Patent Application
20210395448
The present disclosure relates to the field of film-laminated metal plates for metal packaging of food, and more particularly to a film-laminated steel having a long-lasting high surface tension for food packaging and a method of manufacturing the same.
In the traditional industry of metal packaging containers, a thermosetting coating is usually applied to the surface of a metal material for making a can/lid, and a layer of thermosetting coating film is formed on the surface of the metal material by volatilization of the organic solvent to protect the metal from corrosion by the content. As people are increasingly demanding on living surroundings and food safety, this kind of thermosetting coatings that pollute environment and risk food safety have difficulty in satisfying the increasingly strict requirements of packaging containers.
In recent years, by compounding a biaxially oriented thermoplastic polyester film (BOPET) to the surface of a steel plate by hot melt lamination, the environmental pollution problem caused by the thermosetting coating has been solved effectively, and the risk in food safety caused by the traditional thermosetting coating is eliminated. The emergence of such film-laminated metal materials has innovated food and beverage packaging materials.
The BOPET film itself has excellent properties. However, the PET molecular chain itself is rigid, and the heat setting during the production process renders its crystallinity high. As a result, its melting point is relatively high. Hence, it has high difficulty in bonding to a metal surface. If the problem of the high crystallinity of the BOPET film and its difficulty in bonding to the metal surface can be solved, it will be extremely conducive to reducing the amount of the material to be sprayed on the packaging and reducing the weight, and will help simplify the process of the composite applications of steel plates. In recent years, polyester films modified accordingly (CN 102432984A, US 20170152075A1) have been reported successively in this field. These films may be applied to the field of film-laminated metal materials. The present applicant also reported a polyester film having a long-lasting high surface tension and prepared in a way with no additive (CN 201510044905.3).
When film-laminated steel is used for a food or beverage packaging container, it is necessary to print exquisite patterns, trademarks, words and the like on the surface of the film-laminated steel, film-laminated can/lid by various printing processes. Currently, a printable layer is often introduced to the skin layer of a film by coating to improve the wettability of an ink (CN 106957616A), or the surface tension of a printing substrate is increased by flame treatment (CN 201680033425X) or other methods to improve the wetting and spreading ability of an ink on its surface, thereby improving its printability. As such, downstream users have to add additional investment in surface treatment equipment and related manpower.
In order to solve this technical problem, the present disclosure provides a film-laminated steel, wherein the film-laminated steel is obtained by thermal lamination of a polyester film having a long-lasting high surface tension on a steel plate and has excellent printability. Hence, surface treatments such as flame treatment and corona treatment before printing the film-laminated steel can be dispensed with for downstream users, and the investment of the downstream users in equipment for surface treatment of the film-laminated steel and related manpower can be reduced. The film-laminated steel provided by the present disclosure can be used for metal containers for medium-end to high-end food and beverage packaging, and meet the requirements of containers used for packaging food, beverage, etc.
In order to achieve the above object, the following technical solution is adopted according to the present disclosure.
According to one aspect of the present disclosure, there is provided a polyester film having a long-lasting high surface tension for food packaging, wherein the polyester film is formed by copolymerization of terephthalic acid, isophthalic acid, ethylene glycol and a fourth component, followed by biaxial stretching, wherein a feeding molar ratio is: terephthalic acid:ethylene glycol:isophthalic acid:the fourth component=(135-165):(148-194):(11-15):(0.01-12), wherein the fourth component is at least one selected from the group consisting of 5-sulfonate-isophthalic acid salts, 1,4-cyclohexanedimethanol, neopentyl glycol, and trimellitic acid, wherein 800-2000 ppm, preferably 1000-1500 ppm, more preferably 1200 ppm by mass of SiO2 is added to the polyester film by in-situ polymerization.
In the polyester film having a long-lasting high surface tension for food packaging according to one aspect of the present disclosure, the 5-sulfonate-isophthalic acid salt is sodium 5-sulfonate-isophthalic acid, potassium 5-sulfonate-isophthalic acid or lithium 5-sulfonate-isophthalic acid.
In the polyester film having a long-lasting high surface tension for food packaging according to one aspect of the present disclosure, the polyester film is formed by copolymerization of terephthalic acid, isophthalic acid, ethylene glycol, a 5-sulfonate-isophthalic acid salt, 1,4-cyclohexanedimethanol and neopentyl glycol, followed by biaxial stretching, wherein a feeding molar ratio is terephthalic acid:ethylene glycol:isophthalic acid:5-sulfonate-isophthalic acid salt:1,4-cyclohexanedimethanol:neopentyl glycol=(135-165):(148-194):(11-15):(0.01-5):(0.01-3.5):(0.5-3.5).
In the polyester film having a long-lasting high surface tension for food packaging according to one aspect of the present disclosure, the polyester film has a surface tension≥45 dynes/cm.
In the polyester film having a long-lasting high surface tension for food packaging according to one aspect of the present disclosure, polyester films having different colors are prepared by adding different pigments and fillers.
According to another aspect of the present disclosure, there is provided a film-laminated steel, wherein the film-laminated steel comprises a steel plate and the abovementioned polyester film having a long-lasting high surface tension for food packaging laminated on the steel plate by thermal lamination, wherein the film-laminated steel has excellent printability.
In the film-laminated steel according to another aspect of the present disclosure, the steel plate is selected from the group consisting of a chromium-plated steel plate, a tin-plated steel plate, a low-tin steel plate, a galvanized steel plate, a cold-rolled steel plate, and a stainless steel plate.
According to still another aspect of the present disclosure, there is provided a metal container for medium-end to high-end food or beverage packaging, wherein the metal container is made of the film-laminated steel described above.
According to yet another aspect of the present disclosure, there is provided a method of preparing a polyester film having a long-lasting high surface tension for food packaging, wherein the method comprises the following steps:
Adding terephthalic acid, isophthalic acid, ethylene glycol, and a fourth component into a reactor at a feeding molar ratio of terephthalic acid:ethylene glycol:isophthalic acid:the fourth component=(135-165):(148-194):(11-15):(0.01-12), with the fourth component being at least one selected from the group consisting of 5-sulfonate-isophthalic acid salts, 1,4-cyclohexanedimethanol, neopentyl glycol, and trimellitic acid; adding a catalyst; heating under stirring with N2 as a protective gas to a temperature being controlled at 175-260° C. to allow for copolymerization for a period of time of 1-3 h; releasing a pressure to ambient pressure; then further heating and depressurizing with the temperature in the reactor being increased to 240-310° C., and the pressure being reduced to 50-100Pa to start vacuum polycondensation; continuing the vacuum polycondensation for a period of time of 1.6-2.3 h to obtain a polyester melt; cooling and pelletizing the polyester melt to obtain a chemically modified polyester, wherein 1200 ppm by mass of SiO2 is added to the chemically modified polyester by in-situ polymerization;
Drying the chemically modified polyester obtained in step (1) on a fluidized bed; extruding the dried chemically modified polyester through a twin-screw extruder to obtain a cast sheet; stretching the cast sheet first longitudinally, then transversely to obtain a film; heat setting the film at a temperature of 150-230° C. for a period of time of 6-14 s; and finally cooling and winding the film to obtain a biaxially stretched polyester film.
In the method of preparing a polyester film having a long-lasting high surface tension for food packaging according to yet another aspect of the present disclosure, the catalyst is at least one selected from the group consisting of antimony trioxide, antimony acetate, poly(antimony ethylene glycoxide), and titanates.
In the method of preparing a polyester film having a long-lasting high surface tension for food packaging according to yet another aspect of the present disclosure, the catalyst has a mass fraction of 60-300 ppm, based on an amount of the polyester produced.
In the method of preparing a polyester film having a long-lasting high surface tension for food packaging according to yet another aspect of the present disclosure, in step (2), a temperature of each section of a screw of the twin-screw extruder is 250-270° C.; a die temperature is 270-285° C.; a rotational speed of the screw of the extruder is 45-50 r/min; and the cast sheet has a thickness of 0.15-0.25 mm
In the method of preparing a polyester film having a long-lasting high surface tension for food packaging according to yet another aspect of the present disclosure, in step (2), the cast sheet is first stretched longitudinally at a stretching temperature of 70-80° C. and a stretching ratio of 3-4, and then stretched transversely, before heat setting, at a stretching temperature of 95-105° C. and a stretching ratio of 2.5-3.5.
The present disclosure provides a modified polyester, the monomers of which are terephthalic acid, isophthalic acid, ethylene glycol and a fourth component, wherein the molar ratio of the terephthalic acid, ethylene glycol, isophthalic acid and the fourth component in the modified polyester is A:B:C:D; wherein A is 135-165, preferably 140-160; B is 148-194, preferably 155-194, more preferably 160-192; C is 11-15, preferably 12-15; D is 0.01-12, preferably 3-12; wherein the fourth component is at least one selected from the group consisting of 5-sulfonate-isophthalic acid salts, 1,4-cyclohexanedimethanol, neopentyl glycol and trimellitic acid, and wherein the modified polyester comprises 800-2000 ppm, preferably 1000-1500 ppm, more preferably 1200 ppm by mass of SiO2. Preferably, the SiO2 is added to the modified polyester by in-situ polymerization. The term “added by in-situ polymerization” as used herein refers to mixing SiO2 with the monomers for synthesizing the modified polyester, and then polymerizing to produce the modified polyester according to the present disclosure.
In the present disclosure, the 5-sulfonate-isophthalic acid salt is an alkali metal salt of 5-sulfonate-isophthalic acid, such as sodium 5-sulfonate-isophthalic acid, potassium 5-sulfonate-isophthalic acid or lithium 5-sulfonate-isophthalic acid. One or more 5-sulfonate-isophthalic acid salts may be used. When a 5-sulfonate-isophthalic acid salt is used, its molar ratio value may be in the range of 0.01-5, such as 0.5-5 or 1-4. When 1,4-cyclohexanedimethanol is used, its molar ratio value may be in the range of 0.01-3.5, such as 0.05-3.5 or 0.5-2. When neopentyl glycol is used, its molar ratio value may be in the range of 0.5-3.5, such as 1-3.5. When trimellitic acid is used, its molar ratio value may be in the range of 0.5-5, such as 0.5-4.
In some embodiments, the monomers used to form the modified polyester of the present disclosure are terephthalic acid, ethylene glycol, isophthalic acid, a 5-sulfonate-isophthalic acid salt, 1,4-cyclohexanedimethanol, neopentyl glycol and optional trimellitic acid. In these embodiments, preferably, the molar ratio of these monomers is (135-165):(148-194):(11-15):(0.01-5):(0.01-3.5):(0.5-3.5):(0-5). In preferred embodiments, the molar ratio of these monomers is (135-165):(160-192):(11-15):(0.01-5):(0.01-3.5):(1-3.5):(0-4).
In some preferred embodiments, the modified polyester of the present disclosure is formed by copolymerization of terephthalic acid, isophthalic acid, ethylene glycol, a 5-sulfonate-isophthalic acid salt, 1,4-cyclohexanedimethanol and neopentyl glycol, and 1000-1500 ppm SiO2 is added by in-situ polymerization, wherein the molar ratio of the monomers is terephthalic acid:ethylene glycol:isophthalic acid: 5-sulfonate-isophthalic acid salt:1,4-cyclohexanedimethanol:neopentyl glycol=(135-165):(148-194):(11-15):(0.01-5):(0.01-3.5):(0.5-3.5), preferably (135-165):(160-192):(11-15):(0.01-5):(0.01-3.5):(1-3.5).
The preparation of the modified polyester of the present disclosure comprises feeding the raw materials described herein into the reactor according to the feeding molar ratio of terephthalic acid:ethylene glycol:isophthalic acid:the fourth component=(135-165) : (148-194):(11-15):(0.01-12), and allowing them to react in the presence of a catalyst under the protection of an inert gas such as nitrogen. At the time of feeding, 800-2000 ppm by mass of SiO2 is added at the same time, wherein SiO2 is added to the modified polyester of the present disclosure by in-situ polymerization. The reaction temperature may be in the range of 175-260° C., and the copolymerization time may be controlled in the range of 1-3 hours. Subsequently, the pressure in the reactor is released to ambient pressure, and then the temperature is further increased and the pressure is further reduced. Particularly, the temperature in the reactor is increased to 240-310° C., and the pressure is reduced to 50-120 Pa, so as to start vacuum polycondensation. The vacuum polycondensation time may be controlled in the range of 1.6-2.3 hours to obtain a polyester melt which is then cooled to obtain the chemically modified polyester of the present disclosure. The modified polyester may be pelletized. In some embodiments, the method further comprises a drying step, such as drying on a fluidized bed for 3-6 hours, wherein the drying temperature may be 120-160° C.
Preferably, the copolymerization temperature may be controlled in the range of 175-200° C., and the copolymerization time may be controlled in the range of 1.2-2.2 hours. At the beginning of the copolymerization reaction, the pressure in the reactor may be controlled in the range of 0.08-0.2 MPa, preferably in the range of 0.05-0.12 MPa. In the vacuum polycondensation reaction, the reaction temperature may be controlled in the range of 260-300° C., preferably in the range of 265-285° C.; the reaction time may be controlled in the range of 1.6-2.0 hours; and the pressure may be controlled in the range of from 80 to 120 Pa, preferably to about 100 Pa.
In the present disclosure, the catalyst may be at least one selected from the group consisting of antimony-based catalysts and titanate-based catalysts. The antimony-based catalysts include, but are not limited to, antimony trioxide, antimony acetate, and poly(antimony ethylene glycoxide). The titanate catalysts include, but are not limited to, tetrabutyl titanate, isopropyl titanate, tetramethyl titanate, tetraethyl titanate, and tetrapropyl titanate. Any one or more of these catalysts may be used. Generally, based on the mass of the modified polyester produced, the catalyst is added in an amount of 60-300 ppm by mass, such as 60-280 ppm. The antimony-based catalyst is usually added in an amount of 80-280 ppm by mass, such as 80-280 ppm; and the titanate-based catalyst is usually added in an amount of 200-280 ppm by mass, such as 200-260 ppm. When these two types of catalysts are added together, the total amount added is usually in the range of 60-300 ppm by mass.
The modified polyester of the present disclosure may be used to prepare a polyester film having a long-lasting high surface tension for food packaging. Preferably, the surface tension of the polyester film is ≥45 dynes/cm.
Therefore, in some embodiments of the present disclosure, there is provided a polyester film which is prepared from the modified polyester according to any embodiment of the present disclosure. In some embodiments, the surface tension of the polyester film is ≥45 dynes/cm.
The polyester film of the present disclosure may be prepared as follows: the modified polyester of the present disclosure is extruded into a cast sheet through a twin-screw extruder, then biaxially stretched, and finally heat set and cooled to obtain the polyester film of the present disclosure. Preferably, the temperature of each section of the extruder screw is 250-270° C.; the die temperature is 270-285° C.; the rotational speed of the extruder screw is 45-50 r/min; and the thickness of the cast sheet is 0.15-0.25 mm. In the biaxial stretching, preferably, the cast sheet is first stretched longitudinally at a stretching temperature of 70-80° C. and a stretching ratio of 3-4, and then stretched transversely at a stretching temperature of 95-105° C. and a stretching ratio of 2.5-3.5. In the heat setting, preferably, the heat setting temperature is 150-230° C., and the time is 6-14 s.
Polyester films in different colors may be prepared by adding different pigments and fillers.
The modified polyester or polyester film of the present disclosure may be used to prepare a film-laminated steel. Therefore, the present disclosure provides a film-laminated steel comprising a steel plate and the modified polyester or polyester film according to any embodiment of the present disclosure. The polyester film of the present disclosure can be laminated on the steel plate by thermal lamination. The film-laminated steel of the present disclosure has excellent printability. In the present disclosure, the steel plate in the film-laminated steel may be selected from the group consisting of a chromium-plated steel plate, a tin-plated steel plate, a low-tin steel plate (having a tin coating weight of ≤1.1 g/m2), a galvanized steel plate, a cold-rolled steel plate, and a stainless steel plate.
The film-laminated steel of the present disclosure can be used to prepare metal containers for medium-end to high-end food and beverage packaging. Therefore, the present disclosure also provides a metal container which is made of the film-laminated steel of the present disclosure.
Compared with the prior art, the present disclosure shows the following beneficial technical effects:
The present disclosure provides a film-laminated steel having excellent printability and a method of preparing the same. The film-laminated steel is prepared by direct thermal lamination of a polyester film having a long-lasting high surface tension on a steel plate. The polyester film is prepared by a biaxial stretching process with common polyethylene terephthalate (PET) as a master batch which is modified by designed chemical modification of molecular chains and an embedding means. The mechanism of action is to introduce a new functional group to destroy the rigid structure of common polyethylene terephthalate to reduce its crystallinity, so that direct thermal laminatability can be obtained. At the same time, hydrophilic and alkali-soluble groups are introduced to greatly increase the surface tension of the polyester film (≥45 dynes/cm), thereby providing long-lasting constancy. The film-laminated steel can guarantee a long-lasting high surface tension with no need of surface treatment, and the wetting and spreading ability of an ink on the surface of the film-laminated steel can be improved greatly. Good ink printability can be achieved without surface treatment such as flame treatment and corona treatment.
The film-laminated steel of the present disclosure has balanced characteristics of no high temperature deformation, good barrier property, good corrosion resistance, no pollution to contents, no blocking, etc., and can be widely used for various beverage and food packaging containers. At the same time, the film-laminated steel of the present disclosure may have excellent printability without surface treatment such as corona or flame treatment.
Due to the addition of SiO2 to the polymer by in-situ polymerization, the crystallization properties of the polyester film are improved uniformly on the whole. By substituting the traditional way of adding SiO2 in the form of master batch, addition of a high melting point resin to the film is avoided. The above two points have improved the overall performance of the polyester film significantly, and the complex processing endurance and corrosion resistance of the film-laminated steel comprising the film of the present disclosure have been improved notably.
Due to the addition of 800-2000 ppm by mass of SiO2 by in-situ polymerization, the polyester film and the film-laminated steel of the present disclosure have the following three characteristics at the same time: the polyester film has an attribute of high-level food safety, endurance in deep drawing processing and complex deformation processing, and excellent corrosion resistance, widely useful in the medium-end to high-end metal packaging industry.
In the following detailed description, the objectives, features, and advantages of the present disclosure will become clearer and more apparent with reference to the non-limiting examples. The content is sufficient to enable those skilled in the art to appreciate and implement the present disclosure.
Preparation of a modified polyester: The experiment was carried out in a 10 L reactor. Terephthalic acid, isophthalic acid, and ethylene glycol were added to the reactor according to the molar ratio of terephthalic acid:ethylene glycol:isophthalic acid=135:160:12, and then a catalyst, 1,4-cyclohexanedimethanol, neopentyl glycol and dimethyl isophthalate-5-sodium sulfonate were added. The catalyst was antimony trioxide (300 ppm by mass). The molar ratio value of 1,4-cyclohexanedimethanol was 3.5; the molar ratio value of neopentyl glycol was 1; and the molar ratio value of dimethyl isophthalate-5-sodium sulfonate was 0.01. N2 was used as a protective gas, and stirring and heating were conducted under a gas pressure of 0.1 MPa. The temperature was controlled at 185° C. After about two hours when water produced by esterification became less significantly, the pressure was released to ambient pressure to complete the esterification reaction. Next, heating and depressurization were performed. The temperature in the reactor was raised to 280° C., and the pressure was reduced to 100 Pa to start vacuum polycondensation. The polycondensation continued for 1.8 hours to provide a polyester melt. The polyester melt was cooled in a water tank and pelletized to provide a chemically modified polyester. 1200 ppm by mass of SiO2 was added to the modified polyester by in-situ polymerization.
Preparation of a modified polyester film: The master batch thus obtained was dried on a fluidized bed at a drying temperature of 120-160° C. for 4 hours, and extruded through a twin-screw extruder to obtain a cast sheet. The temperature of each section of the extruder screw was 250-270° C., the die temperature was 270-285° C., the rotational speed of the extruder screw was 45-50 r/min, and the thickness of the cast sheet was 0.15-0.25 mm The cast sheet was first stretched longitudinally at a stretching temperature of 70-80° C. and a stretching ratio of 3-4; then stretched transversely at a stretching temperature of 95-105° C. and a stretching ratio of 2.5-3.5; and subsequently heat set at a heat setting temperature of 150-230° C. for 6-14 s to obtain a film. Finally, the film was cooled, wound, and slit for use.
Preparation of a film-laminated steel: the polyester film prepared by the biaxial stretching process was thermally bonded to the surface of a 0.10-0.50 mm thin steel plate at a pressure of 2-10 kg and a temperature of 180-260° C. to obtain a film-laminated steel.
Preparation of a modified polyester: The experiment was carried out in a 10 L reactor. Terephthalic acid, isophthalic acid, and ethylene glycol were added to the reactor at a molar ratio of terephthalic acid:ethylene glycol:isophthalic acid=150:180:14, and then a catalyst and sodium 5-sulfonate-isophthalic acid were added. The catalyst was a mixture of antimony trioxide (40 ppm by mass) and a titanate (tetrabutyl titanate, 260 ppm by mass). The molar ratio value of sodium 5-sulfonate-isophthalic acid was 3.8. Replacement with N2 was performed, and heating under stirring at a gas pressure of 0.1 MPa was conducted. The temperature was controlled at 175° C. After about 1.5 h when water produced by esterification became less significantly, the pressure was released to ambient pressure to complete the esterification reaction. Next, heating and depressurization were performed. The temperature in the reactor was raised to 280° C., and the pressure was reduced to 100 Pa to start vacuum polycondensation. The polycondensation continued for 1.8 hours to provide a polyester melt. The polyester melt was cooled in a water tank and pelletized to provide a chemically modified polyester. 1200 ppm by mass of SiO2 was added to the modified polyester by in-situ polymerization.
The preparation method of the modified polyester film and the preparation method of the film-laminated steel are the same as in Application Example 1.
Preparation of a modified polyester: The experiment was carried out in a 10 L reactor. Terephthalic acid, isophthalic acid, and ethylene glycol were added to the reactor at a molar ratio of terephthalic acid: ethylene glycol: isophthalic acid=158:168:15, and then a catalyst, trimellitic acid and sodium 5-sulfonate-isophthalic acid were added. The catalyst was a mixture of antimony trioxide (40 ppm by mass) and a titanate (isopropyl titanate, 200 ppm by mass). The molar ratio value of trimellitic acid was 0.5, and the molar ratio value of sodium 5-sulfonate-isophthalic acid was 2. Replacement with N2 was performed, and heating under stirring at a gas pressure of 0.1 MPa was conducted. The temperature was controlled at 175° C. After about 1.4 h when water produced by esterification became less significantly, the pressure was released to ambient pressure to complete the esterification reaction. Next, heating and depressurization were performed. The temperature in the reactor was raised to 270° C., and the pressure was reduced to 100 Pa to start vacuum polycondensation. The polycondensation continued for 1.8 hours to provide a polyester melt. The polyester melt was cooled in a water tank and pelletized to provide a chemically modified polyester. 1200 ppm by mass of SiO2 was added to the modified polyester by in-situ polymerization.
The preparation method of the modified polyester film and the preparation method of the film-laminated steel are the same as in Application Example 1.
Preparation of a modified polyester: The experiment was carried out in a 10 L reactor. Terephthalic acid, isophthalic acid, and ethylene glycol were added to the reactor according to the molar ratio of terephthalic acid:ethylene glycol:isophthalic acid=165:192:11, and then a catalyst, 1,4-cyclohexanedimethanol, neopentyl glycol, trimellitic acid and potassium 5-sulfonate-isophthalic acid were added. The catalyst was antimony acetate (180 ppm by mass). The molar ratio value of 1,4-cyclohexanedimethanol was 1; the molar ratio value of neopentyl glycol was 2.5; the molar ratio value of trimellitic acid was 0.5; and the molar ratio value of potassium 5-sulfonate-isophthalic acid was 1. N2 was used as a protective gas, and stirring and heating were conducted under a gas pressure of 0.1 MPa. The temperature was controlled at 185° C. After about two hours when water produced by esterification became less significantly, the pressure was released to ambient pressure to complete the esterification reaction. Next, heating and depressurization were performed. The temperature in the reactor was raised to 280° C., and the pressure was reduced to 100 Pa to start vacuum polycondensation. The polycondensation continued for 1.8 hours to provide a polyester melt. The polyester melt was cooled in a water tank and pelletized to provide a chemically modified polyester. 1200 ppm by mass of SiO2 was added to the modified polyester by in-situ polymerization.
The preparation method of the modified polyester film and the preparation method of the film-laminated steel are the same as in Application Example 1.
Preparation of a modified polyester: The experiment was carried out in a 10 L reactor. Terephthalic acid, isophthalic acid, and ethylene glycol were added to the reactor according to the molar ratio of terephthalic acid:ethylene glycol:isophthalic acid=140:190:13, and then a catalyst, 1,4-cyclohexanedimethanol, neopentyl glycol, trimellitic acid and sodium 5-sulfonate-isophthalic acid were added. The catalyst was a mixture of antimony trioxide (40 ppm by mass) and a titanate (tetramethyl titanate, 60 ppm by mass). The molar ratio value of 1,4-cyclohexanedimethanol was 0.01; the molar ratio value of neopentyl glycol was 3.5; the molar ratio value of trimellitic acid was 2.8; and the molar ratio value of sodium 5-sulfonate-isophthalic acid was 0.2. N2 was used as a protective gas, and stirring and heating were conducted under a gas pressure of 0.1 MPa. The temperature was controlled at 185° C. After about two hours when water produced by esterification became less significantly, the pressure was released to ambient pressure to complete the esterification reaction. Next, heating and depressurization were performed. The temperature in the reactor was raised to 280° C., and the pressure was reduced to 100 Pa to start vacuum polycondensation. The polycondensation continued for 1.8 hours to provide a polyester melt. The polyester melt was cooled in a water tank and pelletized to provide a chemically modified polyester. 1200 ppm by mass of SiO2 was added to the modified polyester by in-situ polymerization.
The preparation method of the modified polyester film and the preparation method of the film-laminated steel are the same as in Application Example 1.
Preparation of a modified polyester: The experiment was carried out in a 10 L reactor. Terephthalic acid, isophthalic acid, and ethylene glycol were added to the reactor according to the molar ratio of terephthalic acid:ethylene glycol:isophthalic acid=150:180:12, and then a catalyst, 1,4-cyclohexanedimethanol, neopentyl glycol and sodium 5-sulfonate-isophthalic acid were added. The catalyst was a titanate (tetraethyl titanate, 60 ppm by mass). The molar ratio value of 1,4-cyclohexanedimethanol was 3; the molar ratio value of neopentyl glycol was 1.5; and the molar ratio value of sodium 5-sulfonate-isophthalic acid was 0.5. N2 was used as a protective gas, and stirring and heating were conducted under a gas pressure of 0.1 MPa. The temperature was controlled at 185° C. After about two hours when water produced by esterification became less significantly, the pressure was released to ambient pressure to complete the esterification reaction. Next, heating and depressurization were performed. The temperature in the reactor was raised to 280° C., and the pressure was reduced to 100 Pa to start vacuum polycondensation. The polycondensation continued for 1.8 hours to provide a polyester melt. The polyester melt was cooled in a water tank and pelletized to provide a chemically modified polyester. 1200 ppm by mass of SiO2 was added to the modified polyester by in-situ polymerization.
The preparation method of the modified polyester film and the preparation method of the film-laminated steel are the same as in Application Example 1.
Preparation of a modified polyester: The experiment was carried out in a 10 L reactor. Terephthalic acid, isophthalic acid, and ethylene glycol were added to the reactor according to the molar ratio of terephthalic acid:ethylene glycol:isophthalic acid=155:175:13, and then a catalyst, 1,4-cyclohexanedimethanol, neopentyl glycol and sodium 5-sulfonate-isophthalic acid were added. The catalyst was antimony acetate (300 ppm by mass). The molar ratio value of 1,4-cyclohexanedimethanol was 0.05; the molar ratio value of neopentyl glycol was 3.5; and the molar ratio value of sodium 5-sulfonate-isophthalic acid was 3.5. N2 was used as a protective gas, and stirring and heating were conducted under a gas pressure of 0.1 MPa. The temperature was controlled at 185° C. After about two hours when water produced by esterification became less significantly, the pressure was released to ambient pressure to complete the esterification reaction. Next, heating and depressurization were performed. The temperature in the reactor was raised to 280° C., and the pressure was reduced to 100 Pa to start vacuum polycondensation. The polycondensation continued for 1.8 hours to provide a polyester melt. The polyester melt was cooled in a water tank and pelletized to provide a chemically modified polyester. 1200 ppm by mass of SiO2 was added to the modified polyester by in-situ polymerization.
The preparation method of the modified polyester film and the preparation method of the film-laminated steel are the same as in Application Example 1.
Preparation of a modified polyester: The experiment was carried out in a 10 L reactor. Terephthalic acid, isophthalic acid, and ethylene glycol were added to the reactor according to the molar ratio of terephthalic acid:ethylene glycol:isophthalic acid=135:182:15, and then a catalyst, 1,4-cyclohexanedimethanol, neopentyl glycol and sodium 5-sulfonate-isophthalic acid were added. The catalyst was a titanate (tetrabutyl titanate, 200 ppm by mass). The molar ratio value of 1,4-cyclohexanedimethanol was 0.01; the molar ratio value of neopentyl glycol was 0.5; and the molar ratio value of sodium 5-sulfonate-isophthalic acid was 5. N2 was used as a protective gas, and stirring and heating were conducted under a gas pressure of 0.1 MPa. The temperature was controlled at 185° C. After about two hours when water produced by esterification became less significantly, the pressure was released to ambient pressure to complete the esterification reaction. Next, heating and depressurization were performed. The temperature in the reactor was raised to 280° C., and the pressure was reduced to 100 Pa to start vacuum polycondensation. The polycondensation continued for 1.8 hours to provide a polyester melt. The polyester melt was cooled in a water tank and pelletized to provide a chemically modified polyester. 1200 ppm by mass of SiO2 was added to the modified polyester by in-situ polymerization.
The preparation method of the modified polyester film and the preparation method of the film-laminated steel are the same as in Application Example 1.
Preparation of a modified polyester: The experiment was carried out in a 10 L reactor. Terephthalic acid, isophthalic acid, and ethylene glycol were added to the reactor according to the molar ratio of terephthalic acid:ethylene glycol:isophthalic acid=148:180:15, and then a catalyst, 1,4-cyclohexanedimethanol, neopentyl glycol and sodium 5-sulfonate-isophthalic acid were added. The catalyst was antimony trioxide (60 ppm by mass). The molar ratio value of 1,4-cyclohexanedimethanol was 2; the molar ratio value of neopentyl glycol was 2; and the molar ratio value of sodium 5-sulfonate-isophthalic acid was 1. N2 was used as a protective gas, and stirring and heating were conducted under a gas pressure of 0.1 MPa. The temperature was controlled at 185° C. After about two hours when water produced by esterification became less significantly, the pressure was released to ambient pressure to complete the esterification reaction. Next, heating and depressurization were performed. The temperature in the reactor was raised to 280° C., and the pressure was reduced to 100 Pa to start vacuum polycondensation. The polycondensation continued for 1.8 hours to provide a polyester melt. The polyester melt was cooled in a water tank and pelletized to provide a chemically modified polyester. 1200 ppm by mass of SiO2 was added to the modified polyester by in-situ polymerization.
The preparation method of the modified polyester film and the preparation method of the film-laminated steel are the same as in Application Example 1.
Preparation of a modified polyester: The experiment was carried out in a 10 L reactor. Terephthalic acid, isophthalic acid, and ethylene glycol were added to the reactor according to the molar ratio of terephthalic acid:ethylene glycol:isophthalic acid=150:188:12, and then a catalyst, 1,4-cyclohexanedimethanol, neopentyl glycol, trimellitic acid and potassium 5-sulfonate-isophthalic acid were added. The catalyst was poly(antimony ethylene glycoxide) (180 ppm by mass). The molar ratio value of 1,4-cyclohexanedimethanol was 2; the molar ratio value of neopentyl glycol was 2; the molar ratio value of trimellitic acid was 4; and the molar ratio value of potassium 5-sulfonate-isophthalic acid was 0.1. N2 was used as a protective gas, and stirring and heating were conducted under a gas pressure of 0.1 MPa. The temperature was controlled at 185° C. After about two hours when water produced by esterification became less significantly, the pressure was released to ambient pressure to complete the esterification reaction. Next, heating and depressurization were performed. The temperature in the reactor was raised to 280° C., and the pressure was reduced to 100 Pa to start vacuum polycondensation. The polycondensation continued for 1.8 hours to provide a polyester melt. The polyester melt was cooled in a water tank and pelletized to provide a chemically modified polyester. 1200 ppm by mass of SiO2 was added to the modified polyester by in-situ polymerization.
The preparation method of the modified polyester film and the preparation method of the film-laminated steel are the same as in Application Example 1.
A modified polyester was prepared with reference to the method of Example 1, except that 800 ppm by mass of SiO2 was added. A modified polyester film and a film-laminated steel were prepared from the modified polyester prepared in Example 11 as described in Example 1.
A modified polyester was prepared with reference to the method of Example 2, except that 2000 ppm by mass of SiO2 was added. A modified polyester film and a film-laminated steel were prepared from the modified polyester prepared in Example 12 as described in Example 1.
The film-laminated steels prepared in Examples 1-12 were subjected to a surface tension test.
The standard applied in the surface tension test is: JISK-6763-71. The specific method is as follows: a series of mixed solutions having various surface tension values were formulated. Subsequently, a clean cotton swab was dipped into a mixed solution, and then the cotton swab was used to wipe a surface of a film-laminated steel to form a 6 cm2 liquid membrane. If the liquid membrane didn't break for more than 2 s, it indicates that the surface tension of the film-laminated steel was greater than that of the mixed solution used. Then, a solution having a higher surface tension was used to continue the test. On the contrary, if the liquid membrane broke, it indicates that the surface tension of the film-laminated steel was less than that of the mixed solution. Then, a mixed solution having a lower surface tension was tried. Such a trial was continued until a critical condition was reached. If a preceding mixed solution having a specific level of surface tension could spread, but a succeeding mixed solution having a higher level of surface tension could not, then the surface tension of the preceding mixed solution was the surface tension of the film-laminated steel.
A bulk modification method was applied to the film for preparing the film-laminated steel according to the present disclosure. In the design of the molecular chain, a fourth component capable of maintaining a long-lasting surface tension was added, so the surface tension of the resulting film-laminated steel didn't degrade as the storage time was prolonged. The surface tension test was performed on Examples 1-12, and the test results were all between 45-52 dynes/cm.
Finally, it should be pointed out that although the present disclosure has been described with reference to the specific examples, those skilled in the art should appreciate that the above examples are only used to illustrate the present disclosure, and are not used to limit the present disclosure. Various equivalent changes or substitutions can be made without departing from the concept of the present disclosure. Therefore, without departing from the essential spirit of the present disclosure, all changes and variations of the abovementioned examples will fall in the scope of the claims in the present disclosure.
| Number | Date | Country | Kind |
|---|---|---|---|
| 201811090601.0 | Sep 2018 | CN | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/CN2019/106617 | 9/19/2019 | WO | 00 |
