CN206124164U - PET composite sheet forming device - Google Patents
PET composite sheet forming device Download PDFInfo
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- CN206124164U CN206124164U CN201621044305.3U CN201621044305U CN206124164U CN 206124164 U CN206124164 U CN 206124164U CN 201621044305 U CN201621044305 U CN 201621044305U CN 206124164 U CN206124164 U CN 206124164U
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- barrel
- extruder
- pet
- forming device
- runner
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Abstract
The utility model belongs to the technical field of the plastic is moulded plastics, a PET composite sheet forming device is related to, include first extruder, second extruder and crowd the mould altogether, first extruder has first feed cylinder, the second extruder has the second feed cylinder, crowded mould includes well runner and lies in altogether the first side flow of well runner both sides is said and second side flow way, well runner is connected the export of second feed cylinder, first side flow say with the second side flow is said and is connected the export of first feed cylinder. The utility model discloses make the outer three ply board that contains the opening agent with the PET board, it can be brighter than seeming to solidify the the sheet surface who forms, and be more smooth moreover.
Description
Technical field
The utility model is related to plastic-injection technical field, and more particularly to one kind can produce the high slippery PET of low haze and answer
The shaped device of plywood.
Background technology
PET (Polyethylene terephthalate, polyethylene terephthalate) is common one in life
Resin is planted, is exchanged with glycol ester by dimethyl terephthalate (DMT) or is first synthesized to benzene two with terephthalic acid (TPA) and ethylene glycol esterification
The double hydroxyl ethyl esters of formic acid, then carry out again polycondensation reaction and are obtained.PET belongs to crystal type saturated polyester, is milky or light yellow, height
The polymer of crystallization, surface smooths glossy.PET has excellent physical and mechanical properties within the scope of wider temperature, for a long time
Using temperature up to 120 DEG C, electrical insulating property is excellent, or even under high-temperature high-frequency, its electrical property still preferably, but corona resistance compared with
Difference, creep resistance, fatigue durability, rub resistance, dimensional stability are all fine.
Client needs that sheet material is used on some packages, and relatively low frictional resistance, institute are needed in transportation
To have higher requirement to outward appearance and slippery.And the plate surface prepared using single PET material is creamy white, frictional resistance
Height, does not meet these requirements.
Therefore, it is necessary to provide a kind of new technology to solve the above problems.
Utility model content
Main purpose of the present utility model is to provide a kind of shaping dress that can produce the high slippery PET composite plates of low haze
Put.
The utility model is achieved through the following technical solutions above-mentioned purpose:A kind of PET is combined plate forming device, including first
Extruder, the second extruder and coextruding die;First extruder has the first barrel;Second extruder has the second material
Cylinder;The coextruding die includes middle runner and the first side runner and the second side runner positioned at the middle runner both sides, it is described in
Runner connects the outlet of second barrel, and first side runner and second side runner connect going out for first barrel
Mouthful.
Specifically, the barrel dliameter of second barrel is 2~3 times of the first barrel barrel dliameter.
Further, first extruder also has the first drain hopper above, under first drain hopper
Outlet the first barrel of connection.
Further, the bottom of first drain hopper is provided with the first inlet chamber and the supply toward in first inlet chamber
First air inlet pipe, first inlet chamber is connected with first drain hopper inner side by some gas holes.
Further, second extruder also has the second drain hopper above, under second drain hopper
Outlet the second barrel of connection.
Further, the bottom of second drain hopper is provided with the second inlet chamber and the supply toward in second inlet chamber
Second air inlet pipe, second inlet chamber is connected with second drain hopper inner side by some gas holes.
Using above-mentioned technical proposal, the beneficial effect of technical solutions of the utility model is:
1st, PET sheet is made three ply board of the outer layer containing opening agent by the utility model, and concretionary plate surface can be than aobvious
Must be brighter, and it is more smooth;
2nd, drying materials structure is equipped with drain hopper, after shaping is produced from inside because of the presence of moisture to prevent fused materials
Life is bad;
3rd, the barrel dliameter of the second barrel is 2~3 times of the first barrel barrel dliameter, so adapts to the raw material under the premise of cost optimization
Supply ratio.
Description of the drawings
Fig. 1 is the structural representation of the compound plate forming devices of PET;
Fig. 2 is the structural representation of the first extruder;
Fig. 3 is the structural representation of the second extruder;
Fig. 4 is the production principle figure of PET composite plates.
Numeral is represented in figure:
The extruders of 1- first,
The drain hoppers of 11- first,
The inlet chambers of 111- first,
The air inlet pipe of 112- first,
The barrels of 12- first,
The screw rods of 13- first,
14- pair hoppers,
141- impellers;
The extruders of 2- second,
The drain hoppers of 21- second,
The inlet chambers of 211- second,
The air inlet pipe of 212- second,
The barrels of 22- second,
The screw rods of 23- second;
3- coextruding dies,
Runner in 31-,
The side runners of 32- first,
The side runners of 33- second.
Specific embodiment
The utility model is described in further detail with reference to specific embodiment.
As shown in Figures 1 to 4, a kind of compound plate forming devices of PET of the present utility model, including the first extruder 1, second
Extruder 2 and coextruding die 3;First extruder 1 has the first drain hopper 11 above, the 11 times outlets of the first drain hopper of connection
The first barrel 12 and for push the first barrel 12 in material the first screw rod 13;Second extruder 2 has above
Second drain hopper 21, the second barrel 22 of the connection outlet of the second drain hopper 21 time and for the of material in the second barrel 22 of push
Two screw rods 23;Coextruding die 3 includes middle runner 31 and the first side runner 32 and the second side runner 33 positioned at the both sides of middle runner 31,
Middle runner 31 connects the second barrel 22 and exports, and the first side runner 32 and the second side runner 33 connect the first barrel 12 and export.First
The material of the extrusion of extruder 1 is the mixture of PET and opening agent, and the material of the extrusion of the second extruder 2 is PET, and Jing second is extruded
The PET of the extrusion of machine 2 can be extruded into middle material band, PET and the opening agent composition point of the extrusion of the first extruders of Jing 1 in middle runner 31
For two strands, outside material strip is extruded into from the first side runner 32 and the second side runner 33 respectively, middle material band is fitted in then
Both sides, so be coextruded material strip directly be three ply board.It is concretionary because increased opening agent in the material strip of outside
Plate surface can comparison be bright than seeming, and more smooth.
As shown in Figure 1 to Figure 3, the bottom of the first drain hopper 11 is provided with the first inlet chamber 111 and toward in the first inlet chamber 111
First air inlet pipe 112 of supply, the first inlet chamber 111 is connected by some gas holes with the inner side of the first drain hopper 11 and (not marked
Note);The bottom of the second drain hopper 21 is provided with the second inlet chamber 211 and the second air inlet pipe toward supply in the second inlet chamber 211
212, the second inlet chamber 211 is connected (do not mark) with the inner side of the second drain hopper 21 by some gas holes.The He of first drain hopper 11
Material in second drain hopper 21 can lean on air inlet pipe 112,212 to carry out hot gas supply.Because material is entered before extruder 1,2
All be cut into it is short grained, so the material grain that hot gas is blown in drain hopper 11,12 just can play a part of to dry moisture, it is to avoid molten
After shaping internal generation is bad because of the presence of moisture to melt material.
As shown in Fig. 2 a secondary hopper 14 for being located at the side of the first drain hopper 11 is additionally provided with the first extruder 11, pair material
The outlet of bucket 14 is connected to the middle part of the first barrel 12, and an impeller 141 is additionally provided with the outlet of secondary hopper 14.During work, PET is from
One drain hopper 11 adds the first barrel 12 to be melted then, and the PET of melting is promoted by the first screw rod 13 and mixed while forward
Conveying.Opening agent is added from secondary hopper 14, and is directly added to the interlude of the first barrel 12, in the first barrel 12
Opening agent will puddle in the middle of PET, melt while smashing mixing by the shearing force that the first screw rod 13 is produced, therefore open
Mouthful agent in PET dispersedly evenly.Impeller 141 can control the addition speed of opening agent, as long as adjusting impeller 141 and
The rotating speed of one screw rod 13 can just make PET and opening agent and be mixed with more fixed ratio, it is ensured that product quality is stablized.
As shown in figure 1, the barrel dliameter of the second barrel 22 is 2~3 times of the barrel dliameter of the first barrel 12.In actual production, because PET
The outward appearance of composite plate essentially consists in the quality that two outside material strip outermosts show, the thickness of outside material strip corresponds to opening agent
Dosage, in order to save opening agent cost, the thickness of outside material strip need not be very thick, and intermediate layer thickness probably can be outer layer thickness
8 times or so of summation, so can just make cost optimization, so the barrel dliameter of the second barrel 22 increases, to adapt to same rotational speed under it is former
The supply ratio of material.
As shown in Figure 1 and Figure 4, the production stage of PET composite plates is:
1. the single raw materials of PET are added into the second drain hopper 21 and then are melted and clamp-on middle runner 31, during control temperature
Degree is extruded as middle material band then at 260~300 DEG C;
2. PET is mixed with opening agent in the first extruder 1, Adding Way is added for PET from the first drain hopper 11, is opened
Mouthful agent is added from secondary hopper 14, is adjusted and then is melted and clamp-ons the first side runner 32 and the second side runner 33, during control
Temperature is extruded as two outside material strips and fits in the both sides of middle material band then at 260~300 DEG C;
3. three layered material bands are made to extrude while hardening by cooling forms PET composite plates;
4. the anterior waste material of excision after balanced condition is extruded, carries out collecting materials.
Wherein:Amount of PET in first extruder 1 accounts for 10~15wt% of total material amounts, in the second extruder 2
Amount of PET account for total material amounts for 85~90wt%, opening agent consumption is 0.3~0.4wt% of total material amounts, opening agent
Formulation be nanometer grade silica powder.
The different amounts ratio and condition of adjustment raw material, skin-friction coefficient is carried out to obtained PET composite plates and mist degree is surveyed
Examination, and contrasted as reference examples using single PET sheet material, concrete outcome is shown in Table 1.
Table 1:
As shown in Table 1, with the PET composite plates of this technique productions compared with conventional PET sheet, coefficient of friction is lower, so more
Plus it is smooth;Mist degree is lower, so brighter.
Above-described is only some embodiments of the present utility model.For the person of ordinary skill of the art,
On the premise of design is created without departing from the utility model, some deformations and improvement can also be made, these belong to this practicality
New protection domain.
Claims (6)
1. a kind of PET is combined plate forming device, it is characterised in that:Including the first extruder, the second extruder and coextruding die;It is described
First extruder has the first barrel;Second extruder has the second barrel;The coextruding die includes middle runner and position
In first side runner and the second side runner of the middle runner both sides, the middle runner connects the outlet of second barrel, institute
State the first side runner and second side runner connects the outlet of first barrel.
2. PET according to claim 1 is combined plate forming device, it is characterised in that:The barrel dliameter of second barrel is institute
State the first barrel barrel dliameter 2~3 times.
3. PET according to claim 1 and 2 is combined plate forming device, it is characterised in that:First extruder also has
First drain hopper above, the lower outlet of first drain hopper connects the first barrel.
4. PET according to claim 3 is combined plate forming device, it is characterised in that:The bottom of first drain hopper sets
There are the first inlet chamber and the first air inlet pipe supplied toward in first inlet chamber, first inlet chamber and first blowing
Bucket inner side is connected by some gas holes.
5. PET according to claim 1 and 2 is combined plate forming device, it is characterised in that:Second extruder also has
Second drain hopper above, the lower outlet of second drain hopper connects the second barrel.
6. PET according to claim 5 is combined plate forming device, it is characterised in that:The bottom of second drain hopper sets
There are the second inlet chamber and the second air inlet pipe supplied toward in second inlet chamber, second inlet chamber and second blowing
Bucket inner side is connected by some gas holes.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621044305.3U CN206124164U (en) | 2016-09-08 | 2016-09-08 | PET composite sheet forming device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621044305.3U CN206124164U (en) | 2016-09-08 | 2016-09-08 | PET composite sheet forming device |
Publications (1)
Publication Number | Publication Date |
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CN206124164U true CN206124164U (en) | 2017-04-26 |
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ID=58568836
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201621044305.3U Active CN206124164U (en) | 2016-09-08 | 2016-09-08 | PET composite sheet forming device |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108381891A (en) * | 2018-04-24 | 2018-08-10 | 华南农业大学 | A kind of manufacturing equipment for manufacturing the PET wood plastic composites with sandwich |
CN108608633A (en) * | 2018-04-24 | 2018-10-02 | 华南农业大学 | A kind of operating method of PET wood plastic composites manufacturing equipment |
CN114228092A (en) * | 2022-01-17 | 2022-03-25 | 河北格瑞尔斯塑机制造有限公司 | A extrusion device that is used for high thermal resistance xps extrusion molding heated board production |
-
2016
- 2016-09-08 CN CN201621044305.3U patent/CN206124164U/en active Active
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108381891A (en) * | 2018-04-24 | 2018-08-10 | 华南农业大学 | A kind of manufacturing equipment for manufacturing the PET wood plastic composites with sandwich |
CN108608633A (en) * | 2018-04-24 | 2018-10-02 | 华南农业大学 | A kind of operating method of PET wood plastic composites manufacturing equipment |
CN114228092A (en) * | 2022-01-17 | 2022-03-25 | 河北格瑞尔斯塑机制造有限公司 | A extrusion device that is used for high thermal resistance xps extrusion molding heated board production |
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