CN112829412B - High-performance polypropylene aluminum-plated base film and preparation method thereof - Google Patents

High-performance polypropylene aluminum-plated base film and preparation method thereof Download PDF

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CN112829412B
CN112829412B CN202110010638.3A CN202110010638A CN112829412B CN 112829412 B CN112829412 B CN 112829412B CN 202110010638 A CN202110010638 A CN 202110010638A CN 112829412 B CN112829412 B CN 112829412B
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surface layer
polypropylene
base film
master batch
film
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CN112829412A (en
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郑国星
薛圣光
尤良铁
徐董
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Wenzhou Gettel Plastic Co ltd
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Wenzhou Gettel Plastic Co ltd
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/06Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material
    • B32B27/08Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material of synthetic resin
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29DPRODUCING PARTICULAR ARTICLES FROM PLASTICS OR FROM SUBSTANCES IN A PLASTIC STATE
    • B29D7/00Producing flat articles, e.g. films or sheets
    • B29D7/01Films or sheets
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/18Layered products comprising a layer of synthetic resin characterised by the use of special additives
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/32Layered products comprising a layer of synthetic resin comprising polyolefins
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65DCONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
    • B65D65/00Wrappers or flexible covers; Packaging materials of special type or form
    • B65D65/38Packaging materials of special type or form
    • B65D65/40Applications of laminates for particular packaging purposes
    • 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
    • C08J5/00Manufacture of articles or shaped materials containing macromolecular substances
    • C08J5/18Manufacture of films or sheets
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2250/00Layers arrangement
    • B32B2250/24All layers being polymeric
    • B32B2250/242All polymers belonging to those covered by group B32B27/32
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2553/00Packaging equipment or accessories not otherwise provided for
    • 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
    • C08J2323/10Homopolymers or copolymers of propene
    • C08J2323/12Polypropene
    • 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
    • C08J2323/10Homopolymers or copolymers of propene
    • C08J2323/14Copolymers of propene
    • 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
    • C08J2423/00Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
    • C08J2423/02Characterised 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
    • C08J2423/10Homopolymers or copolymers of propene
    • C08J2423/12Polypropene
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/10Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working

Abstract

The invention discloses a high-performance polypropylene aluminized base film, which comprises an upper surface layer, a core layer and a lower surface layer, wherein the upper surface layer is prepared from 94-98 wt% of binary copolymer polypropylene, 2-4 wt% of an anti-sticking agent and 2-4 wt% of electret master batch; the core layer is prepared from 100 wt% of homopolymerized polypropylene; the lower surface layer is prepared from 96-98 wt% of binary copolymer polypropylene and 2-4 wt% of anti-sticking agent. According to the technical scheme, the electret master batch is added in the film, so that the surface wetting tension of the film is greatly improved, the aluminizing fastness is remarkably improved, the surface wetting tension is good, the aluminizing fastness is high, the practicability is good, the problem of pain in aluminizing of the film of a downstream customer is solved, and the added value of a product is improved.

Description

High-performance polypropylene aluminum-plated base film and preparation method thereof
Technical Field
The invention relates to the technical field of film production, in particular to a high-performance polypropylene aluminized base film and a preparation method thereof.
Background
With the continuous improvement of people's life, the need for packaging food is increasing, and the BOPP food packaging bag is widely used in people's life as a good-quality and cheap commodity. The BOPP food packaging bag has the advantages of high tensile strength, high heat resistance, good moisture resistance and the like, but also has the defects of weaker oxygen resistance and short food shelf life. In order to improve the oxygen resistance of the BOPP film, downstream manufacturers can carry out aluminum plating treatment on the surface of the film according to requirements.
After corona treatment, the surface wetting tension of a common BOPP film is temporarily greatly improved, but the problem of fast attenuation easily occurs after aging, so that the later aluminizing fastness is low, and even aluminizing cannot be performed.
Disclosure of Invention
Aiming at the defects in the prior art, the invention aims to provide a high-performance polypropylene aluminized base film with good surface wetting tension, high aluminizing fastness and good practicability and a preparation method thereof.
In order to realize the purpose, the invention provides the following technical scheme: a high-performance polypropylene aluminized base film comprises an upper surface layer, a core layer and a lower surface layer, wherein the upper surface layer is prepared from 94-98 wt% of binary copolymer polypropylene, 2-4 wt% of an anti-sticking agent and 2-4 wt% of electret master batch; the core layer is prepared from 100 wt% of homopolymerized polypropylene; the lower surface layer is prepared from 96-98 wt% of binary copolymer polypropylene and 2-4 wt% of anti-sticking agent.
Preferably, the thickness of the upper surface layer is 1.1-1.5 microns, and the thickness of the lower surface layer is 0.9-1.2 microns.
Preferably, the melt index of the binary copolymer polypropylene is 7.5-9.5g/10min, and the type is KS 407.
Preferably, the anti-sticking agent is an organic anti-sticking agent with the model AB6056 PPR.
Preferably, the melting index of the electret master batch is 6-8g/10min, and the main components of the electret master batch are polypropylene and an electret material.
Preferably, the isotactic polypropylene has an isotacticity of 97-98%, a melt index of 2.5-3.5g/10min, and a type F03D (QD).
Preferably, the preparation method of the electret masterbatch comprises the following steps:
1. stirring and uniformly mixing the required raw materials in proportion, and loading the mixture into a hopper of an extruder;
2. controlling the temperature and the rotating speed of the extruder, and extruding the mixed raw materials into a plurality of strips from a die head;
3. cooling the extruded strip master batch by using cooling water quickly, and drying by using circulating air after shaping;
4. and cutting the dried master batch into small particles by a granulator, sucking the small particles into a storage bin, drying the small particles again and then bagging the dried small particles.
The invention also provides a preparation method of the high-performance polypropylene aluminized base film, which comprises the following steps:
(1) preparing materials: the raw materials of each component required by the core layer, the first surface layer and the second surface layer are proportioned according to the proportioning requirement and are respectively and fully mixed uniformly;
(2) extruding and casting sheets: melting and plasticizing the uniformly mixed raw materials of each layer in respective extruders; the core layer raw material uses a double-screw extruder, redundant air is removed during raw material plasticization, the extruded raw material is subjected to secondary plasticization, metering and filtration, the set temperature is 245-; finally, extruding the three layers of raw materials from the die head together through corresponding connecting pipes, wherein the temperature of the die head is 235-; the extruded raw materials are uniformly adhered to the surface of the cold roll under the action of an air knife to form a sheet with uniform thickness, and the sheet is rapidly shaped by a chill roll and a water tank and then dried.
(3) And (3) bidirectional stretching: the dried sheet enters a longitudinal stretching area, and longitudinal stretching is completed through preheating, stretching and shaping of different rollers; the thick sheet enters a transverse stretching area, and is sequentially preheated, stretched, shaped and cooled by an air box and a chain to finish transverse stretching; the longitudinal stretching ratio is controlled between 4.8 and 5.5, and the transverse stretching ratio is controlled between 9 and 10.
(4) Traction, thickness measurement and winding: cooling, flattening and trimming the formed film, then measuring the thickness and automatically controlling, then improving the surface tension through corona treatment, and finally winding the film on a steel core through a double-station winding machine to obtain a semi-finished product;
(5) aging treatment and slitting: and (3) storing the semi-finished product on an aging rack with the temperature of 20-35 ℃ and the humidity of 45-70% for about 48 hours, and slitting the semi-finished product by a slitting machine according to the width required by a customer to obtain a corresponding finished product roll.
The invention has the advantages that: compared with the prior art, the electret master batch is added in the film, so that the surface wetting tension of the film is greatly improved, the aluminizing fastness is obviously improved, the surface wetting tension is good, the aluminizing fastness is high, the practicability is good, the problem of pain points of downstream customer film aluminizing is solved, and the added value of products is improved.
The invention is further described with reference to the following description and specific examples.
Detailed Description
The invention discloses a high-performance polypropylene aluminized base film, which comprises an upper surface layer, a core layer and a lower surface layer, wherein the upper surface layer is prepared from 94-98 wt% of binary copolymer polypropylene, 2-4 wt% of an anti-sticking agent and 2-4 wt% of electret master batch; the core layer is prepared from 100 wt% of homo-polypropylene; the lower surface layer is prepared from 96-98 wt% of binary copolymer polypropylene and 2-4 wt% of anti-sticking agent.
Preferably, the thickness of the upper surface layer is 1.1-1.5 microns, and the thickness of the lower surface layer is 0.9-1.2 microns.
Preferably, the melt index of the binary copolymer polypropylene is 7.5-9.5g/10min, and the type is KS 407.
Preferably, the anti-sticking agent is an organic anti-sticking agent with the model AB6056 PPR.
Preferably, the melting index of the electret master batch is 6-8g/10min, and the main components of the electret master batch are polypropylene and an electret material.
Preferably, the isotactic polypropylene has an isotacticity of 97-98%, a melt index of 2.5-3.5g/10min, and a type F03D (QD).
Preferably, the preparation method of the electret masterbatch comprises the following steps:
1. stirring and uniformly mixing the required raw materials in proportion, and loading the mixture into a hopper of an extruder;
2. controlling the temperature and the rotating speed of the extruder, and extruding the mixed raw materials into a plurality of strips from a die head;
3. cooling the extruded strip master batch by using cooling water quickly, and drying by using circulating air after shaping;
4. and cutting the dried master batch into small particles by a granulator, sucking the small particles into a storage bin, drying the small particles again and then bagging the dried small particles.
The invention also provides a preparation method of the high-performance polypropylene aluminized base film, which comprises the following steps:
(1) preparing materials: the raw materials of each component required by the core layer, the first surface layer and the second surface layer are proportioned according to the proportioning requirement and are respectively and fully mixed uniformly;
(2) extruding and casting sheets: melting and plasticizing the uniformly mixed raw materials of each layer in respective extruders; the core layer raw material uses a double-screw extruder, redundant air is removed during raw material plasticization, the extruded raw material is subjected to secondary plasticization, metering and filtering, the set temperature is 245-minus ice ℃ and 255 ℃, the upper surface layer raw material is extruded and filtered by the single-screw extruder, the set temperature is 235-minus ice ℃ and 245 ℃, the lower surface layer raw material is extruded and filtered by the single-screw extruder, and the set temperature is 235-minus ice ℃ and 245 ℃; finally, extruding the three layers of raw materials from the die head together through corresponding connecting pipes, wherein the temperature of the die head is 235-; the extruded raw material is uniformly adhered to the surface of the cold roll under the action of an air knife to form a sheet with uniform thickness, and the sheet is rapidly shaped by a chilling roll and a water tank and then dried.
(3) And (3) bidirectional stretching: the dried sheet enters a longitudinal stretching area, and longitudinal stretching is completed through preheating, stretching and shaping of different rollers; the thick sheet enters a transverse stretching area, and is sequentially preheated, stretched, shaped and cooled by an air box and a chain to finish transverse stretching; the longitudinal stretching ratio is controlled between 4.8 and 5.5, and the transverse stretching ratio is controlled between 9 and 10.
(4) Traction, thickness measurement and winding: after cooling, flattening and trimming the formed film, performing thickness measurement and automatic control, improving the surface tension through corona treatment, and finally winding the film on a steel core through a double-station winding machine to obtain a semi-finished product;
(5) aging treatment and slitting: and storing the semi-finished product on an aging rack with the temperature of 20-35 ℃ and the humidity of 45-70% for about 48 hours, and slitting by a slitting machine according to the width required by a client to obtain a corresponding finished product roll.
Example 1
A30 micron high-performance polypropylene aluminized base film and a preparation method thereof comprise the following steps:
a high-performance polypropylene aluminized base film comprises an upper surface layer, a core layer and a lower surface layer, wherein the upper surface layer comprises the following components in percentage by weight: 95 percent of binary copolymerized polypropylene, 2.5 percent of anti-sticking agent and 2.5 percent of electret master batch; the core layer comprises the following components in percentage by weight: 100% of homopolymerized polypropylene; the following layers are selected according to the weight percentage: 97.5 percent of binary copolymer polypropylene and 22.5 percent of anti-sticking agent. The thickness of the film is 28.5 microns, wherein the thickness of the upper surface layer is 1.1-1.5 microns, and the thickness of the lower surface layer is 0.9-1.2 microns.
A preparation method of a high-performance polypropylene aluminized base film comprises the following steps:
preparing materials: the components of the upper surface layer, the core layer and the lower surface layer are respectively put into the corresponding double-screw extruder through a feeding system according to the weight percentage;
extruding and plasticizing: the core layer raw material enters a double-screw extruder, the raw material is plasticized, vacuumized and subjected to secondary plasticizing measurement and then extruded, the set temperature is 250 ℃, the upper layer raw material is extruded through a single-screw extruder, the set temperature is 240 ℃, the lower layer raw material is extruded through the single-screw extruder, and the set temperature is 240 ℃; the three layers of raw materials are extruded out of the die head together through corresponding connecting pipes, and the temperature of the die head is 245 ℃.
Cooling the cast sheet: the air knife tightly attaches the extruded molten thick sheet to the chilling roller, and the thick sheet is rapidly cooled by the rotation of the chilling roller in the water tank. The surface temperature of the chill roll is controlled at 38 ℃, and the temperature of the water tank is controlled at 38 ℃; the slab is cooled and dried twice and then stretched in the longitudinal direction.
Longitudinal stretching: the longitudinal stretching is divided into three parts of preheating, stretching and shaping. The temperature of the preheating roller is 130 ℃; the temperature of the stretching roller is 120 ℃, and the stretching magnification is 5.2; the setting roller temperature is 135 ℃. The film drawn longitudinally at 360 meters per second was then passed through a set of guide rolls and stretched transversely.
And (3) transverse stretching: the longitudinal stretching is divided into four parts of preheating, stretching, shaping and cooling. The temperature of the preheating zone for transverse stretching is 174 ℃, the temperature of the stretching zone is 156 ℃, the temperature of the periodic zone is 167 ℃, and the temperature of the cooling zone is indoor temperature. The maximum draw ratio of the film was 9.0 and the exit speed was 345 m/s. The exiting film is again cooled in air and enters the pulling area.
Traction and winding: and the film entering the traction area is subjected to processes of cooling, trimming, thickness measurement, corona winding and the like to complete the winding work of the film.
And (4) aging and slitting, namely performing primary detection on the collected large film roll through a grade pipe part, placing the large film roll on an aging rack after the large film roll is qualified, performing secondary detection after the aging is finished, and changing the large film roll into the specification required by a customer by a slitting machine after the large film roll is qualified.
Example 2
A common 30-micron polypropylene aluminized base film and a preparation method thereof comprise the following steps:
a common polypropylene aluminized base film comprises an upper surface layer, a core layer and a lower surface layer, wherein the upper surface layer comprises the following components in percentage by weight: 97.5 percent of binary copolymer polypropylene, 2.5 percent of anti-sticking agent and the components; the core layer comprises the following components in percentage by weight: 100% of homopolymerized polypropylene; the following layers are selected according to the weight percentage: 97.5 percent of binary copolymer polypropylene and 22.5 percent of anti-sticking agent. The thickness of the film is 28.5 microns, wherein the thickness of the upper surface layer is 1.1-1.5 microns, and the thickness of the lower surface layer is 0.9-1.2 microns.
A preparation method of a high-performance polypropylene aluminized base film comprises the following steps:
preparing materials: the components of the upper surface layer, the core layer and the lower surface layer are respectively put into the corresponding double-screw extruder through a feeding system according to the weight percentage;
extruding and plasticizing: the core layer raw material enters a double-screw extruder, the raw material is plasticized, vacuumized and measured for secondary plasticization and then extruded, the set temperature is 250 ℃, the upper-layer raw material is extruded by a single-screw extruder, the set temperature is 240 ℃, and the lower-layer raw material is extruded by the single-screw extruder, and the set temperature is 240 ℃; the three layers of raw materials are extruded together from a die head through corresponding connecting pipes, and the temperature of the die head is 245 ℃.
Cooling the cast sheet: the air knife tightly attaches the extruded molten thick sheet to the chilling roller, and the thick sheet is rapidly cooled by the rotation of the chilling roller in the water tank. The surface temperature of the chill roll is controlled at 38 ℃, and the temperature of the water tank is controlled at 38 ℃; the slab is cooled and dried twice and then stretched in the longitudinal direction.
Longitudinal stretching: the longitudinal stretching is divided into three parts of preheating, stretching and shaping. The temperature of the preheating roller is 130 ℃; the temperature of the stretching roller is 120 ℃, and the stretching magnification is 5.2; the setting roller temperature is 135 ℃. The film drawn longitudinally at 360 meters per second was then passed through a set of guide rolls and stretched transversely.
Transverse stretching: the longitudinal stretching is divided into four parts of preheating, stretching, shaping and cooling. The temperature of the preheating zone for transverse stretching is 174 ℃, the temperature of the stretching zone is 156 ℃, the temperature of the periodic zone is 167 ℃, and the temperature of the cooling zone is indoor temperature. The maximum draw ratio of the film was 9.0 and the exit velocity was 345 m/s. The exiting film is again cooled in air and enters the pulling area.
Traction and winding: and the film entering the traction area is subjected to the processes of cooling, trimming, thickness measurement, corona winding and the like to finish the winding work of the film.
And (4) aging and slitting, namely performing primary detection on the collected large film roll through a product pipe part, placing the large film roll on an aging rack after the large film roll is detected to be qualified, performing secondary detection after the aging is finished, and changing the large film roll into a specification required by a customer by a slitting machine after the large film roll is detected to be qualified.
The following results are obtained by collecting relevant film products and detecting and analyzing the performance indexes of the film products.
And (3) data detection: see table 1.
Figure GDA0003723241750000081
TABLE 1
The data show that the physical properties of the films produced under the same process conditions are basically the same by using the same detection method, but the surface wetting tension of the films is greatly improved after the electret master batch is added into the films. The film added with the electret master batch is used by downstream customers, so that the aluminizing fastness is obviously improved, which shows that the technical scheme of the invention is reliable and practical.
The above embodiments are described in detail for the purpose of further illustrating the present invention and should not be construed as limiting the scope of the present invention, and the skilled engineer can make insubstantial modifications and variations of the present invention based on the above disclosure.

Claims (6)

1. A high-performance polypropylene aluminized base film comprises an upper surface layer, a core layer and a lower surface layer, and is characterized in that: the upper surface layer is prepared from 94-98 wt% of binary copolymer polypropylene, 2-4 wt% of anti-sticking agent and 2-4 wt% of electret master batch; the core layer is prepared from 100 wt% of homopolymerized polypropylene; the lower surface layer is prepared from 96-98 wt% of binary copolymer polypropylene and 2-4 wt% of anti-sticking agent;
the preparation method of the electret master batch comprises the following steps:
1. stirring and uniformly mixing the required raw materials in proportion, and loading the mixture into a hopper of an extruder;
2. controlling the temperature and the rotating speed of the extruder, and extruding the mixed raw materials into a plurality of strips from a die head;
3. cooling the extruded strip master batch by using cooling water quickly, and drying by using circulating air after shaping;
4. cutting the dried master batch into small particles by a granulator, sucking the small particles into a storage bin, drying the small particles again and then bagging the small particles;
the preparation method of the high-performance polypropylene aluminized base film comprises the following steps:
(1) preparing materials: the raw materials of each component required by the core layer, the first surface layer and the second surface layer are proportioned according to the proportioning requirement and are respectively and fully mixed uniformly;
(2) extruding and casting sheets: melting and plasticizing the uniformly mixed raw materials of each layer in respective extruders; the core layer raw material uses a double-screw extruder, redundant air is removed during raw material plasticization, the extruded raw material is subjected to secondary plasticization, metering and filtration, the set temperature is 245-; finally, extruding the three layers of raw materials from the die head together through corresponding connecting pipes, wherein the temperature of the die head is 235-; the extruded raw materials are uniformly adhered to the surface of a cold roll under the action of an air knife to form a sheet with uniform thickness, and the sheet is rapidly shaped by a chill roll and a water tank and then dried;
(3) and (3) bidirectional stretching: the dried sheet enters a longitudinal stretching area, and longitudinal stretching is completed through preheating, stretching and shaping of different rollers; the thick sheet enters a transverse stretching area, and is sequentially preheated, stretched, shaped and cooled by an air box and a chain to finish transverse stretching; the longitudinal stretching ratio is controlled to be between 4.8 and 5.5, and the transverse stretching ratio is controlled to be between 9 and 10;
(4) traction, thickness measurement and winding: after cooling, flattening and trimming the formed film, performing thickness measurement and automatic control, improving the surface tension through corona treatment, and finally winding the film on a steel core through a double-station winding machine to obtain a semi-finished product;
(5) aging treatment and slitting: and storing the semi-finished product on an aging rack with the temperature of 20-35 ℃ and the humidity of 45-70% for about 48 hours, and slitting by a slitting machine according to the width required by a client to obtain a corresponding finished product roll.
2. The high-performance polypropylene aluminized base film according to claim 1, characterized in that: the thickness of the upper surface layer is 1.1-1.5 micrometers, and the thickness of the lower surface layer is 0.9-1.2 micrometers.
3. The high-performance polypropylene aluminized base film according to claim 2, characterized in that: the melt index of the binary copolymer polypropylene is 7.5-9.5g/10min, and the type is KS 407.
4. The high-performance polypropylene aluminum-plated base film according to claim 3, characterized in that: the anti-sticking agent is an organic anti-sticking agent with the model AB6056 PPR.
5. The high-performance polypropylene aluminized base film according to claim 4, characterized in that: the melting index of the electret master batch is 6-8g/10min, and the main components of the electret master batch are polypropylene and electret materials.
6. The high-performance polypropylene aluminum-plated base film according to claim 5, wherein: the isotactic degree of the homopolymerized polypropylene is 97-98%, the melt index is 2.5-3.5g/10min, and the type is F03D (QD).
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