CN202895501U - Water tank direct-cooling type granulator based on melting method - Google Patents
Water tank direct-cooling type granulator based on melting method Download PDFInfo
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- CN202895501U CN202895501U CN 201220410873 CN201220410873U CN202895501U CN 202895501 U CN202895501 U CN 202895501U CN 201220410873 CN201220410873 CN 201220410873 CN 201220410873 U CN201220410873 U CN 201220410873U CN 202895501 U CN202895501 U CN 202895501U
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- water tank
- conveyer belt
- cooling type
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- discharging opening
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Abstract
The utility model discloses a water tank direct-cooling type granulator based on a melting method, which uses water as a cooling medium. The water tank direct-cooling type granulator based on the melting method comprises a granulator head, wherein the granulator head is mounted on a headstock, and is connected with a driving motor through a transmission belt; a water tank is mounted below a discharging opening of the granulator head; a conveyor belt is mounted in the water tank; the lower end of the conveyor belt faces to the discharging opening of the granulator head; the granulator head is arranged below the discharging opening in the water tank; a retaining plate for ensuring that material particles output by the granulator head fall down the conveyor belt is mounted at the position of the upper part of the lower end of the conveyor belt; and the upper end of the conveyor belt extends out of the water tank. The water tank direct-cooling type granulator based on the melting method has the characteristics of simple structure, fast cooling speed and good granulation effect.
Description
Technical field
The utility model relates to a kind of chemical machinery, the comminutor of the industrial chemicals such as especially a kind of PUR, plastics, resin, specifically a kind of fusion method water tank direct-cooling type comminutor.
Background technology
At present; utilize comminutor to industrial chemicals granulation process such as PUR, plastics, resins in; cool off rapidly granulating in order to make through the feed particulate material of pellet head output; must adopt the very complicated cooling device of structure or bulky Cooling System, in order to shorten cool time, the refrigeration plant that has even employing involves great expense cools off; and can't connect work; all all, have all that equipment investment is large, energy consumption is large, the shortcoming of maintenance difficulty.In order to solve above-mentioned all deficiencies, so our exigence is short a kind of cool time, the comminutor that granulating is effective and simple in structure.
The utility model content
The purpose of this utility model provides a kind of simple in structure, and what cooling was fast, granulating is effective utilizes water as the fusion method water tank direct-cooling type comminutor of cooling medium.
The technical solution of the utility model is:
A kind of fusion method water tank direct-cooling type comminutor; comprise pellet head; pellet head is installed on the headstock and by driving-belt and links to each other with drive motors; the below that it is characterized in that the pellet head discharging opening is equipped with water tank; conveyer belt is installed in water tank; the lower end of conveyer belt is over against the pellet head discharging opening; in water tank; the below of pellet head discharging opening; corresponding position, conveyer belt lower end is equipped with the thing grain that makes pellet head output and drops on striker plate on the conveyer belt, and stretch out outside the water tank upper end of conveyer belt.
Further, described conveyer belt is the stainless steel band that water falling hole is arranged, and its aperture should be less than the particle diameter of formed thereby particle.
Further, the bottom, upper end that conveyer belt stretches out water tank is equipped with material-receiving device, and material-receiving device comprises hopper, packing machine, weigher.
Further, the end position place that conveyer belt stretches out water tank is equipped with hot-air drier, so that the rapid drying of granular material shortens and packs time.
Further, be connected with the liquid level recovery tank that communicates with it in the upper end of water tank, the bottom of liquid level recovery tank is connected with return pipe, is connected with water inlet pipe in the bottom of water tank.
The beneficial effects of the utility model:
1. the utility model is applicable to that all do not absorb water, the quick cooling and shaping of the meltbility industrial chemicals of undissolved water, has a cooling fast, granular attractive in appearance, odorlessness, environmental protection, energy-conservation, life-span is long, and can connect uninterrupted production, has advantages of simultaneously maintenance, easy to operate, cost is low.
2. the cooling medium in the water tank can differently according to the kind of granulating raw material select the liquid such as water, alcohol, propyl alcohol as cooling medium.
Description of drawings
Fig. 1 is the utility model structural representation.
Fig. 2 is that the A of Fig. 1 is to view.
Fig. 3 is the cassette mechanism structure schematic diagram of pellet head of the present utility model.
Fig. 4 is the A-A sectional structure schematic diagram of Fig. 3.
The specific embodiment
Relevant aforementioned and other technology contents of the present utility model, Characteristic can be known to present in the following detailed description that cooperates with reference to graphic preferred embodiment.Explanation by the specific embodiment, when can being to reach technological means and the effect that predetermined purpose takes to be able to more deeply and concrete understanding to the utility model, yet appended graphic only provide with reference to the usefulness of explanation, the utility model is limited.
Below in conjunction with drawings and Examples the utility model is further described.
Shown in Fig. 1-4.A kind of fusion method water tank direct-cooling type comminutor; comprise pellet head 1; the outer tube 15 that is covered with hole by head core 14 and tube wall forms; head core 14 off-centre are combined closely with outer tube 15 bottoms; head core 14 tops " V " type arranges two groups by spring-supported feather key 16, has a heating pore 17 on head core 14 cross sections at least, also has a charging pore 18 and a discharging pore 19; be provided with blanking between charging pore 18 and the discharging pore 19 and distribute passage 20, shown in Fig. 3,4.The surface of pellet head 1 is covered with stay-warm case 5; it is installed on the headstock 2 and by driving-belt 3(and can be belt transmission) link to each other with drive motors 4; drive its rotation by drive motors 4; the below of pellet head 1 discharging opening is equipped with water tank 6; conveyer belt 7(is installed in the water tank 6 can adopts the stainless steel band manufacturing; on it processing be convenient to again with the aperture that falls under water); the lower end of conveyer belt 7 is over against pellet head 1 discharging opening; in water tank 6; the below of pellet head 1 discharging opening; upper position place, conveyer belt 7 lower end is equipped with the thing grain that makes pellet head 1 output and drops on striker plate 9 on the conveyer belt 7; stretch out outside the water tank 6 upper end of conveyer belt 7; its underpart is equipped with by hopper 21; packing machine 22; the material-receiving device 8 that weigher 23 grades form; the end position place that conveyer belt 7 stretches out water tank is equipped with hot-air drier 10; so that the rapid drying of granular material shortens and packs time.Be using water wisely, can be connected with the liquid level recovery tank 11 that communicates with it at the upper end place of water tank 6, the bottom of liquid level recovery tank is connected with return pipe 12, is connected with water inlet pipe 13 in the bottom of water tank 6.
The workflow of above-mentioned a kind of fusion method water tank direct-cooling type comminutor is as follows:
At first; pellet head 1 it be installed on the headstock 2 and by driving-belt 3(can be belt transmission) link to each other with drive motors 4; drive its rotation by drive motors 4; the below of pellet head 1 discharging opening is equipped with water tank 6; conveyer belt 7(is installed in the water tank 6 can adopts the stainless steel band manufacturing; on it processing be convenient to again with the aperture that falls under water); the lower end of conveyer belt 7 is over against pellet head 1 discharging opening; in water tank 6; the below of pellet head 1 discharging opening; upper position place, conveyer belt 7 lower end is equipped with the thing grain that makes pellet head 1 output and drops on slanting baffle 9 on the conveyer belt 7; stretch out outside the water tank 6 upper end of conveyer belt 7; its underpart is equipped with by hopper 21; packing machine 22; the material-receiving device 8 that weigher 23 grades form; the end position place that conveyer belt 7 stretches out water tank is equipped with hot-air drier 10; so that the rapid drying of granular material shortens and packs time.When pellet head 1 is produced particle; particle can be dropped on the lower end of conveyer belt 7; because conveyer belt 7 is incline structure; its lower end places again water tank 6; therefore the particle of drippage also just is dropped in the water on the conveyer belt 7; for preventing that particle is slipped to the water tank 6 from conveyer belt; so in the lower end of conveyer belt 7 slanting baffle 9 is installed, constantly plastic grain is produced, and they are transferred is with 7 to be transported in the material-receiving device 8; in the process of transporting; particle can be cooled off rapidly through cooling medium, and conveyer belt 7 can adopt the stainless steel band manufacturing, its processing be convenient to again with the aperture that falls under water; like this on the particle with water or other cooling mediums can reflux.Hot-air drier 10 is arranged above conveyer belt 7, can fall within after the drying in the hopper 8 rapidly with particle drying like this, hopper 8 is comprised of hopper 21, packing machine 22, weigher 23 etc., formation product that therefore can be very fast.Be using water wisely, can be connected with the liquid level recovery tank 11 that communicates with it at the upper end place of water tank 6, the bottom of liquid level recovery tank is connected with return pipe 12, is connected with water inlet pipe 13 in the bottom of water tank 6.
The above, it only is preferred embodiment of the present utility model, be not that the utility model is done any pro forma restriction, although the utility model discloses as above with preferred embodiment, yet be not to limit the utility model, any those skilled in the art, within not breaking away from the technical solutions of the utility model scope, when the technology contents that can utilize above-mentioned announcement is made a little change or is modified to the equivalent embodiment of equivalent variations, in every case be the content that does not break away from technical solutions of the utility model, any simple modification that foundation technical spirit of the present utility model is done above embodiment, equivalent variations and modification all still belong in the scope of technical solutions of the utility model.
Claims (5)
1. fusion method water tank direct-cooling type comminutor; comprise pellet head; pellet head is installed on the headstock and by driving-belt and links to each other with drive motors; the below that it is characterized in that the pellet head discharging opening is equipped with water tank; conveyer belt is installed in the water tank; the lower end of conveyer belt is over against the pellet head discharging opening; in water tank; the below of pellet head discharging opening; corresponding position, conveyer belt lower end is equipped with the thing grain that makes pellet head output and drops on striker plate on the conveyer belt, and stretch out outside the water tank upper end of conveyer belt.
2. fusion method water tank direct-cooling type comminutor according to claim 1 is characterized in that at described conveyer belt be stainless steel band with holes.
3. fusion method water tank direct-cooling type comminutor according to claim 1 is characterized in that in the bottom, upper end that described conveyer belt stretches out outside the water tank material-receiving device being installed.
4. fusion method water tank direct-cooling type comminutor according to claim 1 is characterized in that an end position place of stretching out water tank at described conveyer belt is equipped with hot-air drier.
5. fusion method water tank direct-cooling type comminutor according to claim 1 is characterized in that being connected with the liquid level recovery tank that communicates with it at the upper end place of water tank, and the bottom of liquid level recovery tank is connected with return pipe, is connected with water inlet pipe in the bottom of water tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220410873 CN202895501U (en) | 2012-08-20 | 2012-08-20 | Water tank direct-cooling type granulator based on melting method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220410873 CN202895501U (en) | 2012-08-20 | 2012-08-20 | Water tank direct-cooling type granulator based on melting method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202895501U true CN202895501U (en) | 2013-04-24 |
Family
ID=48116211
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220410873 Withdrawn - After Issue CN202895501U (en) | 2012-08-20 | 2012-08-20 | Water tank direct-cooling type granulator based on melting method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202895501U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109732805A (en) * | 2019-02-25 | 2019-05-10 | 齐齐哈尔大学 | A kind of equipment that spheric granules being made in recycled plastic with softening extrusion |
| CN110328773A (en) * | 2019-05-31 | 2019-10-15 | 长兴悦成塑料制品有限公司 | A kind of plastic pellet production and processing integrated equipment |
| CN114917835A (en) * | 2022-05-16 | 2022-08-19 | 荆门市维佳实业有限公司 | Compound wax pelletization production line |
-
2012
- 2012-08-20 CN CN 201220410873 patent/CN202895501U/en not_active Withdrawn - After Issue
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109732805A (en) * | 2019-02-25 | 2019-05-10 | 齐齐哈尔大学 | A kind of equipment that spheric granules being made in recycled plastic with softening extrusion |
| CN110328773A (en) * | 2019-05-31 | 2019-10-15 | 长兴悦成塑料制品有限公司 | A kind of plastic pellet production and processing integrated equipment |
| CN114917835A (en) * | 2022-05-16 | 2022-08-19 | 荆门市维佳实业有限公司 | Compound wax pelletization production line |
| CN114917835B (en) * | 2022-05-16 | 2023-09-08 | 荆门市维佳实业有限公司 | Compound wax grain production line |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20130424 Effective date of abandoning: 20130619 |
|
| C20 | Patent right or utility model deemed to be abandoned or is abandoned |