CN201538799U - Regenerative non-oxidation heating furnace - Google Patents
Regenerative non-oxidation heating furnace Download PDFInfo
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- CN201538799U CN201538799U CN200920246650.9U CN200920246650U CN201538799U CN 201538799 U CN201538799 U CN 201538799U CN 200920246650 U CN200920246650 U CN 200920246650U CN 201538799 U CN201538799 U CN 201538799U
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- 230000001172 regenerating effect Effects 0.000 title claims abstract description 52
- 238000010438 heat treatment Methods 0.000 title claims abstract description 24
- 230000003647 oxidation Effects 0.000 title claims abstract description 20
- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 20
- 239000007789 gas Substances 0.000 claims abstract description 111
- 230000001105 regulatory effect Effects 0.000 claims abstract description 33
- 239000000779 smoke Substances 0.000 claims abstract description 33
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 32
- 239000003546 flue gas Substances 0.000 claims abstract description 32
- 238000002485 combustion reaction Methods 0.000 claims description 67
- 238000005338 heat storage Methods 0.000 claims description 24
- 239000000919 ceramic Substances 0.000 claims description 6
- 238000012544 monitoring process Methods 0.000 claims description 3
- 230000001590 oxidative effect Effects 0.000 claims 1
- 239000000446 fuel Substances 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 238000005246 galvanizing Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- -1 aluminum-zinc-silicon Chemical compound 0.000 description 2
- 238000000137 annealing Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 238000004364 calculation method Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
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- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
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Abstract
本实用新型提供一种蓄热式无氧化加热炉,包括:炉体;第一蓄热烧嘴,设置在炉体外的一侧,配置有第一空气蓄热室和第一燃气蓄热室,其中第一空气蓄热室通过第一空气/烟气管道与空气换向阀的第一端口连接,空气换向阀的第二端口通过空气管道依次与空气流量计、空气流量电动调节阀和空气助烟风机连接,空气换向阀的第三端口通过空气排烟管道依次与空气排烟电动调节阀和空气排烟风机连接,且在空气排烟管道上设置有空气排烟温度传感器;第一燃气蓄热室通过第一燃气/烟气管道与燃气换向阀的第一端口连接,所述燃气换向阀的第二端通过燃气管道依次与燃气流量计、燃气流量电动调节阀和燃气气源连接,能够有效提高热能利用率。
The utility model provides a regenerative non-oxidation heating furnace, comprising: a furnace body; a first regenerative burner arranged on one side of the furnace body, equipped with a first air regenerator and a first gas regenerator, The first air regenerator is connected to the first port of the air reversing valve through the first air/flue gas pipeline, and the second port of the air reversing valve is connected to the air flow meter, the electric air flow regulating valve and the air flow through the air pipeline in turn. The smoke assist fan is connected, and the third port of the air reversing valve is connected with the air smoke electric control valve and the air smoke fan in turn through the air smoke exhaust pipe, and an air smoke exhaust temperature sensor is arranged on the air smoke exhaust pipe; the first The gas regenerator is connected to the first port of the gas reversing valve through the first gas/flue gas pipeline, and the second end of the gas reversing valve is connected to the gas flow meter, the electric gas flow control valve and the gas Source connection can effectively improve the utilization rate of heat energy.
Description
技术领域technical field
本实用新型涉及一种蓄热式工业炉,尤其涉及一种可应用于冶金板带连退生产线,以及热镀锌、热镀铝和热镀铝锌硅生产线的蓄热式无氧化加热炉。The utility model relates to a regenerative industrial furnace, in particular to a regenerative non-oxidation heating furnace which can be applied to a metallurgical strip continuous annealing production line, as well as hot-dip galvanizing, hot-dip aluminum and hot-dip aluminum-zinc-silicon production lines.
背景技术Background technique
在森吉米尔法镀锌工艺中,预热炉加热带钢氧化相对严重,同时排烟温度较高,即使有换热措施,换热效率低,炉内气氛难控制,直至目前国内还不能将低热值燃料(如高炉煤气)应用于冶金板带连退生产线,热镀锌、热镀铝、热镀铝锌硅生产线。In the Sendzimir galvanizing process, the oxidation of the steel strip heated by the preheating furnace is relatively serious, and the temperature of the exhaust gas is relatively high. Even if there are heat exchange measures, the heat exchange efficiency is low, and the atmosphere in the furnace is difficult to control. Value fuels (such as blast furnace gas) are used in metallurgical strip continuous annealing production lines, hot-dip galvanizing, hot-dip aluminum, and hot-dip aluminum-zinc-silicon production lines.
实用新型内容Utility model content
为了解决上述问题,本实用新型的目的是提供一种蓄热式无氧化加热炉,能够有效提高热能利用率。In order to solve the above problems, the purpose of this utility model is to provide a regenerative non-oxidation heating furnace, which can effectively improve the utilization rate of heat energy.
为了达到上述目的,本实用新型提供一种蓄热式无氧化加热炉,包括:In order to achieve the above purpose, the utility model provides a regenerative non-oxidation heating furnace, comprising:
炉体;Furnace body;
第一蓄热烧嘴1,设置在所述炉体外的一侧,所述第一蓄热烧嘴1配置有第一空气蓄热室3和第一燃气蓄热室2,其中所述第一空气蓄热室3通过第一空气/烟气管道27与空气换向阀13的第一端口连接;所述第一燃气蓄热室2通过第一燃气/烟气管道26与燃气换向阀8的第一端口连接;The first regenerative burner 1 is arranged on one side of the furnace body, and the first regenerative burner 1 is equipped with a
第一预混室38,设置在所述炉体内,且与所述第一蓄热烧嘴1的位置对应,所述第一预混室38的上部通过第一补燃空气管道4与第一补燃空气快切阀5的一端口连接,所述第一补燃空气快切阀5的另一端口与二次补燃总管道28的一端连接;The
第二蓄热烧嘴19,设置在所述炉体外的另一侧,所述第二蓄热烧嘴19配置有第二空气蓄热室21和第二燃气蓄热室20,其中,所述第二空气蓄热室21通过第二空气/烟气管道24与所述空气换向阀13的第四端口连接;所述第二燃气蓄热室20通过第二燃气/烟气管道25与所述燃气换向阀(8)的第四端口连接;The second
第二预混室39,设置在所述炉体内,且与所述第二蓄热烧嘴19的位置对应,所述第二预混室39的上部通过第二补燃空气管道22与第二补燃空气快切阀18的一端口连接,所述第二补燃空气快切阀18的另一端口与所述二次补燃总管道28的一端连接。The
优选的,所述第一燃气蓄热室2、第一空气蓄热室3、第二燃气蓄热室20和第二空气蓄热室21内放置有陶瓷蓄热球或蜂窝陶瓷蓄热体。Preferably, ceramic heat storage balls or honeycomb ceramic heat storage bodies are placed in the first gas
优选的,所述燃气换向阀8的第二端通过燃气管道29依次与燃气流量计9、燃气流量电动调节阀10和燃气气源36连接,所述燃气换向阀8的第三端口通过燃气排烟管道30依次与燃气排烟电动调节阀12和燃气排烟风机35连接,所述燃气排烟管道30设置有燃气排烟温度传感器11。Preferably, the second end of the
优选的,所述空气换向阀13的第二端口通过空气管道31依次与空气流量计14、空气流量电动调节阀15和空气助烟风机34连接,所述空气换向阀13的第三端口通过空气排烟管道32依次与空气排烟电动调节阀17和空气排烟风机33连接,且所述空气排烟管道32上设置有空气排烟温度传感器16。Preferably, the second port of the
优选的,所述二次补燃总管道28的另一端依次与二次补燃空气流量计6、二次补燃空气流量电动调节阀7和二次补燃风机37连接。Preferably, the other end of the secondary supplementary combustion
优选的,所述空气换向阀13、所述空气流量电动调节阀15、所述空气排烟电动调节阀17、所述燃气流量电动调节阀10、所述燃气换向阀8、所述燃气排烟电动调节阀12、所述二次补燃空气流量电动调节阀7、所述第一补燃空气快切阀5和所述第二补燃空气快切阀18为电磁阀、电动阀和气动阀中的任意一种。Preferably, the
优选的,所述炉体的顶部或炉体的侧面设置有炉温监测点23。Preferably, a furnace
由上述可知,本实用新型中的蓄热式无氧化加热炉的炉体两侧布置有蓄热燃烧装置,可交替在两侧同时加热和蓄热即将进入炉内燃烧的空气和燃气,大大提高热能利用率。同时保留了原有补燃措施,能有效精确控制炉内空燃比,实现还原气氛加热,同时确保过剩空气系数小于1的烟气中的能源不浪费。实现无氧化加热的前提下,进一步提高热能利用率,实现了低热值燃料在板带热处理领域的应用,开创了新型节能的蓄热式无氧化加热技术。It can be seen from the above that the regenerative non-oxidation heating furnace in the utility model is equipped with regenerative combustion devices on both sides of the furnace body, which can alternately heat and store the air and gas that are about to enter the furnace for combustion at the same time on both sides, greatly improving Heat utilization rate. At the same time, the original supplementary combustion measures are retained, which can effectively and accurately control the air-fuel ratio in the furnace, realize the heating of the reducing atmosphere, and at the same time ensure that the energy in the flue gas with an excess air coefficient less than 1 is not wasted. On the premise of realizing non-oxidation heating, the utilization rate of heat energy is further improved, the application of low calorific value fuel in the field of strip heat treatment is realized, and a new energy-saving regenerative non-oxidation heating technology is created.
附图说明Description of drawings
图1为本实用新型中的蓄热式无氧化加热炉的结构示意图。Fig. 1 is a schematic structural view of the regenerative non-oxidation heating furnace in the present invention.
具体实施方式Detailed ways
为了使本实用新型实施例的目的、技术方案和优点更加清楚明白,下面结合实施例和附图,对本实用新型实施例做进一步详细地说明。在此,本实用新型的示意性实施例及说明用于解释本实用新型,但并不作为对本实用新型的限定。In order to make the purpose, technical solutions and advantages of the embodiments of the present invention clearer, the embodiments of the present invention will be further described in detail below in conjunction with the embodiments and the accompanying drawings. Here, the exemplary embodiments and descriptions of the utility model are used to explain the utility model, but not as a limitation to the utility model.
参见图1,为本实施例中的蓄热式无氧化加热炉的结构示意图,该蓄热式无氧化加热炉包括:炉体、第一蓄热烧嘴1、第一预混室38、第二蓄热烧嘴19和第二预混室39,其中Referring to Fig. 1, it is a schematic structural diagram of a regenerative non-oxidation heating furnace in this embodiment, which includes: a furnace body, a first regenerative burner 1, a
第一蓄热烧嘴1,设置在该炉体外的一侧,该第一蓄热烧嘴1配置有第一空气蓄热室3和第一燃气蓄热室2,其中该第一空气蓄热室3通过第一空气/烟气管道27与空气换向阀13的第一端口连接,该空气换向阀13的第二端口通过空气管道31依次与空气流量计14、空气流量电动调节阀15和空气助烟风机34连接,该空气换向阀13的第三端口通过空气排烟管道32依次与空气排烟电动调节阀17和空气排烟风机33连接,且在该空气排烟管道32上设置有空气排烟温度传感器16;该第一燃气蓄热室2通过第一燃气/烟气管道26与燃气换向阀8的第一端口连接,该燃气换向阀8的第二端口通过燃气管道29依次与燃气流量计9、燃气流量电动调节阀10和燃气气源36连接,该燃气换向阀8的第三端口通过燃气排烟管道30依次与燃气排烟电动调节阀12和燃气排烟风机35连接,且燃气排烟管道30设置有燃气排烟温度传感器11;The first regenerative burner 1 is arranged on one side of the furnace body. The first regenerative burner 1 is equipped with a
第一预混室38,设置在该炉体内,且与该第一蓄热烧嘴1的位置对应,该第一预混室38的上部通过第一补燃空气管道4与第一补燃空气快切阀5的一端口连接,该第一补燃空气快切阀5的另一端口通过二次补燃总管道28依次与二次补燃空气流量计6、二次补燃空气流量电动调节阀7和二次补燃风机37连接;The
第二蓄热烧嘴19,设置在该炉体外的另一侧,该第二蓄热烧嘴19配置有第二空气蓄热室21和第二燃气蓄热室20,其中,该第二空气蓄热室21通过第二空气/烟气管道24与该空气换向阀13的第四端口连接;该第二燃气蓄热室20通过第二燃气/烟气管道25与燃气换向阀8的第四端口连接;The second
第二预混室39,设置在该炉体内,且与第二蓄热烧嘴19的位置对应,该第二预混室39的上部通过第二补燃空气管道22与第二补燃空气快切阀18的一端口连接,第二补燃空气快切阀18的另一端口与二次补燃总管道28连接,,即该二次补燃总管道28的一端分别与第一补燃空气快切阀5和第二补燃空气快切阀18连接,该二次补燃总管道28的另一端则连接二次补燃空气流量计6,通过采用电气自动化控制对流体回路进行周期性切换,对空气和燃气的流量进行精确控制。The
在本实施例中,上述第一燃气蓄热室2、第一空气蓄热室3、第二燃气蓄热室20和第二空气蓄热室21内放置有陶瓷蓄热球或蜂窝陶瓷蓄热体。In this embodiment, ceramic heat storage balls or honeycomb ceramic heat storage body.
上述空气换向阀13、空气流量电动调节阀15、空气排烟电动调节阀17、燃气流量电动调节阀10、燃气换向阀8、燃气排烟电动调节阀12、二次补燃空气流量电动调节阀7、第一补燃空气快切阀5、第二补燃空气快切阀18为电磁阀、电动阀和气动阀中的任意一种。例如该空气换向阀13可选用空气二位四通换向阀,燃气换向阀8可选用燃气二位四通换向阀。The
为了能够有效监控炉体内的温度,在本实施例中还可在炉体的顶部或炉体的侧面设置有炉温监测点23。In order to effectively monitor the temperature in the furnace body, in this embodiment, a furnace
由上述可知,本实用新型中的蓄热式无氧化加热炉的炉体两侧布置有蓄热燃烧装置,可交替在两侧同时加热和蓄热即将进入炉内燃烧的空气和燃气,大大提高热能利用率,保留了原有补燃措施,能有效精确控制炉内空燃比实现还原气氛加热,同时确保过剩空气系数小于1的烟气中的能源不浪费。It can be seen from the above that the regenerative non-oxidation heating furnace in the utility model is equipped with regenerative combustion devices on both sides of the furnace body, which can alternately heat and store the air and gas that are about to enter the furnace for combustion at the same time on both sides, greatly improving The utilization rate of heat energy retains the original supplementary combustion measures, which can effectively and accurately control the air-fuel ratio in the furnace to achieve heating in the reducing atmosphere, and at the same time ensure that the energy in the flue gas with an excess air coefficient less than 1 is not wasted.
实现无氧化加热的前提下,进一步提高热能利用率,实现了低热值燃料在板带热处理领域的应用,开创了新型节能的蓄热式无氧化加热技术。On the premise of realizing non-oxidation heating, the utilization rate of heat energy is further improved, the application of low calorific value fuel in the field of strip heat treatment is realized, and a new energy-saving regenerative non-oxidation heating technology is created.
下面结合附图对本实用技术进行详细描述:在工作时,A侧的第一蓄热烧嘴1与B侧的第二蓄热烧嘴19分别交替工作在燃烧和蓄热状态。当A侧的第一蓄热烧嘴1在燃烧时,空气换向阀13把A侧的空气管道31与第一空气/烟气管道27相通;同时把B侧的空气排烟管道32与第二空气/烟气管道24相通;The practical technology will be described in detail below with reference to the accompanying drawings: when working, the first regenerative burner 1 on the A side and the second
与此同时,燃气换向阀8把A侧的燃气管道29与第一燃气/烟气管道26相通;同时把B侧的燃气/烟气管道25与燃气烟气管道30相通。此时空气由鼓风机加压经过空气流量电动调节阀15控制流量,然后经过空气流量计14监测,经过空气换向阀13,然后经过A侧的第一空气/烟气管道27,经过A侧的第一空气蓄热室3把空气加热(放热),热空气到达A侧的第一预混室38。At the same time, the
燃气与经过燃气流量电动调节阀10控制流量,经过燃气流量计9监测,经过燃气换向阀8,经过A侧的第一燃气/烟气管道26,经过A侧的第一燃气蓄热烧嘴2的燃气混合并燃烧。由于空气、燃气都能进行精确流量控制,为保证掌握炉内还原气氛创造有利条件。The flow of gas is controlled by the gas flow electric regulating
与此同时,B侧的第二补燃空气快切阀18开启;A侧的第一补燃空气快切阀5关闭;经过二次补燃风机37加压的空气经过二次补燃空气流量电动调节阀7控制流量,经过二次补燃空气流量计6监测,经过B侧的二次补燃空气快切阀18,经过B侧的二次补燃空气管道22供来的补燃空气与炉内过来的烟气中过剩的燃气在此完全燃烧,燃尽的高温烟气经过B侧的蓄热室降温(蓄热)后,经过B侧的第二空气/烟气管道24和第二燃气/烟气管道25,经过燃气换向阀8和空气换向阀13,经过燃气排烟管道30和空气排烟管道32,经过空气排烟电动调节阀17和燃气排烟电动调节阀12,经过排烟风机排出,如此便实现了A侧的第一蓄热烧嘴1的燃烧,B侧的第二蓄热烧嘴19的蓄热(蓄热分为空气蓄热和燃气蓄热)。At the same time, the second supplementary combustion air quick-
当B侧的第二蓄热烧嘴19在燃烧时,空气换向阀13把B侧的空气管道31与第二空气/烟气管道24相通,经过第二空气蓄热室21将空气送入第二预混室39,与此同时,燃气换向阀8把燃气管道29和第二燃气/烟气管道25相通,经过第二燃气蓄热室20将燃气送入第二预混室39,预混燃烧、此时烟气经过第一空气蓄热室3和第一燃气蓄热室2,然后空气换向阀13把空气排烟管道32与第一空气/烟气管道27相通;同时燃气换向阀8把燃气排烟管道30和第一燃气/烟气管道26相通,经过空气排烟电动调节阀17和燃气排烟电动调节阀12,经过排烟风机排出。如此便实现了B侧得第二蓄热烧嘴19的燃烧,A侧的第一蓄热烧嘴1的蓄热(蓄热分为空气蓄热和燃气蓄热),这时A侧的第一补燃空气快切阀5打开,B侧的第二补燃空气快切阀18关闭,二次补燃空气经过二次补燃空气流量电动调节阀7,经过二次补燃空气流量计6,经过第一补燃空气管道4让补燃空气与炉内烟气剩余燃气混合完全燃烧。燃尽后的高温烟气经空气和燃气蓄热室蓄热后,经排烟管道排出。When the second
如此一个周期结束,下一个周期开始;周而复始,排烟温度在120~180℃之间周期性变化,实现了蓄热、放热的过程。工作前先由设置的烘炉烧嘴将炉温升到800℃,才能启动蓄热烧嘴投入燃烧,通过电脑适时控制各换向阀;二次补燃空气快切阀实现定时换向,定温换向;实现烟气热能最佳回收,通过电脑精确计算控制空气流量电动调节阀;燃气流量电动调节阀实现最佳空燃比。Such a cycle ends, and the next cycle begins; the cycle repeats, and the exhaust gas temperature changes periodically between 120 and 180°C, realizing the process of heat storage and heat release. Before work, the furnace temperature is raised to 800°C by the set oven burner before the regenerative burner can be started for combustion, and the reversing valves are controlled in a timely manner through the computer; the secondary combustion air quick-cut valve realizes timing reversing and constant temperature Reversing; realize the best recovery of flue gas heat energy, and control the air flow electric regulating valve through precise calculation by computer; the gas flow electric regulating valve realizes the best air-fuel ratio.
以上所述仅是本实用新型的优选实施方式,应当指出,对于本技术领域的普通技术人员来说,在不脱离本实用新型原理的前提下,还可以作出若干改进和润饰,这些改进和润饰也应视为本实用新型的保护范围。The above is only a preferred embodiment of the utility model, it should be pointed out that for those of ordinary skill in the art, without departing from the principle of the utility model, some improvements and modifications can also be made. These improvements and modifications It should also be regarded as the protection scope of the present utility model.
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| CN103014310A (en) * | 2012-12-03 | 2013-04-03 | 攀钢集团西昌钢钒有限公司 | Timing constant-temperature reversing device of regenerative furnace and method thereof |
| CN103014312A (en) * | 2012-12-26 | 2013-04-03 | 中冶南方(武汉)威仕工业炉有限公司 | Control method of regenerative burner of regenerative heating furnace |
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| CN103436684B (en) * | 2013-08-03 | 2016-04-20 | 石家庄新华能源环保科技股份有限公司 | A kind of heat accumulating type billet heating furnace |
| CN103436684A (en) * | 2013-08-03 | 2013-12-11 | 石家庄新华能源环保科技股份有限公司 | Heat-accumulating billet heating furnace |
| CN104006406A (en) * | 2014-05-21 | 2014-08-27 | 江苏华德工业炉有限公司 | Regenerative heating furnace |
| CN105018717A (en) * | 2015-06-26 | 2015-11-04 | 江苏宏宇模具集团有限公司 | Kiln used for producing hot roll steel |
| CN105063531A (en) * | 2015-08-08 | 2015-11-18 | 桐乡市桐德电力配件有限公司 | Galvanizing furnace |
| CN105087899A (en) * | 2015-08-26 | 2015-11-25 | 江苏省沙钢钢铁研究院有限公司 | Heat accumulating type heating furnace and flue gas circulating combustion method thereof |
| CN105087899B (en) * | 2015-08-26 | 2017-06-23 | 江苏省沙钢钢铁研究院有限公司 | Heat accumulating type heating furnace and flue gas circulating combustion method thereof |
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Assignee: ChangShu Burner Factory Co., Ltd. Assignor: Beijing Jingjie Ruisi Technology Development Co, Ltd. Contract record no.: 2011990001075 Denomination of utility model: Heat-storage type non-oxidizing heating furnace and combustion method thereof Granted publication date: 20100804 License type: Common License Record date: 20111206 |
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