CN110142941A - A dust-free plastic particle production line - Google Patents
A dust-free plastic particle production line Download PDFInfo
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- CN110142941A CN110142941A CN201910436720.5A CN201910436720A CN110142941A CN 110142941 A CN110142941 A CN 110142941A CN 201910436720 A CN201910436720 A CN 201910436720A CN 110142941 A CN110142941 A CN 110142941A
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- 238000004519 manufacturing process Methods 0.000 title claims abstract description 27
- 229920003023 plastic Polymers 0.000 title abstract description 11
- 239000002245 particle Substances 0.000 title abstract description 10
- 239000000843 powder Substances 0.000 claims abstract description 135
- 238000005303 weighing Methods 0.000 claims abstract description 83
- 239000008188 pellet Substances 0.000 claims abstract description 50
- 229920000426 Microplastic Polymers 0.000 claims abstract 10
- 235000013339 cereals Nutrition 0.000 claims abstract 9
- 230000008878 coupling Effects 0.000 claims abstract 9
- 238000010168 coupling process Methods 0.000 claims abstract 9
- 238000005859 coupling reaction Methods 0.000 claims abstract 9
- 238000000605 extraction Methods 0.000 claims abstract 7
- 235000013312 flour Nutrition 0.000 claims abstract 7
- 238000009955 starching Methods 0.000 claims abstract 5
- 238000009434 installation Methods 0.000 claims abstract 3
- 239000000428 dust Substances 0.000 claims description 57
- 239000004744 fabric Substances 0.000 claims description 15
- 239000006185 dispersion Substances 0.000 claims description 13
- 238000003756 stirring Methods 0.000 claims description 10
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 7
- 239000000741 silica gel Substances 0.000 claims description 7
- 229910002027 silica gel Inorganic materials 0.000 claims description 7
- 238000002156 mixing Methods 0.000 claims description 6
- 238000001914 filtration Methods 0.000 claims description 4
- 238000000926 separation method Methods 0.000 claims 1
- 230000035611 feeding Effects 0.000 description 23
- 239000008187 granular material Substances 0.000 description 17
- 239000002994 raw material Substances 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- 238000001125 extrusion Methods 0.000 description 4
- 238000000465 moulding Methods 0.000 description 4
- 230000009471 action Effects 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 239000000463 material Substances 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 239000000654 additive Substances 0.000 description 1
- 230000004323 axial length Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000009194 climbing Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000005469 granulation Methods 0.000 description 1
- 230000003179 granulation Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 238000010137 moulding (plastic) Methods 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 210000002345 respiratory system Anatomy 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/025—General arrangement or layout of plant
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
- B29C48/04—Particle-shaped
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/27—Cleaning; Purging; Avoiding contamination
- B29C48/271—Cleaning; Purging; Avoiding contamination of feeding units
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/285—Feeding the extrusion material to the extruder
- B29C48/286—Raw material dosing
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/285—Feeding the extrusion material to the extruder
- B29C48/288—Feeding the extrusion material to the extruder in solid form, e.g. powder or granules
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Abstract
Description
技术领域technical field
本发明涉及塑料粒子生产技术领域,尤其是一种无尘的塑料粒子生产线。The invention relates to the technical field of plastic particle production, in particular to a dust-free plastic particle production line.
背景技术Background technique
工业上塑料成型用的原料主要有粉料、粒料、溶液和分散体,部分成型采用单体和预聚体,应用比较广泛的是粉料和粒料。粉料是将粉状的原料树脂和各种不同助剂混合分散均匀所制得的,粒料是将粉料通过塑炼作业,使之进一步塑化并通过不同的方法制成的混合粒状物料。粒料在加工过程中可以减少对成型过程的要求,从而使成型易操作。The raw materials used in plastic molding in industry mainly include powder, granule, solution and dispersion. Part of the molding adopts monomer and prepolymer, and powder and granule are widely used. Powder is prepared by mixing and dispersing powdery raw material resin and various additives evenly. Granule is a mixed granular material made by plasticizing the powder and making it further plasticized by different methods. . The pellets can reduce the requirements for the molding process during processing, so that the molding is easy to operate.
在塑料造粒过程中,需要将粒料熔融后,再加入粉料进行熔融,然后造粒,整个生产过程需要两步成型,电费和人工成本较高,生产线长度也很长,占用厂房空间,提高了生产成本。此外,工人爬上高台,将粉料投放到分散釜内进行分散搅拌,由称重装置上称重,再与粒料一起按一定重量比例送入挤制机进行挤制。在粉料投放过程中会有大量的粉料飘散到空气中,一是会污染车间空气环境,二是原料会产生浪费,三是工人劳动强度大,多数车间会配备布袋除尘器对粉尘进行回收利用,但是需要工人定期从布袋除尘器的集尘袋中回收粉料予以利用,使用起来比较麻烦,尚待改进。In the process of plastic granulation, it is necessary to melt the granules, then add powder to melt, and then granulate. The entire production process requires two-step molding. Increased production costs. In addition, workers climb up the high platform, put the powder into the dispersing kettle for dispersion and stirring, weigh it on the weighing device, and then send it to the extruder together with the pellets in a certain weight ratio for extrusion. In the process of powder feeding, a large amount of powder will be scattered into the air. First, it will pollute the air environment of the workshop. Second, the raw materials will be wasted. Third, the labor intensity of workers is high. Most workshops will be equipped with bag dust collectors to recover dust. However, it requires workers to periodically recycle the powder from the dust bag of the bag filter for use, which is troublesome to use and needs to be improved.
发明内容SUMMARY OF THE INVENTION
本发明的目的是克服上述背景技术中的不足,提供一种无尘的塑料粒子生产线,能够自动完成粉料和粒料的上料,节约厂房空间,而且可以将粉尘进行回收利用,改善车间环境,减少原材料浪费,降低人生产成本和劳动强度。The object of the present invention is to overcome the deficiencies in the above-mentioned background technology, and provide a dust-free plastic particle production line, which can automatically complete the feeding of powder and pellets, save plant space, and can recycle dust and improve workshop environment. , reduce the waste of raw materials, reduce production costs and labor intensity.
本发明的技术目的是这样实现的:The technical purpose of the present invention is achieved in this way:
一种无尘的塑料粒子生产线,包括粉料支路、粒料支路和挤制机,其中,A dust-free plastic particle production line includes a powder branch, a pellet branch and an extruder, wherein,
所述粉料支路包括上粉机、分散釜、第一粉料斗、第二粉料斗、第一称重装置以及第二称重装置;上粉机的正面制有投料口,顶部设置有集尘罩,集尘罩的顶部通过管道与风机入口连接,风机出口通过集尘管分别连接两个粉尘分离器的第一入口,上粉机底部的出口通过第一螺旋输送机连接到分散釜顶部的入口,分散釜底部的出口通过第一气力输送机和第一输送管连接到两个粉尘分离器的第二入口;两个粉尘分离器分别设置在第一粉料斗和第二粉料斗的顶部,第一粉料斗底部的出口通过软连接与第一称重装置的入口连接,第一称重装置的出口通过软连接与第一出粉管连接,第二粉料斗底部的出口通过软连接与第二称重装置的入口连接,第二称重装置的出口通过软连接与第二出粉管连接;The powder branch circuit includes a powder feeding machine, a dispersion kettle, a first powder hopper, a second powder hopper, a first weighing device and a second weighing device; Dust hood, the top of the dust hood is connected to the inlet of the fan through a pipe, the outlet of the fan is connected to the first inlets of the two dust separators respectively through the dust collecting pipe, and the outlet at the bottom of the powder feeder is connected to the top of the dispersion kettle through the first screw conveyor The inlet at the bottom of the dispersion kettle is connected to the second inlet of the two dust separators through the first pneumatic conveyor and the first conveying pipe; the two dust separators are respectively arranged on the top of the first powder hopper and the second powder hopper , the outlet at the bottom of the first powder hopper is connected to the inlet of the first weighing device through a soft connection, the outlet of the first weighing device is connected to the first powder outlet pipe through a soft connection, and the outlet at the bottom of the second powder hopper is connected to the first powder through a soft connection. The inlet of the second weighing device is connected, and the outlet of the second weighing device is connected with the second powder outlet pipe through a soft connection;
所述粒料支路包括粒料仓、粒料斗以及第三称重装置,粒料仓底部的出口通过第二气力输送机和第二输送管连接到粒料斗顶部的进料口,粒料斗底部的出口通过软连接与第三称重装置的入口连接,第三称重装置的出口通过软连接与出粒管连接,出粒管的下部斜向下布置并且与第二出粉管的上段接通,第二出粉管的下段形成粉料和粒料的混合出料管;The pellet branch circuit includes a pellet silo, a pellet hopper and a third weighing device. The outlet at the bottom of the pellet silo is connected to the feed port at the top of the pellet hopper through a second pneumatic conveyor and a second conveying pipe. The outlet of the third weighing device is connected to the inlet of the third weighing device through a soft connection, and the outlet of the third weighing device is connected to the particle outlet pipe through a soft connection. The lower section of the second powder discharge pipe forms a mixed discharge pipe for powder and granules;
所述挤制机包括机座、安装在基座上的机筒、安装在机筒尾部的挤制模具,以及安装在机筒头部的机头,机筒具有两个上料口,第一个上料口位于机筒头部,与混合出料管连接,第二个上料口位于机筒中部,与螺旋输送机的出口连接,螺旋输送机的入口与第一出粉管连接。The extruder includes a machine base, a barrel installed on the base, an extrusion die installed at the tail of the barrel, and a head installed at the head of the barrel. The barrel has two feeding ports, the first One feeding port is located at the head of the barrel and is connected with the mixing discharge pipe, and the second feeding port is located in the middle of the barrel and is connected with the outlet of the screw conveyor, and the inlet of the screw conveyor is connected with the first powder outlet pipe.
作为优选,所述粉尘分离器包括由上至下依次连接的进粉段、过滤段以及出粉段,进粉段由支架固定支撑在第一或第二粉料斗上,并且制有所述第一、第二入口,过滤段采用圆筒状的过滤布制作,用于过滤粉尘和排出空气,出粉端的底部与第一或第二粉料斗顶部的入口连接。Preferably, the dust separator includes a powder feeding section, a filtering section and a powder discharging section which are connected in sequence from top to bottom, the powder feeding section is fixedly supported on the first or second powder hopper by a bracket, and the first or second powder hopper is made of 1. The second inlet, the filter section is made of cylindrical filter cloth, which is used to filter dust and discharge air. The bottom of the powder outlet is connected to the inlet on the top of the first or second powder hopper.
作为优选,所述第一、第二、第三称重装置均包括一个电子秤、一个第二螺旋输送机以及一个称重斗,第二螺旋输送机固定安装在电子秤上,第二螺旋输送机的出口作为称重装置的出口,第二螺旋输送机的入口与称重斗底部的出口固定连接,称重斗顶部的入口作为称重装置的入口。Preferably, the first, second and third weighing devices include an electronic scale, a second screw conveyor and a weighing bucket, the second screw conveyor is fixedly installed on the electronic scale, and the second screw conveyor is fixed on the electronic scale. The outlet of the machine is used as the outlet of the weighing device, the inlet of the second screw conveyor is fixedly connected with the outlet at the bottom of the weighing bucket, and the inlet at the top of the weighing bucket is used as the inlet of the weighing device.
作为优选,所述第一粉料斗、第二粉料斗、粒料斗以及称重斗的顶部均设置均有辅助排气口,该辅助排气口上罩盖有粉尘过滤器。Preferably, the tops of the first powder hopper, the second powder hopper, the pellet hopper and the weighing hopper are all provided with auxiliary exhaust ports, and the auxiliary exhaust ports are covered with dust filters.
作为优选,所述粉尘过滤器包括围绕辅助排气口设置的骨架,以及包覆在骨架顶面以及四周外壁的粉尘滤布。Preferably, the dust filter includes a frame arranged around the auxiliary exhaust port, and a dust filter cloth covered on the top surface of the frame and the surrounding outer walls.
作为优选,所述分散釜、第一粉料斗、第二粉料斗、第一称重斗和第二称重斗均设置有由电机驱动的搅拌轴,搅拌轴上设置有搅拌叶片。Preferably, the dispersion kettle, the first powder hopper, the second powder hopper, the first weighing hopper and the second weighing hopper are all provided with a stirring shaft driven by a motor, and a stirring blade is arranged on the stirring shaft.
作为优选,所述第一粉料斗、第二粉料斗以及粒料斗底部的出口分别设置有电动阀门。Preferably, the first powder hopper, the second powder hopper and the outlet at the bottom of the pellet hopper are respectively provided with electric valves.
作为优选,所述第一粉料斗、第二粉料斗以及粒料斗安装在第三层平台上;第一称重斗、第二称重斗以及第三称重斗安装在第二层平台上;上粉机、分散釜以及粒料仓安装在地面上。Preferably, the first powder hopper, the second powder hopper and the pellet hopper are installed on the third platform; the first weighing bucket, the second weighing bucket and the third weighing bucket are installed on the second platform; The powder feeding machine, dispersing kettle and pellet silo are installed on the ground.
作为优选,所述软连接采用卷曲成圆筒状的防尘布或者硅胶制作,防尘布或者硅胶的两端设置抱箍或者法兰。Preferably, the soft connection is made of a dustproof cloth or silica gel that is rolled into a cylindrical shape, and both ends of the dustproof cloth or silica gel are provided with hoops or flanges.
本发明与现有技术相比具有以下优点:Compared with the prior art, the present invention has the following advantages:
(1)本发明将粉料分成两次上料,第一次少量粉料与粒料混合,到机筒中间时,第一次加入的粉料和粒料已经在高温下全部或部分熔融,然后第二次加入粉料,粉料能够较好地与熔融的塑料混合,并在机筒后段完全熔融,只需要一条生产线,节约了电费和人工成本,也节约了厂房的空间,降低了生产成本。(1) the present invention divides the powder into two feedings, the first time a small amount of powder is mixed with the granules, and when reaching the middle of the barrel, the powder and the granules added for the first time have been fully or partially melted at high temperature, Then the powder is added for the second time. The powder can be well mixed with the molten plastic and completely melted at the back of the barrel. Only one production line is needed, which saves electricity and labor costs, and saves the space of the workshop and reduces the cost of production. Cost of production.
(2)本发明可以实现粉料和粒料的自动上料和自动称重,降低工人劳动强度,工人投料时产生的粉尘可以被集尘罩收集,由风机抽走送入粉尘分离器,过滤布排出空气后使粉尘可以重新利用,粉尘过滤器可以辅助粉斗排气和过滤粉尘,可以避免车间内粉尘弥漫,改善车间的生产环境,保障工人的呼吸系统健康,减少原材料浪费,节约成本。(2) The present invention can realize automatic feeding and automatic weighing of powders and granules, reduce the labor intensity of workers, and the dust generated by workers when feeding materials can be collected by the dust collecting hood, and then pumped away by the fan and sent to the dust separator for filtering. After the air is discharged, the dust can be reused. The dust filter can assist the powder hopper to exhaust and filter the dust, which can avoid the dust in the workshop, improve the production environment of the workshop, ensure the health of the workers' respiratory system, reduce the waste of raw materials, and save costs.
附图说明Description of drawings
图1是本发明的结构示意图。Figure 1 is a schematic structural diagram of the present invention.
具体实施方式Detailed ways
下面结合说明书附图,对本发明作进一步说明,但本发明并不局限于以下实施例。The present invention will be further described below with reference to the accompanying drawings, but the present invention is not limited to the following embodiments.
如图1所示,一种无尘的塑料粒子生产线,包括粉料支路、粒料支路、挤制机以及控制单元(可以商购工控机或者PLC控制器)。As shown in Figure 1, a dust-free plastic particle production line includes a powder branch, a pellet branch, an extruder and a control unit (a commercial industrial computer or a PLC controller can be purchased).
所述粉料支路包括上粉机2、分散釜7、第一粉料斗16.1、第二粉料斗16.2、第一称重装置以及第二称重装置。上粉机的正面制有投料口1,工人可以从投料口将成袋的粉料倒入上粉机内,无需登高。上粉机的顶部设置有集尘罩3,集尘罩的顶部通过管道与风机18的入口连接,风机的出口通过末端分叉的集尘管19分别连接两个粉尘分离器的第一入口,在风机的作用下,集尘罩收集的粉尘通过集尘管送入两个粉尘分离器。上粉机底部的出口通过第一螺旋输送机6(现有成熟设备)连接到分散釜顶部的入口,将工人投入的粉料送入分散釜内。The powder branch circuit includes a powder feeding machine 2, a dispersion kettle 7, a first powder hopper 16.1, a second powder hopper 16.2, a first weighing device and a second weighing device. There is a feeding port 1 on the front of the powder feeding machine, and workers can pour the bagged powder into the powder feeding machine from the feeding port without climbing. The top of the dust collector is provided with a dust collecting hood 3. The top of the dust collecting hood is connected to the inlet of the fan 18 through a pipe, and the outlet of the fan is connected to the first inlets of the two dust separators respectively through the dust collecting pipes 19 with bifurcated ends. Under the action of the fan, the dust collected by the dust collecting hood is sent to the two dust separators through the dust collecting pipe. The outlet at the bottom of the powder feeding machine is connected to the inlet at the top of the dispersion kettle through the first screw conveyor 6 (existing mature equipment), and the powder input by the workers is fed into the dispersion kettle.
分散釜底部的出口通过第一气力输送机9(现有成熟设备)和末端分叉的第一输送管10连接到两个粉尘分离器的第二入口。两个粉尘分离器分别设置在第一粉料斗和第二粉料斗的顶部,第一粉料斗底部的出口设置有电动阀门25(现有成熟设备),并且通过软连接26与第一称重装置的入口连接,第一称重装置的出口通过软连接26与第一出粉管30.1连接。第二粉料斗底部的出口设置有电动阀门25,并且通过软连接26与第二称重装置的入口连接,第二称重装置的出口通过软连接26与第二出粉管30.2连接。The outlet at the bottom of the dispersion kettle is connected to the second inlet of the two dust separators through a first pneumatic conveyor 9 (existing mature equipment) and a first delivery pipe 10 with a bifurcated end. Two dust separators are respectively arranged on the top of the first powder hopper and the second powder hopper, the outlet at the bottom of the first powder hopper is provided with an electric valve 25 (existing mature equipment), and is connected with the first weighing device through a soft connection 26. The inlet of the first weighing device is connected to the first powder outlet pipe 30.1 through the flexible connection 26. The outlet at the bottom of the second powder hopper is provided with an electric valve 25, and is connected to the inlet of the second weighing device through a soft connection 26, and the outlet of the second weighing device is connected to the second powder outlet pipe 30.2 through the soft connection 26.
所述粒料支路包括粒料仓23、粒料斗20以及第三称重装置。粒料仓底部的出口通过第二气力输送机24和第二输送管22连接到粒料斗顶部的进料口21,粒料斗底部的出口设置有电动阀门25,并且通过软连接26与第三称重装置的入口连接,第三称重装置的出口通过软连接26与出粒管30.3连接,出粒管的下部斜向下布置并且与第二出粉管30.2的上段接通,第二出粉管的下段形成粉料和粒料的混合出料管30.4;The pellet branch includes a pellet bin 23, a pellet hopper 20 and a third weighing device. The outlet at the bottom of the pellet silo is connected to the feed port 21 at the top of the pellet hopper through the second pneumatic conveyor 24 and the second conveying pipe 22. The outlet at the bottom of the pellet hopper is provided with an electric valve 25, and is connected to the third scale through a soft connection 26. The inlet of the weighing device is connected, the outlet of the third weighing device is connected with the granule outlet pipe 30.3 through the soft connection 26, the lower part of the granule outlet pipe is arranged obliquely downward and is connected with the upper section of the second powder outlet pipe 30.2, the second powder outlet pipe 30.2 is connected. The lower section of the pipe forms a mixed discharge pipe 30.4 for powder and granules;
所述挤制机包括机座31、安装在基座上的机筒34、安装在机筒尾部的挤制模具35,以及安装在机筒头部的机头32,机筒具有两个上料口,第一个上料口位于机筒头部,与混合出料管30.4连接,第二个上料口位于机筒中部,与螺旋输送机33的出口连接,螺旋输送机的入口与第一出粉管30.1连接。The extruder includes a machine base 31, a barrel 34 installed on the base, an extrusion die 35 installed at the tail of the barrel, and a head 32 installed at the head of the barrel. The barrel has two feeding The first feeding port is located at the head of the barrel and is connected to the mixing discharge pipe 30.4. The second feeding port is located in the middle of the barrel and is connected to the outlet of the screw conveyor 33. The inlet of the screw conveyor is connected to the first The powder outlet pipe 30.1 is connected.
所述粉尘分离器包括由上至下依次连接的进粉段11、过滤段12以及出粉段14,进粉段由支架13固定支撑在第一或第二粉料斗上,并且制有所述第一、第二入口,过滤段采用圆筒状的过滤布制作,用于过滤粉尘和排出空气,出粉段的底部与第一或第二粉料斗顶部的入口连接。The dust separator includes a powder feed section 11, a filter section 12 and a powder output section 14 which are connected in sequence from top to bottom. The powder feed section is fixedly supported on the first or second powder hopper by a bracket 13, and the For the first and second inlets, the filter section is made of cylindrical filter cloth, which is used to filter dust and discharge air. The bottom of the powder outlet section is connected to the inlet of the top of the first or second powder hopper.
所述第一、第二、第三称重装置均包括一个电子秤29(工业用电子秤,可以外购获得,不作详细介绍)、一个第二螺旋输送机28以及一个称重斗27,第二螺旋输送机固定安装在电子秤上,第二螺旋输送机的出口作为称重装置的出口,第二螺旋输送机的入口与称重斗底部的出口固定连接,称重斗顶部的入口作为称重装置的入口。The first, second, and third weighing devices all include an electronic scale 29 (an industrial electronic scale, which can be purchased and not described in detail), a second screw conveyor 28 and a weighing bucket 27. The second screw conveyor is fixedly installed on the electronic scale, the outlet of the second screw conveyor is used as the outlet of the weighing device, the inlet of the second screw conveyor is fixedly connected with the outlet at the bottom of the weighing bucket, and the inlet at the top of the weighing bucket is used as the weighing device. Entrance to heavy equipment.
所述第一粉料斗、第二粉料斗、粒料斗以及称重斗的顶部均设置均有辅助排气口,该辅助排气口上罩盖有粉尘过滤器17。所述粉尘过滤器17包括围绕辅助排气口设置的骨架,以及包覆在骨架顶面以及四周外壁的粉尘滤布。The tops of the first powder hopper, the second powder hopper, the pellet hopper and the weighing hopper are all provided with auxiliary exhaust ports, and the auxiliary exhaust ports are covered with a dust filter 17 . The dust filter 17 includes a frame arranged around the auxiliary exhaust port, and a dust filter cloth covering the top surface of the frame and the surrounding outer walls.
所述分散釜、第一粉料斗、第二粉料斗、第一称重斗和第二称重斗均设置有由电机8驱动的搅拌轴4,搅拌轴上设置有搅拌叶片5。粒料无需搅拌,所以粒料斗以及第三称重斗不设置搅拌叶片。The dispersion kettle, the first powder hopper, the second powder hopper, the first weighing hopper and the second weighing hopper are all provided with a stirring shaft 4 driven by a motor 8, and a stirring blade 5 is arranged on the stirring shaft. The pellets do not need to be stirred, so the pellet hopper and the third weighing hopper do not have stirring blades.
所述第一粉料斗、第二粉料斗以及粒料斗安装在第三层平台15.1上;第一称重斗、第二称重斗以及第三称重斗安装在第二层平台15.2上;上粉机、分散釜以及粒料仓安装在地面上。利用粉料和粒料的重力,从各粉料斗和粒料斗进入各称重斗,再进入各出粉管和出粒管。The first powder hopper, the second powder hopper and the granular hopper are installed on the third platform 15.1; the first weighing bucket, the second weighing bucket and the third weighing bucket are installed on the second platform 15.2; The powder machine, dispersing kettle and pellet silo are installed on the ground. Using the gravity of the powder and granules, it enters each weighing hopper from each powder hopper and granule hopper, and then enters each powder outlet and granule outlet.
所述软连接采用卷曲成圆筒状的防尘布或者硅胶制作,防尘布或者硅胶的两端设置用于连接的抱箍或者法兰。一般地,防尘布和硅胶的轴向长度大于需要连接的距离,因此可以使两个被连接的部件之间产生一段相对位移而连接部位不受影响。The soft connection is made of a dustproof cloth or silica gel that is curled into a cylindrical shape, and both ends of the dustproof cloth or silica gel are provided with hoops or flanges for connection. Generally, the axial length of the dustproof cloth and the silica gel is greater than the distance to be connected, so a relative displacement can be generated between the two connected parts without affecting the connection part.
所述机头、风机、各螺旋输送机、各气力输送机、电机、电动阀门以及电子秤均与控制单元电连接并受其控制。粉料出料管、粉料支管以及粒料支管每次的原料量根据需要确定,具体可由第一、第二、第三称重装置控制。在实际生产过程中,第一次加入50%重量的粒料和30%重量的粉料,第二次加入20%重量的粉料,造出的塑料粒子质量符合要求。The machine head, fan, screw conveyors, pneumatic conveyors, motors, electric valves and electronic scales are all electrically connected to and controlled by the control unit. The amount of raw materials in the powder discharge pipe, the powder branch pipe and the granular material branch pipe is determined according to needs, and can be specifically controlled by the first, second and third weighing devices. In the actual production process, 50% by weight of pellets and 30% by weight of powder are added for the first time, and 20% by weight of powder is added for the second time, and the quality of the produced plastic particles meets the requirements.
本发明的工作原理是:在风机的负压作用下,粉尘向着集尘罩内汇集,经集尘管送入粉尘分离器,空气从过滤布的网孔排出,粉尘在过滤布的作用下被留下,汇集到出粉段之后进入第一粉料斗或第二粉料斗;粉料经过第一螺旋输送机送到分散釜进行分散后,通过第一气力输送机送到两个粉尘分离器内,分离空气后进入第一粉料斗或第二粉料斗,与回收的粉料搅拌均匀,搅拌时产生的粉尘以及过滤布未及时排出的空气可以由粉尘过滤器过滤和辅助排气;The working principle of the invention is as follows: under the action of the negative pressure of the fan, the dust is collected in the dust collecting hood, and sent to the dust separator through the dust collecting pipe, the air is discharged from the mesh of the filter cloth, and the dust is removed by the filter cloth under the action of the filter cloth. Leave it, collect it into the powder discharge section, and then enter the first powder hopper or the second powder hopper; the powder is sent to the dispersing kettle through the first screw conveyor for dispersion, and then sent to the two dust separators through the first pneumatic conveyor , after the air is separated, it enters the first powder hopper or the second powder hopper, and mixes with the recovered powder evenly. The dust generated during stirring and the air not discharged by the filter cloth in time can be filtered and assisted by the dust filter;
粒料经过第二气力输送机送到粒料斗后,空气从粉尘过滤器排出,粒料存储在粒料斗内;After the pellets are sent to the pellet hopper through the second pneumatic conveyor, the air is discharged from the dust filter, and the pellets are stored in the pellet hopper;
各电动阀门打开口,根据挤制机预先设定的粉料用量,粉料进入第一称重装置和第二称重装置的称重斗,粒料进入第三称重装置的称重斗,由电子秤对粉料和粒料分别进行称重,达到预定重量时电动阀们关闭,各第二螺旋输送机开启,将第二粉料斗16.2对接的称重斗内的粉料送到第二出粉管30.2,将粒料斗20对接的称重斗内的粒料送到出粒管30.3,粉料与粒料进入混合出料管30.4进行第一次上料,将第一粉料斗16.1对接的称重斗内的粉料送到第一出粉管30.1进行二次上料,最终从挤制模具挤出塑料粒子。The openings of each electric valve are opened. According to the pre-set amount of powder in the extruder, the powder enters the weighing hoppers of the first weighing device and the second weighing device, and the pellets enter the weighing hopper of the third weighing device. The powder and pellets are weighed separately by the electronic scale. When the predetermined weight is reached, the electric valves are closed, and the second screw conveyors are opened, and the powder in the weighing hopper connected to the second powder hopper 16.2 is sent to the second powder hopper 16.2. The powder outlet pipe 30.2 sends the pellets in the weighing hopper connected to the pellet hopper 20 to the pellet outlet pipe 30.3, the powder material and the pellets enter the mixing outlet pipe 30.4 for the first feeding, and the first powder hopper 16.1 is docked The powder in the weighing hopper is sent to the first powder outlet pipe 30.1 for secondary feeding, and finally the plastic particles are extruded from the extrusion die.
需要说明的是,由于称重装置的入口和出口设置的均是软连接,相当于将电子秤与其余部件隔离,电子秤秤出来的重量变化即是称重斗内粉料或者粒料的重量。It should be noted that since the inlet and outlet of the weighing device are both set with soft connections, which is equivalent to isolating the electronic scale from the rest of the components, the weight change from the electronic scale is the weight of the powder or pellets in the weighing hopper. .
以上所述仅为本发明的优选实施例,对于本领域的技术人员来说,本发明可以有各种更改和变化。凡在本发明的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。The above descriptions are only preferred embodiments of the present invention, and for those skilled in the art, the present invention may have various modifications and variations. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present invention shall be included within the protection scope of the present invention.
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