CN206318925U - Glass fiber reinforcement chinlon 6 section process units - Google Patents
Glass fiber reinforcement chinlon 6 section process units Download PDFInfo
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- CN206318925U CN206318925U CN201621311709.4U CN201621311709U CN206318925U CN 206318925 U CN206318925 U CN 206318925U CN 201621311709 U CN201621311709 U CN 201621311709U CN 206318925 U CN206318925 U CN 206318925U
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- discharging opening
- measuring tank
- blending tanks
- screw extruder
- double screw
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- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Reinforced Plastic Materials (AREA)
Abstract
The utility model is glass fiber reinforcement chinlon 6 section process units, its structure is nylon resin measuring tank, silane coupler measuring tank and four [β (3, the hydroxy phenyl of 5 di-tert-butyl 4) propionic acid] pentaerythritol ester measuring tank discharging opening connection A blending tanks, A blending tanks connect double screw extruder, barrel is set in double screw extruder, 5th area of barrel sets A sides drawing-in device, SECTOR-SEVEN sets B sides drawing-in device, A sides drawing-in device connects the first discharging opening of B blending tanks, B sides drawing-in device connects the second discharging opening of B blending tanks, B blending tanks connect aluminium borosilicate glass measuring tank, the discharging opening of carbon fiber measuring tank and ZnOw measuring tank, double screw extruder connects hobboing cutter pelleter, hobboing cutter pelleter connects dewaterer, dewaterer connects drying tower.Advantage of the present utility model：The glass fiber reinforcement chinlon 6 section of production, improves adhesion, improves mechanical property；Reduce cost；Improve technique.
Description
Technical field
The utility model relates to glass fiber reinforcement chinlon 6 section process units.
Background technology
Polyamide fibre, scientific name Fypro is commonly called as nylon (Nylon), English name Polyamide (abbreviation PA), polyamide fibre is poly-
The trade name of nylon, density 1.15g/cm3, it is the thermoplastic for containing recurring amide radical group (- NHCO-) on molecular backbone
Property resin general name.Principal item has polyamide fibre 6 and polyamide fibre 66 etc..Polyamide fibre 6 has good combination property, including mechanical property, resistance to
Hot, wear resistance, chemical proofing and self lubricity, and coefficient of friction is low, has certain anti-flammability, it is easy to process, and fits
In with glass fibre and other filler filling enhancing modifieds, material property is improved with this and expands application.
The glass fiber content of traditional glass fiber reinforced materials is general to disclosure satisfy that the requirement of general plastic products below 50%,
But sayed relative to the intensity and dimensional stability of metal material superelevation, traditional fiberglass reinforced polyamide fibre 6 can't reach to mould
Dai Gang purpose.
Utility model content
The utility model proposes glass fiber reinforcement chinlon 6 section process units, its purpose is intended to overcome existing skill
There is provided a kind of chinlon 6 section for the drawbacks described above that art is present, it is to avoid with the increase of content of glass fiber, and the mobility of product declines,
Adverse effect is brought for processing and forming.
Technical solution of the present utility model：Glass fiber reinforcement chinlon 6 section process units, its structure is mixed including A
Close tank, double screw extruder and B blending tanks, the wherein discharging opening of nylon resin measuring tank, the discharging of silane coupler measuring tank
The discharging opening connection A blending tanks of mouth and four [β-(3,5- di-tert-butyl -4- hydroxy phenyls) propionic acid] pentaerythritol ester measuring tanks, A
Blending tank connects in double screw extruder, double screw extruder and sets barrel, and the 5th area of barrel sets A sides drawing-in device, barrel
SECTOR-SEVEN sets B sides drawing-in device, and A sides drawing-in device connects the first discharging opening of B blending tanks, B sides drawing-in device connection B blending tanks
The second discharging opening, the B blending tanks connection discharging opening of aluminium borosilicate glass measuring tank, the discharging opening and oxygen of carbon fiber measuring tank
Change the discharging opening of zinc whisker measuring tank, double screw extruder connection hobboing cutter pelleter, hobboing cutter pelleter connection dewaterer, dewaterer
Connect drying tower.
Advantage of the present utility model：Simple in construction effective, the glass fiber reinforcement chinlon 6 section of production uses silane even
Connection agent processing fiberglass surfacing improves adhesion, and glass surface is enhanced between glass and nylon after organic-treating
Bonding force, improves the mechanical property of product；By adjusting carbon fiber and other added materials such as glass fibre, carbon fiber and nothing
The consumption of machine whisker, while the rigidity of enhancing polyamide fibre 6 and intensity is played, reduces the cost of raw material；By adjusting various originals
The ratio of material, it is ensured that the good mobility of product, is solved because of the too high adverse effect brought to processing and forming of glass fiber content,
The mobility of materiel machining is ensure that for large-scale, labyrinth product, meanwhile, processing technology is further improved, system is met
The requirement of product.
Brief description of the drawings
Fig. 1 is the structural representation of glass fiber reinforcement chinlon 6 section process units.
1 in figure it is nylon resin measuring tank, 2 be silane coupler measuring tank, 3 is four [β-(3,5- di-tert-butyls -4-
Hydroxy phenyl) propionic acid] pentaerythritol ester measuring tank, 4 be A blending tanks, 5 be double screw extruder, 6 be barrel, 7 be A sides feeding
Device, 8 be B sides drawing-in device, 9 be B blending tanks, 10 be aluminium borosilicate glass measuring tank, 11 be carbon fiber measuring tank, 12 be
ZnOw measuring tank, 13 be hobboing cutter pelleter, 14 be dewaterer, 15 be drying tower.
Embodiment
The utility model is described in further detail with reference to embodiment and embodiment.
As shown in figure 1, glass fiber reinforcement chinlon 6 section process units, its structure includes A blending tanks 4, twin-screw extrusion
Machine 5 and B blending tanks 9, the wherein discharging opening of nylon resin measuring tank 1, the discharging opening of silane coupler measuring tank 2 and four [β-(3,
5- di-tert-butyl -4- hydroxy phenyls) propionic acid] pentaerythritol ester measuring tank 3 discharging opening connection A blending tanks 4, A blending tanks 4 are connected
Barrel 6 is set in double screw extruder 5, double screw extruder 5, the 5th area of barrel 6 sets A sides drawing-in device 7, the 7th of barrel 6 the
Area sets B sides drawing-in device 8, the first discharging opening of the connection B of A sides drawing-in device 7 blending tanks 9, the connection B blending tanks of B sides drawing-in device 8
9 the second discharging opening, the discharging opening of the connection aluminium borosilicate glass of B blending tanks 9 measuring tank 10, the discharging of carbon fiber measuring tank 11
The discharging opening of mouth and ZnOw measuring tank 12, the connection hobboing cutter of double screw extruder 5 pelleter 13, hobboing cutter pelleter 13 is connected
Dewaterer 14, the connection drying tower 15 of dewaterer 14.
According to above structure, during production, (one) dispensing is first carried out：Parts by weight meter, prepares 60 parts of nylon resins, 30 parts of aluminium boron
Silicate glass, 5 parts of carbon fibers, 2 parts of ZnOws, 5 parts of silane couplers and 0.8 part of four [β-(3,5- di-tert-butyls -4-
Hydroxy phenyl) propionic acid] pentaerythritol ester, by nylon resin, silane coupler and four [β-(3,5- di-tert-butyl -4- hydroxy benzenes
Base) propionic acid] the well mixed addition double screw extruder of pentaerythritol ester.
(2) extrusion cooling：By aluminium borosilicate glass, carbon fiber, ZnOw from the 5th area of barrel and SECTOR-SEVEN
Side drawing-in device at be uniformly added into double screw extruder, material is extruded after melting through module nib, with less than 15 DEG C
Chilled water is quickly cooled to type.
(3) granulate：Polymer after shaping obtains the particle of glass fiber reinforcement polyamide fibre 6 by hobboing cutter shearing.
(4) dry：Because granulation, cooling procedure are directly to be contacted with water, so the glass fibers after expressing technique
Dimension enhancing polyamide fibre 6 its water content is at a relatively high, and by industry requirement chinlon 6 section, aqueous to have to be lower than 0.08% be just certified products.Institute
Also needed to the section of obtained high rigidity high-strength polyamide 6 by being processed further that certified products can be turned into.Cut into slices first and water
Be dehydrated by dewaterer, the section after dehydration in drying tower with high temperature nitrogen countercurrently, by high temperature nitrogen will cut into slices in
Moisture content take away.
Above-described is only preferred embodiment of the present utility model, it is noted that for the ordinary skill of this area
For personnel, on the premise of the utility model creation design is not departed from, various modifications and improvements can be made, these all belong to
In protection domain of the present utility model.
Claims (1)
1. glass fiber reinforcement chinlon 6 section process units, it is mixed that its feature includes A blending tanks (4), double screw extruder (5) and B
Close tank (9), the wherein discharging opening of nylon resin measuring tank (1), the discharging opening of silane coupler measuring tank (2) and four [β-(3,5-
Di-tert-butyl -4- hydroxy phenyls) propionic acid] pentaerythritol ester measuring tank (3) discharging opening connection A blending tanks (4), A blending tanks (4)
Connect in double screw extruder (5), double screw extruder (5) and set barrel (6), the 5th area of barrel (6) sets A sides drawing-in device
(7), the SECTOR-SEVEN of barrel (6) sets B sides drawing-in device (8), and A sides drawing-in device (7) connects the first discharging opening of B blending tanks (9),
Second discharging opening of B sides drawing-in device (8) connection B blending tanks (9), B blending tanks (9) connection aluminium borosilicate glass measuring tank
(10) discharging opening of discharging opening, the discharging opening of carbon fiber measuring tank (11) and ZnOw measuring tank (12), twin-screw is squeezed
Go out machine (5) connection hobboing cutter pelleter (13), hobboing cutter pelleter (13) connection dewaterer (14), dewaterer (14) connection drying tower
(15)。
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621311709.4U CN206318925U (en) | 2016-12-01 | 2016-12-01 | Glass fiber reinforcement chinlon 6 section process units |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621311709.4U CN206318925U (en) | 2016-12-01 | 2016-12-01 | Glass fiber reinforcement chinlon 6 section process units |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206318925U true CN206318925U (en) | 2017-07-11 |
Family
ID=59265293
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621311709.4U Active CN206318925U (en) | 2016-12-01 | 2016-12-01 | Glass fiber reinforcement chinlon 6 section process units |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206318925U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108440957A (en) * | 2018-06-12 | 2018-08-24 | 江苏海阳锦纶新材料有限公司 | A kind of graphene modified Pa 6 process units and production technology |
| CN108517116A (en) * | 2018-06-12 | 2018-09-11 | 江苏海阳锦纶新材料有限公司 | A kind of graphene in-situ polymerization PA6 preparation systems and preparation method |
-
2016
- 2016-12-01 CN CN201621311709.4U patent/CN206318925U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108440957A (en) * | 2018-06-12 | 2018-08-24 | 江苏海阳锦纶新材料有限公司 | A kind of graphene modified Pa 6 process units and production technology |
| CN108517116A (en) * | 2018-06-12 | 2018-09-11 | 江苏海阳锦纶新材料有限公司 | A kind of graphene in-situ polymerization PA6 preparation systems and preparation method |
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