CN106519629A - Extra-dark PC/ABS alloy material and preparation method thereof - Google Patents
Extra-dark PC/ABS alloy material and preparation method thereof Download PDFInfo
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- CN106519629A CN106519629A CN201611073375.6A CN201611073375A CN106519629A CN 106519629 A CN106519629 A CN 106519629A CN 201611073375 A CN201611073375 A CN 201611073375A CN 106519629 A CN106519629 A CN 106519629A
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L69/00—Compositions of polycarbonates; Compositions of derivatives of polycarbonates
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/92—Measuring, controlling or regulating
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L55/00—Compositions of homopolymers or copolymers, obtained by polymerisation reactions only involving carbon-to-carbon unsaturated bonds, not provided for in groups C08L23/00 - C08L53/00
- C08L55/02—ABS [Acrylonitrile-Butadiene-Styrene] polymers
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92504—Controlled parameter
- B29C2948/9258—Velocity
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92504—Controlled parameter
- B29C2948/92704—Temperature
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2201/00—Properties
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2205/00—Polymer mixtures characterised by other features
- C08L2205/03—Polymer mixtures characterised by other features containing three or more polymers in a blend
- C08L2205/035—Polymer mixtures characterised by other features containing three or more polymers in a blend containing four or more polymers in a blend
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Abstract
The invention provides an extra-dark PC/ABS alloy material and a preparation method thereof. The alloy material comprises the following raw material components in parts by weight: 40-70 parts of PC resin, 30-60 parts of ABS resin, 1.5-2 parts of carbon black, 2-6 parts of mineral oil, 2-4 parts of PE wax and 0.5-2 parts of a coupling agent. The preparation method comprises the following steps: raw material mixing, melting and co-mixing, extruding and pelletizing, cooling, drying, grain-sized dicing and the like. According to the extra-dark PC/ABS alloy material and the preparation method thereof provided by the invention, dispersion of carbon block and liquidity of the alloy material are improved in a processing process, so that a color characterization value L of the alloy material is reduced to be 2, a melt flow rate reaches 27 g/10min, and a surface pitting phenomenon and a surface white-spot phenomenon are avoided; meanwhile, a preparation process is improved, pollution on environment in a preparation process is reduced, and finally, the PC/ABS alloy material which has excellent processing characteristics, extra-dark color, excellent dispersion, good surface glossiness and ultraviolet light resistance is finally prepared.
Description
Technical field
The present invention relates to polymer blended, Polymer Processing field, and in particular to a kind of goth black PC/ABS alloy materials
Material and preparation method thereof.
Background technology
The copolymer and mixture of PC/ABS, i.e. Merlon and acrylonitrile-butadiene-styrene (ABS), is by Merlon
(Polycarbonate) and polyacrylonitrile (ABS) alloy thermoplastic plastic rubber, combine the excellent spy of bi-material
Property, the property such as the mechanicalness of the mouldability and PC of ABS material, impact strength and heatproof, uvioresistant (UV), can be widely used in
On automotive interior parts, Business Machine, the communication apparatus, electrical home appliances and lighting apparatus.
The purpose of carbon black dispersion is for the requirement for meeting client to properties of product, by carbon black dispersion in PC/ABS, energy
Black and the PC/ABS alloy materials with premium properties are prepared enough, to meet the demand to market.However, due to carbon black
Dispersion and stability can not meet requirement sometimes, can affect the performance of product, cause material injection a large amount of numb into occurring during product
Point and hickie, the blackness of product decline, and outward appearance dimness does not have gloss.In addition the dust pollution when mixing is serious with resin for carbon black,
Certain harm is caused while pollution environment to human body, thus the target that the production technology of environmental protection is plant produced to be pursued it
One.
The mobility of material can greatly improve its processing characteristics, and general PC/ABS alloy material mobility is poor, leads
Cause which to be difficult machine-shaping, the very big wasting of resources can be brought to client, therefore, on the premise of other performances are not affected, such as
It is also a urgent problem that what effectively improves the mobility of material.
The content of the invention
In view of the shortcomings of the prior art, the invention provides a kind of goth black PC/ABS alloy materials and its preparation side
Method, improves the dispersiveness and the mobility of alloy material of carbon black in process so as to obtain excellent surface quality
And processing characteristics, while improving preparation technology, pollution of the dust to environment in preparation process is reduced, color is finally prepared
Goth black, surface gloss is good and the PC/ABS alloy materials with uvioresistant photosensitiveness.
In a first aspect, the present invention provides a kind of goth black PC/ABS alloy materials, the alloy material by mass parts contain with
Lower raw material components:
In the present invention, color table value indicative is L, and L values are less, illustrates color deeper (black), and when L≤3, the color can claim
For goth black.
In the present invention, synergy can be produced between mineral oil and PE waxes, greatly improves the mobility of material so as to be molten
Body flow rate has reached 27g/10min, obtains good processing characteristics;Association is produced between mineral oil, PE waxes and coupling agent
Same-action, greatly improves the dispersiveness of carbon black so as to which color table value indicative L value falls below 2, and surface is without pit and hickie phenomenon;Enter
And prepare Dispersion on surface well, color is goth black, and glossiness has well the goth black PC/ABS alloy materials of uvioresistant photosensitiveness concurrently.
According to the present invention, the content of the PC resin is 40-70 parts, can for example be 40 parts, 45 parts, 50 parts, 55 parts, 60
Part, the concrete point value between 65 parts or 70 parts, and above-mentioned numerical value, as space is limited and for simple and clear consideration, the present invention is no longer
The concrete point value that scope described in exclusive list includes.
According to the present invention, the content of the ABS resin is 30-60 parts, can for example be 30 parts, 35 parts, 40 parts, 45 parts,
Concrete point value between 50 parts, 55 parts or 60 parts, and above-mentioned numerical value, as space is limited and for simple and clear consideration, the present invention is not
The concrete point value that scope described in exclusive list includes again.
According to the present invention, the content of the carbon black is 1.5-2 parts, can for example be 1.5 parts, 1.6 parts, 1.7 parts, 1.8 parts,
Concrete point value between 1.9 parts or 2 parts, and above-mentioned numerical value, as space is limited and for simple and clear consideration, no longer limit of the invention
Enumerate the concrete point value that the scope includes.
According to the present invention, the content of the mineral oil is 2-6 parts, for example, can be 2 parts, 3 parts, 4 parts, 5 parts or 6 parts, with
And the concrete point value between above-mentioned numerical value, as space is limited and for simple and clear consideration, scope no longer described in exclusive list of the invention
Including concrete point value.
Mineral oil is also referred to as white oil, and the addition of mineral oil can make resin in moistened surface state, then adds carbon black and carry out
Mixing, now carbon black uniformly will be attached in resin surface, reduce the pollution of dust in mixing procedure.
In the present invention, synergy can be produced between mineral oil and PE waxes, greatly improves the mobility of material, mineral
Oil, between PE waxes and coupling agent, synergy is produced, greatly improve the dispersiveness of carbon black, obtain surface perfect and easy to process
The alloy resin of shaping.
According to the present invention, the content of the PE waxes is 2-4 parts, for example, can be 2 parts, 2.5 parts, 3 parts, 3.5 parts or 4 parts,
And the concrete point value between above-mentioned numerical value, as space is limited and for simple and clear consideration, model no longer described in exclusive list of the invention
Enclose including concrete point value.
PE waxes, also referred to as Tissuemat E, obtain because of its excellent cold resistance, heat resistance, chemical resistance and wearability extensively
Application.PE waxes can increase the gloss and processing characteristics of product as a kind of additive, improve the mobility of material, while energy
Play internal lubrication and the scattered effect of colouring agent.In the present invention, PE waxes and mineral oil can produce synergy together, greatly
Width improves the mobility of alloy material so as to obtain good processing characteristics.
According to the present invention, the content of the coupling agent is 0.5-2 parts, can for example be 0.5 part, 0.7 part, 0.9 part, 1 part,
Concrete point value between 1.2 parts, 1.4 parts, 1.6 parts, 1.8 parts or 2 parts, and above-mentioned numerical value, as space is limited and for simple and clear
Consider, the present invention concrete point value that no longer scope described in exclusive list includes.
In the present invention, coupling agent produces synergy with mineral oil and PE waxes, the dispersiveness of carbon black greatly improved, makes
Obtained PC/ABS alloy material surfaces favorable dispersibility, without pit and hickie phenomenon, color is goth black, and surface gloss is good.
According to the present invention, in the goth black PC/ABS alloy materials, contain 1-2 part antioxidant, the content of the antioxidant can
Being 1 part, 1.1 parts, 1.2 parts, 1.3 parts, 1.4 parts, 1.5 parts, 1.6 parts, 1.7 parts, 1.8 parts, 1.9 parts or 2 parts, and above-mentioned number
Concrete point value between value, as space is limited and for simple and clear consideration, the present invention tool that no longer scope described in exclusive list includes
Body point value.
According to the present invention, the antioxidant is irgasfos 168, antioxidant 1010, antioxidant 1076,6- book butyl -3- first
In the double lauryls of base phenol or thio-2 acid any one or at least two combination, can for example be irgasfos 168, anti-
Any one in the double lauryls of oxygen agent 1010, antioxidant 1076,6- books butyl -3- methylphenols or thio-2 acid, example
But non-limiting is combined as irgasfos 168 and antioxidant 1010, antioxidant 1076 and 6- book butyl -3- methylphenols, antioxygen
The double lauryls of agent 168 and antioxidant 1076,6- books butyl -3- methylphenols and thio-2 acid, irgasfos 168, antioxidant
1010 and antioxidant 1076, the double lauryls of irgasfos 168, antioxidant 1076,6- books butyl -3- methylphenols and thio-2 acid
Deng.
In the present invention, the antioxidant is preferably the combination of irgasfos 168 and antioxidant 1010.
According to the present invention, the irgasfos 168 is (1-3) with the mass ratio of antioxidant 1010:1, can for example be 1:1、
1.5:1、2:1、2.5:1 or 3:Concrete point value between 1, and above-mentioned numerical value, as space is limited and for simple and clear consideration, this
The concrete point value that scope described in bright no longer exclusive list includes.
Heretofore described irgasfos 168 is preferably 1 with the mass ratio of antioxidant 1010:1.
For most of plastics varieties, in its manufacture, processing, storage and application process, oxidative degradation is had
Certain sensitiveness, oxygen are penetrated into and almost can be reacted with most polymers and cause to degrade or be crosslinked in plastics, so as to
Change the performance of material.A small amount of oxygen can just make intensity, outward appearance and the performance of these macromolecular materials that violent change occurs, and resist
The addition of oxygen agent can prevent because oxygen penetrate into and caused material property it is aging, while with ultraviolet light shine effect.
According to the present invention, contain 1-2 part lubricants in the goth black PC/ABS alloy materials, the lubricant contains
Amount can be 1 part, 1.1 parts, 1.2 parts, 1.3 parts, 1.4 parts, 1.5 parts, 1.6 parts, 1.7 parts, 1.8 parts, 1.9 parts or 2 parts, Yi Jishang
The concrete point value between numerical value is stated, as space is limited and for simple and clear consideration, no longer scope described in exclusive list of the invention includes
Concrete point value.
In the present invention, the lubricant is that ethylene group bis-stearamides (EBS), glyceryl monostearate (GMS) or three are hard
In glycerol (HTG) any one or at least two combination, can for example be any one in EBS, GMS or HTG
Kind;It is typical but infinite be combined as EBS and GMS, EBS and HTG, GMS and HTG, EBS, GMS and HTG.
In the present invention, the lubricant is preferably ethylene group bis-stearamides (EBS).
Exemplary, the goth black PC/ABS alloy materials are made up of following raw material components by mass parts, but non-are only limitted to
This:
Exemplary, the goth black PC/ABS alloy materials are made up of following raw material components by mass parts, but non-are only limitted to
This:
According to the present invention, the particle diameter of the carbon black is 10-14nm, can for example be 10nm, 11nm, 12nm, 13nm or
Concrete point value between 14nm, and above-mentioned numerical value, as space is limited and for simple and clear consideration, the present invention no longer exclusive list institute
State the concrete point value that scope includes.
According to the present invention, the tinting strength, tinting power of the carbon black is 160-170, can for example be 160,161,162,163,164,
165th, the concrete point value between 166,167,168,169 or 170, and above-mentioned numerical value, as space is limited and for simple and clear consideration,
The present invention concrete point value that no longer scope described in exclusive list includes.
According to the present invention, the oil factor of the carbon black is 310-350m2/ g, for example, can be 310m2/g、315m2/g、
320m2/g、325m2/g、330m2/g、335m2/g、340m2/g、345m2/ g or 350m2It is concrete between/g, and above-mentioned numerical value
Point value, as space is limited and for simple and clear consideration, the present invention concrete point value that no longer scope described in exclusive list includes.
The carbon black that the present invention is selected is a kind of with the high-quality extremely pure carbon black of special construction, dispersiveness little with granularity
Well, high coloring power, ultraviolet resistance and anlistatig feature, the light resistance and weather resisteant of the carbon black are stronger, while and a kind of high
The cheap photomask agent of effect, so goth black PC/ABS alloys prepared by the present invention have the anti-characteristic of uvioresistant light shine.It is high-quality
The addition of the carbon black of amount is favorably improved its dispersiveness in alloy material.
In the present invention, the coupling agent is silane coupler or titanate coupling agent.
In the present invention, the coupling agent is preferably silane coupler KH570.
Second aspect, the present invention provide a kind of preparation method of goth black PC/ABS alloy materials as described in relation to the first aspect,
The method is comprised the following steps:
(1) the raw material PC resin of formula ratio, ABS resin, PE waxes, mineral oil and coupling agent are mixed, obtains compound A;
(2) add carbon black to be mixed in the compound A obtained to step (1), obtain compound B;
(3) the compound B that step (2) is obtained is added to into extruder, sequentially passing through nine hot-zones carries out melt blending;
(4) compound after step (3) melt blending is extruded, Jing coolings, dry, pelletizing obtain goth black PC/ABS and close
Golden material.
According to the present invention, in the raw material of step (1) formula ratio, also contain antioxidant and/or lubricant.
According to the present invention, step (1) and step (2) mixing are carried out in high-speed mixer.
According to the present invention, during step (1) mixing, the rotating speed of mixer is 750-800r/min, for example, can be
It is concrete between 750r/min, 760r/min, 770r/min, 780r/min, 790r/min or 800r/min, and above-mentioned numerical value
Point value, as space is limited and for simple and clear consideration, the present invention concrete point value that no longer scope described in exclusive list includes.
According to the present invention, the time of step (1) mixing is 2-3min, can for example be 2min, 2.2min,
Concrete point value between 2.4min, 2.6min, 2.8min or 3min, and above-mentioned numerical value, is examined as space is limited and for simple and clear
Consider, the present invention concrete point value that no longer scope described in exclusive list includes.
According to the present invention, during step (2) mixing, the rotating speed of mixer is 1500-1600r/min, for example, can be
1500r/min、1510r/min、1520r/min、1530r/min、1540r/min、1550r/min、1560r/min、1570r/
Concrete point value between min, 1580r/min, 1590r/min or 1600r/min, and above-mentioned numerical value, as space is limited and for
Simple and clear consideration, the present invention concrete point value that no longer scope described in exclusive list includes.
In the present invention, by selecting first by PC resin, ABS resin, PE waxes, mineral oil, antioxidant, lubricant and coupling agent
Mixed under relatively low mixing velocity, then adding carbon black carries out the mode of mixed at high speed, and selects specific dispersion
Speed and jitter time make carbon black carry out more efficient dispersion with resin, improve the dispersiveness of carbon black, contribute to acquisition table
Face is well dispersed, the good PC/ABS alloy materials of outward appearance.
According to the present invention, the time of step (2) mixing is 3-5min, can for example be 3min, 3.5min, 4min,
Concrete point value between 4.5min or 5min, and above-mentioned numerical value, as space is limited and for simple and clear consideration, the present invention is no longer poor
Enumerate to the greatest extent the concrete point value that the scope includes.
According to the present invention, step (3) extruder is double screw extruder.
According to the present invention, in the double screw extruder, screw speed is 250-350r/min, for example, can be 250r/
min、260r/min、270r/min、280r/min、290r/min、300r/min、310r/min、320r/min、330r/min、
Concrete point value between 340r/min or 350r/min, and above-mentioned numerical value, as space is limited and for simple and clear consideration, the present invention
The concrete point value that no longer scope described in exclusive list includes.
According to the present invention, the temperature of step (3) melt blending is 210-275 DEG C, for example, can be 210 DEG C, 215
DEG C, 220 DEG C, 225 DEG C, 230 DEG C, 235 DEG C, 240 DEG C, 245 DEG C, 255 DEG C, 260 DEG C, 265 DEG C, 270 DEG C or 275 DEG C, Yi Jishang
The concrete point value between numerical value is stated, as space is limited and for simple and clear consideration, no longer scope described in exclusive list of the invention includes
Concrete point value.
In the present invention, it is described sequentially pass through nine hot-zones and carry out melt blending mean:After compound is added to extruder, Jing
Cross first hot-zone, first hot-zone, second hot-zone, the 3rd hot-zone, the 4th hot-zone, the 5th hot-zone, the 6th it is hot
Area, the 7th hot-zone, the 8th hot-zone and the 9th hot-zone, each hot-zone set different temperature, and successively compound is carried out
Heating so as to melt blending.
According to the present invention, in step (3) nine hot-zones, the temperature of first hot-zone is 210-230 DEG C, for example can be with
It is the concrete point value between 210 DEG C, 215 DEG C, 220 DEG C, 225 DEG C or 230 DEG C, and above-mentioned numerical value, as space is limited and for letter
Bright consideration, the present invention concrete point value that no longer scope described in exclusive list includes.
According to the present invention, in step (3) nine hot-zones, the temperature of second hot-zone is 230-245 DEG C, for example can be with
It is the concrete point value between 230 DEG C, 235 DEG C, 240 DEG C or 245 DEG C, and above-mentioned numerical value, examines as space is limited and for simple and clear
Consider, the present invention concrete point value that no longer scope described in exclusive list includes.
According to the present invention, in step (3) nine hot-zones, the temperature of the 3rd hot-zone is 245-255 DEG C, for example can be with
It is the concrete point value between 245 DEG C, 248 DEG C, 250 DEG C, 253 DEG C or 255 DEG C, and above-mentioned numerical value, as space is limited and for letter
Bright consideration, the present invention concrete point value that no longer scope described in exclusive list includes.
According to the present invention, in step (3) nine hot-zones, the temperature of the 4th hot-zone is 255-265 DEG C, for example can be with
It is the concrete point value between 255 DEG C, 258 DEG C, 260 DEG C, 263 DEG C or 265 DEG C, and above-mentioned numerical value, as space is limited and for letter
Bright consideration, the present invention concrete point value that no longer scope described in exclusive list includes.
According to the present invention, in step (3) nine hot-zones, the temperature of the 5th hot-zone is 265-270 DEG C, for example can be with
The concrete point value between 265 DEG C, 266 DEG C, 267 DEG C, 268 DEG C, 269 DEG C or 270 DEG C, and above-mentioned numerical value, as space is limited and
For simple and clear consideration, the present invention concrete point value that no longer scope described in exclusive list includes.
According to the present invention, in step (3) nine hot-zones, the temperature of the 6th hot-zone is 270-275 DEG C, for example can be with
The concrete point value between 270 DEG C, 271 DEG C, 272 DEG C, 273 DEG C, 274 DEG C or 275 DEG C, and above-mentioned numerical value, as space is limited and
For simple and clear consideration, the present invention concrete point value that no longer scope described in exclusive list includes.
According to the present invention, in step (3) nine hot-zones, the temperature of the 7th hot-zone is 265-270 DEG C, for example can be with
The concrete point value between 265 DEG C, 266 DEG C, 267 DEG C, 268 DEG C, 269 DEG C or 270 DEG C, and above-mentioned numerical value, as space is limited and
For simple and clear consideration, the present invention concrete point value that no longer scope described in exclusive list includes.
According to the present invention, in step (3) nine hot-zones, the temperature of the 8th hot-zone is 250-265 DEG C, for example can be with
It is the concrete point value between 250 DEG C, 253 DEG C, 255 DEG C, 258 DEG C, 260 DEG C, 263 DEG C or 265 DEG C, and above-mentioned numerical value, is limited to
Length and for simple and clear consideration, the present invention concrete point value that no longer scope described in exclusive list includes.
According to the present invention, in step (3) nine hot-zones, the temperature of the 9th hot-zone is 245-260 DEG C, for example can be with
It is the concrete point value between 245 DEG C, 248 DEG C, 250 DEG C, 253 DEG C, 255 DEG C, 258 DEG C or 260 DEG C, and above-mentioned numerical value, is limited to
Length and for simple and clear consideration, the present invention concrete point value that no longer scope described in exclusive list includes.
According to the present invention, step (3) it is described melting co-extrusion time be 1-3min, can for example be 1min, 1.5min,
Concrete point value between 2min, 2.5min or 3min, and above-mentioned numerical value, as space is limited and for simple and clear consideration, the present invention
The concrete point value that no longer scope described in exclusive list includes.
In the present invention, compound is sequentially passed through nine hot-zones carries out melting co-extrusion, specific by setting each hot-zone
Temperature so as to good mobility is obtained during flow forward co-extrusion, the processing characteristics of material is favorably improved.
Compared with prior art, the present invention at least has the advantages that:
(1) improve dispersiveness of the carbon black in PC/ABS alloy materials so as to which color table value indicative L value falls below 2, surface
Without pit and hickie phenomenon, Dispersion on surface is prepared well, color is goth black, and glossiness has well the goth black PC/ of uvioresistant photosensitiveness concurrently
ABS alloy material.
(2) improve the mobility of PC/ABS alloy materials so as to which melt flow rate (MFR) has reached 27g/10min, and then
Obtain excellent processing characteristics.
(3) preparation technology environmental protection, reduces harm of the dust to environment and human body in process of production.
Description of the drawings
The outside drawing of goth black PC/ABS alloy materials of the Fig. 1 to prepare in the embodiment of the present invention 3.
Fig. 2 is further processed into the outer of product for the goth black PC/ABS alloy materials prepared in the embodiment of the present invention 3
See figure.
Specific embodiment
For ease of understanding, it is as follows that the present invention enumerates embodiment.It will be understood to those of skill in the art that following examples are only
The preferred embodiments of the present invention, are only used for help and understand the present invention, thus should not be taken as limiting the scope of the invention.
Embodiment 1
By raw material proportioning (being shown in Table 1), by PC resin, ABS resin, PE waxes, mineral oil, antioxidant, lubricant and coupling agent
It is mixed in high-speed mixer, 2min is blended under the rotating speed of 750r/min;Carbon black is added thereto to, turning in 1500r/min
Speed is lower to continue blending 3min;The compound for obtaining is added in double screw extruder and is extruded, sequentially passing through nine hot-zones is carried out
Melting co-extrusion, set the rotating speed of double screw extruder as 250r/min, area's temperature be 210 DEG C, two area's temperature be 230 DEG C, three
Area's temperature is 245 DEG C, and four area's temperature are 255 DEG C, and five area's temperature are 265 DEG C, and six area's temperature are 270 DEG C, and seven area's temperature are 265
DEG C, eight area's temperature are 250 DEG C, and nine area's temperature are 245 DEG C, co-extrusion 1min;Compound after melting co-extrusion is extruded, Jing coolings,
Dry, pelletizing, obtains goth black PC/ABS alloy materials.
Embodiment 2
By raw material proportioning (being shown in Table 1), by PC resin, ABS resin, PE waxes, mineral oil, antioxidant, lubricant and coupling agent
It is mixed in high-speed mixer, 3min is blended under the rotating speed of 800r/min;Carbon black is added thereto to, turning in 1600r/min
Speed is lower to continue blending 5min;The compound for obtaining is added in double screw extruder, nine hot-zones is sequentially passed through and is melted
Co-extrusion, sets the rotating speed of double screw extruder as 350r/min, and area's temperature is 230 DEG C, and two area's temperature are 245 DEG C, three area's temperature
Spend for 255 DEG C, four area's temperature are 265 DEG C, five area's temperature are 270 DEG C, six area's temperature are 275 DEG C, seven area's temperature are 270 DEG C, eight
Area's temperature is 265 DEG C, and nine area's temperature are 260 DEG C, co-extrusion 3min;By after melt blending compound extrude, Jing cooling, be dried,
Pelletizing, obtains goth black PC/ABS alloy materials.
Embodiment 3
By raw material proportioning (being shown in Table 1), by PC resin, ABS resin, PE waxes, mineral oil, antioxidant, lubricant and coupling agent
It is mixed in high-speed mixer, 2.5min is blended under the rotating speed of 780r/min;Carbon black is added thereto to, 1550r/min's
Continue blending 4min under rotating speed;The compound for obtaining is added in double screw extruder, nine hot-zones is sequentially passed through and is melted
Melting co-extrusion, the rotating speed of double screw extruder being set as 300r/min, area's temperature is 220 DEG C, two area's temperature are 240 DEG C, 3rd area
Temperature is 250 DEG C, and four area's temperature are 260 DEG C, and five area's temperature are 265 DEG C, and six area's temperature are 270 DEG C, and seven area's temperature are 275 DEG C,
Eight area's temperature are 260 DEG C, and nine area's temperature are 255 DEG C, and 3min is blended;Compound after melt blending is extruded, Jing is cooled down, done
Dry, pelletizing, obtains goth black PC/ABS alloy materials.
The outside drawing of the goth black PC/ABS alloy materials that Fig. 1 is prepared for the present embodiment, as seen from the figure, the resin alloy
Material surface is perfect, and color is goth black, and color table value indicative L of general same type black material is 5-6, but its L value has reached 2,
Give people a kind of enjoyment of U.S..
Fig. 2 is further processed into the outer of product for the goth black PC/ABS alloy materials prepared in the embodiment of the present invention 3
See figure.As seen from the figure, the products appearance being molded is goth black, and surface is smooth and has the same gloss of metal, great aesthetic values.
According to the preparation method of embodiment 3, embodiment 4 and 5 and the PC/ABS alloy materials in comparative example 1-7 are prepared,
The raw material components (mass parts) of each embodiment and comparative example are as shown in table 1.
Table 1
Performance test:
The measure of color table value indicative:It is measured on colour photometer, color table value indicative is L, and L values are less, illustrates that color is got over
Deep (black), the dispersiveness of carbon black are better.
Fluidity testing:Its melt flow rate (MFR) is entered using melt flow rate (MFR) tester by the test method of GB3682
Row is determined, and melt flow rate (MFR) is bigger, and material flowability is better.
The evaluation of surface quality:Surface quality grades are carried out to which according to the standard in table 2 to evaluate, surface quality is got over
It is good, illustrate that the dispersiveness of carbon black is better.
Table 2
Measurement result is as shown in table 3.
Table 3
Understand through contrast:
The melt flow rate (MFR) of the PC/ABS alloy materials obtained in embodiment 3 has reached 27g/10min, color table value indicative
L is 2, and surface quality grades are 1 grade, and very well, color is goth black for its mobility.Embodiment 1 and 2 is by comparison, although component is the same,
But its preparation technology is slightly different, the PC/ABS alloy materials performance which prepares is more weaker than embodiment 3.Equally, implement
Compared with Example 3, preparation technology is although identical for example 4 and 5, but component proportion is different, the PC/ABS alloy materials which obtains
Performance is also not so good as embodiment 3, therefore embodiment 3 for the optimum component proportion of the present invention and preparation technology.
Compared with Example 3, mineral oil, PE waxes and coupling agent are eliminated in comparative example 1, its melt flow rate (MFR) is 14g/
10min, color table value indicative L are 6, and surface quality grades are 4 grades, and properties decline obvious.
Compared with comparative example 1, comparative example 2 adds mineral oil, and its melt flow rate (MFR) increased 7g/10min, color table
Value indicative L reduces 2, and surface quality grades improve 1 grade, illustrates only to add mineral oil to can be good at improving the mobility of material
With the dispersiveness of carbon black, but the effect of embodiment 3 can not be reached.
Compared with comparative example 1, comparative example 3 adds PE waxes, and its melt flow rate (MFR) increased 2g/10min, characterization
Value L reduces 1, and surface quality grades improve 1 grade, illustrates only to add PE waxes slightly improve the mobility of material, but carries
High is limited, while the dispersiveness of carbon black can be improved, but can not reach the effect of embodiment 3.
Compared with comparative example 1, in comparative example 4, coupling agent is added, its melt flow rate (MFR), color table value indicative and surface
Credit rating does not change, and illustrates only to add coupling agent to have no impact to the dispersiveness of the mobility and carbon black of material.
Compared with comparative example 1, mineral oil and PE waxes in comparative example 5, are added, its melt flow rate (MFR) is 27g/10min,
It is in the same manner as in Example 3, understand with reference to comparative example 2 and comparative example 3, mineral oil and PE waxes produce synergy, greatly improved
The mobility of material.Compare with comparative example 2 with comparative example 3, its color table value indicative L is 3, and surface quality grades are improved to 2 grades, are said
It is bright to there is therebetween synergy, it is possible to increase the dispersiveness of carbon black, but the effect of embodiment 3 can not be reached.
Compared with comparative example 1, mineral oil and coupling agent in comparative example 6, are added, now the properties of material and contrast
All same in example 2, illustrates there is no therebetween synergy.
Compared with comparative example 1, PE waxes and coupling agent in comparative example 7, are added, compared with comparative example 3, its every numerical value is equal
Do not change, illustrate there is no therebetween synergy.
Compared with comparative example 5, in embodiment 3, coupling agent is added, its color table value indicative L reduces 1, surface quality grades
1 grade is improve, understands that the addition of coupling agent can produce association and mineral oil and PE waxes between with reference to comparative example 6 and comparative example 7
Same-action, improves the dispersiveness of carbon black, and which individually has no synergy, three's collective effect and mineral oil and PE waxes between
Improve the dispersiveness of carbon black, it is indispensable.
In sum, synergy can be produced between mineral oil and PE waxes, greatly improves the mobility of material so as to melt
Flow rate has reached 27g/10min;In addition synergy is produced between mineral oil, PE waxes and coupling agent three, greatly improve
The dispersiveness of carbon black so as to which color table value indicative L falls below 2, and surface quality grades have reached 1 grade;And then prepare Dispersion on surface
Well, color is goth black, and glossiness has well the goth black PC/ABS alloy materials of uvioresistant photosensitiveness concurrently.
The preferred embodiment of the present invention described in detail above, but, the present invention is not limited in above-mentioned embodiment
Detail, the present invention range of the technology design in, various simple variants can be carried out to technical scheme, this
A little simple variants belong to protection scope of the present invention.
It is further to note that each particular technique feature described in above-mentioned specific embodiment, in not lance
In the case of shield, can be combined by any suitable means, in order to avoid unnecessary repetition, the present invention to it is various can
The combination of energy is no longer separately illustrated.
Additionally, can also be combined between a variety of embodiments of the present invention, as long as which is without prejudice to this
The thought of invention, which should equally be considered as content disclosed in this invention.
Claims (10)
1. a kind of goth black PC/ABS alloy materials, it is characterised in that the alloy material contains following raw material components by mass parts:
2. goth black PC/ABS alloy materials as claimed in claim 1, it is characterised in that contain 1-2 parts in the alloy material
Antioxidant;
Preferably, the antioxidant be irgasfos 168, antioxidant 1010, antioxidant 1076,6- books butyl -3- methylphenols or
In the double lauryl of thio-2 acid any one or at least two combination, preferably irgasfos 168 and antioxidant 1010
Combination;
Preferably, the irgasfos 168 and the mass ratio of antioxidant 1010 are (1-3):1, preferably 1:1;
Preferably, the goth black PC/ABS alloy materials contain 1-2 part lubricants;
Preferably, the lubricant is appointing in ethylene group bis-stearamides, glyceryl monostearate or glyceryl tristearate
Meaning it is a kind of or at least two combinations, preferably ethylene group bis-stearamides.
3. goth black PC/ABS alloy materials as claimed in claim 1 or 2, it is characterised in that the alloy material presses mass parts
It is made up of following raw material components:
4. goth black PC/ABS alloy materials as described in any one of claim 1-3, it is characterised in that the alloy material presses matter
Amount part is made up of following raw material components:
5. goth black PC/ABS alloy materials as described in any one of claim 1-4, it is characterised in that the particle diameter of the carbon black is
10-14nm;
Preferably, the tinting strength, tinting power of the carbon black is 160-170;
Preferably, the oil factor of the carbon black is 310-350m2/g。
6. goth black PC/ABS alloy materials as described in any one of claim 1-5, it is characterised in that the coupling agent is silane
Coupling agent or titanate coupling agent, preferably silane coupler KH570.
7. the preparation method of the goth black PC/ABS alloy materials as described in any one of claim 1-6, it is characterised in that the side
Method is comprised the following steps:
(1) the raw material PC resin of formula ratio, ABS resin, PE waxes, mineral oil and coupling agent are mixed, obtains compound A;
(2) add carbon black to be mixed in the compound A obtained to step (1), obtain compound B;
(3) the compound B that step (2) is obtained is added to into extruder, sequentially passing through nine hot-zones carries out melt blending;
(4) compound after step (3) melt blending is extruded, Jing coolings, dry, pelletizing obtain goth black PC/ABS alloy materials
Material.
8. preparation method as claimed in claim 7, it is characterised in that the raw material of step (1) formula ratio also includes antioxygen
Agent and/or lubricant;
Preferably, step (1) and step (2) mixing is carried out in high-speed mixer;
Preferably, during step (1) mixing, the rotating speed of mixer is 750-800r/min;
Preferably, the time of step (1) mixing is 2-3min;
Preferably, during step (2) mixing, the rotating speed of mixer is 1500-1600r/min;
Preferably, the time of step (2) mixing is 3-5min.
9. preparation method as claimed in claim 7 or 8, it is characterised in that step (3) extruder is twin-screw extrusion
Machine;
Preferably, in the double screw extruder, screw speed is 250-350r/min.
10. the preparation method as described in any one of claim 7-9, it is characterised in that the temperature of step (3) melt blending
For 210-275 DEG C;
Preferably, in step (3) nine hot-zones, the temperature of first hot-zone is 210-230 DEG C;
Preferably, in step (3) nine hot-zones, the temperature of second hot-zone is 230-245 DEG C;
Preferably, in step (3) nine hot-zones, the temperature of the 3rd hot-zone is 245-255 DEG C;
Preferably, in step (3) nine hot-zones, the temperature of the 4th hot-zone is 255-265 DEG C;
Preferably, in step (3) nine hot-zones, the temperature of the 5th hot-zone is 265-270 DEG C;
Preferably, in step (3) nine hot-zones, the temperature of the 6th hot-zone is 270-275 DEG C;
Preferably, in step (3) nine hot-zones, the temperature of the 7th hot-zone is 265-270 DEG C;
Preferably, in step (3) nine hot-zones, the temperature of the 8th hot-zone is 250-265 DEG C;
Preferably, in step (3) nine hot-zones, the temperature of the 9th hot-zone is 245-260 DEG C;
Preferably, the time of step (3) melt blending is 1-3min.
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Cited By (3)
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CN110724373A (en) * | 2019-09-27 | 2020-01-24 | 上海长伟锦磁工程塑料有限公司 | PC/ABS alloy with no pockmark, high weather resistance, high black and bright and spraying-free effect and preparation method thereof |
CN110982239A (en) * | 2019-12-23 | 2020-04-10 | 上海日之升科技有限公司 | High-blackness PC/ABS alloy material for automotive interior parts and preparation method thereof |
CN112375366A (en) * | 2020-12-01 | 2021-02-19 | 上海中镭新材料科技有限公司 | Highlight spray-free ultra-black PC/ASA alloy material and preparation method thereof |
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CN104479325A (en) * | 2014-12-08 | 2015-04-01 | 苏州新区佳合塑胶有限公司 | Plastic material for electronic product casing |
CN104788931A (en) * | 2015-04-28 | 2015-07-22 | 上海锦湖日丽塑料有限公司 | Sunlight-resistant PC/ABS alloy material and preparation method thereof |
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CN104479325A (en) * | 2014-12-08 | 2015-04-01 | 苏州新区佳合塑胶有限公司 | Plastic material for electronic product casing |
CN104788931A (en) * | 2015-04-28 | 2015-07-22 | 上海锦湖日丽塑料有限公司 | Sunlight-resistant PC/ABS alloy material and preparation method thereof |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
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CN110724373A (en) * | 2019-09-27 | 2020-01-24 | 上海长伟锦磁工程塑料有限公司 | PC/ABS alloy with no pockmark, high weather resistance, high black and bright and spraying-free effect and preparation method thereof |
CN110724373B (en) * | 2019-09-27 | 2022-04-05 | 上海长伟锦磁工程塑料有限公司 | PC/ABS alloy with no pockmark, high weather resistance, high black and bright and spraying-free effect and preparation method thereof |
CN110982239A (en) * | 2019-12-23 | 2020-04-10 | 上海日之升科技有限公司 | High-blackness PC/ABS alloy material for automotive interior parts and preparation method thereof |
CN110982239B (en) * | 2019-12-23 | 2022-03-11 | 上海日之升科技有限公司 | High-blackness PC/ABS alloy material for automotive interior parts and preparation method thereof |
CN112375366A (en) * | 2020-12-01 | 2021-02-19 | 上海中镭新材料科技有限公司 | Highlight spray-free ultra-black PC/ASA alloy material and preparation method thereof |
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