CN206287389U - Vertical circulation dewaterer - Google Patents
Vertical circulation dewaterer Download PDFInfo
- Publication number
- CN206287389U CN206287389U CN201621209909.9U CN201621209909U CN206287389U CN 206287389 U CN206287389 U CN 206287389U CN 201621209909 U CN201621209909 U CN 201621209909U CN 206287389 U CN206287389 U CN 206287389U
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- centrifugal dehydrator
- water tank
- dewaterer
- filter
- processing procedure
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- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Abstract
The utility model discloses a kind of vertical circulation dewaterer, including main platform, centrifugal dehydrator and cyclic water tank, the cyclic water tank is arranged on the main platform, the centrifugal dehydrator is arranged on the main platform by a dewaterer mounting bracket, and the dewaterer mounting bracket is located at the cyclic water tank side;Centrifugal dehydrator lower end sidepiece is provided with charging aperture, and centrifugal dehydrator upper end sidepiece is provided with discharging opening;The charging aperture top is connected with the first water filter, and first water filter is connected with processing procedure return pipe;The charging aperture downside sets delivery port, and the delivery port is arranged on the top of the cyclic water tank, corresponding with the second filter for being arranged on the cyclic water tank top, and the cyclic water tank is connected by processing procedure water pump with processing procedure outlet pipe.The simple structure of the vertical circulation dewaterer, can carry out dewatered drying to plastic grain, while cooling water Recovery and recycle is utilized.
Description
Technical field
The utility model is related to plastic granulator technical field, more particularly to a kind of vertical circulation dewaterer.
Background technology
The operation principle of traditional waste plastics recovery extruding granulator is by single-step form or two steps type extruder, by plastics
Melt filteration, extrudes tie rod, then the pelletizing after cooling and solidifying, and underwater cutpellet extruding granulator is without tie rod or can not to draw
Under conditions of bar, directly a kind of novel mechanical of pelletizing, melt pelletizing are contacted simultaneously with cooling water in the moment of melt extrusion die face
There is obvious advantage with respect to solid-state pelletizing.Because plastics are scraped by blade under melt state, solidified after circulating water
, the high polymer of different viscosities can use this granulating form, and pelletizing will not form any dust under melt state, and cut
Particle shape shape is regular, and packaging, transport are more convenient;The load and pelletizing speed of die head are adjusted according to extrusion capacity Auto-matching,
To change the size of pelletizing, it is also possible to which knife rest when manually using different blade numbers changes pelletizing size and shape;Pelletizing,
Cooling combines together and eliminates 4-6m cold rinse banks long, greatly reduces floor space;Prilling realizes automation, operation side
Just, noise is relatively low, chipping qualities is good.With the yield bigger than traditional tie rod pelletizing, lower energy consumption.
Underwater cutpellet granulation unit generally comprise single-step form or two rank vented extruders, underwater pelletizer, flexible tool rest,
Automatic dehydration (drying) device, shaker separator, blast system, gather materials hopper, control system composition.When uniform high-temperature fusion
Shape material enters die head runner from upstream equipment (reactor/screw extruder/Melt Pump etc.) end, and material leaves mould just
The pelletizing machine knife blade rotated at a high speed during nib is cut into drop and enters in processing water, because particle specific surface area is maximized
Physical characteristic and fusing drop-wise polymer with processing water the temperature difference, drop solidifies and forms the particle close to spheroid.
The granulation mode of this " somewhere between fervent and cold cut critical condition " determines that it can be good at competent molten state intensity difference, glues
Property big, high to heat sensitivity material granulation operation.
Underwater cutpellet granulation unit needs to use substantial amounts of cooling water, and the consumption to water resource is big, is unfavorable for water-saving and environmental protection,
After the general plastic grain dewater treatment for using automatic dehydration (drying) device to machine, cooling water is directly discharged;Or
Cooling water is transported to water treatment facilities by person, so easily causes pipeline connection complexity, and auxiliary equipment is more.
Utility model content
The technical problems to be solved in the utility model is to provide a kind of vertical circulation dewaterer, and simple structure can be to modeling
Material particle carries out dewatered drying, while cooling water Recovery and recycle is utilized.
In order to solve the above-mentioned technical problem, the technical solution of the utility model is as follows:
A kind of vertical circulation dewaterer, including main platform, centrifugal dehydrator and cyclic water tank, the cyclic water tank are installed
On the main platform, the centrifugal dehydrator is arranged on the main platform by a dewaterer mounting bracket, the dewaterer
Mounting bracket is located at the cyclic water tank side;Centrifugal dehydrator lower end sidepiece is provided with charging aperture, the centrifugal dehydrator
Upper end sidepiece is provided with discharging opening;The charging aperture top is connected with the first water filter, first water filter and processing procedure backwater
Pipe is connected;Charging aperture downside sets delivery port, and the delivery port is arranged on the top of the cyclic water tank, and is arranged on institute
The second filter for stating cyclic water tank top is corresponding, and the cyclic water tank is connected by processing procedure water pump with processing procedure outlet pipe.Make
It is used time, right after processing procedure return pipe enters into the first filter by the mixture of the mach plastic grain of pelletizing and cooling water
Enter from the charging aperture of centrifugal dehydrator afterwards, storage box is transported to from discharging opening through the dry plastics particle after centrifugal dehydration, from
Cooling water after heart dehydration is separated is flowed in cyclic water tank by the delivery port on the downside of centrifugal dehydrator, is passed through by processing procedure water pump
Processing procedure outlet pipe is connected with upper pelleter, realizes the recycling of cooling water.
Further, block barrier is provided with first water filter, described piece of barrier downside is provided with and catches block mouthful.
When using, plastic grain enters into block barrier top, the bulk of mixture with the mixture of cooling water by processing procedure return pipe
Plastics are blocked and are dropped from block mouthful is caught.
Further, second filter is provided with filter residue fine-structure mesh, and the filter residue fine-structure mesh is inclined at described second
It is described to catch the top that block mouthful and the delivery port are arranged on the filter residue silk screen in filter.Filter residue fine-structure mesh is obliquely installed so that
Plastic residues can roll along incline direction, be easy to collect and clear up.
Further, the centrifugal dehydrator upper end is provided with motor, the motor and the centrifugal dehydration
The screw shaft connection of machine.
Further, heat exchanger is additionally provided with the main platform, the processing procedure water pump is connected with the heat exchanger
Connected with the processing procedure outlet pipe afterwards.
Further, the upside of the centrifugal dehydrator is provided with air exhauster, the air exhauster by a support mounting seat
Upper lumen with the centrifugal dehydrator is connected.
Further, a side of the centrifugal dehydrator bottom is provided with electric cabinet and shift knob, the switch
Button, the motor, the air exhauster, the processing procedure water pump are electrically connected with the electric cabinet.
Further, working bank is additionally provided with the main platform, the working bank is located at the centrifugal dehydrator
With the side of the cyclic water tank.
Using above-mentioned technical proposal, as a result of cyclic water tank and centrifugal dehydrator so that pelleter obtains plastics
Grain can rapidly realize the separation of cooling water and particle, treatment is dried by centrifugal dehydrator and air exhauster, to cold
But water is reclaimed by cyclic water tank, and cooling water real-time circulation is enabled by processing procedure water pump.
Brief description of the drawings
Fig. 1 is vertical circulation dewaterer tomograph of the present utility model;
Fig. 2 is another visual angle tomograph of vertical circulation dewaterer of the present utility model;
Fig. 3 is centrifugal dehydrator tomograph of the present utility model;
Fig. 4 is the partial enlarged drawing of the first water filter of the present utility model;
Fig. 5 is the tomograph of the second filter of the present utility model.
In figure, the main platforms of 1-, 2- processing procedure water pumps, 3- heat exchangers, 4- dewaterer mounting brackets, 5- electric cabinets, 6- switches are pressed
Button, 7- centrifugal dehydrators, 8- motors, 9- air exhausters, the water filters of 10- first, the filters of 11- second, 12- cyclic water tanks,
13- working banks, 14- processing procedure outlet pipes, 15- processing procedure return pipes, 16- discharging openings, 17- charging apertures, 18- delivery ports;71- spirals
Rotating shaft, 101- catches block mouthful, 102- block barriers, 111- filter residue fine-structure meshes.
Specific embodiment
Specific embodiment of the present utility model is described further below in conjunction with the accompanying drawings.Herein it should be noted that
It is used to help understand the utility model for the explanation of these implementation methods, but does not constitute to restriction of the present utility model.This
Outward, as long as technical characteristic involved in the utility model disclosed below each implementation method does not constitute conflict each other
Can just be mutually combined.
As shown in Figure 1, 2, 3, a kind of vertical circulation dewaterer, including main platform 1, centrifugal dehydrator 7 and cyclic water tank
14, the cyclic water tank 12 is arranged on the main platform 1, and the centrifugal dehydrator 7 is arranged on by a dewaterer mounting bracket 4
On the main platform 1, the dewaterer mounting bracket 4 is located at the side of the cyclic water tank 12;The lower end sidepiece of the centrifugal dehydrator 7
Charging aperture 17 is provided with, the upper end sidepiece of the centrifugal dehydrator 7 is provided with discharging opening 16;The top of the charging aperture 17 and the first filter
Hydrophone 10 is connected, and first water filter 10 is connected with processing procedure return pipe 15;The downside of the charging aperture 17 sets delivery port 18, institute
The top that delivery port 18 is arranged on the cyclic water tank 12 is stated, with the second filter 11 for being arranged on the top of the cyclic water tank 12
Corresponding, the cyclic water tank 12 is connected by processing procedure water pump 2 with processing procedure outlet pipe 14.When using, by the mach modeling of pelletizing
The mixture of material particle and cooling water is entered into after the first filter 10 then from centrifugal dehydrator 7 by processing procedure return pipe 15
Charging aperture 17 enters, and storage box is transported to from discharging opening 16 through the dry plastics particle after centrifugal dehydration, after centrifugal dehydration is separated
Cooling water flowed in cyclic water tank 18 by the delivery port 18 of the downside of centrifugal dehydrator 7, gone out by processing procedure by processing procedure water pump 2
Water pipe 14 is connected with upper pelleter, realizes the recycling of cooling water.
As shown in figure 4, being provided with block barrier 102 in first water filter 10, the described piece of downside of barrier 102 is set
Catch block mouthful 101.When using, plastic grain enters into block barrier 102 with the mixture of cooling water by processing procedure return pipe 15
Top, the block plastics of mixture are blocked and are dropped from block mouthful 101 is caught.
As shown in figure 5, second filter 11 is provided with filter residue fine-structure mesh 111, the filter residue fine-structure mesh 111 is inclined at
It is described to catch block mouthfuls 101 and the delivery port 18 is arranged on the top of the filter residue silk screen 111 in second filter 11.Filter
Slag fine-structure mesh 111 is obliquely installed so that plastic residues can roll along incline direction, be easy to collect and clear up.
Wherein, the upper end of the centrifugal dehydrator 7 is provided with motor 8, the motor 8 and the centrifugal dehydrator
7 screw shaft 71 is connected.
Wherein, heat exchanger 3 is additionally provided with the main platform 1, the processing procedure water pump 2 is connected with the heat exchanger 3
Connected with the processing procedure outlet pipe 14 afterwards.
Wherein, the upside of the centrifugal dehydrator 7 is provided with air exhauster 9 by a support mounting seat, the air exhauster 9 with
The upper lumen connection of the centrifugal dehydrator 7.
Wherein, a side of the bottom of the centrifugal dehydrator 7 is provided with electric cabinet 5 and shift knob 6, and the switch is pressed
Button 6, the motor 8, the air exhauster 9, the processing procedure water pump 2 are electrically connected with the electric cabinet 5.
Wherein, working bank 13 is additionally provided with the main platform 1, the working bank 13 is located at the centrifugal dehydrator
7 and the side of the cyclic water tank 12.
Implementation method of the present utility model is explained in detail above in association with accompanying drawing, but the utility model is not limited to be retouched
The implementation method stated.For a person skilled in the art, it is right in the case where the utility model principle and spirit is not departed from
These implementation methods carry out various changes, modification, replacement and modification, still fall within protection domain of the present utility model.
Claims (8)
1. a kind of vertical circulation dewaterer, it is characterised in that:It is described to follow including main platform, centrifugal dehydrator and cyclic water tank
Ring water tank is arranged on the main platform, and the centrifugal dehydrator is arranged on the main platform by a dewaterer mounting bracket,
The dewaterer mounting bracket is located at the cyclic water tank side;Centrifugal dehydrator lower end sidepiece is provided with charging aperture, described
Centrifugal dehydrator upper end sidepiece is provided with discharging opening;The charging aperture top is connected with the first water filter, first water filter
Connected with processing procedure return pipe;The charging aperture downside sets delivery port, and the delivery port is arranged on the top of the cyclic water tank,
Corresponding with the second filter for being arranged on the cyclic water tank top, the cyclic water tank is by processing procedure water pump and processing procedure water outlet
Pipe is connected.
2. a kind of vertical circulation dewaterer according to claim 1, it is characterised in that:It is provided with first water filter
Block barrier, described piece of barrier downside is provided with and catches block mouthful.
3. a kind of vertical circulation dewaterer according to claim 2, it is characterised in that:Second filter is provided with filter
Slag fine-structure mesh, the filter residue fine-structure mesh is inclined in second filter, and block mouthful and the delivery port of catching is arranged on institute
State the top of filter residue silk screen.
4. a kind of vertical circulation dewaterer according to claim 3, it is characterised in that:Install the centrifugal dehydrator upper end
There is motor, the motor is connected with the screw shaft of the centrifugal dehydrator.
5. a kind of vertical circulation dewaterer according to claim 3, it is characterised in that:Heat is additionally provided with the main platform
Exchanger, the processing procedure water pump is connected after being connected with the heat exchanger with the processing procedure outlet pipe.
6. a kind of vertical circulation dewaterer according to claim 4, it is characterised in that:The upside of the centrifugal dehydrator leads to
Cross a support mounting seat and be provided with air exhauster, the air exhauster is connected with the upper lumen of the centrifugal dehydrator.
7. a kind of vertical circulation dewaterer according to claim 6, it is characterised in that:The one of the centrifugal dehydrator bottom
Individual side is provided with electric cabinet and shift knob, the shift knob, the motor, the air exhauster, the processing procedure water
Pump is electrically connected with the electric cabinet.
8. a kind of vertical circulation dewaterer according to claim 1, it is characterised in that:Work is additionally provided with the main platform
Make step, the working bank is located at the side of the centrifugal dehydrator and the cyclic water tank.
Priority Applications (1)
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CN201621209909.9U CN206287389U (en) | 2016-11-01 | 2016-11-01 | Vertical circulation dewaterer |
Applications Claiming Priority (1)
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CN201621209909.9U CN206287389U (en) | 2016-11-01 | 2016-11-01 | Vertical circulation dewaterer |
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CN206287389U true CN206287389U (en) | 2017-06-30 |
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107672136A (en) * | 2017-11-04 | 2018-02-09 | 李督 | A kind of water circulation system of household articles injection-moulding device |
CN108237647A (en) * | 2018-01-09 | 2018-07-03 | 张家港市格雷斯机械有限公司 | A kind of Water ring granulator |
CN110127304A (en) * | 2019-04-13 | 2019-08-16 | 江苏力赛柯环保材料科技有限公司 | A kind of plastic particle hoisting machine inner main axis device |
CN112123623A (en) * | 2020-09-08 | 2020-12-25 | 广东聚诚智能科技有限公司 | Underwater granulator capable of effectively filtering waste scraps |
CN112179061A (en) * | 2020-09-30 | 2021-01-05 | 无锡华辰机电工业有限公司 | Particle dehydrator |
-
2016
- 2016-11-01 CN CN201621209909.9U patent/CN206287389U/en active Active
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107672136A (en) * | 2017-11-04 | 2018-02-09 | 李督 | A kind of water circulation system of household articles injection-moulding device |
CN107672136B (en) * | 2017-11-04 | 2019-08-30 | 惠州市明晟精密模具有限公司 | A kind of water circulation system of household items injection-moulding device |
CN108237647A (en) * | 2018-01-09 | 2018-07-03 | 张家港市格雷斯机械有限公司 | A kind of Water ring granulator |
CN110127304A (en) * | 2019-04-13 | 2019-08-16 | 江苏力赛柯环保材料科技有限公司 | A kind of plastic particle hoisting machine inner main axis device |
CN110127304B (en) * | 2019-04-13 | 2021-06-08 | 江苏力赛柯环保材料科技有限公司 | Inner main shaft device for plastic particle elevator |
CN112123623A (en) * | 2020-09-08 | 2020-12-25 | 广东聚诚智能科技有限公司 | Underwater granulator capable of effectively filtering waste scraps |
CN112179061A (en) * | 2020-09-30 | 2021-01-05 | 无锡华辰机电工业有限公司 | Particle dehydrator |
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Legal Events
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GR01 | Patent grant | ||
GR01 | Patent grant | ||
CP03 | "change of name, title or address" |
Address after: No. 45, Shuxin Market Road, Changping Town, Dongguan City, Guangdong Province 523000 Patentee after: Guangdong Jucheng Intelligent Technology Co., Ltd Address before: 523000 Shuxin wudui Industrial Park, Changping Town, Dongguan City, Guangdong Province Patentee before: GUANGDONG JUCHENG XINJINGGONG MACHINERY Co.,Ltd. |
|
CP03 | "change of name, title or address" |