CN105647005B - A kind of low-luster polypropylene and preparation method thereof for automotive interior material - Google Patents
A kind of low-luster polypropylene and preparation method thereof for automotive interior material Download PDFInfo
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- CN105647005B CN105647005B CN201410673597.6A CN201410673597A CN105647005B CN 105647005 B CN105647005 B CN 105647005B CN 201410673597 A CN201410673597 A CN 201410673597A CN 105647005 B CN105647005 B CN 105647005B
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Abstract
The low-luster polypropylene and preparation method thereof that the invention discloses a kind of for automotive interior material, it is by 100 parts of polypropylene, 0 ~ 50 part of inorganic filler, 0 ~ 25 part of toughener, 0 ~ 0.5 part of coupling agent, 0.1 ~ 0.5 part of antioxidant, 0 ~ 0.5 part of the steady agent of light, 0.2 ~ 0.8 part of lubricant, 3 ~ 10 parts of matt master are mixed in batches, squeeze out to make and expect to be made.Wherein matt master is to be mixed by low density polyethylene (LDPE), aromatic amides class compound, lubricant and antioxidant, squeeze out to make and expect to be made.The present invention reduces the glossiness of polypropylene material significantly, to meet its comfort requirement as automotive interior material, has a extensive future by the way that special matt master is added.
Description
Technical field:
The present invention relates to polymer modification fields, the more particularly, to low-luster polypropylene of automotive interior material
And preparation method thereof.
Background technique:
Polypropylene (referred to as: PP) material due at low cost, light weight, chemical-resistance is good, processing performance is excellent, Yi Huishou
The advantages that, it is widely used in automobile and household electric appliances in recent years, is applied especially to inner and outer decorative parts of automobile, such as: door internal decoration plate, instrument
Plate, column, seat backplate, bumper, side encirclement, deflector, mud guard etc..With the improvement of people's life quality, people couple
Comfort and requirement in car steering room is also higher and higher, if the glossiness of plastic ornament is higher in driver's cabin, just has
Stronger light reflection, to influence the comfort of driver.Therefore in recent years, many automobile main frame maker require vapour one after another
Vehicle developing material quotient develops the polypropylene interior material of low gloss to adapt to the demand in market.
The method for reducing material glossiness at present is roughly divided into three classes:
1, coated matte paint reduces surface gloss on automotive material product, increases production process and is produced into
This.
2, texture processing is carried out to mold, so that the article surface got has lines to reduce surface gloss, increases mould
Have development cost and article surface easily hides ash and is not easy to clean.
3, processing is modified to automotive material itself, adds some delustering agents, such as: silica, talcum powder, calcium carbonate
Deng.But addition the above material need to control partial size in 5 microns, and additive amount is best in 5 ~ 10% effects, right this institute
It calls that optimal extinction effect is also very unsatisfactory, still can not meet requirement of certain main engine plants to low-luster polypropylene material.
Summary of the invention:
The low-luster polypropylene and preparation method thereof that the purpose of the present invention is to provide a kind of for automotive interior material.
Aromatic amides class compound is used as polypropylene delustering agent for the first time and is made into delustring mother with low density polyethylene (LDPE) by the present invention
Grain is added in PP composite material, and dispersion effect is good, and extinction effect is good.
A kind of low-luster polypropylene for automotive interior material is prepared by weight by following components:
100 parts of polypropylene,
0 ~ 50 part of inorganic filler,
0 ~ 25 part of toughener,
0 ~ 0.5 part of coupling agent,
0.1 ~ 0.5 part of antioxidant,
0 ~ 0.5 part of the steady agent of light,
0.2 ~ 0.8 part of lubricant,
3 ~ 10 parts of matt master;
The matt master is made by weight through mixing, extruding pelletization by following component:
100 parts of low density polyethylene (LDPE),
20 ~ 40 parts of aromatic amides class compound,
0.1 ~ 0.3 part of lubricant,
0.1 ~ 0.3 part of antioxidant.
The matt master the preparation method comprises the following steps: by low density polyethylene (LDPE), aromatic amides class compound, lubricant, antioxygen
Room temperature mixes 3 ~ 8 minutes in a high speed mixer for agent, and wherein the revolving speed of high-speed mixer is 200 ~ 300 revs/min;It will mix
Particle be added in double screw extruder extruding pelletization to get matt master.
Further, the inorganic filler is at least one of talcum powder, calcium carbonate, mica.
The toughener is at least one of polyethylene (PE), ethylene-octene copolymer (POE).
The coupling agent is at least one of silane coupling agent, titanate coupling agent.
The antioxidant is that both Hinered phenols and phosphorous acid esters are used in compounding.
The steady agent of light is that hindered amines, benzotriazole and benzophenone three are used in compounding.
The lubricant is that both ethylene bis stearamide (EBS), calcium stearate are used in compounding.
The aromatic amides class compound is two Cyclohexamide of dicyclohexyl terephthalamide or naphthalene.
Another goal of the invention of the invention is to provide the system of the above-mentioned low-luster polypropylene for automotive interior material
Preparation Method, steps are as follows:
(1) weigh 100 parts of polypropylene, 0 ~ 25 part of toughener, 0 ~ 0.5 part of coupling agent in revolving speed be 200 ~ 300 revs/min
Room temperature mixes 3 ~ 5 minutes in high-speed mixer;
(2) it weighs in 0 ~ 50 part of inorganic filler addition high-speed mixer and is further continued for room temperature mixing 3 ~ 5 minutes;
(3) 0.1 ~ 0.5 part of antioxidant is weighed, the steady agent of 0 ~ 0.5 part of light, 0.2 ~ 0.8 part of lubricant, 3 ~ 10 parts of matt masters add
Enter to be further continued for room temperature in high-speed mixer to mix 3 ~ 5 minutes;
(4) the above-mentioned particle mixed is added twin-screw extrude and carries out melting extrusion, granulation, drying, cooling, dress
Wrap to obtain low-luster polypropylene;The temperature of double screw extruder be followed successively by from feeding section to head 180 DEG C, 195 DEG C, 200 DEG C,
210℃、210℃、210℃、215℃、215℃、215℃、215℃。
So the beneficial effects of the present invention are as follows:
1, the present invention is used aromatic amides class compound as polypropylene delustering agent;
2, aromatic amides class compound and low density polyethylene (LDPE) matt master is made into be added in PP composite material,
Keep its dispersion effect good, extinction effect is good.
3, the present invention can obtain the PP composite material of low-luster by common processing technology.
4, preparation method of the invention keeps material more fully mixed and keeps matt master abundant by mixed material in batches
It is evenly dispersed in polypropylene base-material, to balancedly reduce polypropylene glossiness.
Specific embodiment:
Below with reference to some embodiments, the invention will be further described with comparative example.Following embodiment is of the invention
Typical case, scope of protection of the present invention is not limited thereto.
Glossiness in following embodiment and comparative example is according to GB8807-1988 " plastics bright luster test method " standard
It is tested with vancometer, and 60 ° of incidence angles is selected to be tested.
The material used in embodiment and comparative example is as follows:
One, the primary raw material that matt master is used is prepared:
Low density polyethylene (LDPE):
LDPE model: 6201XR producer: Exxon Mobil;
Dicyclohexyl terephthalamide model: TMB-4 producer: Shanxi chemical research institute;
Two Cyclohexamide model of naphthalene: TMB-5 producer: Shanxi chemical research institute.
Two, the primary raw material that low-luster polypropylene material is used is prepared:
Polypropylene:
PP model: K7726H producer: middle petrochemical industry Yanshan Petrochemical;
Inorganic filler:
Talcum powder model: AH51105 producer: Liaoning Ai Hai;
Calcium carbonate model: LD-1000C producer: vertical to reach ultra micro;
Mica powder model: GM-3 producer: Chuzhou lattice are sharp;
Toughener:
PE model: 1018HA producer: Exxon Mobil;
POE model: 8200 producers: DOW Chemical;
Coupling agent:
Silane coupling agent model: KH550 producer: Tianzhang City's green chemical industry;
Titanate coupling agent model: TMC-981 producer: Tianzhang City's green chemical industry;Antioxidant:
Antioxidant:
Hinered phenols model: 1010 producers: Yixing City angel synthesizes chemistry;
Phosphorous acid esters model: 168 producers: Yixing City angel synthesizes chemistry;
The steady agent of light:
Hindered amines model: UV3808PP5 producer: U.S.'s cyanogen is special;
Benzotriazole model: UV5411 producer: U.S.'s cyanogen is special;
Benzophenone model: UV531 producer: U.S.'s cyanogen is special;
Lubricant:
Ethylene bis stearamide model: 500 mesh producer of EBS: the prosperous chemical industry of Guangzhou wound brocade;
Calcium stearate model: calcium stearate producer: the prosperous chemical industry of Guangzhou wound brocade.
Embodiment 1
Weigh 100 parts of LDPE 6201XR, 20 parts of aromatic amides class compound dicyclohexyl terephthalamides, 0.06 part
Lubricate EBS, 0.04 part of lubricant stearic acid calcium, 0.05 part of antioxidant 1010,0.05 part of irgasfos 168 are in high-speed mixer
Room temperature mixes 3 minutes, and wherein the revolving speed of high-speed mixer is 200 revs/min.The particle mixed is added to twin-screw extrusion
Extruding pelletization is in machine to get matt master.
Weigh 100 parts of polypropylene K7726H, 0.04 part of antioxidant 1010,0.06 part of irgasfos 168,0.07 part of lubricant
EBS, 0.13 part of lubricant stearic acid calcium, 3 parts of matt masters are added room temperature in high-speed mixer and mix 3 minutes, and high speed is mixed
The revolving speed of conjunction machine is 200 revs/min.By the above-mentioned particle mixed add twin-screw extrude carry out melting extrusion, granulation,
Dry, cooling, dress wraps to obtain low-luster polypropylene.The temperature of double screw extruder be followed successively by from feeding section to head 180 DEG C,
195℃、200℃、210℃、210℃、210℃、215℃、215℃、215℃、215℃。
Comparative example 1: matt master is not added
100 parts of polypropylene K7726H, 0.04 part of antioxidant 1010,0.06 part of irgasfos 168,0.07 part of lubrication are weighed first
Room temperature mixing 3 minutes in high-speed mixer are added in agent EBS, 0.13 part of lubricant stearic acid calcium, wherein the revolving speed of high-speed mixer
It is 200 revs/min.By the above-mentioned particle mixed add twin-screw extrude carry out melting extrusion, granulation, drying, cooling,
Dress packet.The temperature of double screw extruder is followed successively by 180 DEG C, 195 DEG C, 200 DEG C, 210 DEG C, 210 DEG C, 210 from feeding section to head
℃、215℃、215℃、215℃、215℃。
Embodiment 2
Weigh 100 parts of LDPE 6201XR, 40 parts of two Cyclohexamides of aromatic amides class compound naphthalene, 0.12 part of lubricant
EBS, 0.18 part of lubricant stearic acid calcium, 0.2 part of antioxidant 1010,0.1 part of irgasfos 168 room temperature in high-speed mixer mix
8 minutes, wherein the revolving speed of high-speed mixer was 300 revs/min.The particle mixed is added in double screw extruder and is squeezed out
It is granulated to get matt master.
Weigh 100 parts of polypropylene K7726H, 17 parts of toughener PE 1018HA, 8 parts of toughening POE, 8200,0.3 parts of coupling agents
KH550,0.2 part of coupling agent TMC-981 are mixed 5 minutes with room temperature in high-speed mixer, and wherein the revolving speed of high-speed mixer is 300
Rev/min;Then 20 parts of inorganic filler AH51105,20 parts of inorganic filler LD-1000C, 10 parts of inorganic filler GM-3 are weighed to be added
Room temperature mixes 5 minutes in high-speed mixer, and wherein the revolving speed of high-speed mixer is 300 revs/min;Finally weigh 0.36 part of antioxygen
1010,0.14 parts of irgasfos 168s of agent, the steady agent UV3808PP5 of 0.12 part of light, the steady agent UV5411 of 0.17 part of light, 0.21 part of steady agent of light
UV531,0.47 part of Lubricate EBS, 0.33 part of lubricant stearic acid calcium, 10 parts of matt masters are added room temperature in high-speed mixer and mix
It closes 5 minutes, wherein the revolving speed of high-speed mixer is 300 revs/min.The above-mentioned particle mixed is added twin-screw extrude
Progress melting extrusion, granulation, drying, cooling, dress wrap to obtain low-luster polypropylene.The temperature of double screw extruder from feeding section to
Head is followed successively by 180 DEG C, 195 DEG C, 200 DEG C, 210 DEG C, 210 DEG C, 210 DEG C, 215 DEG C, 215 DEG C, 215 DEG C, 215 DEG C.
Comparative example 2: matt master is not added
100 parts of polypropylene K7726H, 17 parts of toughener PE 1018HA, 8 parts of toughening POE, 8200,0.3 parts of idols are weighed first
Connection agent KH550,0.2 part of coupling agent TMC-981 mix 5 minutes with room temperature in high-speed mixer, wherein the revolving speed of high-speed mixer
It is 300 revs/min;Then 20 parts of inorganic filler AH51105,20 parts of inorganic filler LD-1000C, 10 parts of inorganic filler GM- are weighed
3, which are added room temperature in high-speed mixer, mixes 5 minutes, and wherein the revolving speed of high-speed mixer is 300 revs/min;Finally weigh 0.36
Part antioxidant 1010,0.14 part of irgasfos 168, the steady agent UV3808PP5 of 0.12 part of light, the steady agent UV5411 of 0.17 part of light, 0.21 part
The steady agent UV531 of light, 0.47 part of Lubricate EBS, 0.33 part of lubricant stearic acid calcium are added room temperature in high-speed mixer and mix 5 points
Clock, wherein the revolving speed of high-speed mixer is 300 revs/min.The above-mentioned particle mixed is added twin-screw extrude into progress
Melting extrusion, granulation, drying, cooling, dress packet.The temperature of double screw extruder is followed successively by 180 DEG C, 195 from feeding section to head
℃,200℃,210℃,210℃,210℃,215℃,215℃,215℃,215℃.Performance is shown in Table -1.
Embodiment 3
Weigh 100 parts of LDPE 6201XR, 29.5 parts of two Cyclohexamides of aromatic amides class compound naphthalene, 0.09 part of lubricant
EBS, 0.1 part of lubricant stearic acid calcium, 0.08 part of antioxidant 1010,0.11 part of irgasfos 168 room temperature in high-speed mixer are mixed
It closes 4.9 minutes, wherein the revolving speed of high-speed mixer is 268 revs/min.The particle mixed is added in double screw extruder
Extruding pelletization is to get matt master.
100 parts of polypropylene K7726H, 15 parts of toughener PE 1018HA, 0.19 part of coupling agent KH550 and high speed are weighed first
Room temperature mixes 3.7 minutes in mixing machine, and wherein the revolving speed of high-speed mixer is 246 revs/min;Then 18 parts of inorganic fillers are weighed
AH51105 is added room temperature in high-speed mixer and mixes 3.2 minutes, and wherein the revolving speed of high-speed mixer is 238 revs/min;Finally
Weigh 0.11 part of antioxidant 1010,0.13 part of irgasfos 168, the steady agent UV3808PP5 of 0.05 part of light, 0.04 part of steady agent of light
UV5411, the steady agent UV531 of 0.03 part of light, 0.29 part of Lubricate EBS, 0.18 part of lubricant stearic acid calcium, 5.4 parts of matt masters add
Enter room temperature in high-speed mixer to mix 4.1 minutes, wherein the revolving speed of high-speed mixer is 284 revs/min.It is mixed above-mentioned
Particle adds twin-screw extrude and carries out melting extrusion, granulation, drying, cooling, dress wrap to obtain low-luster polypropylene.Twin-screw
The temperature of extruder is followed successively by 180 DEG C, 195 DEG C, 200 DEG C, 210 DEG C, 210 DEG C, 210 DEG C, 215 DEG C, 215 from feeding section to head
℃、215℃、215℃。
Embodiment 4
Weigh 100 parts of LDPE 6201XR, 34.9 parts of two Cyclohexamides of aromatic amides class compound naphthalene, 0.18 part of lubricant
EBS, 0.12 part of lubricant stearic acid calcium, 0.14 part of antioxidant 1010,0.11 part of irgasfos 168 room temperature in high-speed mixer are mixed
It closes 7.6 minutes, wherein the revolving speed of high-speed mixer is 298 revs/min.The particle mixed is added in double screw extruder
Extruding pelletization is to get matt master.
100 parts of polypropylene K7726H, 21 parts of toughening POE, 8200,0.34 parts of coupling agent TMC-981 and high speed are weighed first
Room temperature mixes 4.4 minutes in mixing machine, and wherein the revolving speed of high-speed mixer is 278 revs/min;Then 18 parts of inorganic fillers are weighed
Room temperature mixing 4.3 minutes in high-speed mixer are added in LD-1000C, 6 parts of inorganic filler GM-3, wherein the revolving speed of high-speed mixer
It is 264 revs/min;Finally weigh 0.22 part of antioxidant 1010,0.11 part of irgasfos 168, the steady agent UV3808PP5 of 0.1 part of light,
The steady agent UV5411 of 0.07 part of light, the steady agent UV531 of 0.13 part of light, 0.23 part of Lubricate EBS, 0.12 part of lubricant stearic acid calcium, 8.7
Part matt master is added room temperature in high-speed mixer and mixes 4.7 minutes, and wherein the revolving speed of high-speed mixer is 289 revs/min.It will
The above-mentioned particle mixed, which adds twin-screw extrude, carries out melting extrusion, granulation, drying, cooling, dress packet.Twin-screw extrusion
The temperature of machine be followed successively by from feeding section to head 180 DEG C, 195 DEG C, 200 DEG C, 210 DEG C, 210 DEG C, 210 DEG C, 215 DEG C, 215 DEG C,
215℃、215℃。
The polypropylene material of above-described embodiment 1-4 and comparative example 1-2 preparation detects its glossiness, table 1 specific as follows respectively
It is shown:
1 embodiment 1 ~ 4 of table and 1 ~ 2 performance of comparative example
Test item | Embodiment 1 | Comparative example 1 | Embodiment 2 | Comparative example 2 | Embodiment 3 | Embodiment 4 |
Glossiness | 62 | 89 | 37 | 64 | 49 | 43 |
From upper 1 embodiment 1 ~ 4 of table and comparative example 1 ~ 2 it will be evident that the aromatic amides class compound that uses of the present invention and
Matt master made of low density polyethylene (LDPE) can significantly reduce the glossiness of PP composite material.Such as embodiment 1 and comparative example 1
It can be seen that, it can be so that glossiness drops to 62 from 89 as long as 3 parts of matt master of the invention is added.This low light of the invention
Damp degree automotive interior material can meet requirement of the partial automobile main engine plants to automobile interior decoration low-luster material, and application prospect is wide
It is wealthy.
Claims (7)
1. a kind of low-luster polypropylene for automotive interior material, it is characterised in that: prepared by weight by following components
It forms:
100 parts of polypropylene,
18 ~ 50 parts of inorganic filler,
15 ~ 25 parts of toughener,
0.19 ~ 0.5 part of coupling agent,
0.1 ~ 0.5 part of antioxidant,
0.12 ~ 0.5 part of the steady agent of light,
0.2 ~ 0.8 part of lubricant,
3 ~ 10 parts of matt master;
The matt master is made by weight through mixing, extruding pelletization by following component:
100 parts of low density polyethylene (LDPE),
20 ~ 40 parts of aromatic amides class compound,
0.1 ~ 0.3 part of lubricant,
0.1 ~ 0.3 part of antioxidant;
The steady agent of light is that hindered amines, benzotriazole and benzophenone three are used in compounding;The aromatic amides class
Compound is two Cyclohexamide of naphthalene.
2. the low-luster polypropylene according to claim 1 for automotive interior material, it is characterised in that: described inorganic
Filler is at least one of talcum powder, calcium carbonate, mica.
3. the low-luster polypropylene according to claim 1 for automotive interior material, it is characterised in that: the toughening
Agent is at least one of polyethylene, ethylene-octene copolymer.
4. the low-luster polypropylene according to claim 1 for automotive interior material, it is characterised in that: the coupling
Agent is at least one of silane coupling agent, titanate coupling agent.
5. the low-luster polypropylene according to claim 1 for automotive interior material, it is characterised in that: the antioxygen
Agent is that both Hinered phenols and phosphorous acid esters are used in compounding.
6. the low-luster polypropylene according to claim 1 for automotive interior material, it is characterised in that: the lubrication
Agent is that both ethylene bis stearamide, calcium stearate are used in compounding.
7. the preparation method of the low-luster polypropylene as claimed in any one of claims 1 to 6 for automotive interior material,
Be characterized in that: steps are as follows:
(1) weigh 100 parts of polypropylene, 15 ~ 25 parts of toughener, 0.19 ~ 0.5 part of coupling agent in revolving speed be 200 ~ 300 revs/min
Room temperature mixes 3 ~ 5 minutes in high-speed mixer;
(2) it weighs in 18 ~ 50 parts of inorganic fillers addition high-speed mixers and is further continued for room temperature mixing 3 ~ 5 minutes;
(3) 0.1 ~ 0.5 part of antioxidant is weighed, the steady agent of 0.12 ~ 0.5 part of light, 0.2 ~ 0.8 part of lubricant, 3 ~ 10 parts of matt masters add
Enter to be further continued for room temperature in high-speed mixer to mix 3 ~ 5 minutes;
(4) the above-mentioned particle mixed is added twin-screw extrude and carries out melting extrusion, granulation, drying, cooling, dress wrap
Low-luster polypropylene, the temperature of the double screw extruder be followed successively by from feeding section to head 180 DEG C, 195 DEG C, 200 DEG C,
210℃、210℃、210℃、215℃、215℃、215℃、215℃。
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