CN205048883U - Modular spray fluidized drying machine - Google Patents
Modular spray fluidized drying machine Download PDFInfo
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- CN205048883U CN205048883U CN201520769341.5U CN201520769341U CN205048883U CN 205048883 U CN205048883 U CN 205048883U CN 201520769341 U CN201520769341 U CN 201520769341U CN 205048883 U CN205048883 U CN 205048883U
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- drying machine
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Abstract
Description
技术领域technical field
本实用新型涉及到一种组合式喷雾流化干燥机,属于干燥设备技术领域。The utility model relates to a combined spray fluidized 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℃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, and then sent to 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.
对于干燥度要求在1-3的物料,喷雾干燥机经分离后的废空气温度在50℃左右,含有的热量不高,如果物料干燥度要求在0.3以下,直接采用喷雾干燥机达到预定干燥度,则需要250℃以上的热空气进行干燥,而且从干燥塔排出的混合气体温度能达到100℃左右,能耗极高。For materials whose dryness is required to be 1-3, the temperature of the waste air after separation by the spray dryer is about 50°C, and the heat contained is not high. If the dryness of the material is required to be below 0.3, the spray dryer can be used directly to achieve the predetermined dryness. , you need hot air above 250°C for drying, and the temperature of the mixed gas discharged from the drying tower can reach about 100°C, which consumes a lot of energy.
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、提高物料干燥度的组合式喷雾流化干燥机。The purpose of the utility model is to overcome the deficiencies of the prior art and provide a combined spray fluidized dryer which reduces energy consumption and improves the dryness of materials.
本实用新型采用的技术方案为:一种组合式喷雾流化干燥机,包括喷雾干燥塔、流化干燥机、旋风分离器、布袋除尘器以及引风机;The technical solution adopted by the utility model is: a combined spray fluidized dryer, including a spray drying tower, a fluidized dryer, a cyclone separator, a bag filter and an induced draft fan;
所述喷雾干燥塔顶部设有雾化器,雾化器与料槽连接,所述喷雾干燥塔顶部还设有进风管;The top of the spray drying tower is provided with an atomizer, and the atomizer is connected to the trough, and the top of the spray drying tower is also provided with an air inlet pipe;
所述喷雾干燥塔还包括设置在底部的出料口和设置在侧面的出风管,所述流化干燥机上设置有空气入口、进料口、出料口和排气口,所述出风管通过管道连接流化干燥机的空气入口,所述出料口通过送料器连接到流化干燥机的进料口,流化干燥机的排风口依次连接旋风分离器、布袋除尘器以及引风机,旋风分离器、布袋除尘器底部均设有出料口。The spray drying tower also includes a discharge port arranged at the bottom and an air outlet pipe arranged at the side, and the fluidized dryer is provided with an air inlet, a feed port, a discharge port and an exhaust port, and the air outlet The pipe is connected to the air inlet of the fluidized dryer through a pipeline, and the outlet is connected to the feed port of the fluidized dryer through a feeder, and the exhaust outlet of the fluidized dryer is connected to the cyclone separator, the bag filter, and the air outlet in turn. Fans, cyclone separators, and bag filters are all equipped with discharge ports at the bottom.
本实用新型中,喷雾干燥塔和流化干燥机连用,对于干燥度要求极高的物料而言,在喷雾干燥塔内进行初步干燥,物料的干燥度达到0.5-0.7,然后在流化干燥机中进行进一步干燥,使干燥度降到0.3以下,可以大幅降低能耗、节约能源。In the utility model, the spray drying tower and the fluidized dryer are used together. For materials with extremely high dryness requirements, preliminary drying is carried out in the spray drying tower. Further drying is carried out in the middle to reduce the dryness to below 0.3, which can greatly reduce energy consumption and save energy.
附图说明Description of drawings
图1为本实用新型的组合式喷雾流化干燥机的结构示意图。Fig. 1 is a schematic structural view of the combined spray fluidized dryer of the present invention.
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,本组合式喷雾流化干燥机,包括喷雾干燥塔1、流化干燥机2、旋风分离器3、布袋除尘器4以及引风机5;As shown in Figure 1, the combined spray fluidized dryer includes a spray drying tower 1, a fluidized dryer 2, a cyclone separator 3, a bag filter 4 and an induced draft fan 5;
所述喷雾干燥塔顶部设有雾化器6,雾化器6与料槽连接,所述喷雾干燥塔顶部还设有进风管11;The top of the spray-drying tower is provided with an atomizer 6, and the atomizer 6 is connected with a trough, and the top of the spray-drying tower is also provided with an air inlet pipe 11;
所述喷雾干燥塔还包括设置在底部的出料口12和设置在侧面的出风管13,所述流化干燥机上设置有空气入口21、进料口22、出料口23和排气口24,所述出风管12通过管道连接流化干燥机2的空气入口21,所述喷雾干燥塔1的出料口12通过送料器连接到流化干燥机2的进料口22,流化干燥机的排风口24依次连接旋风分离器3、布袋除尘器4以及引风机5,旋风分离器3、布袋除尘器4底部均设有出料口。The spray drying tower also includes a discharge port 12 arranged at the bottom and an air outlet pipe 13 arranged at the side, and the fluidized dryer is provided with an air inlet 21, a feed port 22, a discharge port 23 and an exhaust port 24. The air outlet pipe 12 is connected to the air inlet 21 of the fluidized dryer 2 through a pipeline, and the outlet 12 of the spray drying tower 1 is connected to the feed port 22 of the fluidized dryer 2 through a feeder, and the fluidized The air outlet 24 of the dryer is connected to the cyclone separator 3, the bag filter 4 and the induced draft fan 5 in sequence, and the bottoms of the cyclone separator 3 and the bag filter 4 are all provided with outlets.
工作时,送料泵将液化物料从料槽中送入雾化器中喷出,220℃的热空气进入干燥塔中与雾状物料混合,物料微粒水分蒸发,大颗粒进入干燥塔底部,通过出料口进入流化干燥机,此时大颗粒的干燥度在0.5左右,小颗粒与空气的混合物从出风管排出,从流化干燥机的空气入口中仍然进入流化干燥机,该混合物的温度为70-90℃左右,在流化干燥机中对大颗粒进行进一步的干燥,使大颗粒的干燥度降低到0.3以下。When working, the feeding pump sends the liquefied material from the trough to the atomizer and sprays it out. The hot air at 220°C enters the drying tower and mixes with the mist material. The feed port enters the fluidized dryer, at this time the dryness of the large particles is about 0.5, the mixture of small particles and air is discharged from the air outlet pipe, and still enters the fluidized dryer from the air inlet of the fluidized dryer, the mixture The temperature is about 70-90°C, and the large particles are further dried in a fluidized dryer to reduce the dryness of the large particles to below 0.3.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201520769341.5U CN205048883U (en) | 2015-09-30 | 2015-09-30 | Modular spray fluidized drying machine |
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| CN201520769341.5U CN205048883U (en) | 2015-09-30 | 2015-09-30 | Modular spray fluidized drying machine |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105941823A (en) * | 2016-05-25 | 2016-09-21 | 刘新旗 | High-soluble soybean peptide dry powder and preparation method thereof |
| CN111715139A (en) * | 2020-07-10 | 2020-09-29 | 江苏瑞升华能源科技有限公司 | A kind of high-concentration mother liquor granulation device and granulation method |
-
2015
- 2015-09-30 CN CN201520769341.5U patent/CN205048883U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105941823A (en) * | 2016-05-25 | 2016-09-21 | 刘新旗 | High-soluble soybean peptide dry powder and preparation method thereof |
| CN111715139A (en) * | 2020-07-10 | 2020-09-29 | 江苏瑞升华能源科技有限公司 | A kind of high-concentration mother liquor granulation device and granulation method |
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Granted publication date: 20160224 |