CN209775216U - Granule material compounding and material drying processing apparatus - Google Patents
Granule material compounding and material drying processing apparatus Download PDFInfo
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- CN209775216U CN209775216U CN201920399550.3U CN201920399550U CN209775216U CN 209775216 U CN209775216 U CN 209775216U CN 201920399550 U CN201920399550 U CN 201920399550U CN 209775216 U CN209775216 U CN 209775216U
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- 239000000463 material Substances 0.000 title claims abstract description 187
- 238000001035 drying Methods 0.000 title claims abstract description 28
- 238000013329 compounding Methods 0.000 title claims abstract description 27
- 239000008187 granular material Substances 0.000 title claims description 6
- 238000003860 storage Methods 0.000 claims abstract description 54
- 238000007599 discharging Methods 0.000 claims abstract description 29
- 238000003756 stirring Methods 0.000 claims abstract description 27
- 230000007246 mechanism Effects 0.000 claims abstract description 6
- 238000009826 distribution Methods 0.000 claims description 25
- 238000005303 weighing Methods 0.000 claims description 20
- 230000001105 regulatory effect Effects 0.000 claims description 17
- 239000011236 particulate material Substances 0.000 claims 9
- 235000011194 food seasoning agent Nutrition 0.000 claims 4
- 239000002245 particle Substances 0.000 abstract description 9
- 238000001746 injection moulding Methods 0.000 abstract description 5
- 239000000203 mixture Substances 0.000 abstract description 5
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 238000000034 method Methods 0.000 description 9
- 230000008569 process Effects 0.000 description 8
- 238000005516 engineering process Methods 0.000 description 6
- 230000005484 gravity Effects 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 3
- 101100372509 Mus musculus Vat1 gene Proteins 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 230000006870 function Effects 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 206010063385 Intellectualisation Diseases 0.000 description 1
- 229920000426 Microplastic Polymers 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
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Abstract
The utility model relates to the technical field of injection molding processing, and discloses a particle material mixing and drying processing device, which comprises a mixing barrel and a plurality of storage barrels, wherein an air inlet of the mixing barrel is communicated with a hot air mechanism; a plurality of groups of mixing augers for stirring materials are arranged in the mixing barrel; the discharge gate of every storage vat all communicates with the feed inlet of compounding bucket, and the discharge gate department of storage vat all is equipped with unloading control unit, and unloading control unit is including the governing valve that is located the regulation material unloading speed of storage vat discharge gate department. According to the scheme, the discharging speed of the material corresponding to the discharging port of the storage barrel is adjusted by the adjusting valve according to the mixing proportion of a plurality of materials, so that the proportion of different material discharging speeds is the same as the mixing proportion; the proportion of the materials entering the mixing barrel in the same time is the same as the mixing proportion, the batching precision is high, manual proportioning is not needed, and the labor intensity of people is reduced; and the processing device can simultaneously mix and dry materials, so that the production efficiency is improved.
Description
Technical Field
The utility model relates to an injection-molded technology field, concretely relates to granule material compounding and material drying processing apparatus.
Background
The raw materials for injection molding are rubber particle materials or plastic particle materials, and before injection molding, the particle materials are dried (namely, material drying) and different materials are uniformly mixed (namely, material mixing) according to requirements. The existing mixing equipment has the disadvantages of uneven mixing and serious material layering. Some small factories even adopt manual work to mix a large amount of materials, or use mixing equipment to mix the materials, and then use manual work or pneumatic conveying to an injection molding machine, and the materials generally generate the layering phenomenon in the conveying process. Batch formula gravity mixes material system and adopts unique agitator a plurality of kilograms of minibatches of production material subdivision, and the cooperation manual input stirring time makes the material misce bene, and the material after the mixture directly produces, and this mechanism function singleness simple structure, efficiency is not high, can't satisfy quick and violent market competition.
For example, the chinese patent publication No. CN104589531B provides a mixing device, which can mix old materials with new materials, but the materials are easy to stack and difficult to mix uniformly. For example, chinese utility model patent publication No. CN207669663U provides an intelligent injection molding feeding and drying apparatus, which uses a heater for drying, and a stirrer is provided in a storage bin, but the material is accumulated due to the gravity of the material; and the energy loss in the process of drying the materials is large, the time for drying the materials is too long, and the mixing of various different materials cannot be realized.
In summary, the prior art mainly has the following problems: 1) the material mixing device cannot dry materials, the material drying device cannot mix materials, and the function is single; 2) the mixing device cannot solve the problem of batching in the production process, multiple materials need to be manually proportioned, the time and the labor are consumed, and the use amount of each material needs to be manually determined; 3) when the material drying device dries materials, the materials are accumulated, the energy loss in the material drying process is large, and the material drying time is too long.
SUMMERY OF THE UTILITY MODEL
The utility model provides a granule material compounding and dry by fire material processing apparatus can carry out the compounding simultaneously and dry by fire the material to solve the unable compounding of current material dryer, the unable problem of drying by fire the material of current blendor.
In order to achieve the above purpose, the utility model adopts the following technical scheme: a particle material mixing and drying processing device comprises a mixing barrel and a plurality of material storage barrels; the mixing barrel is vertically arranged, and is provided with a feeding hole, a discharging hole, an air inlet and an air outlet; the air inlet of the mixing barrel is communicated with a hot air mechanism; at least one group of material mixing auger for stirring materials is arranged in the material mixing barrel, the material mixing auger can rotate relative to the material mixing barrel, and each group of material mixing auger comprises a plurality of blades which are circumferentially arranged; the discharge gate of every storage vat all communicates with the feed inlet of compounding bucket, and the discharge gate department of storage vat all is equipped with unloading control unit.
In the technical scheme, a plurality of different materials (a plurality of particle materials) are firstly arranged in the material storage barrel, and the proportion of the different materials entering the material mixing barrel is controlled by the material discharge control unit according to the mixing proportion of the materials. After the materials enter the mixing barrel, the mixing auger stirs the materials to achieve the purpose of mixing. Meanwhile, hot air of the hot air mechanism enters the mixing barrel and enters a gap between the material and the material to exchange heat with the material, and the material is dried. Compare and dry by fire material and compounding and go on respectively in two equipment, this processing apparatus can compounding simultaneously and dry by fire the material, improves production efficiency.
Further, the blanking amount control unit comprises an electric adjusting valve which is arranged at the discharge port of the storage barrel and used for adjusting the blanking speed of the material. The blanking speed of the materials in the corresponding storage barrel is adjusted through an adjusting valve, so that the proportion of the blanking speed of each material is the same as the mixing proportion; the proportion that the material got into the compounding bucket in the same time is the same with the mixture ratio, and the batching precision is high, and need not artifical ratio, reduces people's intensity of labour.
Further, the blanking amount control unit also comprises a controller and a weighing container which is positioned below the discharge hole of the storage barrel and corresponds to the storage barrel; the weighing containers are internally provided with weight sensors, the output ends of the weight sensors are connected with the first input ends of the corresponding weight comparators, the second input ends of the weight comparators are connected with the threshold value storage, and the first output ends of the controllers are correspondingly connected with the control ends of the regulating valves; the bottom of the weighing container is provided with a feed opening, the feed opening is provided with a feed electromagnetic valve, and the control end of the feed electromagnetic valve is connected with the second output end of the controller.
The controller, the threshold value memory, the weight sensor and the gravity comparator are arranged, so that specific names of various materials can be preset, and meanwhile, the weight ratio among various particle materials of the product is preset. The weight value that the gravity comparator will weigh the sensor and record is compared with the default, and when being equal with the default, controller control governing valve closed, stops the unloading, and the unloading solenoid valve of controller control is opened simultaneously, and the material that needs to mix and dry gets into in the compounding bucket. This scheme is through weighing to the material accuracy to contrast with the default, improve weight ratio accuracy.
Furthermore, the blanking amount control unit also comprises a color sensor corresponding to the storage barrel, and the input end of the color sensor is connected with the color control end of the controller; the output end of the color sensor is connected with the control input end of the controller regulating valve.
The color of various materials is preset, the specific name of the materials is identified through the color sensor, then the materials are proportioned according to the preset proportion of the various materials, the materials can be automatically identified, the automatic proportioning according to the color is realized, and the intelligent automatic proportioning device is more intelligent.
Furthermore, a discharging auger which can rotate relative to the discharging port is arranged at the discharging port of the mixing barrel. After the material is conveyed by the discharging auger, the material can be prevented from being stacked and blocked when being discharged from a discharge port of the mixing barrel.
Furthermore, a stirring motor with double output shafts is arranged in the mixing barrel, one output shaft of the stirring motor is coaxially connected with the mixing auger, and the other output shaft of the stirring motor is coaxially connected with the discharging auger.
Therefore, the mixing auger and the discharging auger can be simultaneously rotated by only one power source, and the volume of the processing device is reduced; when mixing materials, the discharging auger idles, and the energy consumption is low.
Further, the lower part of the mixing barrel is provided with a discharge hopper, and an air distribution plate protruding upwards is arranged in the discharge hopper; the air distribution plate is provided with a plurality of first air vents; the air distribution plate is provided with a discharge opening, and a discharge electromagnetic valve is arranged at the discharge opening; the air inlet of the mixing barrel is positioned below the air distribution plate.
The discharge hopper is arranged to facilitate discharging, and compared with the air distribution plate arranged above the discharge hopper, the air distribution plate arranged in the discharge hopper can reduce the area of the air distribution plate and simultaneously enable the mixing flood space of the mixing barrel to be larger; the air distribution plate protrudes upwards, so that hot air below the air distribution plate is sprayed into all parts in the mixing barrel in a divergent manner, rather than being sprayed into the middle or the edge of the mixing barrel.
Further, still be equipped with vibrating device in the compounding bucket, vibrating device include with the gasbag of the air intake intercommunication of compounding bucket, be equipped with a plurality of vertical hollow on the gasbag and with the vibration branch pipe of gasbag intercommunication, be equipped with a plurality of second ventholes on the vibration branch pipe.
And part of hot air output by the hot air mechanism is conveyed to the vibration branch pipe through the air bag and then discharged through a second vent hole on the vibration branch pipe to dry the materials. In the material mixing process, the vibration branch pipe collides with the material to vibrate, so that the material is further stirred, and the material mixing efficiency is improved. And when the vibration branch pipe swings, the direction of hot air discharged from the second vent hole of the vibration branch pipe also changes, so that certain disturbance effect is exerted on the hot air in the mixing barrel, the hot air reaches all corners of the mixing barrel, the mixing barrel is covered comprehensively, and the drying is more uniform.
Furthermore, a plurality of storage barrels are respectively connected with a material suction device. The material is directly sucked into each storage barrel through the adsorption force of the material sucking device, the material is not required to be manually added into each storage barrel, and the labor intensity of people is reduced.
Furthermore, a discharge electromagnetic valve is arranged at the discharge outlet of the mixing barrel. Set up ejection of compact solenoid valve, be convenient for open the discharge gate after material is dried and the misce bene, need not the manual work and open convenient operation.
Compared with the prior art, the beneficial effects of the utility model are as follows:
(1) A blanking amount control unit is arranged, and two types, three types, four types and more than four types of different particle materials can be proportioned according to different processing technologies; through colour discernment and weight ratio, the ratio precision is high, and need not artifical batching, has reduced people's intensity of labour.
(2) The stirring auger and the vibrating device interact with each other, so that the gap between the granular materials is enlarged, the drying efficiency of the plastic granules is increased, and the heating energy consumption is reduced; the combination of the two can fully stir the material and fine avoidance material layering piles up the phenomenon, improves compounding efficiency.
(3) The arrangement of the air distribution plate enables hot air to be more dispersed in the material barrel, so that the drying is more uniform; the hot air discharged from the second vent hole of the vibration branch pipe has certain disturbance effect on the hot air in the mixing barrel, so that the hot air reaches all corners of the mixing barrel, the mixing barrel is comprehensively covered, and the drying is more uniform.
Drawings
Fig. 1 is a schematic structural view of the material mixing and drying discharging device of the utility model.
Fig. 2 is a schematic top view of the storage bin of fig. 1.
Detailed Description
The present invention will be described in further detail with reference to the following embodiments:
reference numerals in the drawings of the specification include: the device comprises a mixing barrel 1, a discharge hopper 11, a discharge port 12, a discharge auger 13, a discharge electromagnetic valve 14, a storage barrel 2, an adjusting valve 21, a leakage pipe 22, a weighing container 23, a material suction device 24, a mixing auger 31, a stirring motor 32, an air distribution plate 4, a discharge electromagnetic valve 41, an air bag 5, a vibration branch pipe 51, a hot air blower 6, an air inlet pipeline 61, a display device 7 and an operation display 71.
Example one
This embodiment is substantially as shown in fig. 1: a particle material mixing and drying processing device comprises a mixing barrel 1 and a plurality of material storage barrels 2. The mixing barrel 1 is vertically arranged, preferably in a cylindrical shape, and a feed inlet, a discharge outlet 12, an air inlet and an air outlet (not shown in the figure) are arranged on the mixing barrel 1. Storage vat 2 is located the top of drying by the fire the storage vat, and this embodiment explains with the quantity of storage vat 2 as four, and it can be known with fig. 2 that four storage vats 2 are whole for cylindric appearance, all is connected with on every storage vat 2 and inhales glassware 24, through inhaling during glassware 24's adsorption affinity is direct inhales the material respectively every storage vat 2, and need not the manual work and add the material to in every storage vat 2.
The discharge gate of every storage vat 2 all is located compounding bucket 1, and hopper-shaped is leaked to the lower part of storage vat 2, is convenient for the unloading to compounding bucket 1 in from this. Of course, the storage vat 2 can be arranged at a place far away from the mixing vat 1, and the discharge hole of the storage vat 2 is communicated with the feed inlet of the mixing vat 1 through a pipeline. The discharge gate department of storage vat 2 all is equipped with unloading control unit, and unloading control unit is including the governing valve 21 that is located the regulation unloading speed of storage vat 2 discharge gate department, and governing valve 21 is the motorised valve.
The feeding amount control unit further comprises a controller and four weighing containers 23 corresponding to the storage barrel 2 and located below the discharge port 12 of the storage barrel 2, each weighing container 23 is a quarter-cylinder container, and the weighing containers 23 are connected with the storage barrel 2 through material leaking pipes 22. The weighing containers 23 are provided therein with weight sensors (not shown in the drawings) and weight comparators corresponding to the weight sensors one to one. The output end of the weight sensor is connected with the first input end of the corresponding weight comparator, the second input end of the weight comparator is connected with the threshold value (which can be a preset value or a numerical value input by the controller) memory, the output end of the weight comparator is connected with the controller, and the first output end of the controller is correspondingly connected with the control end of the regulating valve 21. The control of the regulating valve 21 is realized through the output result of the weight comparator, for example, when the weight comparator outputs a high level signal (for example, it indicates that the weight has not reached a preset value), the controller controls the regulating valve 21 to continue to open after receiving the high level signal; when the weight comparator outputs a low level signal (e.g., indicating that the weight has reached a predetermined value), the controller receives the low level signal and controls the regulating valve 21 to close.
In the present embodiment, each storage vat is further provided with a color sensor (not shown in the figure), and an input end of the color sensor is connected with a color control end of the controller; the output end of the color sensor is connected with the control end of the regulating valve of the controller. During specific implementation, the color sensor can be started by a color control end of the controller, an output end of the color sensor is connected with a control input end of a regulating valve of the controller, the color sensor transmits a return receipt signal back, and the controller controls the corresponding regulating valve 21 to be opened.
In the embodiment, the controller can adopt a cortex-m3 series single chip microcomputer, and the storage and calling of the process data are realized through the single chip microcomputer technology. The adjusting valve 21 is preferably a YJD-B-12 star-type electric ash discharging valve of zhejiang shi valve ltd, and it is needless to say that a pneumatic flow adjusting valve (a structure of a cylinder, a piston and a return spring) or a hydraulic flow adjusting valve (a structure of a double-piston rod) can be used to adjust the blanking speed of the material in the storage vat, which are the prior art and will not be described herein again. The weight sensor is preferably FP201A-K23-L20A B pressure sensor manufactured by Yokogawa electric corporation, Japan. The weight comparator is preferably of the type pp-700-5 from Airtrol, usa. The color sensor is preferably a loose look color scale sensor series, and the specific model is LX-101.
The bottom of the weighing container is provided with a feed opening, a feed electromagnetic valve (not shown in the figure) is arranged at the feed opening, and the control end of the feed electromagnetic valve is connected with the second output end of the controller. The four weighing containers 23 can share one blanking electromagnetic valve, each weighing container 23 can also be independently provided with the blanking electromagnetic valve, the drift diameter of each blanking electromagnetic valve is large, and materials can rapidly enter the mixing barrel 1. The blanking electromagnetic valve is a conventional on-off electromagnetic valve, and the model of the blanking electromagnetic valve is not specifically selected here.
The lower part of compounding bucket 1 is equipped with conical discharge hopper 11, and the joint has upwards convex air distribution plate 4 on the inner wall of this discharge hopper 11, and air distribution plate 4's shape can be for the toper as shown in fig. 1, also can be upwards convex circular-arc, is equipped with a plurality of first ventilation holes on the air distribution plate 4. The edge low position of the air distribution plate 4 is provided with a discharge opening, the discharge opening is provided with a discharge electromagnetic valve 41, the discharge electromagnetic valve is also a conventional on-off electromagnetic valve, and the model of the discharge electromagnetic valve is not explained here. The air intake of compounding bucket 1 is located the below of this air distribution plate 4, and the air intake intercommunication of compounding bucket 1 has air heater 6 to construct, and air heater 6 constructs including air heater 6, also can add the structure of heating the heating wire for the fan certainly, and it is prior art and does not describe herein again here. The hot air blower 6 is positioned outside the mixing barrel 1, and an air outlet of the hot air blower is communicated with an air inlet of the mixing barrel 1 through an air inlet pipeline 61.
At least one group of material mixing packing augers 31 for stirring materials are arranged in the material mixing barrel 1, three groups of material mixing augers 31 are arranged in the figure 1, and each group of material mixing augers 31 comprises a plurality of blades arranged in the circumferential direction, preferably in a spiral shape. A variable-frequency stirring motor 32 with double output shafts is fixedly arranged below the air distribution plate 4, the stirring motor 32 is connected with the inner wall of the discharge hopper 11 through a support, an output shaft at the upper end of the stirring motor 32 is coaxially connected with the mixing auger 31 through a rotating shaft, a through hole is formed in the center of the air distribution plate 4, and the rotating shaft at the upper end of the stirring motor 32 penetrates through the through hole and can rotate relative to the through hole; the output shaft at the lower end of the stirring motor 32 is also coaxially connected with a discharging auger 13 through a rotating shaft, and the discharging auger 13 is a spiral conveying blade and is positioned above the discharging port 12 of the mixing barrel 1. A discharge electromagnetic valve 14 is further arranged at the discharge port 12 of the mixing barrel 1, and the discharge electromagnetic valve 14 is also a conventional on-off electromagnetic valve, and the type of the on-off electromagnetic valve is not described herein.
Still be equipped with vibrating device in the compounding bucket 1, vibrating device includes the gasbag 5 through the air intake intercommunication of pipeline with compounding bucket 1, 5 whole circles of the establishing of gasbag are on the inner wall of discharge hopper 11, be equipped with a plurality of vertical hollow on the gasbag 5 and with the vibration branch pipe 51 of gasbag 5 intercommunication, for example six vibration branch pipes 51, be equipped with a plurality of second ventholes on the vibration branch pipe 51.
In this embodiment, a display device 7 is further provided, specifically and independently provided or provided on the side wall of the mixing barrel 1, the display device 7 includes a touchable operation display 71, and the controller, the weight comparator, the threshold value memory, the stirring motor 32 and the air heater 6 are all electrically connected with the operation display 71. Thereby, operations are performed by the operation display 71, such as: presetting material color, presetting material weight ratio, starting and stopping the stirring motor 32 or the hot air blower 6, and the like. The specific control method can adopt the existing automatic display technology, and is not described herein.
The specific implementation process is as follows: the four materials are mixed and dried for explanation, and the material suction device 24 sucks the four materials into the four material storage barrels 2 respectively. Initially all regulating valves 21 are closed, the air heater 6 is opened and the temperature of the hot air is regulated, while the stirring motor 32 is started. For example, the weight of the four materials is set to be 10Kg, and if the mixing ratio of the four materials to the weight of the four materials is 2:4:2:6, the corresponding masses are 20Kg, 40Kg, 20Kg and 60Kg respectively; the controller enables the regulating valves 21 to be electrified and opened, and simultaneously correspondingly regulates the rotating speed of the regulating valves 21, so that the material discharging speed ratio of the materials in the material storage barrels 2 is 2:4:2:6, and the materials in the four material storage barrels 2 basically enter the corresponding weighing containers 23 at the same time. After the material enters the weighing container 23, the weight of the material is detected by the weight sensors, and the weight comparator compares the detection values of the four weight sensors with preset values of 10Kg, 20Kg, 10Kg and 30Kg respectively; after the materials in the four weighing containers 23 all reach the preset values, the controller enables the regulating valve 21 to be powered off and closed, meanwhile, the blanking electromagnetic valves in the weighing containers 23 are powered on and opened, and the four materials enter the mixing barrel 1.
The stirring motor 32 rotates, the stirring motor 32 enables the mixing auger 31 to rotate, the mixing auger 31 stirs materials in the mixing barrel 1, and the blades of the mixing auger 31 are spiral, so that after the materials spirally move upwards, the materials fall due to gravity, and the circulation is carried out, and the purpose of uniformly mixing the materials is achieved. Meanwhile, hot air output by the hot air blower 6 enters the discharge hopper 11 through the air inlet pipeline 61, and the hot air can be only conveyed upwards through the air distribution plate 4 and enters the air bag 5 due to the closing of the discharge electromagnetic valve 14. The hot air exhausted from the first vent holes on the air distribution plate 4 dries the materials in the mixing barrel 1. The hot air entering the air bag 5 is discharged through the second vent holes on the vibration branch pipe 51, and the materials in the mixing barrel 1 are also dried; the material is stirred in the material mixing process of the material mixing auger 31 and collides with the vibration branch pipe 51; because gasbag 5 has certain elasticity, vibration branch pipe 51 is collided by the material and is swung, further stirs the material, improves compounding efficiency. When the vibration branch pipe 51 swings, the direction of hot air discharged from the second vent hole of the vibration branch pipe 51 also changes, so that certain disturbance effect is provided for hot air in the mixing barrel 1, the hot air reaches each corner of the mixing barrel 1, the materials are comprehensively covered, and the drying is more uniform.
After four materials in the mixing barrel 1 are dried and mixed, the discharging electromagnetic valve 41 and the discharging electromagnetic valve 14 are opened simultaneously, the materials enter the lower part of the discharging hopper 11 through the discharging opening on the air distribution plate 4 and are discharged after being conveyed to the discharging opening 12 of the storage barrel 2 through the discharging auger 13.
The process data of various materials can be pre-stored in the processing device, such as the corresponding relation between the material name and the material color, for example, the A1 material is yellow, the A2 material is red, and the A3 material is black. The product names and the proportions of the processed materials are, for example, 10Kg of A1 material and 20Kg of A2 material to obtain product A, the proportion of A1 material and A2 material is 1:2, and for example, 20Kg of A1 material and 40Kg of A2 material and 60Kg of A3 material to obtain product B, the proportion of A1 material, A2 material and A3 material is 2:4: 6. Therefore, data can be called quickly according to prestored process data, the name of the material is identified by the device through color according to the name of the product, and the blanking speed of various materials is controlled automatically according to preset proportion, so that intellectualization is achieved.
Example two
The difference between the first embodiment and the second embodiment is that the blanking amount control unit of the present embodiment includes the regulating valve 21, but is not provided with the leaking pipe 22, the weighing container 23, the weight sensor, the weight comparator, and the blanking solenoid valve. Although the structure can be simplified and the volume of the processing device can be reduced, the proportioning precision is relatively low, and the device is suitable for occasions with no particularly high requirement on the batching precision.
The foregoing is only a preferred embodiment of the present invention, and it should be noted that, for those skilled in the art, without departing from the concept of the present invention, several modifications and improvements can be made, which should also be regarded as the protection scope of the present invention, and these will not affect the effect of the present invention and the practicability of the patent. The technology, shape and construction parts which are not described in the present invention are all known technology.
Claims (10)
1. The utility model provides a granule material compounding and material processing apparatus dries by fire which characterized in that: comprises a mixing barrel and a plurality of material storage barrels; the mixing barrel is vertically arranged, and is provided with a feeding hole, a discharging hole, an air inlet and an air outlet; the air inlet of the mixing barrel is communicated with a hot air mechanism; at least one group of material mixing auger for stirring materials is arranged in the material mixing barrel, the material mixing auger can rotate relative to the material mixing barrel, and each group of material mixing auger comprises a plurality of blades which are circumferentially arranged; the discharge gate of every storage vat all communicates with the feed inlet of compounding bucket, and the discharge gate department of storage vat all is equipped with unloading control unit.
2. A particulate material mixing and seasoning apparatus in accordance with claim 1 further comprising: the discharging amount control unit comprises an electric adjusting valve which is positioned at the discharging port of the storage barrel and used for adjusting the discharging speed of the material.
3. A particulate material mixing and material drying treatment apparatus as claimed in claim 2, wherein: the feeding amount control unit also comprises a controller and a weighing container which is positioned below the discharge hole of the storage barrel and corresponds to the storage barrel; the weighing containers are internally provided with weight sensors, the output ends of the weight sensors are connected with the first input ends of the corresponding weight comparators, the second input ends of the weight comparators are connected with the threshold value storage, the output ends of the weight comparators are connected with the controller, and the first output ends of the controller are correspondingly connected with the control ends of the regulating valves; the bottom of the weighing container is provided with a feed opening, the feed opening is provided with a feed electromagnetic valve, and the control end of the feed electromagnetic valve is connected with the second output end of the controller.
4. A particulate material mixing and material drying apparatus as claimed in claim 2 or 3, wherein: the feeding amount control unit also comprises a color sensor corresponding to the storage barrel, and the input end of the color sensor is connected with the color control end of the controller; the output end of the color sensor is connected with the control input end of the controller regulating valve.
5. A particulate material mixing and seasoning apparatus in accordance with claim 1 further comprising: the discharge port of the mixing barrel is provided with a discharge auger which can rotate relative to the discharge port.
6. A particulate material mixing and seasoning apparatus in accordance with claim 5 wherein: the mixing barrel is internally provided with a stirring motor with double output shafts, one output shaft of the stirring motor is coaxially connected with the mixing auger, and the other output shaft of the stirring motor is coaxially connected with the discharging auger.
7. A particulate material mixing and seasoning apparatus in accordance with claim 1 further comprising: the lower part of the mixing barrel is provided with a discharge hopper, and an air distribution plate protruding upwards is arranged in the discharge hopper; the air distribution plate is provided with a plurality of first air vents; the air distribution plate is provided with a discharge opening, and a discharge electromagnetic valve is arranged at the discharge opening; and the air inlet of the mixing barrel is positioned below the air distribution plate.
8. A particulate material mixing and material drying apparatus as claimed in claim 1, 2, 3, 5, 6 or 7 wherein: still be equipped with vibrating device in the compounding bucket, vibrating device includes the gasbag with the air intake intercommunication of compounding bucket, is equipped with a plurality of vertical hollow on the gasbag and with the vibration branch pipe of gasbag intercommunication, be equipped with a plurality of second ventholes on the vibration branch pipe.
9. A particulate material mixing and material drying apparatus as claimed in claim 1, 2, 3, 5, 6 or 7 wherein: the material storage barrels are respectively connected with a material suction device.
10. a particulate material mixing and material drying apparatus as claimed in claim 1, 2, 3, 5, 6 or 7 wherein: and a discharge electromagnetic valve is arranged at the discharge outlet of the mixing barrel.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CN201920399550.3U CN209775216U (en) | 2019-03-27 | 2019-03-27 | Granule material compounding and material drying processing apparatus |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201920399550.3U CN209775216U (en) | 2019-03-27 | 2019-03-27 | Granule material compounding and material drying processing apparatus |
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| CN209775216U true CN209775216U (en) | 2019-12-13 |
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| CN201920399550.3U Expired - Fee Related CN209775216U (en) | 2019-03-27 | 2019-03-27 | Granule material compounding and material drying processing apparatus |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110065172A (en) * | 2019-03-27 | 2019-07-30 | 湖北民族大学 | Mixing and the integrated granule materials processing unit of baking material |
| CN113561348A (en) * | 2021-07-21 | 2021-10-29 | 盐城市材炅汽车配件有限公司 | Preparation and premixing device for automobile injection molding machining raw materials |
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2019
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110065172A (en) * | 2019-03-27 | 2019-07-30 | 湖北民族大学 | Mixing and the integrated granule materials processing unit of baking material |
| CN113561348A (en) * | 2021-07-21 | 2021-10-29 | 盐城市材炅汽车配件有限公司 | Preparation and premixing device for automobile injection molding machining raw materials |
| CN113561348B (en) * | 2021-07-21 | 2023-04-07 | 盐城市材炅汽车配件有限公司 | Preparation and premixing device for automobile injection molding machining raw materials |
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