CN205042132U - New Spray Dryer - Google Patents
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- CN205042132U CN205042132U CN201520722029.0U CN201520722029U CN205042132U CN 205042132 U CN205042132 U CN 205042132U CN 201520722029 U CN201520722029 U CN 201520722029U CN 205042132 U CN205042132 U CN 205042132U
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Abstract
本实用新型公开了一种新型喷雾干燥机,包括送料系统、送风系统、干燥塔、旋风分离器、引风机以及水幕除尘器;还包括热交换室,所述旋风分离器的排气口通过管道与热交换室的进风口连接,所述热交换室的出风口依次与引风机、水幕除尘器连接,所述送料系统的送料泵与雾化器之间的物料管道从热交换室中弯曲通过。本实用新型的新型喷雾干燥机,利用旋风分离后较高温度的废气对物料进行初步加热,使物料喷出时已经具有一定的温度,能缩短物料干燥时间,帮助热敏性物料保持品质,降低能源消耗。经过热交换后的废气经水幕除尘再排放,可以减轻对空气的污染。
The utility model discloses a novel spray dryer, which comprises a feeding system, an air supply system, a drying tower, a cyclone separator, an induced draft fan and a water curtain dust collector; The air inlet of the heat exchange chamber is connected with the air inlet of the heat exchange chamber through the pipeline, and the air outlet of the heat exchange chamber is connected with the induced draft fan and the water curtain dust collector in turn. Middle bend through. The new spray dryer of the utility model uses the high-temperature exhaust gas after cyclone separation to preliminarily heat the material, so that the material already has a certain temperature when it is sprayed out, which can shorten the drying time of the material, help heat-sensitive materials maintain quality, and reduce energy consumption. . After heat exchange, the exhaust gas is dedusted by the water curtain and then discharged, which can reduce air pollution.
Description
技术领域technical field
本实用新型涉及到一种新型喷雾干燥机,属于干燥设备技术领域。The utility model relates to a novel spray dryer, which belongs to the technical field of drying equipment.
背景技术Background technique
喷雾干燥机为连续式常压干燥器的一种,采用雾化器将物料液分散为雾滴,并用热气体干燥雾滴而获得产品,主要工作过程是:外界新鲜空气通过空气过滤器、鼓风机,进入空气加热器,使空气温度提高到160℃-230℃左右,送进干燥塔。在进入干燥塔前,热空气先通过匀风板,使热空气均匀分布,防止旋涡,避免焦粉发生,以保证干燥效果。需干燥处理的物料液,由压力泵送至雾化器,料液以雾状喷出并与热空气混合,物料微粒吸取热量,瞬间水分蒸发,形成粉末向下降落,经过一段恒速干燥,进一步蒸发水分,粗颗粒落入干燥塔的锥形底部并排出。干燥后的物料细粉粒和低温湿空气的混合物经旋风分离器分离,废空气由排风机排放,干燥细粉末产品落下由卸料器连续排出。The spray dryer is a kind of continuous atmospheric pressure dryer. The atomizer is used to disperse the material liquid into mist droplets, and the hot gas is used to dry the mist droplets to obtain the product. The main working process is: fresh air from the outside passes through the air filter, blower , into the air heater to increase the air temperature to about 160°C-230°C, and then send it into the drying tower. Before entering the drying tower, the hot air passes through the air uniform plate to distribute the hot air evenly, prevent the vortex, avoid the occurrence of coke powder, and ensure the drying effect. The material liquid to be dried is pumped to the atomizer by the pressure pump, the material liquid is sprayed out in the form of mist and mixed with hot air, the material particles absorb heat, the water evaporates instantly, and the powder is formed and falls downward. After a period of constant speed drying, The moisture is further evaporated, and the coarse particles fall into the conical bottom of the drying tower and are discharged. The mixture of dried material fine powder and low-temperature humid air is separated by a cyclone separator, the waste air is discharged by an exhaust fan, and the dry fine powder product falls and is continuously discharged by an unloader.
喷雾干燥机经旋风分离后的空气仍有较高的温度,含有大量的热量,直接排出不仅造成能源的浪费,还会加剧全球温室效应。因此对分离空气中的热能进行回收利用很有必要。The air after the cyclone separation of the spray dryer still has a high temperature and contains a lot of heat. Direct discharge will not only cause a waste of energy, but also aggravate the global greenhouse effect. Therefore, it is necessary to recycle the heat energy in the separated air.
实用新型内容Utility model content
本实用新型的目的是克服现有技术的不足,提供一种降低能耗、节约能源的新型喷雾干燥机。The purpose of the utility model is to overcome the deficiencies of the prior art and provide a new type of spray dryer which reduces energy consumption and saves energy.
本实用新型采用的技术方案为:一种新型喷雾干燥机,包括送料系统、送风系统、干燥塔、旋风分离器、引风机以及水幕除尘器;The technical solution adopted by the utility model is: a new spray dryer, including a feeding system, an air supply system, a drying tower, a cyclone separator, an induced draft fan and a water curtain dust collector;
所述送料系统包括通过物料管道依次连接的料槽、过滤器、送料泵和雾化器,所述雾化器设置于干燥塔内;The feeding system includes a material tank, a filter, a feeding pump and an atomizer connected in sequence through a material pipeline, and the atomizer is arranged in a drying tower;
所述送风系统包括通过管道依次连接的初次空气过滤器、鼓风机、二次空气过滤器、加热装置,所述加热装置与干燥塔的进风管相连;The air supply system includes a primary air filter, a blower, a secondary air filter, and a heating device connected in sequence through pipelines, and the heating device is connected to the air inlet pipe of the drying tower;
所述干燥塔还包括设置在侧面的出风管,所述出风管通过管道连接旋风分离器的进气口;The drying tower also includes an air outlet pipe arranged on the side, and the air outlet pipe is connected to the air inlet of the cyclone separator through a pipeline;
还包括热交换室,所述旋风分离器的排气口通过管道与热交换室的进风口连接,所述热交换室的出风口依次与引风机、水幕除尘器连接,所述送料系统的送料泵与雾化器之间的物料管道从热交换室中弯曲通过。It also includes a heat exchange chamber, the exhaust port of the cyclone separator is connected with the air inlet of the heat exchange chamber through a pipeline, the air outlet of the heat exchange chamber is connected with the induced draft fan and the water curtain dust collector in sequence, and the feed system The material pipeline between the feed pump and the atomizer bends through the heat exchange chamber.
优选的,还包括热交换室清洗系统,所述热交换室清洗系统包括依次连接的水箱、水泵、高压水喷头,所述高压水喷头设于热交换室顶部,还包括排水口,设置于所述热交换室的底部。Preferably, it also includes a cleaning system for the heat exchange chamber. The cleaning system for the heat exchange chamber includes a water tank, a water pump, and a high-pressure water nozzle connected in sequence. the bottom of the heat exchange chamber.
本实用新型的新型喷雾干燥机,利用旋风分离后较高温度的废气对物料进行初步加热,使物料喷出时已经具有一定的温度,能缩短物料干燥时间,帮助热敏性物料保持品质,降低能源消耗。经过热交换后的废气经水幕除尘再排放,可以减轻对空气的污染。由于物料管道在热交换室内弯曲通过,容易积灰,故在热交换室顶部设有冲洗装置,可以在需要时对热交换室以及物料管道进行冲洗。The new spray dryer of the utility model uses the high-temperature exhaust gas after cyclone separation to preliminarily heat the material, so that the material already has a certain temperature when it is sprayed out, which can shorten the drying time of the material, help heat-sensitive materials maintain quality, and reduce energy consumption. . After heat exchange, the exhaust gas is dedusted by the water curtain and then discharged, which can reduce air pollution. Since the material pipe bends through the heat exchange chamber, it is easy to accumulate dust, so a flushing device is installed on the top of the heat exchange chamber to flush the heat exchange chamber and the material pipe when necessary.
附图说明Description of drawings
图1为本实用新型的新型喷雾干燥机的结构示意图。Fig. 1 is the structural representation of the novel spray drier of the present utility model.
下面结合附图和实施例对本实用新型作进一步的说明。Below in conjunction with accompanying drawing and embodiment the utility model is described further.
具体实施方式detailed description
实施例1Example 1
如图1所示,本新型喷雾干燥机,包括送料系统、送风系统、干燥塔、旋风分离器、引风机以及水幕除尘器;As shown in Figure 1, the new spray dryer includes a feeding system, an air supply system, a drying tower, a cyclone separator, an induced draft fan and a water curtain dust collector;
所述送料系统包括通过物料管道依次连接的料槽1、过滤器2、送料泵3和雾化器4,所述雾化器4设置于干燥塔5内;The feeding system includes a material tank 1, a filter 2, a feeding pump 3 and an atomizer 4 connected in sequence through a material pipeline, and the atomizer 4 is arranged in a drying tower 5;
所述送风系统包括通过管道依次连接的初次空气过滤器6、鼓风机7、二次空气过滤器8、加热装置9,所述加热装置与干燥塔5的进风管相连;The air supply system includes a primary air filter 6, a blower 7, a secondary air filter 8, and a heating device 9 connected in sequence through pipelines, and the heating device is connected to the air inlet pipe of the drying tower 5;
所述干燥塔5还包括设置在侧面的出风管,所述出风管通过管道连接旋风分离器10的进气口;Described drying tower 5 also comprises the air outlet pipe that is arranged on the side, and described air outlet pipe connects the air inlet of cyclone separator 10 by pipeline;
还包括热交换室11,所述旋风分离器10的排气口通过管道与热交换室11的进风口连接,所述热交换室11的出风口依次与引风机12、水幕除尘器13连接,所述送料系统的送料泵3与雾化器4之间的物料管道14从热交换室11中弯曲通过;Also includes a heat exchange chamber 11, the exhaust port of the cyclone separator 10 is connected to the air inlet of the heat exchange chamber 11 through a pipeline, and the air outlet of the heat exchange chamber 11 is connected with the induced draft fan 12 and the water curtain dust collector 13 in turn , the material pipeline 14 between the feed pump 3 and the atomizer 4 of the feed system bends through the heat exchange chamber 11;
还包括热交换室清洗系统,所述热交换室清洗系统包括依次连接的水箱15、水泵16、高压水喷头17,所述高压水喷头17设于热交换室11顶部,还包括排水口18,设置于所述热交换室11的底部。It also includes a heat exchange chamber cleaning system, which includes a water tank 15, a water pump 16, and a high-pressure water nozzle 17 connected in sequence, and the high-pressure water nozzle 17 is arranged on the top of the heat exchange chamber 11, and also includes a drain 18, It is arranged at the bottom of the heat exchange chamber 11.
工作时,物料经过滤后,进入雾化器中喷出,加热的空气进入干燥塔中与雾状物料混合,物料微粒水分蒸发,大颗粒落入干燥塔底部,小颗粒与空气混合从出风管排出,进入旋风分离器中进行物料分离,含有少量物料颗粒的废气进入热交换室中,对弯曲的物料管道内的物料进行加热,导致从雾化器中喷出的物料具有一定的温度。从热交换室排出的废气在引风机的作用下进入水幕除尘器,除尘后排出。When working, the material is filtered and sprayed into the atomizer. The heated air enters the drying tower and mixes with the mist material. The water in the material particles evaporates, and the large particles fall into the bottom of the drying tower. The exhaust gas is discharged into the cyclone separator for material separation, and the exhaust gas containing a small amount of material particles enters the heat exchange chamber to heat the material in the curved material pipe, resulting in a certain temperature for the material ejected from the atomizer. The exhaust gas discharged from the heat exchange chamber enters the water curtain dust collector under the action of the induced draft fan, and is discharged after dust removal.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201520722029.0U CN205042132U (en) | 2015-09-17 | 2015-09-17 | New Spray Dryer |
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| CN201520722029.0U CN205042132U (en) | 2015-09-17 | 2015-09-17 | New Spray Dryer |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106474754A (en) * | 2016-12-13 | 2017-03-08 | 宜春银锂新能源有限责任公司 | A kind of residual-heat used type lithium chloride spray-drying installation |
| CN106767002A (en) * | 2017-01-23 | 2017-05-31 | 华中农业大学 | A kind of hot water fast cooling device and method |
| CN109294275A (en) * | 2018-10-23 | 2019-02-01 | 江苏德美科化工有限公司 | A kind of high-performance navy blue reactive dye composition and its application |
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2015
- 2015-09-17 CN CN201520722029.0U patent/CN205042132U/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106474754A (en) * | 2016-12-13 | 2017-03-08 | 宜春银锂新能源有限责任公司 | A kind of residual-heat used type lithium chloride spray-drying installation |
| CN106767002A (en) * | 2017-01-23 | 2017-05-31 | 华中农业大学 | A kind of hot water fast cooling device and method |
| CN106767002B (en) * | 2017-01-23 | 2022-09-16 | 华中农业大学 | Hot water rapid cooling device and method |
| CN109294275A (en) * | 2018-10-23 | 2019-02-01 | 江苏德美科化工有限公司 | A kind of high-performance navy blue reactive dye composition and its application |
| CN109294275B (en) * | 2018-10-23 | 2019-12-06 | 江苏德美科化工有限公司 | high-performance navy blue reactive dye composition and application thereof |
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