CN107698848A - A kind of fragrant plastic masterbatch and preparation method thereof - Google Patents

A kind of fragrant plastic masterbatch and preparation method thereof Download PDF

Info

Publication number
CN107698848A
CN107698848A CN201711008478.9A CN201711008478A CN107698848A CN 107698848 A CN107698848 A CN 107698848A CN 201711008478 A CN201711008478 A CN 201711008478A CN 107698848 A CN107698848 A CN 107698848A
Authority
CN
China
Prior art keywords
essence
preparation
fragrant
masterbatch
plastic
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.)
Withdrawn
Application number
CN201711008478.9A
Other languages
Chinese (zh)
Inventor
陈庆
昝航
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.)
Chengdu New Keli Chemical Science Co Ltd
Original Assignee
Chengdu New Keli Chemical Science 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 Chengdu New Keli Chemical Science Co Ltd filed Critical Chengdu New Keli Chemical Science Co Ltd
Priority to CN201711008478.9A priority Critical patent/CN107698848A/en
Publication of CN107698848A publication Critical patent/CN107698848A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J3/00Processes of treating or compounding macromolecular substances
    • C08J3/20Compounding polymers with additives, e.g. colouring
    • C08J3/22Compounding polymers with additives, e.g. colouring using masterbatch techniques
    • C08J3/226Compounding polymers with additives, e.g. colouring using masterbatch techniques using a polymer as a carrier
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2323/00Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
    • C08J2323/02Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
    • C08J2323/04Homopolymers or copolymers of ethene
    • C08J2323/06Polyethene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2453/00Characterised by the use of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Derivatives of such polymers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2491/00Characterised by the use of oils, fats or waxes; Derivatives thereof
    • C08J2491/06Waxes

Landscapes

  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Processes Of Treating Macromolecular Substances (AREA)

Abstract

The invention belongs to the preparing technical field of plastic matrix, there is provided a kind of fragrant plastic masterbatch and preparation method thereof.This method is using powdered plastic essence as masterbatch core, using LDPE resin powder as carrier, is equipped with other auxiliary agents, is pre-mixed in high-speed mixer;Then aerosol adhesive is added in high-speed mixer, its quick refrigeration is condensed into particle, essence powder and LDPE resin powder bonding are got up, and be well mixed under high-speed stirred effect with other components, through drying and crushing after discharging, fragrant plastic masterbatch is made.Compared with conventional method, masterbatch made from preparation method of the invention and essence is uniformly dispersed, lasting fragrance good with vector resin associativity, scatter and disappear relatively slow, while whole preparation process energy consumption is relatively low, it is pollution-free, it is simple to operate, easy to control, large-scale production can be achieved.

Description

A kind of fragrant plastic masterbatch and preparation method thereof
Technical field
The invention belongs to the preparing technical field of plastic matrix, there is provided a kind of fragrant plastic masterbatch and preparation method thereof.
Background technology
Plastic matrix (Plastic Master batch) is that plastic additive super quantity is attached in resin and is made Condensation product;When manufacturing plastic products, it is not necessary to this kind of plastic additive is added, only need to be proportionally added into this masterbatch, Its advantage is:Technique is simple, easy to use, is easy to implement the production automation, raises labour productivity, and avoids environmental pollution again. With the rapid development of plastics industry, a kind of filling master batch not still added material, the production costs of plastic products can be reduced, Also there are some physical properties for improving plastic products, such as reduce breach shrinkage factor, improve outward appearance and feel characteristic and obtain The accreditation in market, it has also become indispensable raw material in some plastic products.It is developed so far, kind is varied, such as fills out Fill masterbatch, color masterbatch, flame-retardant master batch, antistatic master batch, wear-resisting masterbatch, multifunctional concentrate etc..
With the perfect raising of advanced technologies and production technology, kind, performance, the purposes of filling master batch are all adapting to market Demand and constantly change.Wherein fragrant plastic masterbatch is a kind of very important work(for assigning the certain fragrance of polyolefine material Energy sexupara material, its effect can enable product to send aromatic odor, give fresh, Shu Ya, pure and fresh sensation, add modeling The use value of material products, can cover that plastic products are intrinsic or process in smell, excite customer's desire to purchase, play Sales promotion function.Because of the advantageous characteristic of fragrant plastic, make its application in today's society more and more extensive.
Fragrance plastic matrix is the mixture for being uniformly dispersed aromachemicals high concentration in what Thermoplastic resin base material, main To be made up of vector resin, essence, additive, by certain formula and processing technology, be evenly dispersed in essence specific In vector resin.Vector resin is as high molecular polymer, and its molecular weight is big, and intermolecular distance is wide, and intermolecular various row Row order so that make the validity composition of fumet into plastic molecules, form fumet and Polymer Structure is close Multiphase body, dissipate fragrant purpose so as to reach.Because essence has the characteristic such as this low boiling point, volatile mostly, it is necessary to select fusing point low, add Good, the easy to penetrate fragrant resin of work performance, therefore the bond strength and essence of essence and resin are disperseed in vector resin Property be the stable fragrance plastic matrix of processability key.
Certain effect is achieved in terms of functional plastic masterbatch, especially fragrance plastic matrix both at home and abroad at present.Its A kind of High-concentration polyolefin aromatic master batches of middle Gao et al. and preparation method thereof.Composition includes vector resin, essence, adsorbent, filled out Agent, dispersant are filled, tri- kinds of resins of vector resin LLDPE, EVA, SBS, adsorbent is diatomite, and filler is calcium carbonate, point Powder is Tissuemat E, and each component percentage by weight is LLDPE15-18%, EVA18-23%, SBS3-5%, essence 5-20%, diatom Native 18-23%, calcium carbonate 10-25%, Tissuemat E 2-4%.Weigh material by formula rate, first by vector resin, adsorbent, fill out Fill agent, dispersant is added in agitated kettle together, then essence is slowly added under moderate-speed mixer, finally uniform compound is put into same Extruded into parallel double-screw extruder, expressing technique temperature parameter is controlled between 100-120 DEG C, through water-bath and cold front heavy rain Masterbatch is made in pelletizing after drying.In addition, Wang et al. has invented a kind of aroma agglomerate for plastics and preparation method thereof, include perfume (or spice) Essence, additive and vector resin, additive include kaolin, Tissuemat E, and described vector resin is ethane-acetic acid ethyenyl fat Copolymer resin, each component can have following percent by weight proportioning:Essence:10-15%;Kaolin:55-60%;Tissuemat E:3- 4%;Ethylene-vinyl acetate c resin:26-28%.But there is the essence in preparation and vector resin essence exhaustion easily to ooze out And volatilization, make resulting product fragrance be not easy to retain, scatter and disappear very fast, the shortcomings that aroma effect is poor, while preparation process is complicated, into This height, it is unfavorable for large-scale promotion.
The content of the invention
The defects of easily being oozed out for existing plastics flavouring masterbatch, a kind of fragrant plastic masterbatch is proposed, with solid-phase resin and gas The mixing of both collosol adhesives makes stock dispersion uniformly and strengthens combination, avoids oozing out.Can solve fragrant in Traditional flavor masterbatch Essence and vector resin essence exhaustion are easily oozed out and volatilized, and make resulting product fragrance be not easy to retain, and scatter and disappear very fast, and aroma effect is poor to be lacked Fall into.
Preparation method is further provided for, the mixed-powders such as vector resin powder, essence, auxiliary agent are added in high-speed mixer High-temperature aerosol adhesive is pressed into afterwards, makes the fluffy suspension of powder, due to high-temperature aerosol adhesive and inner wall of mixer and resin Contact and quick refrigeration, condense into and essence and toner are adhered to after particle, and under high-speed stirred effect with other raw material groups Divide and uniformly mix, crushed after being dried obtains fragrance masterbatch.The remarkable result of the method be adhesive air-flow condense after enhance with The adhesion of interlaminar resin, essence is not easy to ooze out and is volatilized, also ensure that essence is dispersed, while processing step is succinct and energy Consume low.
To achieve the above object, adopt the following technical scheme that:
A kind of preparation method of fragrant plastic masterbatch, concrete technical scheme are as follows:
(1)Using powdered plastic essence as masterbatch core, using LDPE resin powder as carrier, then it is equipped with a certain proportion of scattered Agent, antioxidant and heat stabilizer, are added in high-speed mixer, are pre-mixed under certain temperature and rotating speed;
(2)The adhesive of certain mass is placed in closed metal container, is pressed to form aerosol adhesive, then by aerosol Bonding dose is transferred in the gas transportation machine with heat insulation function, keeping temperature and pressure stability in transfer and course of conveying, And by the outlet of gas transportation machine and step(1)The gas feed of described high-speed mixer is connected;
(3)High-speed mixer is again started up, stirring makes the fluffy suspension of mixed-powder;After stirring is stable, starts gas transfer pump, make High-temperature aerosol adhesive is pressed into mixer rapidly, aerosol adhesive and temperature relatively low inner wall of mixer and LDPE resin Powder contact, quick refrigeration condense into particle, and essence powder and LDPE resin powder bonding are got up, and are acted in high-speed stirred It is lower to be well mixed with other components;
(4)Stop high-speed mixer, discharging, subsequently into plastic crusher, fragrant plastic masterbatch is produced after crushing.
Preferably, step(1)The particle diameter of the LDPE resin powder crosses 100 mesh sieves.
Preferably, step(1)The powdered plastics essence is the fragrance of a flower, fruity, tea perfume or hay-scented class essence, its high temperature resistant Ability should reach more than 250 DEG C;
Preferably, step(1)The plastic essence and the mixing quality ratio of LDPE resin powder are 1:10~1:5;
Preferably, step(1)The dispersant is low molecule amount PE, atoleine or stearic acid, and its addition is LDPE resin The 3 ~ 5% of powder quality;
Preferably, step(1)The antioxidant is dibutyl hydroxy toluene or TBHQ, and its addition is LDPE The 0.5 ~ 1% of toner quality;
Preferably, step(1)The heat stabilizer is Pb stabilizer, such as dibasic lead stearate, hydration lead sulfate tribasic Or dibasic lead phosphite, its addition are the 0.5 ~ 1% of LDPE resin powder quality;
Preferably, step(1)The temperature of the premixing is 40 ~ 50 DEG C, and rotating speed is 80 ~ 120r/min, and the time is 10 ~ 20min;
Preferably, step(2)Described adhesive is acrylic block copolymer;Aerosol adhesive is formed after pressurization.
Preferably, step(2)The pressurization, pressure 3-5MPa.
Preferably, step(2)The addition of described adhesive is the 4 ~ 6% of LDPE resin powder and essence quality summation;
Preferably, step(3)The temperature of the high-speed stirred mixing is 30 ~ 40 DEG C, and mixing speed is 150 ~ 200r/min.
A kind of fragrant plastic masterbatch, is prepared by the above method.Using powdered plastic essence as masterbatch core, with LDPE Toner is carrier, is equipped with other auxiliary agents, is pre-mixed in high-speed mixer;Then aerosol adhesive is added high In fast mixer, its quick refrigeration is condensed into particle, essence powder and LDPE resin powder bonding are got up, and in high-speed stirring The effect of mixing is lower to be well mixed with other components, and through drying and crushing after discharging, fragrant plastic masterbatch is made.
In the present invention, the dispersing uniformity of the adhesion and essence of essence and LDPE resin, it is to influence fragrance masterbatch An important factor for stable performance.It is aerosolized by adhesive for the adhesion of enhancing essence and LDPE resin, glued in aerosol Mixture enters before high-speed mixer, should first make mixer stirring a period of time, to ensure that mixed-powder reaches fluffy suspension State, mixing speed should properly increase, and aerosol adhesive is rapidly reached uniformly mixing after entering scattered.The temperature of mixed-powder Degree should be controlled below 40 DEG C, to ensure adhesive and mixed-powder and the temperature difference of mixer wall, make adhesive quick refrigeration Condense, essence powder and LDPE resin powder bonding are got up, its bond effect is more preferable.
The invention provides a kind of fragrant plastic masterbatch and preparation method thereof, compared with prior art, the characteristics of it is protruded It is with excellent effect:
1. the preparation method of the present invention, adhesive is by first mode that is aerosolized, then condensing to the cold, by essence powder and LDPE Toner bonds, and bond effect is preferable, and essence is not easy to ooze out and volatilized, and fragrance easily retains, and scatters and disappears slower.
2. the preparation method of the present invention, essence powder, LDPE resin powder and auxiliary agent are pre-mixed in high-speed mixer, Mixed at high speed is carried out again before being contacted with aerosol adhesive so that the dispersed homogeneous degree of essence improves, and itself and aerosol The contact of adhesive is more uniformly distributed.
3. the preparation method of the present invention, energy consumption is relatively low, and does not produce pollution, and the feature of environmental protection is good.
4. the preparation method of the present invention, simple to operate, it is easily controlled, properties of product are stable, and industrialized production can be achieved.
Embodiment
Below by way of embodiment, the present invention is described in further detail, but this should not be interpreted as to the present invention Scope be only limitted to following example.In the case where not departing from above method thought of the present invention, according to ordinary skill The various replacements or change that knowledge and customary means are made, should be included in the scope of the present invention.
Embodiment 1
A kind of fragrant plastic masterbatch and preparation method thereof, it is as follows that it prepares the detailed process of plastic matrix:
Using powdered plastic essence of the 1kg heat-resisting abilities more than 250 DEG C as masterbatch core, 8kgLDPE toners are made For carrier, then 0.32kg stearic acid, 0.08kg dibutyl hydroxy toluenes and 0.08kg dibasic lead stearates are equipped with, are added to height In fast mixer, premixing 10min is carried out at 50 DEG C of temperature and 80r/min rotating speed;By 0.45kg adhesive acrylic acid Based block copolymer is fitted into closed metal container;Aerosol adhesive is formed after pressurization 3MPa;Then by aerosol adhesive It is transferred in the gas transportation machine with heat insulation function, keeping temperature and pressure stability in transfer and course of conveying, and by gas The outlet of conveyer is connected with the gas feed of high-speed mixer;Be again started up high-speed mixer, with 30 DEG C of temperature and 200r/min speed stirring makes the fluffy suspension of mixed-powder.After stirring is stable, starts gas transfer pump, glue high-temperature aerosol Mixture is pressed into mixer rapidly, adhesive and the relatively low inner wall of mixer of temperature and LDPE resin powder contact, quick refrigeration Particle is condensed into, essence powder and LDPE resin powder bonding are got up, and is mixed under high-speed stirred effect with other components Uniformly;Stop high-speed mixer, discharging, subsequently into plastic crusher, fragrant plastic masterbatch is produced after crushing.
The fragrant plastic masterbatch obtained to embodiment 1, respectively behind 5 days, 30 days, half a year and 1 year, it is residual to test its fragrance Office Copy, and contrasted with common fragrance masterbatch, obtained data are as shown in table 1.It can be seen that:, can be obvious using the method for the present invention The bond strength of essence and LDPE resin is improved, oozing out and volatilizing for essence is reduced, makes fragrance be more easy to retain, speed of scattering and disappearing drop It is low.
Embodiment 2
A kind of fragrant plastic masterbatch and preparation method thereof, it is as follows that it prepares the detailed process of plastic matrix:
Using powdered plastic essence of the 1kg heat-resisting abilities more than 250 DEG C as masterbatch core, 9kgLDPE toners are made For carrier, then 0.36kg atoleines, 0.09kg TBHQs and 0.09kg hydration lead sulfate tribasics are equipped with, added Into high-speed mixer, premixing 20min is carried out at 40 DEG C of temperature and 80r/min rotating speed;By 5kg adhesive acrylic acid Based block copolymer is fitted into closed metal container;Aerosol adhesive is formed after pressurization 4MPa;Then by aerosol adhesive It is transferred in the gas transportation machine with heat insulation function, keeping temperature and pressure stability in transfer and course of conveying, and by gas The outlet of conveyer is connected with the gas feed of high-speed mixer;Be again started up high-speed mixer, with 35 DEG C of temperature and 150r/min speed stirring makes the fluffy suspension of mixed-powder.After stirring is stable, starts gas transfer pump, glue high-temperature aerosol Mixture is pressed into mixer rapidly, adhesive and the relatively low inner wall of mixer of temperature and LDPE resin powder contact, quick refrigeration Particle is condensed into, essence powder and LDPE resin powder bonding are got up, and is mixed under high-speed stirred effect with other components Uniformly;Stop high-speed mixer, discharging, subsequently into plastic crusher, fragrant plastic masterbatch is produced after crushing.
The fragrant plastic masterbatch obtained to embodiment 2, respectively behind 5 days, 30 days, half a year and 1 year, it is residual to test its fragrance Office Copy, and contrasted with common fragrance masterbatch, obtained data are as shown in table 1.It can be seen that:, can be obvious using the method for the present invention The bond strength of essence and LDPE resin is improved, oozing out and volatilizing for essence is reduced, makes fragrance be more easy to retain, speed of scattering and disappearing drop It is low.
Embodiment 3
A kind of fragrant plastic masterbatch and preparation method thereof, it is as follows that it prepares the detailed process of plastic matrix:
Using powdered plastic essence of the 1kg heat-resisting abilities more than 250 DEG C as masterbatch core, 5kgLDPE toners are made For carrier, then 0.2kg stearic acid, 0.05kg TBHQs and 0.05kg dibasic lead stearates are equipped with, are added to height In fast mixer, premixing 12min is carried out at 45 DEG C of temperature and 90r/min rotating speed;By 0.3kg adhesive acrylic acid series Block copolymer is fitted into closed metal container;Aerosol adhesive is formed after pressurization 3MPa;Then aerosol adhesive is turned Move in the gas transportation machine with heat insulation function, keeping temperature and pressure stability in transfer and course of conveying, and gas is defeated The outlet of machine is sent to be connected with the gas feed of high-speed mixer;High-speed mixer is again started up, with 35 DEG C of temperature and 180r/ Min speed stirring makes the fluffy suspension of mixed-powder.After stirring is stable, starts gas transfer pump, make high-temperature aerosol adhesive In rapid press-in mixer, adhesive and the relatively low inner wall of mixer of temperature and LDPE resin powder contact, quick refrigeration condense Into particle, essence powder and LDPE resin powder bonding are got up, and are well mixed under high-speed stirred effect with other components; Stop high-speed mixer, discharging, subsequently into plastic crusher, fragrant plastic masterbatch is produced after crushing.
The fragrant plastic masterbatch obtained to embodiment 3, respectively behind 5 days, 30 days, half a year and 1 year, it is residual to test its fragrance Office Copy, and contrasted with common fragrance masterbatch, obtained data are as shown in table 1.It can be seen that:, can be obvious using the method for the present invention The bond strength of essence and LDPE resin is improved, oozing out and volatilizing for essence is reduced, makes fragrance be more easy to retain, speed of scattering and disappearing drop It is low.
Embodiment 4
A kind of fragrant plastic masterbatch and preparation method thereof, it is as follows that it prepares the detailed process of plastic matrix:
Using powdered plastic essence of the 1kg heat-resisting abilities more than 250 DEG C as masterbatch core, 6kgLDPE toners are made For carrier, then 0.24kg stearic acid, 0.06kg dibutyl hydroxy toluenes and 0.06kg dibasic lead phosphites are equipped with, are added to height In fast mixer, premixing 15min is carried out at 50 DEG C of temperature and 100r/min rotating speed;By 0.35kg adhesive acrylic acid Based block copolymer is fitted into closed metal container;Aerosol adhesive is formed after pressurization 5MPa;Then by aerosol adhesive It is transferred in the gas transportation machine with heat insulation function, keeping temperature and pressure stability in transfer and course of conveying, and by gas The outlet of conveyer is connected with the gas feed of high-speed mixer;Be again started up high-speed mixer, with 30 DEG C of temperature and 190r/min speed stirring makes the fluffy suspension of mixed-powder.After stirring is stable, starts gas transfer pump, glue high-temperature aerosol Mixture is pressed into mixer rapidly, adhesive and the relatively low inner wall of mixer of temperature and LDPE resin powder contact, quick refrigeration Particle is condensed into, essence powder and LDPE resin powder bonding are got up, and is mixed under high-speed stirred effect with other components Uniformly;Stop high-speed mixer, discharging, subsequently into plastic crusher, fragrant plastic masterbatch is produced after crushing.
The fragrant plastic masterbatch obtained to embodiment 4, respectively behind 5 days, 30 days, half a year and 1 year, it is residual to test its fragrance Office Copy, and contrasted with common fragrance masterbatch, obtained data are as shown in table 1.It can be seen that:, can be obvious using the method for the present invention The bond strength of essence and LDPE resin is improved, oozing out and volatilizing for essence is reduced, makes fragrance be more easy to retain, speed of scattering and disappearing drop It is low.
Embodiment 5
A kind of fragrant plastic masterbatch and preparation method thereof, it is as follows that it prepares the detailed process of plastic matrix:
Using powdered plastic essence of the 1kg heat-resisting abilities more than 250 DEG C as masterbatch core, 7kgLDPE toners are made For carrier, then 0.28kg atoleines, 0.07kg TBHQs and 0.07kg dibasic lead phosphites are equipped with, be added to In high-speed mixer, premixing 18min is carried out at 40 DEG C of temperature and 90r/min rotating speed;By 0.4kg adhesive acrylic acid Based block copolymer is fitted into closed metal container;Aerosol adhesive is formed after pressurization 3MPa;Then by aerosol adhesive It is transferred in the gas transportation machine with heat insulation function, keeping temperature and pressure stability in transfer and course of conveying, and by gas The outlet of conveyer is connected with the gas feed of high-speed mixer;Be again started up high-speed mixer, with 30 DEG C of temperature and 160r/min speed stirring makes the fluffy suspension of mixed-powder.After stirring is stable, starts gas transfer pump, glue high-temperature aerosol Mixture is pressed into mixer rapidly, adhesive and the relatively low inner wall of mixer of temperature and LDPE resin powder contact, quick refrigeration Particle is condensed into, essence powder and LDPE resin powder bonding are got up, and is mixed under high-speed stirred effect with other components Uniformly;Stop high-speed mixer, discharging, subsequently into plastic crusher, fragrant plastic masterbatch is produced after crushing.
The fragrant plastic masterbatch obtained to embodiment 5, respectively behind 5 days, 30 days, half a year and 1 year, it is residual to test its fragrance Office Copy, and contrasted with common fragrance masterbatch, obtained data are as shown in table 1.It can be seen that:, can be obvious using the method for the present invention The bond strength of essence and LDPE resin is improved, oozing out and volatilizing for essence is reduced, makes fragrance be more easy to retain, speed of scattering and disappearing drop It is low.
Embodiment 6
A kind of fragrant plastic masterbatch and preparation method thereof, it is as follows that it prepares the detailed process of plastic matrix:
Using powdered plastic essence of the 1kg heat-resisting abilities more than 250 DEG C as masterbatch core, 8kgLDPE toners are made For carrier, then 0.32kg stearic acid, 0.08kg dibutyl hydroxy toluenes and 0.08kg hydration lead sulfate tribasics are equipped with, be added to In high-speed mixer, premixing 17min is carried out at 40 DEG C of temperature and 110r/min rotating speed;By 0.45kg adhesive propylene Sour based block copolymer is fitted into closed metal container;Aerosol adhesive is formed after pressurization 5MPa;Then aerosol is bonded Agent is transferred in the gas transportation machine with heat insulation function, keeping temperature and pressure stability in transfer and course of conveying, and by gas The outlet of body conveyer is connected with the gas feed of high-speed mixer;Be again started up high-speed mixer, with 30 DEG C of temperature and 200r/min speed stirring makes the fluffy suspension of mixed-powder.After stirring is stable, starts gas transfer pump, glue high-temperature aerosol Mixture is pressed into mixer rapidly, adhesive and the relatively low inner wall of mixer of temperature and LDPE resin powder contact, quick refrigeration Particle is condensed into, essence powder and LDPE resin powder bonding are got up, and is mixed under high-speed stirred effect with other components Uniformly;Stop high-speed mixer, discharging, subsequently into plastic crusher, fragrant plastic masterbatch is produced after crushing.
The fragrant plastic masterbatch obtained to embodiment 6, respectively behind 5 days, 30 days, half a year and 1 year, it is residual to test its fragrance Office Copy, and contrasted with common fragrance masterbatch, obtained data are as shown in table 1.It can be seen that:, can be obvious using the method for the present invention The bond strength of essence and LDPE resin is improved, oozing out and volatilizing for essence is reduced, makes fragrance be more easy to retain, speed of scattering and disappearing drop It is low.
Embodiment 7
A kind of fragrant plastic masterbatch and preparation method thereof, it is as follows that it prepares the detailed process of plastic matrix:
Using powdered plastic essence of the 1kg heat-resisting abilities more than 250 DEG C as masterbatch core, 10kgLDPE toners are made For carrier, then 0.4kg atoleines, 0.1kg dibutyl hydroxy toluenes and 0.1kg dibasic lead phosphites are equipped with, are added to height In fast mixer, premixing 18min is carried out at 45 DEG C of temperature and 90r/min rotating speed;By 0.55kg adhesive acrylic acid Based block copolymer is fitted into closed metal container;Aerosol adhesive is formed after pressurization 4MPa;Then by aerosol adhesive It is transferred in the gas transportation machine with heat insulation function, keeping temperature and pressure stability in transfer and course of conveying, and by gas The outlet of conveyer is connected with the gas feed of high-speed mixer;Be again started up high-speed mixer, with 35 DEG C of temperature and 160r/min speed stirring makes the fluffy suspension of mixed-powder.After stirring is stable, starts gas transfer pump, glue high-temperature aerosol Mixture is pressed into mixer rapidly, adhesive and the relatively low inner wall of mixer of temperature and LDPE resin powder contact, quick refrigeration Particle is condensed into, essence powder and LDPE resin powder bonding are got up, and is mixed under high-speed stirred effect with other components Uniformly;Stop high-speed mixer, discharging, subsequently into plastic crusher, fragrant plastic masterbatch is produced after crushing.
The fragrant plastic masterbatch obtained to embodiment 7, respectively behind 5 days, 30 days, half a year and 1 year, it is residual to test its fragrance Office Copy, and contrasted with common fragrance masterbatch, obtained data are as shown in table 1.It can be seen that:, can be obvious using the method for the present invention The bond strength of essence and LDPE resin is improved, oozing out and volatilizing for essence is reduced, makes fragrance be more easy to retain, speed of scattering and disappearing drop It is low.
Comparative example 1
Aerosol adhesive is not used, directly mixes essence with LDPE resin masterbatch, other formulas and process conditions and implementation Example 6 is consistent.The fragrant plastic masterbatch obtained to comparative example 1, respectively behind 5 days, 30 days, half a year and 1 year, it is residual to test its fragrance Office Copy, obtained data are as shown in table 1.
Table 1:

Claims (10)

1. a kind of preparation method of fragrant plastic masterbatch, concrete technical scheme are as follows:
(1)Using powdered plastic essence as masterbatch core, using LDPE resin powder as carrier, then it is equipped with a certain proportion of scattered Agent, antioxidant and heat stabilizer, are added in high-speed mixer, are pre-mixed under certain temperature and rotating speed;
(2)The adhesive of certain mass is placed in closed metal container, is pressed to form aerosol adhesive, then by aerosol Bonding dose is transferred in the gas transportation machine with heat insulation function, keeping temperature and pressure stability in transfer and course of conveying, And by the outlet of gas transportation machine and step(1)The gas feed of described high-speed mixer is connected;
(3)High-speed mixer is again started up, stirring makes the fluffy suspension of mixed-powder;After stirring is stable, starts gas transfer pump, make High-temperature aerosol adhesive is pressed into mixer rapidly, aerosol adhesive and temperature relatively low inner wall of mixer and LDPE resin Powder contact, quick refrigeration condense into particle, and essence powder and LDPE resin powder bonding are got up, and are acted in high-speed stirred It is lower to be well mixed with other components;
(4)Stop high-speed mixer, discharging, subsequently into plastic crusher, fragrant plastic masterbatch is produced after crushing.
A kind of 2. preparation method of fragrant plastic masterbatch according to claim 1, it is characterised in that:Step(1)The LDPE The particle diameter of toner crosses 100 mesh sieves.
A kind of 3. preparation method of fragrant plastic masterbatch according to claim 1, it is characterised in that:Step(1)The powder Shape plastic essence is that the fragrance of a flower, fruity, tea perfume or hay-scented class essence, its heat-resisting ability should reach more than 250 DEG C.
A kind of 4. preparation method of fragrant plastic masterbatch according to claim 1, it is characterised in that:Step(1)The plastics The mixing quality ratio of essence and LDPE resin powder is 1:10~1:5;Step(1)The dispersant is low molecule amount PE, liquid Paraffin or stearic acid, its addition are the 3 ~ 5% of LDPE resin powder quality;The antioxidant be dibutyl hydroxy toluene or TBHQ, its addition are the 0.5 ~ 1% of LDPE resin powder quality;The heat stabilizer is Pb stabilizer, such as Dibasic lead stearate, hydration lead sulfate tribasic or dibasic lead phosphite, its addition are LDPE resin powder quality 0.5~1%。
A kind of 5. preparation method of fragrant plastic masterbatch according to claim 1, it is characterised in that:Step(1)The premix The temperature of conjunction is 40 ~ 50 DEG C, and rotating speed is 80 ~ 120r/min, and the time is 10 ~ 20min.
A kind of 6. preparation method of fragrant plastic masterbatch according to claim 1, it is characterised in that:Step(2)The bonding Agent is acrylic block copolymer.
A kind of 7. preparation method of fragrant plastic masterbatch according to claim 1, it is characterised in that:Step(2)The bonding The addition of agent is the 4 ~ 6% of LDPE resin powder and essence quality summation.
A kind of 8. preparation method of fragrant plastic masterbatch according to claim 1, it is characterised in that:Step(2)The pressurization, Pressure is 3-5MPa.
A kind of 9. preparation method of fragrant plastic masterbatch according to claim 1, it is characterised in that:Step(3)The high speed The temperature being stirred is 30 ~ 40 DEG C, and mixing speed is 150 ~ 200r/min.
10. a kind of fragrant plastic masterbatch, it is characterized in being prepared by any one of claim 1-9 methods described.
CN201711008478.9A 2017-10-25 2017-10-25 A kind of fragrant plastic masterbatch and preparation method thereof Withdrawn CN107698848A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201711008478.9A CN107698848A (en) 2017-10-25 2017-10-25 A kind of fragrant plastic masterbatch and preparation method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201711008478.9A CN107698848A (en) 2017-10-25 2017-10-25 A kind of fragrant plastic masterbatch and preparation method thereof

Publications (1)

Publication Number Publication Date
CN107698848A true CN107698848A (en) 2018-02-16

Family

ID=61182332

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201711008478.9A Withdrawn CN107698848A (en) 2017-10-25 2017-10-25 A kind of fragrant plastic masterbatch and preparation method thereof

Country Status (1)

Country Link
CN (1) CN107698848A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112724528A (en) * 2020-12-29 2021-04-30 上海普利特复合材料股份有限公司 Polypropylene material with lasting fragrance and preparation method thereof

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102272224A (en) * 2008-12-30 2011-12-07 3M创新有限公司 Acrylic block copolymers for aerosols and aerosol adhesives
CN102766294A (en) * 2012-04-27 2012-11-07 南风化工集团股份有限公司 High-concentration polyolefin aromatic master batch and its preparation method
CN102993553A (en) * 2011-09-14 2013-03-27 比亚迪股份有限公司 Smell master batch and its preparation method
CN107151382A (en) * 2017-05-09 2017-09-12 武汉纺织大学 The preparation method of fragrant plastic master batch

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102272224A (en) * 2008-12-30 2011-12-07 3M创新有限公司 Acrylic block copolymers for aerosols and aerosol adhesives
CN102993553A (en) * 2011-09-14 2013-03-27 比亚迪股份有限公司 Smell master batch and its preparation method
CN102766294A (en) * 2012-04-27 2012-11-07 南风化工集团股份有限公司 High-concentration polyolefin aromatic master batch and its preparation method
CN107151382A (en) * 2017-05-09 2017-09-12 武汉纺织大学 The preparation method of fragrant plastic master batch

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
丁浩: "《塑料工业实用手册(第二版)上册》", 31 August 2000, 化学工业出版社 *
俞根发等: "《日用香精调配技术》", 30 September 2007, 中国轻工业出版社 *
蒋阳等: "《粉体工程》", 31 December 2008, 武汉理工大学出版社 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112724528A (en) * 2020-12-29 2021-04-30 上海普利特复合材料股份有限公司 Polypropylene material with lasting fragrance and preparation method thereof

Similar Documents

Publication Publication Date Title
CN102796470B (en) High-temperature-resistant EVA (ethylene-vinyl acetate) hot-melt adhesive for woodwork coating and preparation method thereof
CN101412828B (en) Modified polypropylene composition and preparation thereof
CN102766294B (en) High-concentration polyolefin aromatic master batch and its preparation method
CN101423636B (en) High rigid and high heat tolerant polypropylene composition and preparation method thereof
CN102924780B (en) Color master batch and manufacture method thereof
CN102093624B (en) Method for preparing color master batch for ethylene vinyl acetate (EVA) shoe material
CN102993757B (en) Preparation method of stable composite modified asphalt
CN108178870A (en) A kind of injection grade polypropylene wood plastic micro foaming composite material and preparation method thereof
CN106977957A (en) It is a kind of specially to add TPE material of glass and preparation method thereof in encapsulated nylon
WO2020211826A1 (en) Environmentally-friendly composite plastic and plastic product
CN107698848A (en) A kind of fragrant plastic masterbatch and preparation method thereof
CN103319826B (en) A kind of Water-soluble clay composition and preparation method thereof
CN107652507A (en) A kind of preparation method of fire-retardant plastic sheeting
CN103030335A (en) Colored rock paint and preparation method thereof
CN107033567A (en) Peanut shell powder filled polypropylene lactic acid composite material and preparation method thereof
CN108047666A (en) A kind of tensile strength environmentally-friendly plastic Masterbatch macromolecule carrier and its manufacturing method
CN108641181A (en) A kind of toughening type master batch and preparation method thereof
CN112029205A (en) Environment-friendly composite plastic with pearlescent effect and multicolor pattern effect and preparation method thereof
CN107118574A (en) A kind of graininess asphalt modifier with high viscosity and preparation method thereof
CN103387716B (en) Special blue master batch of a kind of BOPS sheet material and preparation method thereof
CN107573590A (en) A kind of environment-friendly polypropylene material with lasting fragrance and preparation method thereof
CN103740185B (en) A kind of atactic copolymerized polypropene coating material
CN104403189A (en) Fluorescent color masterbatch for EVA glue film and preparation method of fluorescent color masterbatch
CN105542279A (en) Preparation method of highly-filled polyethylene master batch
CN105440723A (en) Preparation method of carrier-free precipitated barium sulfate transparent master batch

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
WW01 Invention patent application withdrawn after publication

Application publication date: 20180216

WW01 Invention patent application withdrawn after publication