CN205799928U - A kind of high-concentration colorful Masterbatch process units system - Google Patents
A kind of high-concentration colorful Masterbatch process units system Download PDFInfo
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- CN205799928U CN205799928U CN201620545516.9U CN201620545516U CN205799928U CN 205799928 U CN205799928 U CN 205799928U CN 201620545516 U CN201620545516 U CN 201620545516U CN 205799928 U CN205799928 U CN 205799928U
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- feed mechanism
- discharging opening
- masterbatch
- transfer pipeline
- roll grinder
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- Extrusion Moulding Of Plastics Or The Like (AREA)
Abstract
The utility model discloses a kind of high-concentration colorful Masterbatch process units system, including high low speed batch mixer, the first feed mechanism, three-roll grinder, the second feed mechanism, double screw extruder, the discharging opening of described high low speed batch mixer is connected with the charging aperture of described three-roll grinder by described first feed mechanism, and the discharging opening of described three-roll grinder connects the charging aperture of described double screw extruder by described second feed mechanism.A kind of high-concentration colorful Masterbatch process units system of offer is provided, the Masterbatch color pigment prepared is at concentrations up to 50%~70%, wherein, three-roll grinder serves pivotal role for grinding and the dispersion of high-concentration colorful pigment, coordinating with high low speed batch mixer and make not rise in the course of processing dirt, feed mechanism achieves self-feeding, and collection material mixing plant is collected Masterbatch prepared by double screw extruder, automatically mixed, ensure the gloss on Masterbatch surface, improve production efficiency.
Description
Technical field
This utility model relates to Masterbatch and produces apparatus field, especially one high-concentration colorful Masterbatch process units system
System.
Background technology
Masterbatch is evenly dispersed in pigment in vector resin, has fixing shape, it is simple to client uses, addition
Little, clean without dust.In existing Masterbatch production technology, except titanium dioxide and calcium carbonate master batch concentration can reach 60%~80%
In addition, the organic pigment content that color pigment particularly oil absorption is high more than 20% after be difficult to dispersion.Pigment dispersion effect
Bad, granules of pigments is big, and Masterbatch surface is the most lackluster, but also spottiness and streak.
Utility model content
Utility model purpose: for the problems referred to above, the purpose of this utility model is to solve Masterbatch to produce middle and high concentration coloured silk
The scattering problem of color pigment, it is provided that a kind of high-concentration colorful Masterbatch process units system, prepares high-concentration colorful pigment, dispersion
The Masterbatch that property is good.
Technical scheme:
A kind of high-concentration colorful Masterbatch process units system, grinds including high low speed batch mixer, the first feed mechanism, three rollers
Grinding machine, the second feed mechanism, double screw extruder, the discharging opening of described high low speed batch mixer by described first feed mechanism with
The charging aperture connection of described three-roll grinder, the discharging opening of described three-roll grinder is described by described second feed mechanism connection
The charging aperture of double screw extruder.
Preferably, this process units system also include collect material mixing plant, described collection material mixing plant include aggregate bin,
Transfer pipeline, circulation transfer pipeline, the first aerator, the first loading hopper, the second aerator, the second loading hopper, described collection
Offering the first discharging opening below hopper, side-lower offers the second discharging opening, and described transfer pipeline one end is sequentially connected with described
First aerator and described first loading hopper, described circulation transfer pipeline one end is sequentially connected with described second aerator and described
Second loading hopper, the described transfer pipeline other end and the described circulation transfer pipeline other end all connect with above described aggregate bin
Logical, described second loading hopper is positioned at immediately below described first discharging opening, and described first loading hopper is installed on described twin screw
After extruder below the discharging opening of pelleter after.Masterbatch is sent to gather materials through transfer pipeline under the effect of the first aerator
Bucket, unmixed uniform Masterbatch enters the second loading hopper from the first discharging opening of aggregate bin, through circulation transfer pipeline transmission
To aggregate bin, discharge from the second discharging opening of aggregate bin after mix homogeneously.
Preferably, described the first feed mechanism, the second feed mechanism are elevator scoop.
Beneficial effect: compared with prior art, the utility model has the advantages that a kind of high-concentration colorful Masterbatch of offer is raw
Producing apparatus system, prepared Masterbatch color pigment is at concentrations up to 50%~70%, and wherein, the grinding of three-roll grinder makes coloured silk
Color granules of pigments is little, be uniformly dispersed, and high low speed batch mixer coordinates and makes not rise in the course of processing dirt, and feed mechanism achieves automatically
Feeding, collection material mixing plant collect double screw extruder prepare Masterbatch, automatically mix, it is ensured that the gloss on Masterbatch surface,
Improve production efficiency.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
Fig. 2 is the close-up schematic view in I region in Fig. 1;
Wherein, including 1 being high low speed batch mixer, 2 be the first feed mechanism, 3 be three-roll grinder, 4 being the second feeder
Structure, 5 be double screw extruder, 6 be aggregate bin, 7 be transfer pipeline, 8 be circulation transfer pipeline, 9 be the first aerator, 10 be the
One loading hopper, 11 be the second aerator, 12 be the second loading hopper, 13 be the first discharging opening, 14 be the second discharging opening, 15 be
Bosh, 16 be air-dry machine, 17 for pelleter.
Detailed description of the invention
Below in conjunction with the accompanying drawings and specific embodiment, it is further elucidated with this utility model, it should be understood that these embodiments are only used for
This utility model is described rather than limits scope of the present utility model, after having read this utility model, art technology
Personnel all fall within the application claims limited range to the amendment of the various equivalent form of values of the present utility model.
As shown in accompanying drawing 1,2, a kind of high-concentration colorful Masterbatch process units system, including high low speed batch mixer 1, first
Feed mechanism 2, three-roll grinder the 3, second feed mechanism 4, double screw extruder 5, collection material mixing plant.
The charging aperture of the first feed mechanism 2 is connected with the discharging opening of high low speed batch mixer 1, the discharging of the first feed mechanism 2
Mouth connects the charging aperture of three-roll grinder 3, and the charging aperture of the second feed mechanism 4 connects the discharging opening of three-roll grinder 3, and second send
The discharging opening of material mechanism 4 is connected with the charging aperture of double screw extruder 5.First feed mechanism the 2, second feed mechanism 4 uses and rises
Fall bucket, naturally it is also possible to other feed mechanism transferring raw material, it is achieved automatization's input and output material, improves production efficiency.Claim by proportioning
Take raw material, mix in high low speed batch mixer 1 and form bulk to raw material, by the first feed mechanism 2, block stock is added to three
Being ground in roller mill 3 to being uniformly dispersed, ground raw material adds double screw extruder 5 by the second feed mechanism 4
After extrusion, enter in bosh 15 and cool down, dried addition pelleter 17 pelletizing under the effect of air-dry machine 16.
Collection material mixing plant includes that aggregate bin 6, transfer pipeline 7, circulation transfer pipeline the 8, first aerator 9, first feed
Funnel the 10, second aerator the 11, second loading hopper 12, offers the first discharging opening 13 below aggregate bin 6, side-lower offers
Second discharging opening 14, transfer pipeline 7 one end is sequentially connected with the first aerator 9 and the first loading hopper 10, circulates transfer pipeline 8 one
It is equal that end is sequentially connected with the second aerator 11 and the second loading hopper 12, transfer pipeline 7 other end and circulation transfer pipeline 8 other end
Connecting with above aggregate bin 6, the second loading hopper 12 is positioned at immediately below the first discharging opening 13, and the first loading hopper 10 is installed on to be cut
Below grain machine 17, mix homogeneously during the Masterbatch of preparation adds collection material mixing plant in double screw extruder 5, from the second discharging opening
14 discharge.
First with high low speed batch mixer mixing raw material in this process units system, make the dust source such as color pigment toner and heat
Plastic resin forms bulk, and the dust source claddings such as color pigment are got up by resin, use and add in three-roll grinder process of lapping
The mode of heat utilizes resin heat deliquescing to make not rise in the course of processing dirt to the performance of liquid, and the product after processing is without dust, only
There is chip, pollution-free.
Using three-roll grinder in this process units system, grinding and dispersion for high-concentration colorful pigment serve pass
Key effect, mutually extruded by the surface of the three of level rollers and the friction of friction speed and make colored pigment particles little, point
Dissipating uniformly, the Masterbatch processed through this mode is because good dispersion, so the consumption of color pigment can be reduced.
Collection material mixing plant in this process units system utilizes the first aerator conveying, the second aerator circulation conveying,
Mixed Masterbatch, the most not Masterbatch of abrasion-resistant, mixing rear surface glossiness is good, Masterbatch mix homogeneously, it is to avoid
Use to follow-up Masterbatch brings error.
Claims (3)
1. a high-concentration colorful Masterbatch process units system, it is characterised in that: include high low speed batch mixer (1), first send
Material mechanism (2), three-roll grinder (3), the second feed mechanism (4), double screw extruder (5), described high low speed batch mixer (1)
Discharging opening is connected with the charging aperture of described three-roll grinder (3) by described first feed mechanism (2), described three-roll grinder
(3) discharging opening connects the charging aperture of described double screw extruder (5) by described second feed mechanism (4).
2. according to a kind of high-concentration colorful Masterbatch process units system described in claim 1, it is characterised in that: also include
Collection material mixing plant, described collection material mixing plant includes aggregate bin (6), transfer pipeline (7), circulation transfer pipeline (8), the first drum
Blower fan (9), the first loading hopper (10), the second aerator (11), the second loading hopper (12), described aggregate bin (6) lower section is opened
Being provided with the first discharging opening (13), side-lower offers the second discharging opening (14), and described transfer pipeline (7) one end is sequentially connected with described
First aerator (9) and described first loading hopper (10), described circulation transfer pipeline (8) one end is sequentially connected with described second drum
Blower fan (11) and described second loading hopper (12), described transfer pipeline (7) other end and described circulation transfer pipeline (8) another
End all connects with described aggregate bin (6) top, and described second loading hopper (12) is positioned at immediately below described first discharging opening (13),
After described first loading hopper (10) is installed on below the discharging opening of described double screw extruder (5) pelleter afterwards (17).
3. according to a kind of high-concentration colorful Masterbatch process units system described in claim 1, it is characterised in that: described
First feed mechanism (2), the second feed mechanism (4) are elevator scoop.
Priority Applications (1)
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CN201620545516.9U CN205799928U (en) | 2016-06-07 | 2016-06-07 | A kind of high-concentration colorful Masterbatch process units system |
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CN201620545516.9U CN205799928U (en) | 2016-06-07 | 2016-06-07 | A kind of high-concentration colorful Masterbatch process units system |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108103602A (en) * | 2018-02-01 | 2018-06-01 | 德清县利通绢纺塑化有限公司 | A kind of thin,tough silk bourette silk weaving spinning-drawing machine feed arrangement |
CN109533777A (en) * | 2017-09-22 | 2019-03-29 | 天津益三友色母料有限公司 | A kind of Masterbatch automatic cooling device |
CN109531862A (en) * | 2017-09-22 | 2019-03-29 | 天津益三友色母料有限公司 | A kind of coil type cooling device |
-
2016
- 2016-06-07 CN CN201620545516.9U patent/CN205799928U/en active Active
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109533777A (en) * | 2017-09-22 | 2019-03-29 | 天津益三友色母料有限公司 | A kind of Masterbatch automatic cooling device |
CN109531862A (en) * | 2017-09-22 | 2019-03-29 | 天津益三友色母料有限公司 | A kind of coil type cooling device |
CN108103602A (en) * | 2018-02-01 | 2018-06-01 | 德清县利通绢纺塑化有限公司 | A kind of thin,tough silk bourette silk weaving spinning-drawing machine feed arrangement |
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Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
TR01 | Transfer of patent right | ||
TR01 | Transfer of patent right |
Effective date of registration: 20180413 Address after: No. 80, Dagang Jin Gang Avenue, New District, Zhenjiang, Jiangsu Province Patentee after: OPTA POLYMER JIANGSU CO., LTD. Address before: 212132 Zhenjiang New District, Jiangsu, Hong Kong Avenue, No. 80 Patentee before: Aipute Polymer Jiangsu Co., Ltd. |