CN202770125U - Architectural ceramic monolayer rapid drying dryer - Google Patents
Architectural ceramic monolayer rapid drying dryer Download PDFInfo
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- CN202770125U CN202770125U CN201220323677.5U CN201220323677U CN202770125U CN 202770125 U CN202770125 U CN 202770125U CN 201220323677 U CN201220323677 U CN 201220323677U CN 202770125 U CN202770125 U CN 202770125U
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- 239000002356 single layer Substances 0.000 title claims abstract description 23
- 238000001035 drying Methods 0.000 title claims abstract description 19
- 239000000919 ceramic Substances 0.000 title claims abstract description 17
- 238000002485 combustion reaction Methods 0.000 claims abstract description 33
- 238000010438 heat treatment Methods 0.000 claims description 32
- 238000007791 dehumidification Methods 0.000 claims description 23
- 239000007921 spray Substances 0.000 claims description 10
- 239000000203 mixture Substances 0.000 claims description 4
- 230000005484 gravity Effects 0.000 claims description 3
- 239000011449 brick Substances 0.000 abstract description 5
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 238000004904 shortening Methods 0.000 abstract description 3
- 230000000712 assembly Effects 0.000 abstract 4
- 238000000429 assembly Methods 0.000 abstract 4
- 239000007789 gas Substances 0.000 description 14
- 229910001220 stainless steel Inorganic materials 0.000 description 8
- 239000010935 stainless steel Substances 0.000 description 8
- 238000000034 method Methods 0.000 description 4
- 238000005265 energy consumption Methods 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 239000010410 layer Substances 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 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
- 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
Description
技术领域 technical field
本实用新型涉及建筑陶瓷干燥器设备的技术领域,尤其是指一种建筑陶瓷单层快速干燥器设备。 The utility model relates to the technical field of architectural ceramic dryer equipment, in particular to a single-layer rapid dryer equipment for architectural ceramics.
背景技术 Background technique
目前,国内外采用湿法成型的建筑陶瓷产品(如陶土板、琉璃瓦、劈开砖等)有一个显著的特点,那就是坯体含水率很高,一般含水率在16%左右,而烧成工艺要求坯体进入辊道窑烧成的含水率≤1%,因此,坯体水分的合理干燥非常重要。采用湿法成型后的产品首先进入多层快速干燥器进行一次快速干燥,之后经过输送线进入窑前单层干燥器再进行二次干燥,如果采用传统普通的干燥器对其干燥水分,干燥周期一般须达到20小时,原因因为普通干燥器的温度来自于窑炉余热,温度只能达到180℃左右。因此对于湿法成型的产品如果采用普通窑前单层干燥器干燥坯体,将会严重影响产量的提升,难以满足生产的需要。 At present, architectural ceramic products (such as clay panels, glazed tiles, split bricks, etc.) that are formed by wet methods at home and abroad have a remarkable feature, that is, the moisture content of the green body is very high, generally around 16%. The process requires that the moisture content of the green body when it enters the roller kiln for firing is ≤1%, therefore, the reasonable drying of the green body moisture is very important. The products formed by wet method first enter the multi-layer rapid dryer for a quick drying, and then enter the single-layer dryer in front of the kiln through the conveying line for secondary drying. If the traditional ordinary dryer is used to dry the water, the drying cycle will be shorter. Generally, it must reach 20 hours. The reason is that the temperature of the ordinary dryer comes from the waste heat of the kiln, and the temperature can only reach about 180°C. Therefore, if a common kiln front single-layer dryer is used to dry the green body for wet-formed products, it will seriously affect the increase in output, and it is difficult to meet the needs of production.
发明内容 Contents of the invention
本实用新型的目的在于克服现有技术的不足,提供了一种结构合理,降低能耗,具有节能减排、降低管理成本和运作成本的建筑陶瓷单层快速干燥器设备。 The purpose of the utility model is to overcome the deficiencies of the prior art, and provide a single-layer rapid dryer equipment for building ceramics with reasonable structure, reduced energy consumption, energy saving, emission reduction, management cost and operation cost.
为实现上述目的,本实用新型所提供的技术方案为:一种建筑陶瓷单层快速干燥器设备,包括有单层辊道干燥器,所述的单层辊道干燥器主要由供热和抽湿两大系统组成,其中,所述的供热系统包括有助燃系统、燃烧系统和置于辊道窑内的供热组件,所述的助燃系统对应设在辊道窑的顶部,并且通过其管路与置于辊道窑两侧的燃烧系统相接,用于将外部的空气引入该燃烧系统内,并与该燃烧系统内的燃气混合燃烧,同时,所述的供热组件对应置于辊道窑的辊道上方和下方,并且通过其管路与上述的燃烧系统相接,用于将该燃烧系统内加热后的气体送至辊道窑内干燥坯体;所述的抽湿系统包括有抽湿风管和抽湿风机,所述的抽湿风管对应设在辊道窑的上、下两方,并且与辊道窑内部相通,同时,该抽湿风管与置于辊道窑顶部的抽湿风机相接,通过该抽湿风机的引力将辊道窑内干燥坯体后产生的湿气排到辊道窑外。 In order to achieve the above purpose, the technical solution provided by the utility model is: a single-layer rapid dryer equipment for building ceramics, including a single-layer roller dryer, the single-layer roller dryer is mainly composed of heat supply and exhaust The heating system consists of two systems, wherein the heating system includes a combustion-supporting system, a combustion system and a heating component placed in the roller kiln. The combustion-supporting system is correspondingly arranged on the top of the roller kiln, and through The pipeline is connected to the combustion system placed on both sides of the roller kiln, and is used to introduce the external air into the combustion system and mix it with the gas in the combustion system for combustion. At the same time, the heating components are correspondingly placed Above and below the roller table of the roller kiln, and connected with the above-mentioned combustion system through its pipeline, it is used to send the heated gas in the combustion system to the roller kiln to dry the green body; the dehumidification system It includes a dehumidifying air pipe and a dehumidifying fan. The dehumidifying air pipe is correspondingly arranged on the upper and lower sides of the roller kiln, and communicates with the interior of the roller kiln. At the same time, the dehumidifying air pipe is connected to the The dehumidifying fan on the top of the kiln is connected, and the moisture generated after drying the green body in the roller kiln is discharged to the outside of the roller kiln through the gravity of the dehumidifying fan.
所述的助燃系统包括有助燃风机及与该助燃风机相接的助燃风管,其中,所述的助燃风管与燃烧系统的燃气主管相通。 The combustion-supporting system includes a combustion-supporting fan and a combustion-supporting air duct connected with the combustion-supporting fan, wherein the combustion-supporting air duct communicates with the gas main pipe of the combustion system.
所述的燃烧系统包括有燃气主管及与该燃气主管相接的喷枪,其中,所述的喷枪对应设在供热组件的加热管内。 The combustion system includes a gas main pipe and a spray gun connected to the gas main pipe, wherein the spray gun is correspondingly arranged in the heating pipe of the heating component.
所述的供热组件包括有依次相接的加热管、方风管、供热管,其中,所述供热管的上端或下端均布有多个气流孔。 The heat supply assembly includes a heating pipe, a square air pipe, and a heat supply pipe connected in sequence, wherein a plurality of air holes are evenly distributed on the upper end or the lower end of the heat supply pipe.
所述的抽湿风管包括有抽湿主管、排湿顶抽、排湿底抽,其中,所述的排湿顶抽和排湿底抽按辊道窑的输送方向对应设在辊道窑头部和尾部的上、下方,并且分别与置于辊道窑顶部的抽湿主管相通,同时,该抽湿主管与抽湿风机相接。 The dehumidification air duct includes a dehumidification main pipe, a top pump for dehumidification, and a bottom pump for dehumidification, wherein the top and bottom pumps for dehumidification are arranged in the roller kiln correspondingly The upper and lower parts of the head and tail are respectively connected with the dehumidification main pipe placed on the top of the roller kiln, and at the same time, the dehumidification main pipe is connected with the dehumidification fan.
本实用新型在采用了上述方案后,成功解决了水分高产品不易干燥、易裂砖等问题,具有缩短干燥周期,提高生产效率的优势;具有结构合理,自动化程度高,干燥窑内部热循环高,单位热量消耗低,设备占有土地少,节省土地投资和降低设备运作成本等优点。 After adopting the above-mentioned scheme, the utility model successfully solves the problems such as high-moisture products are not easy to dry and easy to crack bricks, and has the advantages of shortening the drying cycle and improving production efficiency; it has reasonable structure, high degree of automation, and high thermal cycle inside the drying kiln. , low heat consumption per unit, less land occupied by equipment, saving land investment and reducing equipment operating costs, etc.
附图说明 Description of drawings
图1为本实用新型的主视图。 Fig. 1 is the front view of the utility model.
图2为本实用新型的俯视图。 Fig. 2 is a top view of the utility model.
图3为本实用新型的截面示意图。 Fig. 3 is a schematic cross-sectional view of the utility model.
图4为本实用新型的燃烧系统截面示意图。 Fig. 4 is a schematic cross-sectional view of the combustion system of the present invention.
图5为本实用新型的供热组件截面示意图。 Fig. 5 is a schematic cross-sectional view of the heating assembly of the present invention.
图6为本实用新型的抽湿风管的示意图。 Fig. 6 is a schematic diagram of the dehumidifying air duct of the present invention.
具体实施方式 Detailed ways
下面结合具体实施例对本实用新型作进一步说明。 Below in conjunction with specific embodiment the utility model is further described.
参见附图1至附图6所示,本实施例所述的建筑陶瓷单层快速干燥器设备,包括有主要由供热和抽湿两大系统组成的单层辊道干燥器1,其中,本实施例所述的供热系统包括有助燃系统、燃烧系统和置于辊道窑内的供热组件14,所述的助燃系统对应设在辊道窑的顶部,并且通过其管路与置于辊道窑两侧的燃烧系统相接,用于将外部的空气引入该燃烧系统内,并与该燃烧系统内的燃气混合燃烧,同时,所述的供热组件14对应置于辊道窑的辊道上方和下方,并且通过其管路与上述的燃烧系统相接,用于将该燃烧系统内加热后的气体送至辊道窑内干燥坯体。本实施例所述的抽湿系统包括有抽湿风管2和一台置于辊道窑顶部的抽湿风机3,其中,所述的抽湿风管2包括有抽湿主管11、排湿顶抽12、排湿底抽13,所述的排湿顶抽12和排湿底抽13按辊道窑的输送方向对应设在辊道窑头部和尾部的上、下方,并且分别与置于辊道窑顶部的抽湿主管11相通,同时,该抽湿主管11与抽湿风机3相接,通过该抽湿风机3的引力将辊道窑内干燥坯体后产生的湿气排到辊道窑外,时刻保持辊道窑内所需的干燥湿度,从而最终达到辊道窑内温度、气氛和压力制度保持循环稳定,并保证热源充分利用;此外,为了减少抽湿风机3进出口阻力,本实用新型设计抽湿风机3的角度为135°,同时,合理设计进出风管路,起到降低抽湿风机3的使用功率,达到降低抽湿风机3能耗的作用。另外,本实施例上述的助燃系统包括有助燃风机4及与该助燃风机4相接的助燃风管5,其中,所述的助燃风管5与燃烧系统的燃气主管6相通。本实施例上述的燃烧系统包括有燃气主管6及与该燃气主管6相接的喷枪7,其中,所述的喷枪7对应设在供热组件的不锈钢加热管8内。本实施例上述的供热组件14包括有依次相接的不锈钢加热管8、不锈钢方风管9、不锈钢供热管10,其中,所述不锈钢供热管10的上端或下端均布有多个直径为6mm的气流孔,用于将加热后的气体均匀地喷到坯体表面。
Referring to accompanying drawings 1 to 6, the architectural ceramic single-layer rapid dryer equipment described in this embodiment includes a single-layer roller dryer 1 mainly composed of two major systems of heating and dehumidification, wherein, The heating system described in this embodiment includes a combustion-supporting system, a combustion system and a
以下为本实施例上述的建筑陶瓷单层快速干燥器设备的具体工作原理:工作时,助燃风机4将外部空气经助燃风管5引入燃烧系统的燃气主管6内,之后导入喷枪7内部,与喷枪7内的燃气混合后进入供热组件14的不锈钢加热管8中充分燃烧,之后再将加热后的气体送至供热组件14的不锈钢方风管9内,最后通过供热组件14的不锈钢供热管10上的气流孔均匀地将热气吹到坯体表面,由于本实用新型的热气是采用喷枪7加热空气而得来的,所以,本实用新型的热气温度很高,可达到300℃左右,从而降低了干燥周期,达到均匀快速加热干燥坯体的效果。此时,砖坯干燥后产生的湿气,在排湿风机3引力的作用下,分别从辊道窑头部和尾部的上下处的排湿顶抽12和排湿底抽13引入排湿主管11内,并最终通过烟囱排出辊道窑外。总之,综上所述,相比现有技术,本实用新型成功解决了水分高产品不易干燥、易裂砖等问题,具有缩短干燥周期,提高生产效率的优势;具有结构合理,自动化程度高,干燥窑内部热循环高,单位热量消耗低,设备占有土地少,节省土地投资和降低设备运作成本等优点,值得推广。
The following is the specific working principle of the above-mentioned architectural ceramic single-layer rapid dryer equipment in this embodiment: during work, the combustion-supporting blower 4 introduces external air into the gas
以上所述之实施例子只为本实用新型之较佳实施例,并非以此限制本实用新型的实施范围,故凡依本实用新型之形状、原理所作的变化,均应涵盖在本实用新型的保护范围内。 The implementation examples described above are only preferred embodiments of the present utility model, and are not intended to limit the scope of implementation of the present utility model, so all changes made according to the shape and principle of the present utility model should be covered by the scope of the present utility model. within the scope of protection.
Claims (5)
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201220323677.5U CN202770125U (en) | 2012-07-06 | 2012-07-06 | Architectural ceramic monolayer rapid drying dryer |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201220323677.5U CN202770125U (en) | 2012-07-06 | 2012-07-06 | Architectural ceramic monolayer rapid drying dryer |
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| CN202770125U true CN202770125U (en) | 2013-03-06 |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102748926A (en) * | 2012-07-06 | 2012-10-24 | 广东中窑窑业股份有限公司 | Building ceramic single-layer rapid dryer equipment |
| CN105910449A (en) * | 2016-06-28 | 2016-08-31 | 卢爱玲 | Efficient heat energy utilization structure of dehumidification area on ceramic kiln |
| CN106524720A (en) * | 2016-11-21 | 2017-03-22 | 赵宽学 | Integrated furnace for drying and firing ceramics |
-
2012
- 2012-07-06 CN CN201220323677.5U patent/CN202770125U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102748926A (en) * | 2012-07-06 | 2012-10-24 | 广东中窑窑业股份有限公司 | Building ceramic single-layer rapid dryer equipment |
| CN105910449A (en) * | 2016-06-28 | 2016-08-31 | 卢爱玲 | Efficient heat energy utilization structure of dehumidification area on ceramic kiln |
| CN106524720A (en) * | 2016-11-21 | 2017-03-22 | 赵宽学 | Integrated furnace for drying and firing ceramics |
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