CN110157099A - A kind of rotational moulding modified polypropene and preparation method thereof - Google Patents

A kind of rotational moulding modified polypropene and preparation method thereof Download PDF

Info

Publication number
CN110157099A
CN110157099A CN201910507389.1A CN201910507389A CN110157099A CN 110157099 A CN110157099 A CN 110157099A CN 201910507389 A CN201910507389 A CN 201910507389A CN 110157099 A CN110157099 A CN 110157099A
Authority
CN
China
Prior art keywords
crosslinking agent
rotational moulding
preparation
modified
polypropylene
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201910507389.1A
Other languages
Chinese (zh)
Inventor
周卫中
向军
蒋建斌
林志杨
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
JINHUA JIT PACKING CO Ltd
Original Assignee
JINHUA JIT PACKING CO Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by JINHUA JIT PACKING CO Ltd filed Critical JINHUA JIT PACKING CO Ltd
Priority to CN201910507389.1A priority Critical patent/CN110157099A/en
Publication of CN110157099A publication Critical patent/CN110157099A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L23/10Homopolymers or copolymers of propene
    • C08L23/12Polypropene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/02Elements
    • C08K3/08Metals
    • C08K2003/0806Silver
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K2201/00Specific properties of additives
    • C08K2201/011Nanostructured additives
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2201/00Properties
    • C08L2201/08Stabilised against heat, light or radiation or oxydation
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2201/00Properties
    • C08L2201/10Transparent films; Clear coatings; Transparent materials

Abstract

The invention discloses a kind of rotational moulding modified polypropenes and preparation method thereof, it is related to rotational moulding materials technical field, a kind of rotational moulding modified polypropene mainly includes following raw material: polypropylene, EP rubbers, modified additive, antioxidant, crosslinking agent, assistant crosslinking agent, wherein, modified additive is to mix silver nanoparticle silica as core, core outer cladding 1,3:2,4- bis- (3,4- dimethyl) benzylidene sorbitol acetal layer, then be grafted 2-hydroxy-4-n-octoxybenzophenone and be made.A kind of rotational moulding modified polypropene of the invention and preparation method thereof, the modified polypropene being prepared has preferable toughness and shock resistance, while being also equipped with preferable transparency, is suitable for rotational molding technique use.

Description

A kind of rotational moulding modified polypropene and preparation method thereof
Technical field
The present invention relates to rotational moulding materials technical fields more particularly to a kind of rotational moulding modified polypropene and preparation method thereof.
Background technique
Roll moulding shaping technology process is that powdered resin quantitatively is packed into mold, and to mold heating while mold hangs down around mutual Two straight axial-rotations obtain product through cooling and demolding so that resin melting be made to be coated on cavity surface, relative to other at Type mode, device of rotomoulding forming and mould investment are few, and product is almost without internal stress, therefore in recent years, and society is to rotomoulded articles Cognition degree it is higher and higher, rotational moulding industry rapidly develops, and industry size rapidly expands, and rotational moulding new technology, new product emerge one after another.
With the increase of social demand and increasingly mature, the present adoptable resin variety of rotational molding technique of rotational molding technique Also it greatly expands, main includes the polyethylene of various specifications, polycarbonate, polystyrene, nylon etc., the wherein consumption of polyethylene Amount is the largest, and most of is rotational molding grade linear low density polyethylene, but since there is resistance to for linear low density polyethylene The defects of thermal creep performance is poor, tensile strength is poor, in high performance rotational molding product direction, ability is slightly inadequate.
Compared with polyethylene, polypropylene has many advantages, such as that rigidity is good, heat-resist, resistant to environmental cracking performance is good, but its Shock resistance is poor, affects it in the application in rotomoulded articles direction, therefore, is modified to polypropylene, so that it meets Rotational molding technique requirement is that have very big Social benefit and economic benefit.
Summary of the invention
In view of the above-mentioned problems, it is an object of the invention to design to provide a kind of rotational moulding modified polypropene and its preparation side Method, the modified polypropene being prepared has preferable toughness and shock resistance, while being also equipped with preferable transparency, is suitble to It is used in rotational molding technique.
The present invention solves above-mentioned technical problem by following technological means:
A kind of rotational moulding modified polypropene mainly includes following raw material: polypropylene, EP rubbers, modified additive, antioxygen Agent, crosslinking agent, assistant crosslinking agent, the modified additive are the core outer claddings 1,3 to mix silver nanoparticle silica as core: 2,4- bis- (3,4- dimethyl) benzylidene sorbitol acetal layers, then be grafted 2-hydroxy-4-n-octoxybenzophenone and be made.
Rotational moulding modified polypropene of the invention, raw material include EP rubbers, and one side EP rubbers and polypropylene have Preferable compatibility, the addition of another aspect EP rubbers can improve the toughness and anti-impact of polypropylene matrix to a certain extent Performance is hit, while the addition of crosslinking agent and assistant crosslinking agent can increase the degree of cross linking between polypropylene matrix, in conjunction with anti-oxidant Agent can increase polyacrylic service life to a certain extent.
In addition, the modified additive in the present invention is to mix silver nanoparticle silicon oxide pellets as core, first nano-silica SiClx bead as inorganic non-metallic particle, be added in polypropylene matrix itself have increase polypropylene matrix toughness and The effect of shock resistance, and it is doped with silver in nano silica bead, the antibacterial and mouldproof of polypropylene matrix can be increased Effect;But the compatibility mixed between silver nanoparticle silicon oxide pellets and polypropylene matrix is bad, and mixes silver nanoparticle silica It is easy to happen reunion between bead, causes its poor dispersion in polypropylene matrix, therefore, is mixing silver nanoparticle silica Bead outer cladding 1,3:2,4- bis- (3,4- dimethyl) benzylidene sorbitol acetal, firstly, 1,3:2,4- bis- (3,4- dimethyl) Compatibility between benzylidene sorbitol acetal and polypropylene is preferable, can increase the phase between modified additive and polypropylene matrix Capacitive, and the agglomerating force mixed between silver nanoparticle silicon oxide pellets can be reduced, so that modified additive is in polypropylene-base body It is dispersed more preferable, there is better effect, while 1,3:2,4- bis- to the raising of the toughening and shock resistance of polypropylene matrix (3,4- dimethyl) benzylidene sorbitol acetal can be used as heterogeneous nucleation agent, can reduce the crystallinity of polypropylene matrix, and by It is good in its compatibility between polypropylene matrix, the interface between modified additive and polypropylene matrix can be obscured, therefore The transparency of polypropylene matrix can also be improved;In addition, being also grafted 2- hydroxyl -4- n-octyloxy hexichol on modified additive Ketone, one side 2-hydroxy-4-n-octoxybenzophenone can reduce ultraviolet light to polyacrylic old as ultraviolet absorber Change effect, while the presence of 2-hydroxy-4-n-octoxybenzophenone being capable of equilibrium modifiers additive and poly- to a certain extent Adhesion strength between polypropylene matrix prevents the excessive influence composite material of adhesive strength between modified additive and polypropylene matrix Between brittle ductile transition, reduce to the toughening of polypropylene matrix and increase shock resistance effect.
Therefore, modified additive of the invention can not only increase the toughness and shock resistance of polypropylene matrix, moreover it is possible to Its transparency, anti-microbial property and anti-ultraviolet function are enough improved, and modified additive is that the progress of each material is compound and existing Every kind of material exclusive use is compared, during use, the dispersion performance in polypropylene matrix is more preferable, and between material It can complement each other, more preferably play a role.
Further, the quality of the polypropylene, EP rubbers, modified additive, antioxidant, crosslinking agent, assistant crosslinking agent Than for (100-110): (15-20): (1-3): (0.1-0.2): (0.1-0.3): (0.1-0.3).
Further, the quality of the polypropylene, EP rubbers, modified additive, antioxidant, crosslinking agent, assistant crosslinking agent Than for 100:16:2:0.1:0.2:0.2.
Further, the antioxidant is 1,3,5- trimethyls -2,4,6- tri- (3,5- di-tert-butyl-4-hydroxyl benzyl) Benzene, crosslinking agent are cumyl peroxide, and assistant crosslinking agent is divinylbenzene.
In addition, the invention also discloses a kind of preparation method of rotational moulding modified polypropene, the preparation method include with Lower step:
It weighs: according to mass ratio (100-110): (15-20): (1-3): (0.1-0.2): (0.1-0.3): (0.1-0.3) Polypropylene, EP rubbers, modified additive, antioxidant, crosslinking agent, assistant crosslinking agent are weighed respectively;
It mediates: polypropylene, EP rubbers, modified additive, the antioxidant of 25%~30% weight being taken to be placed in kneader It is interior, 15-20min is mediated under conditions of revolving speed is 500-950r/min, temperature is 60-70 DEG C;
Be kneaded: the product that kneading step is prepared is placed in continuous mixer, and titanate coupling agent is added, is being kneaded Temperature is 110 DEG C, extrusion temperature is 155 DEG C, die head temperature is 150 DEG C, mixing revolving speed is kneaded under conditions of being 35r/min 10min obtains functional master batch;
Extruding pelletization: by the functional master batch being prepared, remaining 70%~75% weight polypropylene, crosslinking agent, help friendship Join agent after mixing, through double screw extruder extruding pelletization, obtains modified polypropene.
Further, the modified additive the preparation method comprises the following steps:
Cladding: it will be scattered in methyl phenyl ethers anisole solution by pretreated silver nanoparticle silicon oxide pellets of mixing, ultrasonic disperse 1,3:2,4- bis- (3,4- dimethyl) benzylidene sorbitol acetal is added in 20min, is heated to 70-80 DEG C, after keeping the temperature 30min, stops Heating is filtered, washed, dries after standing 3-4h;
Grafting: taking 2-hydroxy-4-n-octoxybenzophenone stirring and dissolving in dehydrated alcohol, and adjusting pH value is 6-7, obtains To reaction solution, the product that encapsulation steps are prepared is placed in plasma reactor, using ammonia as working gas, into It after row corona treatment 10-20s, is scattered in reaction solution, heating water bath is protected to 50-60 DEG C under the conditions of ultrasonic agitation Temperature reaction 10-12h, after the reaction was completed, be filtered, washed, dry after obtain modified additive.
Using ammonia as reaction gas in the grafting the step of, to being coated with 1,3:2,4- bis- (3,4- dimethyl) benzyl During the nano silica bead progress corona treatment for pitching sorbitol acetal, amino base is introduced on its surface Group, so that 2-hydroxy-4-n-octoxybenzophenone can be preferably grafted.
Further, 1,3:2,4-, bis- (3,4- dimethyl) the benzylidene sorbitol acetal and 2- hydroxyl -4- n-octyloxy two The molar ratio of Benzophenone is 1:0.3.
Pass through (3,4- dimethyl) the benzylidene sorbitol acetal of 1,3:2,4- bis- and 2-hydroxy-4-n-octoxybenzophenone Molar ratio setting, controls the grafting rate of 2-hydroxy-4-n-octoxybenzophenone, with this equilibrium modifiers additive and polypropylene-base Interface binding intensity between body.
Further, the pretreatment are as follows: silver nanoparticle silicon oxide pellets will be mixed and be placed in reaction of low temperature plasma device, one Argon gas is working gas, is 0.4-0.6L/s in gas flow, power carries out at low temperature plasma under conditions of being 80-90W Manage 1-2min.
Low Temperature Plasma Treating is carried out as working gas using argon gas to the surface for mixing silver nanoparticle silicon oxide pellets, During the treatment, argon plasma bombardment is to the surface of silver nanoparticle silicon oxide pellets is mixed, so that mixing silver nanoparticle dioxy SiClx bead surface becomes coarse, so that (3,4- dimethyl) the benzylidene sorbitol acetal of 1,3:2,4- bis- and mixing silver nanoparticle two It is combined between silica bead more preferable.
Further, it is described mix silver nanoparticle silica the preparation method comprises the following steps: 5ml20% is added dropwise into every liter of deionized water Ammonium hydroxide, adjusting pH value with 0.1mol/L sodium hydroxide solution is 10-11, and silver nitrate, tetraethyl orthosilicate, anhydrous second is then added Alcohol is protected from light after stirring 5min, is warming up to 40 DEG C, and oxalic acid solution is added dropwise, and ultrasonic agitation reaction 4-5h is filtered, the anhydrous second of filter cake Alcohol washing, vacuum drying obtain mixing silver nanoparticle silicon oxide pellets.
Beneficial effects of the present invention:
1. a kind of rotational moulding modified polypropene of the invention, changes polypropylene by EP rubbers, modified additive Property, can improve the toughness and shock resistance of polypropylene matrix to a certain extent, while crosslinking agent and assistant crosslinking agent plus Enter the degree of cross linking that can be increased between polypropylene matrix, polyacrylic make can be increased to a certain extent in conjunction with antioxidant Use the service life.
2. modified additive of the invention can not only increase the toughness and shock resistance of polypropylene matrix, additionally it is possible to Its transparency, anti-microbial property and anti-ultraviolet function are improved, and modified additive is that each material is carried out to compound and existing general Every kind of material exclusive use is compared, and during use, the dispersion performance in polypropylene matrix is more preferable, and energy between material It enough complements each other, more preferably plays a role.
Specific embodiment
Below with reference to specific embodiment, the present invention is described in detail:
A kind of rotational moulding modified polypropene of the invention and preparation method thereof, joined modified additive in the feed, should Modified additive is the core outer cladding 1,3:2 to mix silver nanoparticle silica as core, 4- bis- (3,4- dimethyl) benzal sorb Acetal layer, then be grafted 2-hydroxy-4-n-octoxybenzophenone and be made.
Embodiment one
The preparation 1 of modified additive
It mixes the preparation of silver nanoparticle silica: the ammonium hydroxide of 5ml 20% being added dropwise into every liter of deionized water, uses 0.1mol/L It is 10 that sodium hydroxide solution, which adjusts pH value, and 5mg silver nitrate, 10g tetraethyl orthosilicate, 10g dehydrated alcohol, stirring is then added It after 5min, is protected from light, is warming up to 40 DEG C, ultrasonic agitation reaction is molten with the oxalic acid that 245ml 0.035g/L is added dropwise in the speed of 2d/min Liquid, while the pH value for adjusting solution is 9-10, is added dropwise to complete rear insulation reaction 2h, is filtered, filter cake is washed 3 times with dehydrated alcohol, It is dried in vacuo 12h at a temperature of 60 DEG C, obtains mixing silver nanoparticle silicon oxide pellets.
Cladding: will mix silver nanoparticle silicon oxide pellets and be placed in reaction of low temperature plasma device, using argon gas as working gas, It is 0.6L/s in gas flow, power carries out Low Temperature Plasma Treating 1min under conditions of being 90W, is then according to solid-to-liquid ratio 30g/L is scattered in methyl phenyl ethers anisole solution, and ultrasonic disperse 20min obtains suspension, and 18g 1,3:2,4- bis- is added in every liter of suspension (3,4- dimethyl) benzylidene sorbitol acetal is heated to 70 DEG C, after keeping the temperature 30min, stops heating, after standing 4h, filtering, and filter cake It is washed with ethyl acetate and sodium carbonate to being in neutrality, is dried at a temperature of 40 DEG C.
Grafting: take 2-hydroxy-4-n-octoxybenzophenone stirring and dissolving in etc. quality dehydrated alcohol in, use 1mol/L It is 6-7 that sodium hydroxide solution, which adjusts pH value, obtains reaction solution, it is anti-that the product that encapsulation steps are prepared is placed in plasma It answers in device, is 8Pa in pressure, power carries out corona treatment 15s under conditions of being 110W using ammonia as working gas Afterwards, it is scattered in reaction solution according to the solid-to-liquid ratio of 25g/L, heating water bath is to 50 DEG C under the conditions of ultrasonic agitation, insulation reaction 12h, after the reaction was completed, filtering, filter cake acetone washing obtain modified additive after being dried in vacuo at a temperature of 40 DEG C.
Embodiment two
The preparation 2 of modified additive
It mixes the preparation of silver nanoparticle silica: the ammonium hydroxide of 5ml 20% being added dropwise into every liter of deionized water, uses 0.1mol/L It is 11 that sodium hydroxide solution, which adjusts pH value, and 5mg silver nitrate, 10g tetraethyl orthosilicate, 10g dehydrated alcohol, stirring is then added It after 5min, is protected from light, is warming up to 40 DEG C, ultrasonic agitation reaction is molten with the oxalic acid that 245ml 0.035g/L is added dropwise in the speed of 2d/min Liquid, while the pH value for adjusting solution is 9-10, is added dropwise to complete rear insulation reaction 1, is filtered, filter cake is washed 3 times with dehydrated alcohol, in It is dried in vacuo 12h at a temperature of 60 DEG C, obtains mixing silver nanoparticle silicon oxide pellets.
Cladding: will mix silver nanoparticle silicon oxide pellets and be placed in reaction of low temperature plasma device, using argon gas as working gas, It is 0.4L/s in gas flow, power carries out Low Temperature Plasma Treating 2min under conditions of being 80W, is then according to solid-to-liquid ratio 30g/L is scattered in methyl phenyl ethers anisole solution, and ultrasonic disperse 20min obtains suspension, and 18g 1,3:2,4- bis- is added in every liter of suspension (3,4- dimethyl) benzylidene sorbitol acetal is heated to 75 DEG C, after keeping the temperature 30min, stops heating, after standing 3h, filtering, and filter cake It is washed with ethyl acetate and sodium carbonate to being in neutrality, is dried at a temperature of 40 DEG C.
Grafting: take 2-hydroxy-4-n-octoxybenzophenone stirring and dissolving in etc. quality dehydrated alcohol in, use 1mol/L It is 6-7 that sodium hydroxide solution, which adjusts pH value, obtains reaction solution, it is anti-that the product that encapsulation steps are prepared is placed in plasma It answers in device, is 8Pa in pressure, power carries out corona treatment 20s under conditions of being 110W using ammonia as working gas Afterwards, it is scattered in reaction solution according to the solid-to-liquid ratio of 25g/L, heating water bath is to 60 DEG C under the conditions of ultrasonic agitation, insulation reaction 10h, after the reaction was completed, filtering, filter cake acetone washing obtain modified additive after being dried in vacuo at a temperature of 40 DEG C.
Embodiment three
The preparation 3 of modified additive
It mixes the preparation of silver nanoparticle silica: the ammonium hydroxide of 5ml 20% being added dropwise into every liter of deionized water, uses 0.1mol/L It is 10 that sodium hydroxide solution, which adjusts pH value, and 5mg silver nitrate, 10g tetraethyl orthosilicate, 10g dehydrated alcohol, stirring is then added It after 5min, is protected from light, is warming up to 40 DEG C, ultrasonic agitation reaction is molten with the oxalic acid that 245ml 0.035g/L is added dropwise in the speed of 2d/min Liquid, while the pH value for adjusting solution is 9-10, is added dropwise to complete rear insulation reaction 2h, is filtered, filter cake is washed 3 times with dehydrated alcohol, It is dried in vacuo 12h at a temperature of 60 DEG C, obtains mixing silver nanoparticle silicon oxide pellets.
Cladding: will mix silver nanoparticle silicon oxide pellets and be placed in reaction of low temperature plasma device, using argon gas as working gas, It is 0.5L/s in gas flow, power carries out Low Temperature Plasma Treating 1min under conditions of being 85W, is then according to solid-to-liquid ratio 30g/L is scattered in methyl phenyl ethers anisole solution, and ultrasonic disperse 20min obtains suspension, and 18g 1,3:2,4- bis- is added in every liter of suspension (3,4- dimethyl) benzylidene sorbitol acetal is heated to 80 DEG C, after keeping the temperature 30min, stops heating, after standing 4h, filtering, and filter cake It is washed with ethyl acetate and sodium carbonate to being in neutrality, is dried at a temperature of 40 DEG C.
Grafting: take 2-hydroxy-4-n-octoxybenzophenone stirring and dissolving in etc. quality dehydrated alcohol in, use 1mol/L It is 6-7 that sodium hydroxide solution, which adjusts pH value, obtains reaction solution, it is anti-that the product that encapsulation steps are prepared is placed in plasma It answers in device, is 8Pa in pressure, power carries out corona treatment 10s under conditions of being 110W using ammonia as working gas Afterwards, it is scattered in reaction solution according to the solid-to-liquid ratio of 25g/L, heating water bath is to 55 DEG C under the conditions of ultrasonic agitation, insulation reaction 11h, after the reaction was completed, filtering, filter cake acetone washing obtain modified additive after being dried in vacuo at a temperature of 40 DEG C.
Example IV
The preparation 1 of modified polypropene
The present embodiment selects embodiment one to prepare resulting modified additive, the specific steps are as follows:
It weighs: being that 100:16:2:0.1:0.2:0.2 weighs polypropylene, EP rubbers, modified addition respectively according to mass ratio Agent, antioxidant, crosslinking agent, assistant crosslinking agent.
It mediates: taking polypropylene, EP rubbers, modified additive, the antioxidant 1,3 of 25%~30% weight, 5- front three Base -2,4,6- tri- (3,5- di-tert-butyl-4-hydroxyl benzyl) benzene are placed in kneader, revolving speed be 950r/min, temperature 60 15min is mediated under conditions of DEG C.
Be kneaded: the product that kneading step is prepared is placed in continuous mixer, and titanate coupling agent is added, is being kneaded Temperature is 110 DEG C, and extrusion temperature is 155 DEG C, and die head temperature is 150 DEG C, is kneaded under conditions of revolving speed is 35r/min and is kneaded 10min obtains functional master batch.
Extruding pelletization: by the functional master batch being prepared, the polypropylene of remaining 70%~75% weight, crosslinking agent peroxidating Diisopropylbenzene (DIPB), assistant crosslinking agent divinylbenzene after mixing, are placed in double screw extruder, are 150r/min in screw speed, into Material mouth temperature is 130 DEG C, and interlude temperature is 165 DEG C, and head temperature is 175 DEG C, and the condition extrusion that die head temperature is 165 DEG C is made Grain, obtains modified polypropene.
Embodiment five
The preparation 2 of modified polypropene
The present embodiment selects embodiment two to prepare resulting modified additive, the specific steps are as follows:
It weighs: being that 110:20:3:0.1:0.1:0.3 weighs polypropylene, EP rubbers, modified addition respectively according to mass ratio Agent, antioxidant, crosslinking agent, assistant crosslinking agent.
It mediates: taking polypropylene, EP rubbers, modified additive, the antioxidant 1,3 of 25%~30% weight, 5- front three Base -2,4,6- tri- (3,5- di-tert-butyl-4-hydroxyl benzyl) benzene are placed in kneader, revolving speed be 750r/min, temperature 65 18min is mediated under conditions of DEG C.
Be kneaded: the product that kneading step is prepared is placed in continuous mixer, and titanate coupling agent is added, is being kneaded Temperature is 110 DEG C, and extrusion temperature is 155 DEG C, and die head temperature is 150 DEG C, is kneaded under conditions of revolving speed is 35r/min and is kneaded 10min obtains functional master batch.
Extruding pelletization: by the functional master batch being prepared, the polypropylene of remaining 70%~75% weight, crosslinking agent peroxidating Diisopropylbenzene (DIPB), assistant crosslinking agent divinylbenzene after mixing, are placed in double screw extruder, are 150r/min in screw speed, into Material mouth temperature is 130 DEG C, and interlude temperature is 165 DEG C, and head temperature is 175 DEG C, and the condition extrusion that die head temperature is 165 DEG C is made Grain, obtains modified polypropene.
Embodiment six
The preparation 3 of modified polypropene
The present embodiment selects embodiment three to prepare resulting modified additive, the specific steps are as follows:
It weighs: being that 105:15:1:0.2:0.3:0.1 weighs polypropylene, EP rubbers, modified addition respectively according to mass ratio Agent, antioxidant, crosslinking agent, assistant crosslinking agent
It mediates: taking polypropylene, EP rubbers, modified additive, the antioxidant 1,3 of 25%~30% weight, 5- front three Base -2,4,6- tri- (3,5- di-tert-butyl-4-hydroxyl benzyl) benzene are placed in kneader, revolving speed be 500r/min, temperature 70 15min is mediated under conditions of DEG C.
Be kneaded: the product that kneading step is prepared is placed in continuous mixer, and titanate coupling agent is added, is being kneaded Temperature is 110 DEG C, and extrusion temperature is 155 DEG C, and die head temperature is 150 DEG C, is kneaded under conditions of revolving speed is 35r/min and is kneaded 10min obtains functional master batch.
Extruding pelletization: by the functional master batch being prepared, the polypropylene of remaining 70%~75% weight, crosslinking agent peroxidating Diisopropylbenzene (DIPB), assistant crosslinking agent divinylbenzene after mixing, are placed in double screw extruder, are 150r/min in screw speed, into Material mouth temperature is 130 DEG C, and interlude temperature is 165 DEG C, and head temperature is 175 DEG C, and the condition extrusion that die head temperature is 165 DEG C is made Grain, obtains modified polypropene.
Embodiment seven
The present embodiment and example IV the difference is that, do not add modified additive in the present embodiment, will prepare Required nano silica bead in modified additive, 1,3:2,4- bis- (3,4- dimethyl) benzylidene sorbitol acetal, 2- Hydroxyl -4- oxy-octyl benzophenone is directly added into.
The stretching yield stress for the modified polypropene that example IV~embodiment seven is prepared, bending modulus, anti-impact Hit performance, transparency is tested, test result is as follows shown in table:
It can be seen that the modified polypropene being prepared using inventive formulation, toughness and shock resistance by upper table It is all improved, while the modified additive that adds of the present invention is composite material, relative to the existing mode individually added, The effect of toughening and raising shock resistance to polypropylene matrix is more preferable, and more to the effect of polypropylene matrix transparency raising It is good.
The above examples are only used to illustrate the technical scheme of the present invention and are not limiting, although referring to preferred embodiment to this hair It is bright to be described in detail, those skilled in the art should understand that, it can modify to technical solution of the present invention Or equivalent replacement should all cover without departing from the objective and range of technical solution of the present invention in claim of the invention In range.Technology not described in detail in the present invention, shape, construction portion are well-known technique.

Claims (9)

1. a kind of rotational moulding modified polypropene, which is characterized in that mainly include following raw material: polypropylene, EP rubbers, modification add Add agent, antioxidant, crosslinking agent, assistant crosslinking agent, the modified additive is to mix silver nanoparticle silica as core, outside core 1,3:2,4- bis- (3,4- dimethyl) benzylidene sorbitol acetal layer is coated, then is grafted 2-hydroxy-4-n-octoxybenzophenone system ?.
2. a kind of rotational moulding modified polypropene according to claim 1, which is characterized in that the polypropylene, EP rubbers, Modified additive, antioxidant, crosslinking agent, assistant crosslinking agent mass ratio be (100-110): (15-20): (1-3): (0.1- 0.2):(0.1-0.3):(0.1-0.3)。
3. a kind of rotational moulding modified polypropene according to claim 2, which is characterized in that the polypropylene, EP rubbers, Modified additive, antioxidant, crosslinking agent, assistant crosslinking agent mass ratio be 100:16:2:0.1:0.2:0.2.
4. a kind of rotational moulding modified polypropene according to claim 1, which is characterized in that the antioxidant is 1,3,5- Trimethyl -2,4,6- tri- (3,5- di-tert-butyl-4-hydroxyl benzyl) benzene, crosslinking agent is cumyl peroxide, and assistant crosslinking agent is Divinylbenzene.
5. a kind of preparation method of rotational moulding modified polypropene, which is characterized in that the preparation method comprises the following steps:
It weighs: according to mass ratio (100-110): (15-20): (1-3): (0.1-0.2): (0.1-0.3): (0.1-0.3) difference Weigh polypropylene, EP rubbers, modified additive, antioxidant, crosslinking agent, assistant crosslinking agent;
It mediates: polypropylene, EP rubbers, modified additive, the antioxidant of 25%~30% weight being taken to be placed in kneader, Revolving speed is 500-950r/min, temperature mediates 15-20min under conditions of being 60-70 DEG C;
Be kneaded: the product that kneading step is prepared is placed in continuous mixer, titanate coupling agent is added, in melting temperature Be 155 DEG C for 110 DEG C, extrusion temperature, die head temperature is 150 DEG C, is kneaded revolving speed be 35r/min under conditions of be kneaded 10min, obtain To functional master batch;
Extruding pelletization: by the functional master batch being prepared, polypropylene, crosslinking agent, the assistant crosslinking agent of remaining 70%~75% weight After mixing, through double screw extruder extruding pelletization, modified polypropene is obtained.
6. a kind of preparation method of rotational moulding modified polypropene according to claim 5, which is characterized in that the modification adds Add agent the preparation method comprises the following steps:
Cladding: will be scattered in methyl phenyl ethers anisole solution, ultrasonic disperse 20min by pretreated silver nanoparticle silicon oxide pellets of mixing, 1,3:2,4- bis- (3,4- dimethyl) benzylidene sorbitol acetal is added, is heated to 70-80 DEG C, after keeping the temperature 30min, stops heating, After standing 3-4h, it is filtered, washed, dries;
Grafting: taking 2-hydroxy-4-n-octoxybenzophenone stirring and dissolving in dehydrated alcohol, and adjusting pH value is 6-7, obtains anti- Solution is answered, the product that encapsulation steps are prepared is placed in plasma reactor, using ammonia as working gas, carry out etc. It after gas ions handle 10-20s, is scattered in reaction solution, for heating water bath to 50-60 DEG C, heat preservation is anti-under the conditions of ultrasonic agitation Answer 10-12h, after the reaction was completed, be filtered, washed, dry after obtain modified additive.
7. a kind of preparation method of rotational moulding modified polypropene according to claim 6, which is characterized in that described 1,3:2, The molar ratio of (3,4- dimethyl) the benzylidene sorbitol acetal of 4- bis- and 2-hydroxy-4-n-octoxybenzophenone is 1:0.3.
8. a kind of preparation method of rotational moulding modified polypropene according to claim 7, which is characterized in that the pretreatment Are as follows: silver nanoparticle silicon oxide pellets will be mixed and be placed in reaction of low temperature plasma device, using argon gas as working gas, in gas flow For 0.4-0.6L/s, power carries out Low Temperature Plasma Treating 1-2min under conditions of being 80-90W.
9. a kind of preparation method of rotational moulding modified polypropene according to claim 8, which is characterized in that described to mix Yin Na Rice silica the preparation method comprises the following steps: into every liter of deionized water be added dropwise 5ml20% ammonium hydroxide, it is molten with 0.1mol/L sodium hydroxide It is 10-11 that liquid, which adjusts pH value, and silver nitrate, tetraethyl orthosilicate, dehydrated alcohol is then added, and after stirring 5min, is protected from light, is warming up to 40 DEG C, oxalic acid solution is added dropwise, ultrasonic agitation reaction 4-5h is filtered, and filter cake is washed with dehydrated alcohol, is dried in vacuo, is obtained mixing silver Nano silica bead.
CN201910507389.1A 2019-06-12 2019-06-12 A kind of rotational moulding modified polypropene and preparation method thereof Pending CN110157099A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201910507389.1A CN110157099A (en) 2019-06-12 2019-06-12 A kind of rotational moulding modified polypropene and preparation method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201910507389.1A CN110157099A (en) 2019-06-12 2019-06-12 A kind of rotational moulding modified polypropene and preparation method thereof

Publications (1)

Publication Number Publication Date
CN110157099A true CN110157099A (en) 2019-08-23

Family

ID=67628625

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201910507389.1A Pending CN110157099A (en) 2019-06-12 2019-06-12 A kind of rotational moulding modified polypropene and preparation method thereof

Country Status (1)

Country Link
CN (1) CN110157099A (en)

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20030195300A1 (en) * 2001-11-06 2003-10-16 Stevens James C. Crystallization of polypropylene using a semi-crystalline, branched or coupled nucleating agent
US20050249904A1 (en) * 2004-01-23 2005-11-10 Rajnish Batlaw Articles and process of making polypropylene articles having ultraviolet light protection by injection stretch blow molding of polypropylene
CN101067033A (en) * 2007-06-06 2007-11-07 房华江 Prepn process of polypropylene mixture alloy for rotationally molding
CN101759930A (en) * 2008-12-23 2010-06-30 上海金发科技发展有限公司 Flame-retardant polypropylene compound for sanitary ware product
CN102888051A (en) * 2011-07-19 2013-01-23 上海升广科技有限公司 Modified plastic material based on PP plastic and preparation method thereof
KR20130017837A (en) * 2011-08-12 2013-02-20 현대자동차주식회사 Polypropylene resin composition for trims of vehicles
CN103143265A (en) * 2013-01-23 2013-06-12 丽水学院 Ultrafiltration membrane with hydrophilism and antibacterial property and preparation method thereof
CN103571058A (en) * 2013-11-22 2014-02-12 苏州润佳工程塑料股份有限公司 Reinforced scratching-resistant polypropylene material
CN108623901A (en) * 2017-03-26 2018-10-09 合肥杰事杰新材料股份有限公司 A kind of high strength glass fiber reinforced polypropylene compound material and preparation method thereof

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20030195300A1 (en) * 2001-11-06 2003-10-16 Stevens James C. Crystallization of polypropylene using a semi-crystalline, branched or coupled nucleating agent
US20050249904A1 (en) * 2004-01-23 2005-11-10 Rajnish Batlaw Articles and process of making polypropylene articles having ultraviolet light protection by injection stretch blow molding of polypropylene
CN101067033A (en) * 2007-06-06 2007-11-07 房华江 Prepn process of polypropylene mixture alloy for rotationally molding
CN101759930A (en) * 2008-12-23 2010-06-30 上海金发科技发展有限公司 Flame-retardant polypropylene compound for sanitary ware product
CN102888051A (en) * 2011-07-19 2013-01-23 上海升广科技有限公司 Modified plastic material based on PP plastic and preparation method thereof
KR20130017837A (en) * 2011-08-12 2013-02-20 현대자동차주식회사 Polypropylene resin composition for trims of vehicles
CN103143265A (en) * 2013-01-23 2013-06-12 丽水学院 Ultrafiltration membrane with hydrophilism and antibacterial property and preparation method thereof
CN103571058A (en) * 2013-11-22 2014-02-12 苏州润佳工程塑料股份有限公司 Reinforced scratching-resistant polypropylene material
CN108623901A (en) * 2017-03-26 2018-10-09 合肥杰事杰新材料股份有限公司 A kind of high strength glass fiber reinforced polypropylene compound material and preparation method thereof

Non-Patent Citations (4)

* Cited by examiner, † Cited by third party
Title
刘云颖 等: ""载银纳米二氧化硅抗菌粉体材料的制备"", 《无机盐工业》 *
姜淑媛: "《家用纺织品设计与市场开发》", 31 May 2007, 中国纺织出版社 *
王翠英 等: ""以SiO2为载体的纳米银粒子的制备及其在塑料中的应用"", 《塑料工业》 *
辛忠: "《理论与实践 小分子调控大分子结晶》", 31 August 2016, 华东理工大学出版社 *

Similar Documents

Publication Publication Date Title
WO2015165363A1 (en) Material for 3d printing and preparation method therefor and product thereof
CN109575557B (en) PC/ABS mixture for three-dimensional printing, preparation method thereof and direct printing method
CN107190346A (en) A kind of preparation method of nylon fishing net line
CN106750899A (en) A kind of basalt long fiber reinforced polypropylene compound material and application thereof
CN113930030B (en) Warm frame section bar for shutter and manufacturing method thereof
CN105176059A (en) Electro-chemically modified and CF (carbon fiber) reinforced TPU (thermoplastic polyurethane) composite material and preparation method thereof
CN111138767B (en) Weighted and hardened open-cell EPDM rubber blending molding repeated high-rate foaming backing plate and preparation method thereof
CN110157099A (en) A kind of rotational moulding modified polypropene and preparation method thereof
CN110218385A (en) A kind of polyethylene processing aid master batch, preparation method and the purposes for preparing polyethylene products
CN109135008B (en) Filling master batch, preparation method and application thereof, and polypropylene wiredrawing material containing filling master batch
CN101735509B (en) Micron-nano silicon carbide/polypropylene composite and preparation method thereof
CN102399410A (en) ABS (acrylonitrile butadiene styrene) composite material and preparation method thereof
CN103923432A (en) High impact extinctive ABS (Acrylonitrile Butadiene Styrene) modified plastic and preparation method thereof
CN208084800U (en) A kind of Double-color shoemaking mould of single injection-molded
CN109749198A (en) A kind of high tenacity rotational moulding flowerpot material and preparation method thereof
CN101585977B (en) Preparation method of polypropylene reinforced plasticized modifier
CN110878166A (en) Manufacturing process of impact-resistant luggage shell
CN108727686A (en) A kind of automobile handle injection forming mold material and preparation method thereof
CN114163765B (en) Environment-friendly plastic with controllable transparency and multicolor patterns and preparation method thereof
CN1563188B (en) High shock resistant composite material of PCT enhanced by fiberglass
CN106746917B (en) A kind of modified aluminium hydroxide and preparation method thereof and the application in artificial stone
CN100532456C (en) Method for preparing Nano composite material of nylon / clay of laminar silicate
CN106182557A (en) Windscreen manufacture method in a kind of bullet train group annular
CN102744897B (en) Production process for nanometer reinforced PET slabs with high transparency and high weatherability
CN110079013A (en) A kind of Masterbatch and preparation method thereof of luggage shell resistant to high temperature

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20190823