CN205042133U - Energy -saving spray drier - Google Patents
Energy -saving spray drier Download PDFInfo
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- CN205042133U CN205042133U CN201520722052.XU CN201520722052U CN205042133U CN 205042133 U CN205042133 U CN 205042133U CN 201520722052 U CN201520722052 U CN 201520722052U CN 205042133 U CN205042133 U CN 205042133U
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Abstract
Description
技术领域technical field
本实用新型涉及到一种节能型喷雾干燥机,属于干燥设备技术领域。The utility model relates to an energy-saving 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℃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,但有的物料干燥度要求在0.5以下,此时喷雾干燥机经分离后的废空气温度能达到70℃左右,含有大量的热量,直接排出会造成能耗大大提升。因此回收废空气中的热能很有必要。For materials whose dryness is required to be 1-3, the temperature of the waste air after separation of the spray dryer is about 50°C, and the heat contained is not high, but some materials require a dryness of less than 0.5. At this time, the spray dryer is separated The final waste air temperature can reach about 70°C, which contains a lot of heat, and direct discharge will cause a great increase in energy consumption. Therefore, it is necessary to recover the heat energy in the waste 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、节约能源的节能型喷雾干燥机。The purpose of the utility model is to overcome the deficiencies of the prior art and provide an energy-saving spray dryer that reduces energy consumption and saves energy.
本实用新型采用的技术方案为:一种节能型喷雾干燥机,包括送料系统、进风系统、干燥塔、第一旋风分离器、第二旋风分离器、膜分离器以及引风机;The technical solution adopted by the utility model is: an energy-saving spray dryer, including a feeding system, an air inlet system, a drying tower, a first cyclone separator, a second cyclone separator, a membrane separator and an induced draft fan;
所述送料系统包括通过管道依次连接的料槽、送料泵和雾化器,所述雾化器设置于干燥塔内;The feeding system includes a feed tank, a feeding pump and an atomizer connected in sequence through pipelines, and the atomizer is arranged in a drying tower;
所述进风系统包括通过管道依次连接的空气过滤器、鼓风机和加热装置,所述加热装置与干燥塔的进风管相连;The air inlet system includes an air filter, a blower and a heating device connected in sequence through pipelines, and the heating device is connected with the air inlet pipe of the drying tower;
所述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,所述出风管通过管道依次连接第一旋风分离器、第二旋风分离器以及膜分离器,所述第一旋风分离器、第二旋风分离器以及膜分离器底部均设有出料口;The drying tower also includes a discharge port arranged at the bottom and an air outlet pipe arranged on the side, and the air outlet pipe is sequentially connected to the first cyclone separator, the second cyclone separator and the membrane separator through pipelines. The first cyclone separator, the second cyclone separator and the bottom of the membrane separator are all equipped with outlets;
所述膜分离器的排气管通过引风机连接到鼓风机与加热器之间的管道上。The exhaust pipe of the membrane separator is connected to the pipeline between the blower and the heater through an induced draft fan.
优选的,所述第二旋风分离器与膜分离器之间的管道上装有风压测量装置。Preferably, a wind pressure measuring device is installed on the pipeline between the second cyclone separator and the membrane separator.
优选的,所述膜分离器的排气管上装有风压测量装置。Preferably, a wind pressure measuring device is installed on the exhaust pipe of the membrane separator.
本实用新型中,干燥塔排出的混合细颗粒的物料的空气经两次旋风分离后,再通过膜分离器得到彻底的分离,物料回收效率高,膜分离器排出的废气洁净度高,基本接近新鲜空气的洁净度,且含有较多热量,回到鼓风机与加热器之间的管道上参与循环,可以使热量得到充分利用,降低能耗、节约能源。两个旋风分离器的设置可以减轻膜分离器的压力,在膜分离器的进风管和排气管上均设有风压测量装置可以控制进入膜分离器的空气流量,防止对膜分离器的损坏。In the utility model, the air of the mixed fine-grained material discharged from the drying tower is separated by two cyclones, and then completely separated by the membrane separator. The cleanliness of the fresh air contains more heat, and it returns to the pipeline between the blower and the heater to participate in the circulation, so that the heat can be fully utilized, reducing energy consumption and saving energy. The setting of the two cyclone separators can reduce the pressure of the membrane separator, and the air pressure measuring device is installed on the air inlet pipe and the exhaust pipe of the membrane separator to control the air flow into the membrane separator and prevent damage to the membrane separator. damage.
附图说明Description of drawings
图1为本实用新型的节能型喷雾干燥机的结构示意图。Fig. 1 is a structural schematic diagram of an energy-saving spray 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,本节能型喷雾干燥机,包括送料系统、进风系统、干燥塔1、第一旋风分离器2、第二旋风分离器3、膜分离器4以及引风机5;As shown in Figure 1, the energy-saving spray dryer includes a feeding system, an air inlet system, a drying tower 1, a first cyclone separator 2, a second cyclone separator 3, a membrane separator 4 and an induced draft fan 5;
所述送料系统包括通过管道依次连接的料槽6、送料泵7和雾化器8,所述雾化器8设置于干燥塔1内;The feed system includes a feed tank 6, a feed pump 7 and an atomizer 8 connected in sequence through pipelines, and the atomizer 8 is arranged in the drying tower 1;
所述进风系统包括通过管道依次连接的空气过滤器9、鼓风机10和加热装置11,所述加热装置11与干燥塔1的进风管相连;The air inlet system includes an air filter 9, a blower 10 and a heating device 11 connected in sequence through pipelines, and the heating device 11 is connected to the air inlet pipe of the drying tower 1;
所述干燥塔1还包括设置在底部的出料口和设置在侧面的出风管,所述出风管通过管道依次连接第一旋风分离器2、第二旋风分离器3以及膜分离器4,所述第一旋风分离器2、第二旋风分离器3以及膜分离器4底部均设有出料口;The drying tower 1 also includes a discharge port arranged at the bottom and an air outlet pipe arranged on the side, and the air outlet pipe is sequentially connected to the first cyclone separator 2, the second cyclone separator 3 and the membrane separator 4 through pipelines , the bottom of the first cyclone separator 2, the second cyclone separator 3 and the bottom of the membrane separator 4 are all provided with a discharge port;
所述膜分离器4的排气管通过引风机5连接到鼓风机10与加热器11之间的管道上,其中所述第二旋风分离器3与膜分离器4之间的管道以及所述膜分离器4的排气管上均装有风压测量装置。The exhaust pipe of the membrane separator 4 is connected to the pipeline between the blower 10 and the heater 11 through the induced draft fan 5, wherein the pipeline between the second cyclone separator 3 and the membrane separator 4 and the membrane The exhaust pipe of separator 4 is equipped with wind pressure measuring device.
工作时,送料泵将液化物料从料槽中送入雾化器中喷出,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,大颗粒进入干燥塔底部的,通过出料口排出,小颗粒与空气混合从出风管排出,依次进入第一旋风分离器、第二旋风分离器进行物料分离,大部分物料从出料口排出,仍含有少量物料颗粒的空气进入膜分离器中,在膜分离器中,物料和空气彻底分离,物料从出料口排出,空气在引风机的作用下进入鼓风机与加热器之间的管道中,重新参与循环。本节能型喷雾干燥机节省能源,物料回收度高,适合于干燥度要求高的贵重物料。When working, the feeding pump sends the liquefied material from the trough into the atomizer and sprays it out. The heated air enters the drying tower and mixes with the mist material. The small particles are mixed with air and discharged from the outlet pipe, and then enter the first cyclone separator and the second cyclone separator for material separation. Most of the materials are discharged from the outlet, and the air still containing a small amount of material particles enters the membrane separation In the membrane separator, the material and air are completely separated, the material is discharged from the outlet, and the air enters the pipeline between the blower and the heater under the action of the induced draft fan, and participates in the cycle again. This energy-saving spray dryer saves energy, has a high degree of material recovery, and is suitable for valuable materials with high dryness requirements.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201520722052.XU CN205042133U (en) | 2015-09-17 | 2015-09-17 | Energy -saving spray drier |
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| CN201520722052.XU CN205042133U (en) | 2015-09-17 | 2015-09-17 | Energy -saving spray drier |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106482489A (en) * | 2016-12-13 | 2017-03-08 | 宜春银锂新能源有限责任公司 | A kind of fine work lithium carbonate production drying device |
| CN107990322A (en) * | 2017-12-28 | 2018-05-04 | 华西能源工业股份有限公司 | A kind of waste incineration CFB boiler of cyclone separator and membrane type separation apparatuses in series |
| CN108479094A (en) * | 2018-05-31 | 2018-09-04 | 峨眉山市龙腾生物科技有限公司 | A kind of span amino acid mother liquor drying device |
| CN108722313A (en) * | 2018-07-17 | 2018-11-02 | 重庆市易特杰机械制造有限公司 | Multi-functional dry granulator |
| CN112717446A (en) * | 2019-10-14 | 2021-04-30 | 无锡市力胜粉体科技有限公司 | Closed cycle spray dryer |
-
2015
- 2015-09-17 CN CN201520722052.XU patent/CN205042133U/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106482489A (en) * | 2016-12-13 | 2017-03-08 | 宜春银锂新能源有限责任公司 | A kind of fine work lithium carbonate production drying device |
| CN107990322A (en) * | 2017-12-28 | 2018-05-04 | 华西能源工业股份有限公司 | A kind of waste incineration CFB boiler of cyclone separator and membrane type separation apparatuses in series |
| CN108479094A (en) * | 2018-05-31 | 2018-09-04 | 峨眉山市龙腾生物科技有限公司 | A kind of span amino acid mother liquor drying device |
| CN108722313A (en) * | 2018-07-17 | 2018-11-02 | 重庆市易特杰机械制造有限公司 | Multi-functional dry granulator |
| CN112717446A (en) * | 2019-10-14 | 2021-04-30 | 无锡市力胜粉体科技有限公司 | Closed cycle spray dryer |
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