CN201106926Y - A hot stove preheating device - Google Patents
A hot stove preheating device Download PDFInfo
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- CN201106926Y CN201106926Y CNU2007200143551U CN200720014355U CN201106926Y CN 201106926 Y CN201106926 Y CN 201106926Y CN U2007200143551 U CNU2007200143551 U CN U2007200143551U CN 200720014355 U CN200720014355 U CN 200720014355U CN 201106926 Y CN201106926 Y CN 201106926Y
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- heat exchanger
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- blast stove
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- 238000002485 combustion reaction Methods 0.000 claims abstract description 43
- 239000007789 gas Substances 0.000 claims description 45
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 6
- 239000003546 flue gas Substances 0.000 claims description 6
- 239000007921 spray Substances 0.000 claims description 3
- 229910001220 stainless steel Inorganic materials 0.000 claims description 3
- 239000010935 stainless steel Substances 0.000 claims description 3
- 239000003034 coal gas Substances 0.000 abstract description 5
- 238000012423 maintenance Methods 0.000 abstract description 4
- 238000010304 firing Methods 0.000 abstract 2
- 101100006584 Mus musculus Clnk gene Proteins 0.000 abstract 1
- 238000005516 engineering process Methods 0.000 abstract 1
- 230000007774 longterm Effects 0.000 abstract 1
- 239000003595 mist Substances 0.000 abstract 1
- 230000009466 transformation Effects 0.000 abstract 1
- 239000002912 waste gas Substances 0.000 abstract 1
- 238000000034 method Methods 0.000 description 7
- 229910000831 Steel Inorganic materials 0.000 description 4
- 239000010959 steel Substances 0.000 description 4
- 238000003466 welding Methods 0.000 description 3
- 239000000919 ceramic Substances 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000011449 brick Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 239000011819 refractory material Substances 0.000 description 1
- 230000002787 reinforcement Effects 0.000 description 1
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Abstract
Description
技术领域technical field
本实用新型涉及一种热风炉预热装置,尤其是一种采用板式换热器与立式燃烧炉相结合的方式来预热热风炉所需助燃空气和煤气的热风炉预热装置。The utility model relates to a hot blast stove preheating device, in particular to a hot blast stove preheating device which uses a combination of a plate heat exchanger and a vertical combustion furnace to preheat the combustion-supporting air and gas required by the hot blast stove.
背景技术Background technique
提高热风温度,降低炼铁能耗,一直是炼铁生产的攻关内容。目前国内外多采用这样一种工艺,即是利用热风炉烟道废气与燃烧炉燃烧产生的烟气相混合后的混合气体来进行空气、煤气预热,该工艺包含管式换热器和燃烧炉等主要设备,例如专利号为96225818.0的专利,它采用的主要设备是卧式燃烧炉与管式换热器等,专利号为02280459.5的专利它采用的主要设备是采用陶瓷燃烧器的立式燃烧炉和管式换热器等,上述两类预热装置在实际应用中存在一些问题,管式换热器占地面积大,在扩容改造中不能满足场地空间限制的要求,热效率低,卧式燃烧炉占地面积大,立式燃烧炉采用的陶瓷燃烧器,砖型多,且复杂,制作、施工、砌筑难度大,周期长。而且现有的立式燃烧炉都存在整体外形高、钢材用量大的问题。Increasing the temperature of hot air and reducing the energy consumption of ironmaking has always been the key content of ironmaking production. At present, such a process is widely used at home and abroad, that is, the mixed gas mixed with the flue gas generated by the hot blast stove and the flue gas generated by the combustion furnace is used to preheat the air and gas. This process includes a tubular heat exchanger and a combustion Furnace and other main equipment, such as the patent No. 96225818.0, which uses horizontal combustion furnaces and tube heat exchangers, etc., and the patent No. 02280459.5, which uses vertical ceramic burners. Combustion furnace and tube heat exchanger, etc., the above two types of preheating devices have some problems in practical application. The vertical combustion furnace covers a large area, and the ceramic burner used in the vertical combustion furnace has many types of bricks and is complicated. It is difficult to manufacture, construct, and masonry, and the cycle is long. Moreover, the existing vertical combustion furnaces all have the problems of high overall profile and large steel consumption.
发明内容Contents of the invention
本实用新型的目的在于提供体积小、结构简单、维护方便、使用寿命长的改进型附加燃烧炉的一种热风炉预热装置。The purpose of the utility model is to provide a hot blast stove preheating device of an improved additional combustion furnace with small volume, simple structure, convenient maintenance and long service life.
本实用新型的目的是这样实现的:它是由燃烧炉与换热器组成,经管道引出的热风炉烟道废气送到燃烧炉,燃烧炉出口混合气体管道连接到换热器入口,空气和煤气经换热器热交换后连接到热风炉,换热器出口连接到热风炉烟囱,其特征在于,采用格栅式燃烧器的立式燃烧炉及采用板式换热器。The purpose of this utility model is achieved in this way: it is composed of a combustion furnace and a heat exchanger, and the exhaust gas from the hot blast stove flue drawn through the pipeline is sent to the combustion furnace, and the mixed gas pipeline at the outlet of the combustion furnace is connected to the inlet of the heat exchanger, and the air and The coal gas is connected to the hot blast stove after being heat exchanged by the heat exchanger, and the outlet of the heat exchanger is connected to the chimney of the hot blast stove.
本实用新型的燃烧炉由炉壳、炉衬、燃烧室、混合室、各气体进出口等构成。其中燃烧室内设燃烧器,燃烧器中带有煤气通道和空气通道,并且分别与炉体上的煤气入口和空气入口相连通;混合室中心区外有环形烟道,环形烟道与热风炉废气入口相通,环形烟道与中心区之间设有30°~60°的喷出口。The combustion furnace of the utility model is composed of a furnace shell, a furnace lining, a combustion chamber, a mixing chamber, and various gas inlets and outlets. The combustion chamber is equipped with a burner, which has a gas channel and an air channel, and is respectively connected with the gas inlet and the air inlet on the furnace body; there is an annular flue outside the central area of the mixing chamber, and the annular flue is connected to the exhaust gas of the hot blast stove. The entrance is connected, and a 30°-60° spray outlet is provided between the annular flue and the central area.
本实用新型的具体结构是其燃烧炉的燃烧器采用格栅式,由支柱和炉篦子组成。支柱由钢板焊制成曲线型,它既可做炉篦子的结构支撑,又将燃烧室内的空间分隔成煤气通道和空气通道两部分。立柱上面的炉篦子为格栅式结构,由上下交错的两个带长条形格孔的炉篦子和位于它们上面的一个带有方形格孔的炉篦子的三层结构组合而成,每种格孔的炉篦子均采用耐火材料浇注成型。The concrete structure of the present utility model is that the burner of its combustion furnace adopts grid type, is made up of pillar and fire grate. The pillar is welded into a curved shape by steel plate, which can be used as the structural support of the grate, and divides the space in the combustion chamber into two parts, the gas channel and the air channel. The grate above the column is a grid structure, which is composed of two staggered grates with long strip holes and a three-layer structure above them with a grate with square holes. The grates of the grid holes are casted with refractory materials.
本实用新型的板式换热器主要包括混合气和空气(或煤气)的进出接管、板片和支架组成。混合气和空气(或煤气)以逆流方式进入换热器板片间,板片采用0.6~0.8mm的不锈钢薄板,机压、模压制成波纹形式,板片间采用焊接型式连接。The plate heat exchanger of the utility model mainly includes inlet and outlet connecting pipes for mixed gas and air (or gas), plates and brackets. The mixed gas and air (or gas) enter the heat exchanger plates in a countercurrent manner. The plates are made of 0.6-0.8mm stainless steel sheets, machine-pressed and molded into corrugated forms, and the plates are connected by welding.
本实用新型由于采用了格栅式燃烧器,降低了现有立式燃烧炉整体高度,使得工艺布置更灵活。燃烧器本体结构简单,经济适用、气流分布均匀,燃烧充分完全;燃烧炉混合室的环形烟道与喷出口的结构设计,保证了废气与烟气的混合均匀。同时本实用新型采用了板式换热器作为传热换热装置,使得在同样传热面积情况下,设备体积和重量减小了2/3(比管式换热器),工艺布置更紧凑;短流程使得压降低,而传热效率高;板片安装、拆卸简单,使得检修维护方便,设备寿命与可靠性大为提高,寿命可达15年。Because the utility model adopts the grid type burner, the overall height of the existing vertical combustion furnace is reduced, so that the process arrangement is more flexible. The structure of the burner body is simple, economical and applicable, the air flow is evenly distributed, and the combustion is complete and complete; the structural design of the annular flue and the nozzle of the mixing chamber of the combustion furnace ensures that the exhaust gas and flue gas are evenly mixed. At the same time, the utility model uses a plate heat exchanger as a heat transfer device, so that under the same heat transfer area, the volume and weight of the equipment are reduced by 2/3 (compared with the tube heat exchanger), and the process layout is more compact; The short process makes the pressure drop, and the heat transfer efficiency is high; the installation and disassembly of the plate is simple, which makes the maintenance convenient, and the service life and reliability of the equipment are greatly improved, and the service life can reach 15 years.
附图说明Description of drawings
图1为本实用新型的结构示意图;Fig. 1 is the structural representation of the utility model;
图2为燃烧器的结构示意图;Fig. 2 is the structural representation of burner;
图3为燃烧器方格形的炉篦子的结构示意图;Fig. 3 is the structural representation of the grate of burner grid shape;
图4为燃烧器长条形的炉篦子的结构示意图;Fig. 4 is the structural representation of the strip-shaped fire grate of burner;
图5燃烧器的曲线型支柱的结构示意图。Fig. 5 Schematic diagram of the structure of the curved pillar of the burner.
具体实施方式Detailed ways
下面结合附图对本实用新型作进一步说明:Below in conjunction with accompanying drawing, the utility model is further described:
如图1所示,本实用新型主要由立式燃烧炉与板式换热器组成,燃烧炉与板式换热器通过管道连接。As shown in Figure 1, the utility model is mainly composed of a vertical combustion furnace and a plate heat exchanger, and the combustion furnace and the plate heat exchanger are connected through pipelines.
如图1所示,本实用新型的立式燃烧炉1,主要包括由外壳2、炉衬3、燃烧室4和混合室5,在炉体上设有煤气入口6、空气入口7、热风炉废气入口8、混合气出口9。其中燃烧室4内设燃烧器10,燃烧器10中带有煤气通道和空气通道,并且分别与炉体上的煤气入口6和空气入口7相连通;混合室5中心区外有环形烟道11,环形烟道11与热风炉废气入口8相通,环形烟道11与中心区之间设有30°~60°的喷出口12,混合气出口9设在燃烧炉顶部。煤气与空气混合在燃烧室4内燃烧,燃烧后产生的烟气温度达1100℃以上。来自热风炉烟道的温度在100℃~300℃左右的废气从废气入口8进入环形烟道11,从喷出口12喷入中心区,与燃烧炉燃烧产生的烟气混合,混合后气体达到500℃~600℃。燃烧炉顶部的混合气出口经管道18连接到换热器入口。As shown in Figure 1, the vertical combustion furnace 1 of the present utility model mainly comprises shell 2, furnace lining 3, combustion chamber 4 and mixing chamber 5, is provided with gas inlet 6, air inlet 7, hot-blast stove exhaust gas on furnace body Inlet 8, mixed gas outlet 9. Wherein the combustion chamber 4 is provided with a burner 10, the burner 10 has a gas channel and an air channel, and is respectively connected with the gas inlet 6 and the air inlet 7 on the furnace body; there is an annular flue 11 outside the central area of the mixing chamber 5 , the annular flue 11 communicates with the exhaust gas inlet 8 of the hot blast stove, and the ejection port 12 of 30°-60° is arranged between the annular flue 11 and the central area, and the mixed gas outlet 9 is arranged on the top of the combustion furnace. The coal gas and air are mixed and burned in the combustion chamber 4, and the temperature of the flue gas generated after combustion reaches above 1100°C. The exhaust gas from the flue of the hot blast stove with a temperature of about 100°C to 300°C enters the annular flue 11 from the exhaust gas inlet 8, sprays into the central area from the outlet 12, and mixes with the flue gas generated by the combustion furnace, and the mixed gas reaches 500 ℃~600℃. The gas mixture outlet at the top of the burner is connected to the inlet of the heat exchanger through a pipe 18 .
如图2所示,燃烧器10由曲线型支柱13和安装在它上面的炉篦子14、15构成。如图3、4所示,炉篦子为格栅式结构,由上下交错的两个带长条形格孔的炉篦子15和位于它们上面的一个带有方形格孔的炉篦子14的三层结构组合而成,两层炉篦子15为垂直交错布置。炉篦子14、15均采用耐火浇注料浇注成型,为保证强度,采用圆钢做配筋。As shown in Figure 2, the burner 10 is made of a
如图5所示,燃烧器的曲线型支柱13采用钢板焊制,将燃烧室内的空间分隔成煤气通道16和空气通道17两部分,煤气、空气由独立的煤气通道16和空气通道17进入燃烧器上部,经过格栅式炉篦子后,使得空气、煤气在燃烧器表面分布均匀,保证燃烧充分完全。As shown in Figure 5, the
如图1所示,燃烧炉的混合气和空气(或煤气)分别从换热器19的接管21和接管23进入,逆流运行,在换热器板片20间各自独立,间隔分布,板片间采用焊接型式连接,进行热交换后的混合气和空气(或煤气)分别从接管25和接管22排出,利用支架24可承载换热器自重和进行设备安装,板式换热器采用不锈钢薄板作传热元件,传热效率高,流程短压降低;板片可拆卸,检修维护方便。As shown in Figure 1, the mixed gas and air (or coal gas) of the combustion furnace enter from the connecting pipe 21 and the connecting pipe 23 of the heat exchanger 19 respectively, and run countercurrently, and are independently distributed between the heat exchanger plates 20, and the plates The room is connected by welding, and the mixed gas and air (or coal gas) after heat exchange are discharged from the connecting pipe 25 and the connecting pipe 22 respectively. The bracket 24 can bear the weight of the heat exchanger and carry out equipment installation. The plate heat exchanger is made of stainless steel sheet. Heat transfer elements, high heat transfer efficiency, low process short pressure; detachable plates, easy maintenance.
Claims (7)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007200143551U CN201106926Y (en) | 2007-08-29 | 2007-08-29 | A hot stove preheating device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007200143551U CN201106926Y (en) | 2007-08-29 | 2007-08-29 | A hot stove preheating device |
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| CN201106926Y true CN201106926Y (en) | 2008-08-27 |
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| CNU2007200143551U Expired - Fee Related CN201106926Y (en) | 2007-08-29 | 2007-08-29 | A hot stove preheating device |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102759106A (en) * | 2012-07-31 | 2012-10-31 | 中冶南方(武汉)威仕工业炉有限公司 | Tandem type air gas dual-preheating radiation tube preheating system and air coal gas preheating method |
| CN102786235A (en) * | 2012-07-24 | 2012-11-21 | 中信重工机械股份有限公司 | Active lime predecomposition furnace apparatus |
| CN103363811A (en) * | 2012-03-30 | 2013-10-23 | 鞍钢股份有限公司 | Combustion method for mixing oxygen into high-temperature flue gas |
-
2007
- 2007-08-29 CN CNU2007200143551U patent/CN201106926Y/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103363811A (en) * | 2012-03-30 | 2013-10-23 | 鞍钢股份有限公司 | Combustion method for mixing oxygen into high-temperature flue gas |
| CN102786235A (en) * | 2012-07-24 | 2012-11-21 | 中信重工机械股份有限公司 | Active lime predecomposition furnace apparatus |
| CN102759106A (en) * | 2012-07-31 | 2012-10-31 | 中冶南方(武汉)威仕工业炉有限公司 | Tandem type air gas dual-preheating radiation tube preheating system and air coal gas preheating method |
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Legal Events
| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee |
Owner name: ANSTEEL ENGINEERING TECHNOLOGY CO., LTD. Free format text: FORMER NAME: ANGANG GROUP CORPORATION DESIGN + RESEARCH INSTITUTE |
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| CP01 | Change in the name or title of a patent holder |
Address after: 114021 Tiexi District, Liaoning City, Anshan Iron and steel plant Co-patentee after: ANGANG STEEL COMPANY LIMITED Patentee after: ANSTEEL ENGINEERING TECHNOLOGY Corp.,Ltd. Address before: 114021 Tiexi District, Liaoning City, Anshan Iron and steel plant Co-patentee before: ANGANG STEEL COMPANY LIMITED Patentee before: ANSHAN IRON AND STEEL Group DE |
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20080827 Termination date: 20150829 |
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| EXPY | Termination of patent right or utility model |