软水,高温煤气热量经热管传至水中,使软水汽化、蒸汽逸出,从而使煤气降温;换热器上部的软水或蒸汽包4应保持一定水位并具有汽水分离作用,换热器上部的软水或蒸汽包4上有安全阀13、蒸汽放散阀14、定期排污管11、连续排污管12及补水管路。The heat pipe heat exchanger body 1 and the steam or soft water bag 3 in the center of the built-in heat exchanger are both pressure vessels, and thousands of horizontally placed heat pipes 2 are installed on the shell of the heat exchanger center steam or soft water bag 3 . When the gas needs to be heated up, saturated steam is introduced into the central bag, and the heat pipe transfers the heat of the steam to the raw gas on the outside to heat it up. After heat transfer, the steam becomes condensed water, which is recovered through steam trap 5, condensed water tank 6, filter 7, condensed water pump 8, check valve 9, and stop valve 10. When the gas needs to cool down, the steam in the center bag of the heat exchanger is replaced with soft water, and the heat of the high-temperature gas is transferred to the water through the heat pipe, so that the soft water vaporizes and the steam escapes, thereby cooling the gas; the soft water or steam bag 4 on the upper part of the heat exchanger should be kept at a certain The water level has the effect of steam-water separation, and the soft water or steam drum 4 on the upper part of the heat exchanger has a safety valve 13, a steam release valve 14, a regular sewage discharge pipe 11, a continuous sewage discharge pipe 12 and a water supply pipeline.
由于热管水平放置,因此可以双向传热,改变不同介质可以加热或冷却煤气,使之升温或降温。Because the heat pipe is placed horizontally, it can transfer heat in two directions, and changing different media can heat or cool the gas, making it warm up or cool down.
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| CN200920106930XU CN201406440Y (en) | 2009-04-03 | 2009-04-03 | Blast furnace gas dry dust removal heat pipe heating and cooling device |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102296979A (en) * | 2010-06-22 | 2011-12-28 | 武汉高科佳诚动力科技有限公司 | Dedusting and dehydrating process of deep condensation to gas by utilizing natural cold source |
| CN103436649A (en) * | 2013-09-03 | 2013-12-11 | 南京工业大学 | A temperature control system and method for dry bag dust removal |
| CN104087694A (en) * | 2014-07-22 | 2014-10-08 | 攀钢集团工程技术有限公司 | Blast furnace smoke recycling device |
| CN111550756A (en) * | 2020-03-31 | 2020-08-18 | 四川建筑职业技术学院 | A system and method for smoke and dust control and waste heat comprehensive utilization of manganese ferroalloy submerged arc furnace |
-
2009
- 2009-04-03 CN CN200920106930XU patent/CN201406440Y/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102296979A (en) * | 2010-06-22 | 2011-12-28 | 武汉高科佳诚动力科技有限公司 | Dedusting and dehydrating process of deep condensation to gas by utilizing natural cold source |
| CN102296979B (en) * | 2010-06-22 | 2013-09-25 | 武汉高科佳诚动力科技有限公司 | Dedusting and dehydrating process of deep condensation to gas by utilizing natural cold source |
| CN103436649A (en) * | 2013-09-03 | 2013-12-11 | 南京工业大学 | A temperature control system and method for dry bag dust removal |
| CN104087694A (en) * | 2014-07-22 | 2014-10-08 | 攀钢集团工程技术有限公司 | Blast furnace smoke recycling device |
| CN111550756A (en) * | 2020-03-31 | 2020-08-18 | 四川建筑职业技术学院 | A system and method for smoke and dust control and waste heat comprehensive utilization of manganese ferroalloy submerged arc furnace |
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