CN220615015U - Manufacturing equipment for single-sided matte polyester film - Google Patents

Manufacturing equipment for single-sided matte polyester film Download PDF

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CN220615015U
CN220615015U CN202322368111.5U CN202322368111U CN220615015U CN 220615015 U CN220615015 U CN 220615015U CN 202322368111 U CN202322368111 U CN 202322368111U CN 220615015 U CN220615015 U CN 220615015U
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coating
matte
polyester
polyester film
acid
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CN202322368111.5U
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吴培服
陆敬权
刘鸿纬
唐绪成
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Jiangsu Shuangxing Color Plastic New Materials Co Ltd
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Jiangsu Shuangxing Color Plastic New Materials Co Ltd
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Abstract

The application discloses manufacturing equipment for a single-sided matte polyester film, which comprises a slicing preheating and drying device, a double-screw extruder, a longitudinal stretching mechanism, a transverse stretching mechanism, a heat setting mechanism, a cooling mechanism and a first receiving roller; the online coating mechanism for preparing the online coating matte coating is arranged between the double-screw extruder and the longitudinal stretching mechanism; or between the longitudinal stretching mechanism and the transverse stretching mechanism; an offline protective coating mechanism for preparing an offline protective coating is arranged at the downstream of the first receiving roller, and the downstream of the offline protective coating mechanism further comprises an infrared heating device and a second receiving roller for winding the prepared single-sided matte polyester film. The single-sided matte polyester film prepared by the preparation equipment can achieve the matte effect by online coating of the matte coating, the problem of weakening performance after stretching is avoided, and the cost is lower.

Description

Manufacturing equipment for single-sided matte polyester film
Technical Field
The application relates to manufacturing equipment for a single-sided matte polyester film.
Background
CN 106739367B discloses a single-sided matte polyester film, which has a co-extrusion double-layer structure formed by compounding a matte film layer and a base film layer, wherein the matte film layer consists of 10-100% of polyester master batch containing additives and the balance of polyester base material, and the content of the additives in the polyester master batch accounts for 6-10% of the total mass of the polyester master batch. The additive in the polyester master batch consists of silicon dioxide and auxiliary filler, and the particle size of the additive is 6-8 mu m. The auxiliary filler is at least one selected from calcium carbonate, hollow glass beads, aluminum oxide, kaolin and titanium dioxide.
CN 114619745B discloses a matt polyester film with a multilayer structure, which comprises a base film and a matt film, wherein the middle layer is the base film, and the matt film is arranged on two sides of the base film and is obtained by a coextrusion technology; the raw materials of the matte film comprise a matte additive, wherein the matte additive is a polymer grafted modified silicon dioxide microsphere and a polystyrene microsphere, and the polymer grafted modified monomer is alkyl (methyl) acrylate and isobornyl acrylate; the polymer grafted modified silica microsphere D90 is 50-500nm, and the D90 of the polystyrene microsphere is 2-10 mu m.
The single-sided matte polyester film of the prior art is prepared by adopting a multilayer coextrusion process, wherein the matte layer is obtained by adding solid particles such as silicon dioxide into the matte film. In order to obtain a sufficient matte effect, it is generally necessary to add solid particles to a certain extent in particle size, while also requiring a sufficient addition amount. The addition of too much large diameter solid particles can form the cavity in the inside of matte layer in the film stretching process, reduces the density and the intensity of matte layer to lead to the tearing resistance of matte layer in the outside insufficient, easy breakage cracked, moreover because the stretched rete has the hole, appear the plaque for the pigment infiltration easily, the feel of outward appearance will reduce very fast.
Disclosure of Invention
The technical problem to be solved by the present application is to provide a manufacturing device for a single-sided matte polyester film, so as to reduce or avoid the aforementioned problems.
In order to solve the technical problems, the application provides manufacturing equipment for a single-sided matte polyester film, wherein the single-sided matte polyester film comprises a polyester base film, one side surface of the polyester base film is provided with a layer of online coating matte coating, and the outer side of the online coating matte coating is further coated with a layer of offline protective coating; the manufacturing equipment comprises a slice preheating and drying equipment, a double-screw extruder, a longitudinal stretching mechanism, a transverse stretching mechanism, a heat setting mechanism, a cooling mechanism and a first receiving roller; the online coating mechanism for preparing the online coating matte coating is arranged between the double-screw extruder and the longitudinal stretching mechanism; or between the longitudinal stretching mechanism and the transverse stretching mechanism; an offline protective coating mechanism for preparing an offline protective coating is arranged at the downstream of the first receiving roller, and the downstream of the offline protective coating mechanism further comprises an infrared heating device and a second receiving roller for winding the prepared single-sided matte polyester film.
The single-sided matte polyester film prepared by the preparation equipment can achieve the matte effect by online coating of the matte coating, the problem of weakening performance after stretching is avoided, and the cost is lower.
Drawings
The following drawings are only for purposes of illustration and explanation of the present application and are not intended to limit the scope of the present application.
FIG. 1 is a schematic cross-sectional view of a single-sided matte polyester film according to one embodiment of the present application.
Fig. 2 is a schematic cross-sectional view of a single-sided matte polyester film according to another embodiment of the present application.
Fig. 3 is a schematic structural view of a manufacturing apparatus for a single-sided matte polyester film according to an embodiment of the present application.
Fig. 4 is a schematic diagram showing the structure of an off-line protective coating mechanism provided on the basis of fig. 3.
Detailed Description
For a clearer understanding of technical features, objects, and effects of the present application, a specific embodiment of the present application will be described with reference to the accompanying drawings. Wherein like parts are designated by like reference numerals.
Due to the defects of the multilayer co-extrusion matte film in the prior art, the application provides a single-sided matte polyester film and a preparation method thereof. In a specific embodiment of the present application, the single-sided matte polyester film includes a polyester base film 1, and one side surface of the polyester base film 1 is provided with a layer of on-line coating matte coating 2, as shown in fig. 1. In another embodiment of the present application, the single-sided matte polyester film of the present application includes a polyester base film 1, one side surface of the polyester base film 1 has a layer of on-line coating matte coating 2, and an off-line protective coating 3 is coated on the outer side of the on-line coating matte coating 2, as shown in fig. 2.
The matte effect of the single-sided matte polyester film is obtained by online coating of the matte coating in the production process of the polyester base film, the original properties of the polyester base film are kept unchanged, and the situation of weakening of the performance after stretching does not exist. In addition, the online coating is to directly coat chemical substances on the film by using an online coater while the film is stretched, so that the stretching production line of the film is not required to be changed, and compared with a multilayer coextrusion process, the online coating is simpler and has lower cost. The online coating reduces the process of rewinding the film once, and has the advantages of higher operation speed, high efficiency and lower cost. In addition, the finished product can obtain an anti-blocking effect without adding anti-blocking particles into the polyester base film due to the existence of the matte coating.
In addition, in the embodiment shown in fig. 2, in order to improve the durability of the on-line coating matte coating 2, an off-line protective coating 3 may be added on the outer side of the on-line coating matte coating 2 in an off-line coating manner, so that the off-line protective coating 3 not only can provide enough protection, but also can fill the area with uneven thickness caused by stretching of the on-line coating matte coating 2, so that the thickness of the whole finished film layer is kept consistent, the problem of inconsistent matte effect caused by uneven thickness of the film layer is avoided, and the texture and durability of the product can be further improved.
As described above, the components constituting the primer of the in-line coating matte coating layer 2 are not formed by coating the surface of the already prepared polyester film, but are coated during the preparation of the polyester base film 1. That is, the raw materials constituting the polyester base film 1 are melt-extruded to form a base film thickness sheet, and then the mixed primer liquid is coated onto the base film thickness sheet, and then as the base film thickness sheet is stretched to form a film of a desired thickness, the primer liquid component coated on the surface thereof is thinned as it is stretched, and is cured to form the in-line coated matte coating 2 after undergoing mechanical deformation and high-temperature chemical change simultaneously in the stretching process.
Wherein the polyester base film of the present application may be a polyester film formed from one or more selected from polycarboxylic acids containing dibasic acids and their ester-forming derivatives, and one or more selected from polyhydric alcohols containing dibasic alcohols; or polyester films formed from hydroxycarboxylic acids and their ester-forming derivatives; or polyester films formed from cyclic esters. The polyester film can be produced by a conventionally known method. For example, the polyester in the polyester film may be formed by polycondensation of a dibasic acid and a dibasic alcohol. For example, the diacid component thereof includes, but is not limited to, terephthalic acid, isophthalic acid, 2, 6-naphthalenedicarboxylic acid, 3,4 '-diphenylether dicarboxylic acid, hexahydrophthalic acid, 2, 7-naphthalenedicarboxylic acid, phthalic acid, 4' -methylenebisbenzoic acid, oxalic acid, malonic acid, succinic acid, methylsuccinic acid, glutaric acid, adipic acid, 3-methyladipic acid, pimelic acid, suberic acid, azelaic acid, sebacic acid, 1, 11-undecanedicarboxylic acid, 1, 10-decanedicarboxylic acid, undecanedicarboxylic acid, 1, 12-dodecanedicarboxylic acid, hexadecanedicarboxylic acid, behenic acid, tetracosanedioic acid, dimer acid, 1, 4-cyclohexanedicarboxylic acid, 1, 3-cyclohexanedicarboxylic acid, 1-cyclohexanediacetic acid, fumaric acid, maleic acid, and hexahydrophthalic acid. In addition, two or more kinds may be used singly or in combination. For example, glycol components include, but are not limited to, ethylene glycol, 1, 3-propanediol, 1, 4-butanediol, diethylene glycol, 1, 6-hexanediol, 1, 8-octanediol, 1, 10-decanediol, 1, 12-dodecanediol, 1, 14-tetradecanediol, 1, 16-hexadecanediol, dimer diol, diethylene glycol, triethylene glycol, poly (ethyleneether) glycol, poly (butyleneether) glycol, branched diols, hexanediol, or combinations or derivatives thereof, 1, 4-cyclohexanedimethanol, 1, 5-pentanediol, 1, 6-hexanediol, 3-methyl-2, 4-pentanediol, neopentyl glycol, 2-methyl-1, 4-pentanediol, 2, 4-trimethyl-1, 3-pentanediol, 2, 5-ethyl-1, 3-hexanediol, 2-diethyl-1, 3-propanediol, 1, 3-hexanediol. In addition, two or more kinds may be used singly or in combination.
The polyester in the polyester base film of the present application may be formed by hydroxycarboxylic acids and their ester-forming derivatives, or may be formed by cyclic esters. For example, the hydroxycarboxylic acid component therein, including but not limited to: lactic acid, citric acid, malic acid, tartaric acid, glycolic acid, 3-hydroxybutyric acid, p-hydroxybenzoic acid, p- (2-hydroxyethoxy) benzoic acid, 4-hydroxycyclohexane carboxylic acid, and the like. Wherein the ester-forming derivatives of hydroxycarboxylic acids, including, but not limited to: dimethyl terephthalate, dimethyl isophthalate, dimethyl 2, 6-naphthalate, dimethyl 3,4 '-diphenylether dicarboxylate, dimethyl hexahydrophthalate, dimethyl 2, 7-naphthalate, dimethyl phthalate, dimethyl 4,4' -methylenebisbenzoate, dimethyl oxalate, dimethyl malonate, dimethyl succinate, dimethyl glutarate, dimethyl adipate, dimethyl azelate, dimethyl 1, 3-cyclohexanedicarboxylate, and dimethyl 5-sulfoisophthalate. In addition, two or more kinds may be used singly or in combination. For example, cyclic esters include, but are not limited to: epsilon-caprolactone, beta-propiolactone, beta-methyl-beta-propiolactone, delta-valerolactone, glycolide, lactide, and the like. In addition, two or more components may be used singly or in combination.
The polyester in the polyester base film of the present application is preferably polyethylene terephthalate, polybutylene terephthalate, polypropylene terephthalate, 1, 4-cyclohexanedimethanol terephthalate, polyethylene naphthalate, polybutylene naphthalate, polypropylene naphthalate and copolymers thereof, particularly preferably polyethylene terephthalate (PET) and copolymers thereof.
In the polyester base film of the present application, for example, PET is preferably produced by esterification or transesterification of terephthalic acid or dimethyl terephthalate and ethylene glycol, and is industrially produced by a polycondensation method in which the polyester is polycondensed at high temperature under vacuum using a catalyst. In one embodiment, terephthalic acid, ethylene glycol, cyclohexanedimethanol, a catalyst and a heat stabilizer are used as raw materials for esterification; or the raw materials of terephthalic acid, ethylene glycol, isophthalic acid, catalyst and heat stabilizer are esterified. In another specific embodiment, the catalyst is any one of Ti/Si series non-heavy metal catalyst and antimony trioxide, and the addition amount of the catalyst is 0.01-0.09% of the mass of the polyester. In another specific embodiment, the heat stabilizer is a phosphoric acid compound, and the adding amount of the heat stabilizer is 0.0003-0.030% of the mass of the polyester; the phosphoric acid compound comprises any one of phosphoric acid, phosphorous acid, polyphosphoric acid, trimethyl phosphate, triphenyl phosphate and triethyl phosphate. The polyester of another embodiment is prepared as follows: adding 5.0kg of terephthalic acid, 2.2kg of ethylene glycol and 1.10g of germanium dioxide into a 20L general polymerization reaction kettle, carrying out esterification reaction at 230-265 ℃ and 0.2-0.3 Mpa (gauge pressure), decompressing to normal pressure when the water yield reaches 1200ml, adding 1.025g of triethyl phosphate, stirring for 10 minutes at normal pressure, heating to 280 ℃ and decompressing to below 100Pa, extruding, granulating and drying after the reaction is finished for 1-3 hours, and obtaining the polyester chip.
In one embodiment, the polyester base film of the present application may be prepared by the following steps.
For example, polyester chips are used as raw materials, thick sheets are obtained through melt extrusion, after preheating, the thick sheets are longitudinally stretched into stretched sheets, and then the stretched sheets are transversely stretched, shaped, cooled and rolled, so that the polyester base film can be obtained. Of course, since the on-line coating is required in the process of preparing the polyester base film, after the thick sheet is obtained and before the longitudinal stretching, the components of the on-line coating matte coating can be mixed and coated on the thick sheet, and then the single-sided matte polyester film with the on-line coating matte coating can be prepared through the longitudinal stretching and the transverse stretching. Or after longitudinal stretching and before transverse stretching, the components of the online coating matte coating are mixed and then coated on a stretching sheet, and then the single-sided matte polyester film with the online coating matte coating is prepared through transverse stretching. If necessary, a layer of off-line protective coating can be further coated outside the on-line coating matte coating in an off-line coating mode.
In one embodiment, the in-line coating matte coating 2 may be formed from acrylic adhesive, calcium acetate particles, zinc sulfide particles, polydimethylsiloxane, ethyl acrylate, sodium bicarbonate particles by in-line coating curing.
Specifically, the mass ratio of the components of the online coating matte coating 2 is as follows: calcium acetate particles: zinc sulfide particles: polydimethyl siloxane: ethyl acrylate: sodium bicarbonate was 100: (4-8): (5-10): (30-60): (20-40): (3-6). Wherein, the acrylic adhesive can be SAA1451 acrylic adhesive produced by Sanwa chemical Co., ltd. In SiAN, and the solid content is 40-45% by mass. The particle size of the calcium acetate particles, the zinc sulfide particles and the sodium bicarbonate is 100-500 nm.
Example 1
Preheating and drying PET slices at 160-180 ℃, adding the PET slices into a double-screw extruder, adjusting the temperature of the double-screw extruder to 270-280 ℃, melting, filtering, and extruding thick slices. The components of the online coated matte coating of the present application were uniformly mixed and coated onto slabs. And then preheating the thick sheet at 50-90 ℃, entering an infrared heating area at 300-500 ℃, and longitudinally stretching at a linear speed of 40-150 m/min to obtain a stretched sheet, wherein the longitudinal stretching multiplying power is 3.0-4.5. Preheating the stretching sheet at 90-120 ℃, and transversely stretching at 100-160 ℃ with a transverse stretching multiplying power of 3.0-4.5. And then shaping at 160-240 ℃, cooling at 100-50 ℃, shaping, cooling, and finally rolling to obtain the single-sided matte polyester film.
Polyester base film: PET, thickness 20 μm
Coating a matte coating on line: thickness of 1 μm
Example 2
Preheating and drying PETG slices at 160-180 ℃, adding the PETG slices into a double-screw extruder, adjusting the temperature of the double-screw extruder to 270-280 ℃, melting, filtering, and extruding thick slices. Preheating the thick sheet at 50-90 ℃, entering an infrared heating zone at 300-500 ℃, and longitudinally stretching at a linear speed of 40-150 m/min, wherein the longitudinal stretching multiplying power is 3.0-4.5, so as to obtain the stretched sheet. The components of the in-line coated matte coating of the present application were uniformly mixed and coated onto a stretch-panel. Then preheating the stretching sheet at the temperature of 90-120 ℃, and transversely stretching at the temperature of 100-160 ℃ with the transverse stretching multiplying power of 3.0-4.5. And then shaping at 160-240 ℃, cooling at 100-50 ℃, shaping, cooling, and finally rolling to obtain the single-sided matte polyester film.
Polyester base film: PETG with a thickness of 50. Mu.m
Coating a matte coating on line: thickness of 2 μm
The method for producing the single-sided matte polyester film of the present application will be further described with reference to the production apparatus of fig. 3, wherein fig. 3 shows a schematic structural diagram of the production apparatus of the single-sided matte polyester film according to a specific embodiment of the present application.
As shown in the drawing, the manufacturing apparatus of the single-sided matte polyester film of the present application sequentially includes a slice preheating and drying apparatus 100, a twin screw extruder 200, a longitudinal stretching mechanism 300, a transverse stretching mechanism 400, a heat setting mechanism 401, a cooling mechanism 402, and a first receiving roller 500 according to a process flow of film stretching. The in-line coating mechanism 600 is disposed between the twin-screw extruder 200 and the longitudinal stretching mechanism 300; alternatively, as shown by the broken line in the figure, the in-line coating mechanism 600 may be provided between the longitudinal stretching mechanism 300 and the transverse stretching mechanism 400.
The preparation method of the single-sided matte polyester film comprises the following steps.
The polyester chips are metered by an electronic scale and enter chip preheating and drying equipment 100 to be preheated, dried and mixed at 160-180 ℃, then the mixture is added into a double-screw extruder 200, the temperature of the double-screw extruder is adjusted to 270-280 ℃, and after melting, thick chips are extruded through filtration. Preheating the thick sheet at 50-90 ℃, then entering an infrared heating area of a longitudinal stretching mechanism 300, and performing longitudinal stretching by the longitudinal stretching mechanism 300 at the heating temperature of 300-500 ℃ at the linear speed of 40-150 m/min, wherein the longitudinal stretching multiplying power is 3.0-4.5, so as to obtain the stretched sheet. Preheating the stretching sheet at the temperature of 90-120 ℃, then entering a transverse stretching mechanism 400, and transversely stretching the stretching sheet by the transverse stretching mechanism 400 at the temperature of 100-160 ℃, wherein the transverse stretching multiplying power is 3.0-4.5. And then shaping at 160-240 ℃ in a heat shaping mechanism 401, cooling at 100-50 ℃ in a cooling mechanism 402, and finally rolling by a first material receiving roller 500 to obtain the single-sided matte polyester film.
Wherein in-line coating may be performed after extrusion of the slab, before longitudinal stretching. Alternatively, the in-line coating may be performed after the longitudinal stretching and before the transverse stretching. The method comprises the following specific steps: the components of the on-line coating are uniformly mixed into a primer coating liquid, preheated to 80 ℃, and then coated on a thick sheet or a stretched sheet.
Further, in the embodiment shown in fig. 2, a layer of off-line protective coating 3 may be further coated on the outer side of the on-line coated matte coating 2 by off-line coating, so as to protect the on-line coated matte coating 2 by the off-line protective coating 3, and cover the uneven surface of the on-line coated matte coating 2, so as to keep the thickness of the final product consistent.
In one embodiment, the offline protective coating 3 may be composed of 50-60 parts by weight of polymethyl methacrylate, 5-10 parts by weight of dimethyl terephthalate, 10-20 parts by weight of methyltriethoxysilane, 5-10 parts by weight of calcium phosphate particles (particle size 100-500 nm). The components constituting the off-line protective coating 3 can be added into 50-200 parts by weight of diethyl ether and 50-100 parts by weight of deionized water according to the proportion of every 100 parts by weight, uniformly mixed, then coated on the outer side surface of the on-line coated matte coating 2 in an off-line coating mode, and cured for 10-60 seconds at 90-130 ℃ to obtain the off-line protective coating 3.
Thus, the manufacturing apparatus of the present application is further provided with an offline protective coating mechanism 700 for coating and forming an offline protective coating, as shown in fig. 4, on the basis of the manufacturing apparatus shown in fig. 3.
As shown in fig. 4, in the apparatus for manufacturing a single-sided matte polyester film of the present embodiment, an off-line protective coating mechanism 700 provided downstream of the first take-up roll 500 is further included. To cure the offline protective coating, the offline protective coating application mechanism 700 further includes an infrared heating device 701 downstream for infrared radiation curing of the offline protective coating. In addition, the manufacturing apparatus of the present application may further include a second take-up roll 800 for winding up the prepared single-sided matte polyester film, and the single-sided matte polyester film may be packaged for transportation, sales, or the like after being wound into a roll shape by the second take-up roll 800.
Correspondingly, the preparation method of the embodiment further comprises the following steps:
and uniformly mixing all raw material components of the off-line protective coating to obtain the off-line protective coating base coating liquid. The mixed offline protective coating bottom coating liquid is uniformly coated on the surface of the polyester base film, and finally the offline protective coating is formed through heating and curing of infrared heating equipment 701, so that the single-sided matte polyester film is prepared, and finally the single-sided matte polyester film is received and coiled through a second receiving roller 800 for subsequent transportation and sales and the like.
Example 3
Preheating and drying PET slices at 160-180 ℃, adding the PET slices into a double-screw extruder, adjusting the temperature of the double-screw extruder to 270-280 ℃, melting, filtering, and extruding thick slices. The components of the online coated matte coating of the present application were uniformly mixed and coated onto slabs. And then preheating the thick sheet at 50-90 ℃, entering an infrared heating area at 300-500 ℃, and longitudinally stretching at a linear speed of 40-150 m/min to obtain a stretched sheet, wherein the longitudinal stretching multiplying power is 3.0-4.5. Preheating the stretching sheet at 90-120 ℃, and transversely stretching at 100-160 ℃ with a transverse stretching multiplying power of 3.0-4.5. Shaping at 160-240 deg.c, cooling at 100-50 deg.c, shaping, cooling and final winding. The components forming the off-line protective coating are added into 50 parts by weight of diethyl ether and 50 parts by weight of deionized water according to the proportion of each 100 parts by weight, and then the mixture is coated on the outer side surface of the on-line coating matte coating in an off-line coating mode, and the mixture is cured for 30 seconds at the temperature of 90-130 ℃ to prepare the single-sided matte polyester film.
Polyester base film: PET with thickness of 80 μm respectively
Coating a matte coating on line: thickness of 1.5 μm
Offline protective coating: thickness of 2 μm
Example 4
Preheating and drying PETG slices at 160-180 ℃, adding the PETG slices into a double-screw extruder, adjusting the temperature of the double-screw extruder to 270-280 ℃, melting, filtering, and extruding thick slices. Preheating the thick sheet at 50-90 ℃, entering an infrared heating zone at 300-500 ℃, and longitudinally stretching at a linear speed of 40-150 m/min, wherein the longitudinal stretching multiplying power is 3.0-4.5, so as to obtain the stretched sheet. The components of the in-line coated matte coating of the present application were uniformly mixed and coated onto a stretch-panel. Then preheating the stretching sheet at the temperature of 90-120 ℃, and transversely stretching at the temperature of 100-160 ℃ with the transverse stretching multiplying power of 3.0-4.5. Shaping at 160-240 deg.c, cooling at 100-50 deg.c, shaping, cooling and final winding. The components forming the off-line protective coating are added into 200 parts by weight of diethyl ether and 100 parts by weight of deionized water according to the proportion of each 100 parts by weight, and then the mixture is coated on the outer side surface of the on-line coating matte coating in an off-line coating mode, and the mixture is cured for 60 seconds at the temperature of 90-130 ℃ to prepare the single-sided matte polyester film.
Polyester base film: PETG with thickness of 100 μm respectively
Coating a matte coating on line: thickness of 0.5 μm
Offline protective coating: thickness of 3 μm
The raw material components (parts by weight) and the performance parameters of the above examples 1 to 4 are shown in the following table.
The raw material components (parts by weight) and the performance parameters for the comparative examples of the above examples are shown in the following table.
In summary, the matte effect of the single-sided matte polyester film is obtained by online coating of the matte coating in the production process of the polyester base film, the original properties of the polyester base film are kept unchanged, and the situation of weakening of performance after stretching does not exist. In addition, the online coating is to directly coat chemical substances on the film by using an online coater while the film is stretched, so that the stretching production line of the film is not required to be changed, and compared with a multilayer coextrusion process, the online coating is simpler and has lower cost. The online coating reduces the process of rewinding the film once, and has the advantages of higher operation speed, high efficiency and lower cost. In addition, the finished product can obtain an anti-blocking effect without adding anti-blocking particles into the polyester base film due to the existence of the matte coating.
It should be understood by those skilled in the art that although the present application is described in terms of several embodiments, not every embodiment contains only one independent technical solution. The description is given for clearness of understanding only, and those skilled in the art will understand the description as a whole and will recognize that the technical solutions described in the various embodiments may be combined with one another to understand the scope of the present application.
The foregoing is illustrative of the present application and is not to be construed as limiting the scope of the present application. Any equivalent alterations, modifications and combinations thereof will be effected by those skilled in the art without departing from the spirit and principles of this application, and it is intended to be within the scope of this application.

Claims (1)

1. The manufacturing equipment for the single-sided matte polyester film comprises a polyester base film, wherein one side surface of the polyester base film is provided with a layer of online coating matte coating, and the outer side of the online coating matte coating is further coated with a layer of offline protective coating; the manufacturing equipment is characterized by comprising a slice preheating and drying equipment, a double-screw extruder, a longitudinal stretching mechanism, a transverse stretching mechanism, a heat setting mechanism, a cooling mechanism and a first receiving roller; the online coating mechanism for preparing the online coating matte coating is arranged between the double-screw extruder and the longitudinal stretching mechanism; or between the longitudinal stretching mechanism and the transverse stretching mechanism; an offline protective coating mechanism for preparing an offline protective coating is arranged at the downstream of the first receiving roller, and the downstream of the offline protective coating mechanism further comprises an infrared heating device and a second receiving roller for winding the prepared single-sided matte polyester film.
CN202322368111.5U 2023-08-31 2023-08-31 Manufacturing equipment for single-sided matte polyester film Active CN220615015U (en)

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CN202322368111.5U CN220615015U (en) 2023-08-31 2023-08-31 Manufacturing equipment for single-sided matte polyester film

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Application Number Priority Date Filing Date Title
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CN220615015U true CN220615015U (en) 2024-03-19

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