CN207515508U - An energy-saving kiln capable of continuously firing blue bricks and blue tiles - Google Patents
An energy-saving kiln capable of continuously firing blue bricks and blue tiles Download PDFInfo
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- CN207515508U CN207515508U CN201721291696.3U CN201721291696U CN207515508U CN 207515508 U CN207515508 U CN 207515508U CN 201721291696 U CN201721291696 U CN 201721291696U CN 207515508 U CN207515508 U CN 207515508U
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- 238000010304 firing Methods 0.000 title claims abstract description 107
- 239000011449 brick Substances 0.000 title claims abstract description 14
- 230000009467 reduction Effects 0.000 claims abstract description 55
- 230000000391 smoking effect Effects 0.000 claims abstract description 33
- 238000001816 cooling Methods 0.000 claims abstract description 32
- 239000007789 gas Substances 0.000 claims abstract description 25
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 31
- 238000007789 sealing Methods 0.000 claims description 4
- 230000002829 reductive effect Effects 0.000 claims description 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract description 12
- 239000003546 flue gas Substances 0.000 abstract description 12
- 238000005265 energy consumption Methods 0.000 abstract description 6
- 239000000779 smoke Substances 0.000 abstract description 6
- 238000002485 combustion reaction Methods 0.000 abstract description 5
- 238000003912 environmental pollution Methods 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 6
- 230000008569 process Effects 0.000 description 5
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 3
- 239000004566 building material Substances 0.000 description 3
- 238000010924 continuous production Methods 0.000 description 3
- 230000006872 improvement Effects 0.000 description 3
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
Classifications
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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
-
- 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
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/60—Production of ceramic materials or ceramic elements, e.g. substitution of clay or shale by alternative raw materials, e.g. ashes
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Abstract
一种可连续烧制青砖青瓦的节能窑炉,窑炉由预热段,烧成段,还原水冷段构成。各段之间由活动门隔断,预热段前端及还原水冷段后端由封闭门封闭,所述烧成段包括烧成烧嘴,烧成进气支管与烧成进气管,烧成段的设有吸烟口,所述预热段包括预热段支烟管及预热段主烟道,预热段的炉室设有喷火口,烧成段主烟道与预热段喷火口连接;还原烧嘴通过阀门及还原进气支管与还原进气管连接,多余还原气体通过集气斗及集气管道进入烧成段充分燃烧。本实用新型烧成段和预热段内的高温烟气与制品充分热交换后排出窑体,从而保证烟气所带走的热量处于最低水平。另外,水冷还原段的多余还原气体经集气斗收集并从集气管道进入烧成段燃烧,降低能耗,避免污染环境。
An energy-saving kiln capable of continuously firing green bricks and green tiles, the kiln is composed of a preheating section, a firing section, and a reduction water-cooling section. Each section is separated by a movable door, and the front end of the preheating section and the rear end of the reduction water-cooling section are closed by a closed door. The firing section includes a firing burner, a firing air intake branch pipe and a firing air intake pipe, and the firing section is provided with a smoking port. The preheating section includes a preheating section smoke pipe and a preheating section main flue, and the furnace chamber of the preheating section is provided with a flame outlet, and the firing section main flue is connected to the preheating section flame outlet; the reduction burner is connected to the reduction air intake pipe through a valve and a reduction air intake branch pipe, and the excess reduction gas enters the firing section through a gas collecting hopper and a gas collecting pipeline for full combustion. The high-temperature flue gas in the firing section and the preheating section of the utility model is fully heat-exchanged with the product and then discharged from the kiln body, thereby ensuring that the heat carried away by the flue gas is at the lowest level. In addition, the excess reduction gas in the water-cooled reduction section is collected by the gas collecting hopper and enters the firing section from the gas collecting pipeline for combustion, thereby reducing energy consumption and avoiding environmental pollution.
Description
技术领域technical field
本实用新型涉及一种工业窑炉,尤其涉及一种可连续烧制青砖青瓦的节能窑炉。The utility model relates to an industrial kiln, in particular to an energy-saving kiln capable of continuously firing green bricks and blue tiles.
背景技术Background technique
随着生活水平的提高,市场对仿古建筑的建材的需求越来越大而青砖青瓦是仿古建材中广泛使用的一种建筑材料。普通黏土砖因氧化烧成,烧成后铁以三氧化二铁的形式存在呈红色,但如在烧成过程中对三氧化二铁进行还原,铁元素不完全氧化成亚铁则呈青灰色,但在烧成过程的还原及在500-1000℃中的无氧降温要求特别苛刻,控制不好色差大、能耗高、成品率低。With the improvement of living standards, the market's demand for building materials for antique buildings is increasing, and blue bricks and blue tiles are a kind of building materials widely used in antique building materials. Ordinary clay bricks are fired due to oxidation, and the iron in the form of ferrous oxide is red after firing, but if the ferrous oxide is reduced during the firing process, the iron element is not completely oxidized to ferrous iron, and it will be blue-gray , but the reduction in the firing process and the anaerobic cooling at 500-1000 °C are particularly demanding, and the control is not good, the color difference is large, the energy consumption is high, and the yield is low.
目前因环保要求大多青砖青瓦厂家采用以天然气为燃料的梭式窑、分体式的隧道窑、辊道窑生产。梭式窑因生产过程中排出的烟气温度高能量利用低所以能耗大,多余还原气体排出污染环境,装一窑出一窑的生产方式只能用于间歇化生产所以产量低。分体式隧道窑虽可连续化生产,但在转运还原窑过程中制品温度降低,造成制品开裂及到达还原窑后需重新加热后再进行还原,其过程复杂所需人工较多,其能耗亦是不低,成品率也无法保证。辊道窑虽可连续化生产、能耗低,但由于受辊棒的运行速度、承重能力、空间大小限制对大件制品生产无能为力且投资大,中小厂家无力选择,亟需对现有的窑炉进行改进。At present, due to environmental protection requirements, most blue brick and blue tile manufacturers use natural gas as fuel for shuttle kiln, split tunnel kiln, and roller kiln for production. Due to the high temperature of the flue gas discharged during the production process and the low energy utilization, the shuttle kiln consumes a lot of energy, and the excess reducing gas is discharged to pollute the environment. The production method of installing one kiln and one kiln can only be used for intermittent production, so the output is low. Although the split-type tunnel kiln can be used for continuous production, the temperature of the product decreases during the transfer to the reduction kiln, which causes the product to crack and needs to be reheated before reduction after reaching the reduction kiln. The process is complicated and requires more labor and energy consumption. It is not low, and the yield rate cannot be guaranteed. Although the roller kiln can be used for continuous production and low energy consumption, due to the limitations of the running speed, load-bearing capacity and space size of the rollers, it is powerless to produce large products and requires a large investment. Small and medium-sized manufacturers are unable to choose. Furnace improvements.
实用新型内容Utility model content
基于此,有必要针对现有技术中的不足,提供一种可连续烧制青砖青瓦的节能窑炉。Based on this, it is necessary to address the deficiencies in the prior art and provide an energy-saving kiln capable of continuously firing green bricks and green tiles.
本实用新型的技术方案为:The technical scheme of the utility model is:
一种可连续烧制青砖青瓦的节能窑炉,窑炉包括预热段,烧成段,还原水冷段。整体窑炉内铺设路轨,所述烧成段包括炉室、烧成烧嘴,烧成进气支管与烧成进气管,所述烧成烧嘴分成两排设在炉室的侧壁上,烧成烧嘴通过烧成进气支管与烧成进气管连接;烧成段的炉室于窑车台面下方位置设有吸烟口,所述预热段包括炉室、预热段支烟管及预热段主烟道,预热段的炉室设有喷火口,烧成段的吸烟口通过烧成段支烟道与烧成段主烟道连接,烧成段主烟道与预热段喷火口连接;;还原水冷段包括还原烧嘴、阀门、还原进气支管、还原进气管、集气斗、滴水管及滴水阀门,还原烧嘴对称分布在近窑车台面外部两侧,还原烧嘴通过阀门及还原进气支管与还原进气管连接,多余还原气体通过集气斗及集气管道进入烧成段充分燃烧,在还原水冷段窑顶外部设两排均匀分布的滴水管,滴水管通过滴水阀门与进水管连接。An energy-saving kiln capable of continuously firing green bricks and blue tiles. The kiln includes a preheating section, a firing section, and a reducing water cooling section. Rails are laid in the overall kiln. The firing section includes a furnace chamber, a firing burner, a firing intake branch pipe and a firing intake pipe. The firing burners are divided into two rows and arranged on the side wall of the furnace chamber. The firing burner is connected to the firing intake pipe through the firing intake branch pipe; the furnace chamber of the firing section is provided with a smoking port below the kiln car table, and the preheating section includes the furnace chamber, the branch pipe of the preheating section and the The main flue of the preheating section, the furnace chamber of the preheating section is equipped with a flame vent, the smoking port of the firing section is connected to the main flue of the firing section through the branch flue of the firing section, and the main flue of the firing section is connected to the main flue of the preheating section The flame outlet connection; the reduction water cooling section includes reduction burners, valves, reduction intake branch pipes, reduction intake pipes, gas collecting buckets, drip pipes and drip valves. The reduction burners are symmetrically distributed on both sides near the kiln car table. The nozzle is connected to the reduction inlet pipe through the valve and the reduction air intake branch pipe. The excess reduction gas enters the firing section through the gas collecting bucket and the gas collecting pipe and is fully burned. There are two rows of evenly distributed drip pipes outside the kiln roof of the reduction water cooling section. Connect to the water inlet pipe through the drip valve.
优选地,所述预热段的炉室靠近窑车台面的位置设有预热段吸烟口,所述预热段还包括预热段支烟道、预热段主烟道、抽烟风管及抽烟风机,预热段吸烟口通过支烟道与预热段主烟道连接,预热段主烟道通过抽烟风管与抽烟风机连接。Preferably, the furnace chamber of the preheating section is provided with a preheating section smoking port near the kiln car table, and the preheating section also includes a preheating section branch flue, a preheating section main flue, a smoke air duct and The smoking fan, the smoking port of the preheating section is connected with the main flue of the preheating section through the branch flue, and the main flue of the preheating section is connected with the smoking fan through the smoking duct.
优选地,烧成段支烟道、烧成段主烟道设于所述烧成段侧壁的窑墙内,窑炉内还设有窑车烟气通道,所述烧成段的吸烟口与烧成段支烟道、窑车烟气通道连接;所述预热段吸烟口、预热段支烟道及预热段主烟道设于所述预热段的侧壁窑墙内,所述预热段吸烟口与预热段支烟道及窑车烟气通道连接。Preferably, the firing section branch flue and the firing section main flue are arranged in the kiln wall of the side wall of the firing section, and a kiln car flue gas channel is also provided in the kiln, and the smoking port of the firing section It is connected with the branch flue of the firing section and the flue gas channel of the kiln car; the smoking port of the preheating section, the branch flue of the preheating section and the main flue of the preheating section are arranged in the side wall of the kiln wall of the preheating section, The smoking port of the preheating section is connected with the branch flue of the preheating section and the flue gas passage of the kiln car.
优选地,还包括第一封闭门、第二封闭门、第三封闭门、第四封闭门及驱动模组,所述第一封闭门设于预热段的入口端,所述第二封闭门设于预热段与烧成段之间,所述第三封闭门设于烧成段与还原水冷段之间,所述第四封闭门设于还原水冷段的出口端,所述驱动模组带动第一封闭门、第二封闭门、第三封闭门、第四封闭门上下运动,调整预热段、烧成段及还原水冷段的密封状态。Preferably, it also includes a first closed door, a second closed door, a third closed door, a fourth closed door and a driving module, the first closed door is arranged at the inlet end of the preheating section, and the second closed door Set between the preheating section and the firing section, the third closed door is set between the firing section and the reducing water cooling section, the fourth closing door is set at the outlet end of the reducing water cooling section, the driving module Drive the first closed door, the second closed door, the third closed door, and the fourth closed door to move up and down, and adjust the sealing state of the preheating section, firing section and restoring water cooling section.
本实用新型的有益特点在于:烧成段采用高温喷射烧嘴,充分搅动窑内气流且烧成段吸烟口位于窑车台面下部利用垂直气流法则造成烧成段温度均匀,上下温差小于5℃,后高温烟气经支烟口汇入烧成段主烟道进入预热段的喷火口喷出,对预热段的制品充分进行热交换再由预热段分布于窑车台面下部的吸烟口汇入预热段主烟道经抽烟风机排入其他设备。从而保证烟气所带走的热量处于最低水平,能耗也进一步降低。在此过程中预热段前端、还原水冷段后端的封闭窑门处于封闭状态,各段之间的活动门也处于封闭状态,保证还原水冷段的绝对密封,保证了还原水冷段的还原及无氧水冷的顺利进行。多余还原气体经集气斗收集经集气管道进入烧成段燃烧,降低能耗避免污染环境。The beneficial feature of the utility model is that the firing section adopts high-temperature jet burners to fully stir the airflow in the kiln, and the smoking port of the firing section is located at the lower part of the kiln car table, and the temperature of the firing section is uniform by using the vertical air flow law, and the temperature difference between the upper and lower sides is less than 5°C. Afterwards, the high-temperature flue gas enters the main flue of the firing section through the branch smoke port and enters the flame nozzle of the preheating section to be sprayed out. The products in the preheating section are fully exchanged for heat and then distributed to the smoking port at the lower part of the kiln car table from the preheating section. It flows into the main flue of the preheating section and is discharged into other equipment through the exhaust fan. This ensures that the heat taken away by the flue gas is at the lowest level, and the energy consumption is further reduced. During this process, the closed kiln doors at the front end of the preheating section and the back end of the reduction water cooling section are in a closed state, and the movable doors between each section are also in a closed state to ensure the absolute sealing of the reduction water cooling section, and ensure the reduction and safety of the reduction water cooling section. Oxygen water cooling is carried out smoothly. The excess reducing gas is collected by the gas collecting hopper and enters the burning section through the gas collecting pipe for combustion, reducing energy consumption and avoiding environmental pollution.
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为图1所示窑炉的俯视图。Fig. 2 is a top view of the kiln shown in Fig. 1 .
图3为图2所示窑炉沿A-A线的剖示图。Fig. 3 is a sectional view of the kiln shown in Fig. 2 along line A-A.
附图标记:Reference signs:
1、预热段;2、烧成段;3、还原水冷段;4、预热段前端封闭门;5、还原水冷段后端封闭门;6、预热段与烧成段活动门;7、烧成段与还原水冷段活动门;8、路轨;9、烧成进气管;10、还原进气管;11、烧成进气支管;12、阀门;13、烧成烧嘴;14、还原进气支管;15、还原烧嘴;16、抽烟风机;17、抽烟风管;18、进水管;19、滴水管;20、滴水阀门;21、集气斗;22、集气管道;23、预热段喷火口;24、预热段吸烟口;25、预热段主烟道;26、烧成段吸烟口;27、烧成段支烟道;28、烧成段主烟口。1. Preheating section; 2. Firing section; 3. Reduction water cooling section; 4. Front closed door of preheating section; 5. Reducing water cooling section rear closed door; 6. Preheating section and firing section movable door; 7. , the movable door of the firing section and the reduction water-cooling section; 8, the rail; 9, the firing intake pipe; 10, the reduction intake pipe; 11, the firing intake branch pipe; 12, the valve; 13, the firing burner; 14, the reduction Intake branch pipe; 15. Reduction burner; 16. Smoke fan; 17. Smoke duct; 18. Water inlet pipe; 19. Drip pipe; 20. Drip valve; 24. The smoking port of the preheating section; 25. The main flue of the preheating section; 26. The smoking port of the firing section; 27. The branch flue of the firing section; 28. The main smoke port of the firing section.
具体实施方式Detailed ways
为了使实用新型的目的、技术方案及优点更加清楚明白,以下结合附图及实施例,对实用新型进行进一步详细说明。应当理解,此处所描述的具体实施例仅用以解释实用新型,并不用于限定实用新型。In order to make the purpose, technical solutions and advantages of the utility model clearer, the utility model will be further described in detail below in conjunction with the accompanying drawings and embodiments. It should be understood that the specific embodiments described here are only used to explain the utility model, not to limit the utility model.
如图1、图2及图3所示,本实用新型提供一种可连续烧制青砖青瓦的节能窑炉,窑炉由预热段1,烧成段2,还原水冷段3构成。整体窑炉内铺设路轨8,,所述烧成段2包括炉室、烧成烧嘴13、烧成进气支管11、烧成进气管9、烧成段支烟道27及烧成段主烟道28,所述烧成烧嘴13分成上下两排设在炉室的侧壁上,烧成烧嘴13通过烧成进气支管11与烧成进气管9连接;烧成段2的炉室于窑车台面下方位置设有吸烟口26,所述预热段1包括炉室,预热段1的炉室设有喷火口23,烧成段2的吸烟口26通过烧成段支烟道27与烧成段主烟道28连接,烧成段主烟道28与预热段喷火口23连接;预热段1的炉室靠近窑车台面的位置设有预热段吸烟口24,所述预热段1还包括预热段支烟道、预热段主烟道25、抽烟风管17及抽烟风机16,预热段1的吸烟口通过支烟道与预热段主烟道25连接,预热段主烟道25通过抽烟风管17与抽烟风机16连接;还原水冷段3包括还原烧嘴15、阀门12、还原进气支管14、还原进气管10、集气斗21、滴水管19及滴水阀门20,还原烧嘴15对称分布在近窑车台面外部两侧,还原烧嘴15通过阀门12及还原进气支管14与还原进气管10连接,多余还原气体通过集气斗21及集气管道22进入烧成段2充分燃烧,在还原水冷段3窑顶外部设两排均匀分布的滴水管19,滴水管19通过滴水阀门20与进水管18连接。As shown in Fig. 1, Fig. 2 and Fig. 3, the utility model provides an energy-saving kiln capable of continuously firing green bricks and blue tiles. Rails 8 are laid in the overall kiln, and the firing section 2 includes a furnace chamber, a firing burner 13, a firing intake branch pipe 11, a firing intake pipe 9, a firing section branch flue 27 and a firing section main pipe. Flue 28, the burning burners 13 are divided into upper and lower two rows and arranged on the side wall of the furnace chamber, the burning burners 13 are connected with the burning air intake pipe 9 through the burning air intake branch pipe 11; the furnace of the firing section 2 The chamber is provided with a smoking port 26 below the kiln car table. The preheating section 1 includes a furnace chamber, and the furnace chamber of the preheating section 1 is provided with a flame nozzle 23. Road 27 is connected to the main flue 28 of the firing section, and the main flue 28 of the firing section is connected to the flame nozzle 23 of the preheating section; the furnace chamber of the preheating section 1 is provided with a smoking port 24 of the preheating section near the kiln car table. The preheating section 1 also includes a preheating section branch flue, a preheating section main flue 25, a smoking air duct 17 and a smoking fan 16, and the smoking port of the preheating section 1 passes through the branch flue and the preheating section main flue. 25 connection, the main flue 25 of the preheating section is connected with the exhaust fan 16 through the exhaust air pipe 17; Drip pipe 19 and drip valve 20, reduction burners 15 are symmetrically distributed on both sides near the kiln car platform, reduction burners 15 are connected to reduction intake pipe 10 through valve 12 and reduction intake branch pipe 14, excess reduction gas passes through the gas collecting hopper 21 and the gas-collecting pipeline 22 enter the firing section 2 for full combustion, and two rows of evenly distributed drip pipes 19 are arranged outside the kiln roof of the reduction water cooling section 3, and the drip pipes 19 are connected with the water inlet pipe 18 through the drip valve 20.
所述烧成段支烟道27、烧成段主烟道28设于所述烧成段2侧壁的窑墙内,窑炉内还设有窑车烟气通道,所述烧成段2的吸烟口26与烧成段支烟道27、窑车烟气通道连接;所述预热段支烟道及预热段主烟道25设于所述预热段1的侧壁窑墙内,所述预热段吸烟口24与预热段支烟道24及窑车烟气通道连接。The firing section branch flue 27 and the firing section main flue 28 are arranged in the kiln wall of the side wall of the firing section 2, and the kiln car flue gas channel is also provided in the kiln, and the firing section 2 The smoking port 26 of the firing section is connected with the branch flue 27 of the firing section and the kiln car flue gas passage; the branch flue of the preheating section and the main flue 25 of the preheating section are arranged in the side wall kiln wall of the preheating section 1 , the smoking port 24 of the preheating section is connected with the branch flue 24 of the preheating section and the flue gas channel of the kiln car.
本实用新型还包括第一封闭门4、第二封闭门6、第三封闭门7、第四封闭门5及驱动模组(图未示),所述第一封闭门4设于预热段1的入口端,所述第二封闭门6设于预热段1与烧成段2之间,所述第三封闭门7设于烧成段2与还原水冷段3之间,所述第四封闭门5设于还原水冷段3的出口端,所述驱动模组带动第一封闭门4、第二封闭门6、第三封闭门7、第四封闭门5上下运动,调整预热段1、烧成段2及还原水冷段3的密封状态。The utility model also includes a first closed door 4, a second closed door 6, a third closed door 7, a fourth closed door 5 and a drive module (not shown), the first closed door 4 is located in the preheating section 1, the second closed door 6 is set between the preheating section 1 and the firing section 2, the third closed door 7 is set between the firing section 2 and the reducing water cooling section 3, and the first The four closed doors 5 are located at the outlet of the reduction water-cooling section 3, and the driving module drives the first closed door 4, the second closed door 6, the third closed door 7, and the fourth closed door 5 to move up and down to adjust the preheating section 1. The sealing state of firing section 2 and reduction water cooling section 3.
工作原理:进车前将封闭窑门4、5及活动窑门6、7打开,通过专用设备将窑车推入预热段1,窑车上的制品依次推入到预热段1、烧成段2及还原水冷段3进行加工。加工时,关闭封闭窑门4、5,活动窑门6、7,进而使得制器在预热段1、烧成段2及还原水冷段3加工时互不影响,整个窑炉可连续加工。烧成段2通过烧成烧嘴13将烧成段内温度升高,烧成段2内产生的高温烟气通过烧成段2吸烟口26进入主烟道28,后由预热段1喷火口23进入预热段1对制品进行预热。还原水冷段3的还原烧嘴15对进入还原水冷段3的制品进行还原,多余还原气体通过集气斗21、集气管道22进入烧成段2充分燃烧。还原水冷段3还原完成后关闭阀门12控制还原烧嘴15的关闭。打开滴水阀门20通过滴水管19对制品进行水冷,通过滴水阀门20控制滴水管19的滴水量达到控制降温速率,至400℃时还原水冷结束,最终得到合格的青砖青瓦成品。此过程周而复始连续生产。Working principle: before entering the car, open the closed kiln doors 4, 5 and movable kiln doors 6, 7, push the kiln car into the preheating section 1 through special equipment, and push the products on the kiln car into the preheating section 1 in turn, Segment 2 and reduction water cooling section 3 are processed. During processing, the kiln doors 4 and 5 are closed and the kiln doors 6 and 7 are movable, so that the preheating section 1, the firing section 2 and the reducing water cooling section 3 are processed independently of each other, and the entire kiln can be processed continuously. The firing section 2 raises the temperature in the firing section through the firing burner 13, and the high-temperature flue gas generated in the firing section 2 enters the main flue 28 through the smoking port 26 of the firing section 2, and is sprayed by the preheating section 1. The burner 23 enters the preheating section 1 to preheat the product. The reduction burner 15 in the reduction water cooling section 3 reduces the products entering the reduction water cooling section 3, and the excess reducing gas enters the firing section 2 through the gas collecting bucket 21 and the gas collecting pipe 22 for complete combustion. After the reduction water cooling section 3 completes the reduction, the valve 12 is closed to control the closing of the reduction burner 15 . Open the drip valve 20 to water-cool the product through the drip tube 19, control the dripping amount of the drip tube 19 through the drip valve 20 to control the cooling rate, and the reduction water cooling ends at 400°C, and finally obtain qualified blue bricks and blue tiles. This process goes round and round for continuous production.
以上所述实施例仅表达了实用新型的几种实施方式,其描述较为具体和详细,但并不能因此而理解为对实用新型专利范围的限制。应当指出的是,对于本领域的普通技术人员来说,在不脱离实用新型构思的前提下,还可以做出若干变形和改进,这些都属于实用新型的保护范围。因此,实用新型专利的保护范围应以所附权利要求为准。The above-mentioned embodiments only express several implementation modes of the utility model, and the description thereof is relatively specific and detailed, but it should not be understood as limiting the scope of the utility model patent. It should be pointed out that those skilled in the art can make several modifications and improvements without departing from the concept of the utility model, and these all belong to the protection scope of the utility model. Therefore, the scope of protection of a utility model patent should be determined by the appended claims.
Claims (4)
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