CN205323677U - Dry process pelletization system - Google Patents
Dry process pelletization system Download PDFInfo
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- CN205323677U CN205323677U CN201620004172.0U CN201620004172U CN205323677U CN 205323677 U CN205323677 U CN 205323677U CN 201620004172 U CN201620004172 U CN 201620004172U CN 205323677 U CN205323677 U CN 205323677U
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Abstract
本实用新型公开一种干法制粒系统,包括干法制粒机、振动筛、布袋除尘器、排风管道、引风机以及旋风分离器,旋风分离器输入口通过第一物料输送管道与干法制粒机输出口连接,干法制粒机输出口还连接有进风管道,振动筛设于旋风分离器物的下方,旋风分离器出风口通过第二物料输送管道与布袋除尘器输入口连接,布袋除尘器出风口与排风管道相连通,引风机设于排风管道上。该干法制粒系统,干法制粒机制得的颗粒先由旋风分离器按体积大小进行预分离,体积极小的颗粒才进入布袋除尘器,其可有效避免体积符合要求的颗粒随风进入布袋除尘器,以提高制粒成品率。
The utility model discloses a dry granulation system, which comprises a dry granulator, a vibrating screen, a cloth bag dust collector, an exhaust pipe, an induced draft fan and a cyclone separator. The output port of the dry granulator is also connected to the air inlet pipe. The vibrating screen is set under the cyclone separator. The air outlet of the cyclone separator is connected to the input port of the bag filter through the second material delivery pipe. The air outlet is connected with the exhaust duct, and the induced draft fan is arranged on the exhaust duct. In this dry granulation system, the granules produced by the dry granulator are pre-separated by the cyclone separator according to the volume, and the very small particles enter the bag filter, which can effectively prevent the particles with the required volume from entering the bag dust collector with the wind. device to increase the yield of granulation.
Description
技术领域 technical field
本实用新型涉及一种制粒生产线,特别是指一种干法制粒系统。 The utility model relates to a granulation production line, in particular to a dry granulation system.
背景技术 Background technique
中国专利申请公开说明书CN202289975U公开了一种干法制粒系统,包括干法制粒机、粉料设备、振动筛、布袋除尘器、烟仓及引风机,粉料设备通过绞龙与干法制粒机上方的料仓连接,振动筛设于干法制粒机的下方,布袋除尘器一端与干法制粒机连接,另一端与烟仓相连通,引风机设于烟仓上。工作时,干法制粒机制成的微粒进入振动筛,由振动筛筛选出所需体积大小的颗粒,而布袋除尘器用于将干法制机内的粉尘除去,减少生产环境污染。该干法制粒系统,布袋除尘器直接与干法制粒机相连,除尘时,干法制粒机内体积略大或符合生产要求的颗粒易直接进入布袋除尘器,进而影响振动筛筛选出体积符合要求的颗粒的成品率。 Chinese patent application publication CN202289975U discloses a dry granulation system, including a dry granulator, powder equipment, a vibrating screen, a bag filter, a smoke bin and an induced draft fan, and the powder equipment passes through the auger and above the dry granulator. The silo is connected, the vibrating screen is set under the dry granulator, one end of the bag filter is connected to the dry granulator, the other end is connected to the smoke bin, and the induced draft fan is set on the smoke bin. During work, the particles produced by the dry granulator enter the vibrating sieve, and the granules of the required size are screened out by the vibrating sieve, while the bag filter is used to remove the dust in the dry granulator to reduce production environmental pollution. In this dry granulation system, the bag filter is directly connected to the dry granulator. During dust removal, the particles with a slightly larger volume in the dry granulator or that meet the production requirements are easy to enter the bag filter directly, which will affect the screening volume of the vibrating screen to meet the requirements. The yield of pellets.
发明内容 Contents of the invention
本实用新型的目的在于提供一种干法制粒系统。 The purpose of the utility model is to provide a dry granulation system.
为实现本实用新型的目的,现详细说明其技术方案:一种干法制粒系统,包括周转桶、物料输送装置、干法制粒机、振动筛、布袋除尘器、排风管道及引风机,所述物料输送装置的输入、输出端分别与周转桶、干法制粒机的料仓相连,其还包括旋风分离器,旋风分离器输入口通过第一物料输送管道与干法制粒机输出口连接,干法制粒机输出口还连接有进风管道,旋风分离器物料出口连接有第一关风机,所述振动筛设于第一关风机出口的下方,旋风分离器出风口通过第二物料输送管道与布袋除尘器输入口连接,布袋除尘器物料出口连接有第二关风机,布袋除尘器出风口与排风管道相连通,引风机设于排风管道上。 In order to achieve the purpose of this utility model, its technical solution is now described in detail: a dry granulation system, including a turnover barrel, a material conveying device, a dry granulator, a vibrating screen, a bag filter, an exhaust duct and an induced draft fan. The input and output ends of the material conveying device are respectively connected to the turnover barrel and the silo of the dry granulator, and it also includes a cyclone separator, and the input port of the cyclone separator is connected to the output port of the dry granulator through the first material conveying pipeline. The output port of the dry granulator is also connected with an air inlet pipe, and the material outlet of the cyclone separator is connected with the first shut-off fan. It is connected to the input port of the bag filter, the material outlet of the bag filter is connected to a second fan, the outlet of the bag filter is connected to the exhaust pipe, and the induced fan is set on the exhaust pipe.
进一步地,进风管道上设有过滤器和加热器。通过过滤器和加热器对进入第一物料输送管道的风进行过滤和干燥,减少进风中的杂质和水分含量,避免送入旋风分离器的颗粒混入杂质和水分,提高颗粒的纯净度和品质。 Further, a filter and a heater are provided on the air inlet duct. Filter and dry the air entering the first material conveying pipeline through the filter and heater, reduce the impurity and moisture content in the air intake, prevent the particles sent into the cyclone separator from being mixed with impurities and moisture, and improve the purity and quality of the particles .
进一步地,过滤器包括初效过滤器、中效过滤器和高效过滤器,所述初效过滤器、中效过滤器、加热器和高效过滤器由进风管道输入端向干法制粒机输出口依次设置。初效过滤器、中效过滤器和高效过滤器对进入进风管道内的进风进行分级过滤,可有效提高过滤效率,其工作时,初效过滤器和中效过滤器主要对进风中的杂质进行过滤,高效过滤器主要用于除去加热后热风中的水分杂质。 Further, the filter includes an initial effect filter, an intermediate effect filter and a high efficiency filter, and the initial effect filter, intermediate effect filter, heater and high efficiency filter are output to the dry granulator from the input end of the air inlet pipeline Ports are set in turn. The primary effect filter, medium effect filter and high efficiency filter filter the air entering the air intake pipe in stages, which can effectively improve the filtration efficiency. When working, the primary effect filter and medium effect filter mainly The high-efficiency filter is mainly used to remove the moisture and impurities in the hot air after heating.
进一步地,物料输送装置为真空上料机。相比绞龙等其他上料机,真空上料机可实现均匀、精确上料,且上料时不会产生灰尘,影响生产环境。 Further, the material conveying device is a vacuum feeder. Compared with other feeding machines such as augers, the vacuum feeding machine can achieve uniform and accurate feeding, and it will not generate dust during feeding, which will affect the production environment.
本实用新型干法制粒系统,物料置于周转桶内,由物料输送装置输送至干法制粒机,干法制粒机对物料进行加工制成颗粒,颗粒随进风管道进入的风经第一物料输送管道进入旋风分离器,旋风分离器使颗粒按比重、体积分级,体积略大的颗粒经第一关风机卸料落入振动筛,由振动筛筛选出体积符合要求的颗粒,体积极小的颗粒经第二物料输送管道进入布袋除尘器,经布袋除尘器过滤后由第二关风机卸料,而经布袋除尘器除尘后的干净空气由排风管道排出。该干法制粒系统,干法制粒机制得的颗粒先由旋风分离器按体积大小进行预分离,体积极小的颗粒才进入布袋除尘器,其可有效避免体积符合要求的颗粒随风进入布袋除尘器,以提高制粒成品率。 In the dry granulation system of the utility model, the material is placed in the turnover barrel and transported to the dry granulator by the material conveying device. The dry granulator processes the material into granules. The conveying pipeline enters the cyclone separator, and the cyclone separator classifies the particles according to specific gravity and volume. The slightly larger particles are discharged by the first fan and fall into the vibrating screen, and the particles that meet the requirements are screened out by the vibrating screen. The particles enter the bag filter through the second material conveying pipe, and are discharged by the second fan after being filtered by the bag filter, and the clean air after dust removal by the bag filter is discharged from the exhaust pipe. In this dry granulation system, the granules produced by the dry granulator are pre-separated by the cyclone separator according to the volume, and the very small particles enter the bag filter, which can effectively prevent the particles with the required volume from entering the bag dust collector with the wind. device to increase the yield of granulation.
附图说明 Description of drawings
图1是本实用新型一种实施方式的结构示意图。 Fig. 1 is a schematic structural view of an embodiment of the utility model.
具体实施方式 detailed description
下面结合附图对本实用新型干法制粒系统的具体实施方式作详细的说明: The specific embodiment of the dry granulation system of the present invention will be described in detail below in conjunction with the accompanying drawings:
如图1所示,本实用新型干法制粒系统,包括周转桶1、物料输送装置2、干法制粒机3、振动筛5、布袋除尘器6、排风管道7及引风机8,所述物料输送装置2的输入、输出端分别与周转桶1、干法制粒机3的料仓31相连,其还包括旋风分离器4,旋风分离器4输入口通过第一物料输送管道41与干法制粒机3输出口连接,干法制粒机3输出口还连接有进风管道9,旋风分离器4物料出口连接有第一关风机10,所述振动筛5设于第一关风机10出口的下方,旋风分离器4出风口通过第二物料输送管道42与布袋除尘器6输入口连接,布袋除尘器6物料出口连接有第二关风机11,布袋除尘器6出风口与排风管道7相连通,引风机8设于排风管道7上。进风管道9上设有过滤器12和加热器13。过滤器12包括初效过滤器14、中效过滤器15和高效过滤器16,所述初效过滤器14、中效过滤器15、加热器13和高效过滤器16由进风管道9输入端向干法制粒机3输出口依次设置。物料输送装置2为真空上料机。 As shown in Figure 1, the dry granulation system of the utility model includes a turnover barrel 1, a material conveying device 2, a dry granulator 3, a vibrating screen 5, a bag filter 6, an exhaust duct 7 and an induced draft fan 8. The input and output ends of the material conveying device 2 are respectively connected to the turnover barrel 1 and the silo 31 of the dry granulator 3, and it also includes a cyclone separator 4, and the input port of the cyclone separator 4 is connected to the dry granulator through the first material conveying pipeline 41. The output port of the granulator 3 is connected, the output port of the dry granulator 3 is also connected with the air inlet pipe 9, the material outlet of the cyclone separator 4 is connected with the first fan 10, and the vibrating screen 5 is located at the outlet of the first fan 10. Below, the air outlet of the cyclone separator 4 is connected to the input port of the bag filter 6 through the second material delivery pipe 42, the material outlet of the bag filter 6 is connected to the second fan 11, and the air outlet of the bag filter 6 is connected to the exhaust pipe 7 Pass, the induced draft fan 8 is located on the exhaust duct 7. The air inlet duct 9 is provided with a filter 12 and a heater 13 . Filter 12 comprises primary effect filter 14, medium effect filter 15 and high efficiency filter 16, and described primary effect filter 14, medium effect filter 15, heater 13 and high efficiency filter 16 are input by air inlet pipe 9 The 3 output ports of the dry granulator are arranged in sequence. The material conveying device 2 is a vacuum feeder.
本实用新型干法制粒系统,物料置于周转桶1内,由物料输送装置2输送至干法制粒机3,干法制粒机3对物料进行加工制成颗粒,颗粒随进风管道9进入的风经第一物料输送管道41进入旋风分离器4,旋风分离器4使颗粒按比重、体积分级,体积略大的颗粒经第一关风机10卸料落入振动筛5,由振动筛5筛选出体积符合要求的颗粒,体积极小的颗粒经第二物料输送管道42进入布袋除尘器6,经布袋除尘器6过滤后由第二关风机11卸料,而经布袋除尘器6除尘后的干净空气由排风管道7排出。 In the dry granulation system of the utility model, the material is placed in the turnover barrel 1, and is transported to the dry granulator 3 by the material conveying device 2, and the dry granulator 3 processes the material into granules, and the granules enter with the air inlet pipe 9 The wind enters the cyclone separator 4 through the first material conveying pipeline 41, and the cyclone separator 4 classifies the particles according to the specific gravity and volume. Particles that meet the requirements are discharged, and the extremely small particles enter the bag filter 6 through the second material conveying pipeline 42, and are discharged by the second shut-off fan 11 after being filtered by the bag filter 6. Clean air is discharged by exhaust duct 7.
本实用新型干法制粒系统,干法制粒机3制得的颗粒先由旋风分离器4按体积大小进行预分离,体积极小的颗粒才进入布袋除尘器6,其可有效避免体积符合要求的颗粒随风进入布袋除尘器6,以提高制粒成品率。 In the dry granulation system of the present utility model, the granules produced by the dry granulator 3 are pre-separated by the cyclone separator 4 according to the volume, and the very small particles enter the bag filter 6, which can effectively avoid the volume meeting the requirements. The particles enter the bag filter 6 with the wind to improve the yield of granulation.
本实用新型干法制粒系统,为减少进风中的杂质和水分含量,避免送入旋风分离器4的颗粒混入杂质和水分,提高颗粒的纯净度和品质,较佳地,进风管道9上设有过滤器12和加热器13;为有提高过滤效率,较佳地,过滤器12包括初效过滤器14、中效过滤器15和高效过滤器16,所述初效过滤器14、中效过滤器15、加热器13和高效过滤器16由进风管道9输入端向干法制粒机3输出口依次设置;为实现均匀、精确上料,且上料时不会产生灰尘,影响生产环境,较佳地,物料输送装置2为真空上料机。 The dry granulation system of the utility model, in order to reduce the impurity and moisture content in the air intake, prevent the particles sent into the cyclone separator 4 from being mixed with impurities and moisture, and improve the purity and quality of the granules. Be provided with filter 12 and heater 13; For having to improve filtration efficiency, preferably, filter 12 comprises primary effect filter 14, medium effect filter 15 and high efficiency filter 16, described primary effect filter 14, medium effect High-efficiency filter 15, heater 13 and high-efficiency filter 16 are arranged sequentially from the input end of the air inlet pipe 9 to the output port of the dry granulator 3; in order to achieve uniform and accurate feeding, and no dust will be generated during feeding, which will affect production Environment, preferably, the material conveying device 2 is a vacuum feeder.
Claims (4)
Priority Applications (1)
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| CN201620004172.0U CN205323677U (en) | 2016-01-06 | 2016-01-06 | Dry process pelletization system |
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| CN201620004172.0U CN205323677U (en) | 2016-01-06 | 2016-01-06 | Dry process pelletization system |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107265127A (en) * | 2017-08-17 | 2017-10-20 | 长兴国和新材料有限公司 | The dry activation and drawing mechanism of a kind of stone flour |
| CN107328216A (en) * | 2017-08-17 | 2017-11-07 | 长兴国和新材料有限公司 | A kind of stone flour dry activation and drawing mechanism with dust arrester |
| CN107321616A (en) * | 2017-08-17 | 2017-11-07 | 长兴国和新材料有限公司 | A kind of hot air circulation stone flour dry activation device with dust arrester |
| CN107321614A (en) * | 2017-08-17 | 2017-11-07 | 长兴国和新材料有限公司 | A kind of dry activation device of stone flour |
| CN107324370A (en) * | 2017-08-17 | 2017-11-07 | 长兴国和新材料有限公司 | The stone flour dry activation and drawing mechanism of a kind of hot air circulation |
-
2016
- 2016-01-06 CN CN201620004172.0U patent/CN205323677U/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107265127A (en) * | 2017-08-17 | 2017-10-20 | 长兴国和新材料有限公司 | The dry activation and drawing mechanism of a kind of stone flour |
| CN107328216A (en) * | 2017-08-17 | 2017-11-07 | 长兴国和新材料有限公司 | A kind of stone flour dry activation and drawing mechanism with dust arrester |
| CN107321616A (en) * | 2017-08-17 | 2017-11-07 | 长兴国和新材料有限公司 | A kind of hot air circulation stone flour dry activation device with dust arrester |
| CN107321614A (en) * | 2017-08-17 | 2017-11-07 | 长兴国和新材料有限公司 | A kind of dry activation device of stone flour |
| CN107324370A (en) * | 2017-08-17 | 2017-11-07 | 长兴国和新材料有限公司 | The stone flour dry activation and drawing mechanism of a kind of hot air circulation |
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