CN112876860A - Biodegradable antistatic graphene in-situ polymerization copolyester cast film and preparation process thereof - Google Patents
Biodegradable antistatic graphene in-situ polymerization copolyester cast film and preparation process thereof Download PDFInfo
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- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
- C08J5/18—Manufacture of films or sheets
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F31/00—Mixers with shaking, oscillating, or vibrating mechanisms
- B01F31/80—Mixing by means of high-frequency vibrations above one kHz, e.g. ultrasonic vibrations
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
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- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G83/00—Macromolecular compounds not provided for in groups C08G2/00 - C08G81/00
- C08G83/001—Macromolecular compounds containing organic and inorganic sequences, e.g. organic polymers grafted onto silica
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- C08J2387/00—Characterised by the use of unspecified macromolecular compounds, obtained otherwise than by polymerisation reactions only involving unsaturated carbon-to-carbon bonds
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- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
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- C08J2467/00—Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers
- C08J2467/04—Polyesters derived from hydroxy carboxylic acids, e.g. lactones
Abstract
The application discloses a biodegradable antistatic graphene in-situ polymerization copolyester cast film and a preparation process thereof, wherein the antistatic graphene in-situ polymerization copolyester cast film comprises the following raw materials in parts by weight: 70-90 parts of graphene in-situ polymerization biodegradable copolyester, 5-20 parts of polylactic acid, 1-10 parts of a filler, 0.1-1 part of an antioxidant, 0.1-1 part of a compatilizer and 0.1-1 part of a lubricant. According to the in-situ polymerization biodegradable copolyester of graphene, a graphene component is introduced in the polymerization process of a biodegradable polyester material, and the multi-layer gridding structure of graphene enables macromolecules of the biodegradable polyester material to be uniformly distributed, so that the molecular weight distribution is narrower, and due to the regularity of the molecular structure, many new properties which are not possessed originally, such as barrier property, antibacterial property, electric conductivity and the like, are expressed.
Description
Technical Field
The application belongs to the field of biodegradable materials, and particularly relates to a biodegradable antistatic graphene in-situ polymerization copolyester cast film and a preparation process thereof.
Background
In recent years, with the development of new industries such as e-commerce, express delivery, take-out and the like, the consumption of plastic lunch boxes, plastic packages and the like is rapidly increased, and new resource environmental pressure is caused. The plastic waste is randomly discarded to cause white pollution, and environmental risks exist when the plastic waste is not treated in a standard way.
The plastic pollution problem of the express logistics industry can be effectively solved by using the biodegradable express packaging, but some functional logistics packaging such as electronic and electrical packaging have no biodegradable material to replace due to the requirements of static prevention and the like in the transportation process.
Disclosure of Invention
In order to solve the problems, the application provides a biodegradable antistatic graphene in-situ polymerization copolyester cast film and a preparation process thereof, wherein the biodegradable antistatic graphene in-situ polymerization copolyester cast film comprises the following raw materials in parts by weight: 70-90 parts of graphene in-situ polymerization biodegradable copolyester, 5-20 parts of polylactic acid, 1-10 parts of a filler, 0.1-1 part of an antioxidant, 0.1-1 part of a compatilizer and 0.1-1 part of a lubricant.
Preferably, the biodegradable cast film articles produced herein have a thickness of between 0.03 and 0.10mm and a width of between 40 and 300 cm.
Preferably, the chemical structural formula of the graphene in-situ polymerization biodegradable copolyester is as follows:
preferably, the graphene in-situ polymerization biodegradable copolyester has the number average molecular weight of 100000-120000, the intrinsic viscosity of 0.6-1.2 dL/g and the acid value of 15-25.
Preferably, the graphene in-situ polymerization biodegradable copolyester is graphene in-situ polymerization PBAT
Preferably, the polylactic acid is one or more of Ingeo 4032D, Ingeo 4043D, Ingeo 4060D manufactured by Natureworks corporation, usa; the filler is one or more of talcum powder, calcium carbonate, titanium dioxide and white carbon black; the antioxidant is one or more of hindered phenol heat stabilizer and phosphite heat stabilizer; the compatilizer is a polyepoxy group compatilizer; the lubricant is one or more of erucamide, oleamide, stearic acid and calcium stearate.
Preferably, the filler has a particle size specification of 5000 mesh to 8000 mesh.
Preferably, the antioxidant is BASF Irganox 1010; the compatilizer is ADR 4370; the lubricant is one of erucamide.
The application also discloses a biodegradable antistatic graphene in-situ polymerization copolyester cast film, which comprises:
s1: uniformly mixing the graphene in-situ polymerization biodegradable copolyester, polylactic acid, a filling material, an antioxidant, a compatilizer and a lubricant, putting the mixture into a double-screw extruder, and carrying out melt blending at 140-180 ℃;
s2: extruding and granulating, and air-cooling and granulating to obtain the special material for the biodegradable cast film;
s3: putting the prepared special material for the biodegradable cast film into a twin-screw casting forming device, and performing cast forming to prepare the biodegradable antistatic graphene in-situ polymerization copolyester cast film;
the preparation method of the graphene in-situ polymerization biodegradable copolyester sequentially comprises the steps of raw material preparation, esterification, polycondensation, chain extension and discharging, wherein the reaction raw materials comprise graphene, two dibasic acids and one dihydric alcohol, and the graphene accounts for 0.1-1 wt% of the copolyester; the dibasic acid is 2 of purified terephthalic acid, adipic acid and succinic acid, the dibasic alcohol is butanediol, and the molar ratio of the alkyd is (1.05-1.15): 1.
preferably, the casting device has a melting section temperature of 150 ℃ and 180 ℃ and a die temperature of 180 ℃ and 220 ℃.
Preferably, the graphene is hydroxyl graphene oxide; the particle size of the hydroxyl graphene oxide is 2-6 microns.
Preferably, in the preparation process of the graphene in-situ polymerization biodegradable copolyester, the reaction raw materials further comprise a reaction auxiliary agent, wherein the reaction auxiliary agent comprises 0.01-0.05 wt% of a catalyst, 0.05-0.2 wt% of an antioxidant, 0.05-0.2 wt% of a stabilizer and 0.05-0.2 wt% of a lubricant;
the catalyst is one or more of titanium catalysts and tin catalysts such as tetrabutyl titanate, stannous zincate and the like;
the antioxidant is a complex of a phosphite antioxidant and a hindered amine antioxidant, and the complex mass ratio is (0.9-1.2): 1;
the stabilizer is hindered phenol stabilizer;
the lubricant is an amide lubricant.
Preferably, the raw material preparation comprises the steps of graphene dispersion, auxiliary agent preparation and pulping, wherein,
the graphene dispersion comprises the steps of adding graphene into dihydric alcohol, and simultaneously performing pre-dispersion treatment by using a high-speed stirrer and an ultrasonic disperser to obtain graphene dispersion liquid, wherein the content of the graphene in the graphene dispersion liquid is 4-8 wt%, the power of the ultrasonic disperser is 10-15 KW, and the dispersion time is 10-40 min;
the preparation method of the auxiliary agent comprises the steps of adding a reaction auxiliary agent into dihydric alcohol, and performing pre-dispersion treatment by using a high-speed stirrer to obtain an auxiliary agent dispersion liquid, wherein the auxiliary agent content in the auxiliary agent dispersion liquid is 5-10 wt%;
the pulping comprises the steps of adding two dibasic acids and one dihydric alcohol in a certain ratio into a pulping kettle, maintaining the temperature of the pulping kettle at 65-75 ℃, enabling the rotating speed of a stirrer to be 100-120 r/min, pulping for 1 hour, adding a graphene dispersion liquid and an auxiliary dispersion liquid, and continuously pulping for 0.5-1 hour.
Preferably, the esterification step further comprises a pre-esterification step before, wherein the pre-esterification step comprises the steps of conveying the mixture slurry in the pulping kettle to a pre-esterification kettle through a screw pump, maintaining the temperature of the pre-esterification kettle at 165-175 ℃, and carrying out pre-esterification reaction for 1 hour;
the esterification comprises the steps of conveying materials in a pre-esterification kettle into a tower plate type continuous esterification reactor through a metering pump, maintaining the temperature of the reactor at 215-225 ℃, enabling the materials to flow downwards along a tower plate in sequence under the action of self gravity, keeping a high dispersion effect of graphene under the dispersion of ultrasonic waves built in the reactor, and enabling the materials to reach a high esterification degree when flowing to the bottom of the reactor by calculating the height and the distance of the tower plate.
The application also discloses a tower plate type continuous esterification reactor, which comprises a reactor body, a material inlet, a material outlet, a gas phase outlet, a tower plate and an ultrasonic dispersion part, wherein the material inlet is arranged at the upper end of the side wall of the reactor body; the material outlet is arranged at the lower end of the reactor body; the gas phase outlet is arranged at the upper end of the reactor body, the tower plate is arranged in the inner cavity of the reactor body, and the cross section of the tower plate is arranged in an inverted V shape; the ultrasonic dispersion part comprises ultrasonic dispersion probes, the ultrasonic dispersion probes are arranged on the inner side wall of the reactor body, the ultrasonic dispersion probes are matched with the tower plate to enable materials entering from the material inlet to fall on the center of the right upper side of the tower plate, and the materials flow downwards along the tower plate and are dispersed under the action of the ultrasonic dispersion probes.
This application can bring following beneficial effect:
1. according to the in-situ polymerization biodegradable copolyester of graphene, a graphene component is introduced in the polymerization process of a biodegradable polyester material, and the multi-layer gridding structure of graphene enables macromolecules of the biodegradable polyester material to be uniformly distributed, so that the molecular weight distribution is narrower, and due to the regularity of the molecular structure, many new properties which are not possessed originally, such as barrier property, antibacterial property, electric conductivity and the like, are expressed.
2. The graphene used in the invention is hydroxyl graphene oxide, and can be grafted to the molecular structure of the biodegradable polyester material through the end group functional group in the polymerization reaction, so that the in-situ polymerization effect is achieved, the reinforcing and toughening effect is achieved, the physical performance of the material is better, and the excellent anti-aging performance is shown.
3. The invention utilizes the chain extension technology of the reactive double-screw extruder to effectively improve the molecular weight of the graphene in-situ polymerized biodegradable copolyester, and simultaneously carries out end-capping treatment on the polyester molecules through chain extension reaction, thereby greatly reducing the number of active functional groups, enabling the material property to be more stable and obviously improving the weather resistance of the material.
4. The preparation method of the biodegradable antistatic graphene in-situ polymerization copolyester cast film provided by the invention has the advantages of simple process and strong operability, can realize production on the existing casting equipment, does not need additional investment, and has higher practical value.
Drawings
The accompanying drawings, which are included to provide a further understanding of the application and are incorporated in and constitute a part of this application, illustrate embodiment(s) of the application and together with the description serve to explain the application and not to limit the application. In the drawings:
FIG. 1 is a schematic diagram of a plate-type continuous esterification reactor according to the present application;
fig. 2 is a schematic structural view of an ultrasonic dispersion probe according to the present application.
Detailed Description
Example 1
The embodiment discloses a tower plate type continuous esterification reactor, which comprises a reactor body 1, a material inlet 2, a material outlet 3, a tower plate 4 and an ultrasonic dispersion part, wherein the material inlet 2 is arranged at the upper end of the side wall of the reactor body 1; the material outlet 3 is arranged at the lower end of the reactor body 1; the gas phase outlet 8 is arranged at the upper end of the reactor body 1, the tower plate 4 is arranged in the inner cavity of the reactor body 1, and the cross section of the tower plate 4 is arranged in an inverted V shape; the ultrasonic dispersion portion comprises ultrasonic dispersion probes 5, the ultrasonic dispersion probes 5 are arranged on the inner side wall of the reactor body 1, the ultrasonic dispersion probes 5 are matched with the tower plate 4 to enable materials entering from the material inlet 2 to fall on the center of the position right above the tower plate 4, and the materials flow downwards along the tower plate 4 and are dispersed under the action of the ultrasonic dispersion probes 5.
It is understood that the ultrasonic dispersion portion further includes an ultrasonic generator 6, and the ultrasonic generator 6 is connected to the ultrasonic dispersion probe 5.
It can be understood that the ultrasonic dispersion probe 5 is uniformly disposed on the inner wall of the reactor body 1.
Still include heat conduction portion 7, heat conduction portion 7 sets up in the periphery of reactor body 1, and heat conduction oil inlet 71 is provided with to heat conduction portion 7 upper end, and heat conduction oil outlet 72 is provided with to heat conduction portion 7 lower extreme.
When the plate-type continuous esterification reactor in this embodiment is used, the material enters from material inlet 2, falls on column plate 4, and the material flows downwards and around along column plate 4, because the setting of ultrasonic dispersion portion, disperses the graphene in the material, effectively avoids the reunion of graphene for graphene keeps sufficient dispersion degree in reaction process always, makes molecular structure more even, and molecular weight distributes more narrowly.
Example 2: a preparation method of graphene in-situ polymerization biodegradable copolyester comprises the following steps:
s1, dispersing graphene: adding graphene into a proper amount of dihydric alcohol, and simultaneously performing pre-dispersion treatment by using a high-speed stirrer and an ultrasonic disperser to obtain a graphene dispersion liquid, wherein the graphene content in the graphene dispersion liquid is 4-8 wt%.
S2, auxiliary agent preparation: adding an auxiliary agent such as a catalyst, an antioxidant, a stabilizer, a lubricant and the like into a proper amount of dihydric alcohol, and performing pre-dispersion treatment by using a high-speed stirrer to obtain an auxiliary agent dispersion liquid, wherein the auxiliary agent content in the auxiliary agent dispersion liquid is 5-10 wt%.
S3, pulping: adding two dibasic acids and one dihydric alcohol in a certain ratio into a pulping kettle, maintaining the temperature of the pulping kettle at 65-75 ℃, rotating the stirrer at 100-120 r/min, pulping for 1 hour, adding the graphene dispersion liquid and the assistant dispersion liquid in the step (a) and the step (b), and continuously pulping for 0.5-1 hour.
S4, pre-esterification: and conveying the mixture slurry in the pulping kettle to the pre-esterification kettle through a screw pump, maintaining the temperature of the pre-esterification kettle at 165-175 ℃, and carrying out esterification reaction for 1 hour.
S5, esterification: the method comprises the steps of conveying materials in a pre-esterification kettle into a tower plate type continuous esterification reactor through a metering pump, maintaining the temperature of the reactor at 215-225 ℃, enabling the materials to flow downwards along a tower plate in sequence under the action of self gravity, keeping a high dispersion effect of graphene under the dispersion of ultrasonic waves built in the reactor, and enabling the materials to reach a high esterification degree when flowing to the bottom of the reactor by calculating the height and the distance of the tower plate.
S6, polycondensation: and (3) stably conveying the esterified substance in the tower plate type reactor to a horizontal polycondensation kettle through a metering pump, maintaining the temperature of the polycondensation kettle at 235-245 ℃, the rotating speed of a stirrer at 20-30 r/min and the pressure at 20-50 Pa, and discharging after the polycondensation reaction is carried out for 3-3.5 hours.
S7, chain extension: uniformly conveying the polycondensation-finished material into a reactive double-screw extruder through a melt pump, setting the temperature of the extruder to be 150-220 ℃, and setting the rotating speed of a screw to be 120-150 r/min; and simultaneously, uniformly feeding the chain extender into the double-screw extruder by using a weightless metering feeder, carrying out chain extension reaction on the materials in the double-screw extruder for about 4-5 min, and further reducing the melt index.
S8, cutting into granules: and (3) feeding the materials in the extruder into a water ring granulating device through a melt filter, granulating, then feeding the materials into a drying device, drying, packaging and warehousing to obtain the graphene in-situ polymerization biodegradable copolyester.
The specific implementation conditions are as follows:
characterization of
In this embodiment, the obtained graphene in-situ polymerization biodegradable copolyester is tested, wherein the testing method is as follows:
1. the biodegradation rate is tested by the following method: GB/T20197-
2. The surface resistance value is measured by the following method: GB/T1410-
3. The antibacterial performance is tested by the following steps: QB/T2591-
4. The water vapor transmission rate is measured by the following method: GB/T1037-
5. The tensile strength is measured by the following method: GB/T1040-2006
6. The elongation at break is measured by the following method: GB/T1040-2006
Table 1 performance test results of graphene in-situ polymerization biodegradable copolyester
From the data in table 1 above, it can be seen that: the in-situ polymerized biodegradable copolyester of graphene obtained by the method has the advantages of biodegradability of more than 95%, good conductivity, strong antibacterial property and high tensile strength.
Compared with example 1, the comparative example 1 shows that the copolyester does not contain graphene, has no antibacterial property, and has reduced tensile strength, poor barrier property and poor conductivity.
Comparative examples 2 to 5 compared with example 1, it can be seen that the in-situ polymerization biodegradable copolyester of graphene prepared by using only 1 kind of dibasic acid or using 3 kinds of dibasic acids has greatly reduced biodegradability, poor barrier property and poor physical properties.
Example 3: a preparation process of a biodegradable antistatic graphene in-situ polymerization copolyester cast film comprises the following steps:
s1: uniformly mixing 70-90 parts of graphene in-situ polymerization biodegradable copolyester obtained in the embodiment 2, 5-20 parts of polylactic acid, 1-10 parts of a filler, 0.1-1 part of an antioxidant, 0.1-1 part of a compatilizer and 0.1-1 part of a lubricant, putting the mixture into a double-screw extruder, and carrying out melt blending at 140-180 ℃;
s2: extruding and granulating, and air-cooling and granulating to obtain the special material for the biodegradable cast film;
s3: and putting the prepared special material for the biodegradable cast film into a twin-screw cast molding device, and carrying out cast molding to prepare the biodegradable antistatic graphene in-situ polymerization copolyester cast film.
The specific implementation conditions are as follows:
characterization of
The biodegradable antistatic graphene in-situ polymerization copolyester cast film obtained in example 3 was tested according to the following method:
tensile strength GB/T1040-
Elongation at break GB/T1040-
Dart impact strength GB/T9639.1-2008
Water vapor transmission rate GB/T1037-
Heat seal Strength QB/T2358-
The surface resistance value is measured by the following method: GB/T1410-
Table 2 performance test results of biodegradable antistatic graphene in-situ polymerization copolyester cast film
From the data analysis in table 2 above, it can be seen that: the antistatic graphene in-situ polymerization copolyester cast film obtained by the method has high tensile strength, high heat sealing strength and high dart impact strength. And compared with the comparative example 1 and the example 1 and compared with the comparative example 2 and the example 2, the influence of the content of the graphene in-situ polymerization biodegradable copolyester in the antistatic graphene in-situ polymerization copolyester casting film on the performance of the film is larger.
The embodiments in the present specification are described in a progressive manner, and the same and similar parts among the embodiments are referred to each other, and each embodiment focuses on the differences from the other embodiments. In particular, for the system embodiment, since it is substantially similar to the method embodiment, the description is simple, and for the relevant points, reference may be made to the partial description of the method embodiment.
The above description is only an example of the present application and is not intended to limit the present application. Various modifications and changes may occur to those skilled in the art. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present application should be included in the scope of the claims of the present application.
Claims (10)
1. A biodegradable antistatic graphene in-situ polymerization copolyester cast film is characterized by comprising the following raw materials in parts by weight: 70-90 parts of graphene in-situ polymerization biodegradable copolyester, 5-20 parts of polylactic acid, 1-10 parts of a filler, 0.1-1 part of an antioxidant, 0.1-1 part of a compatilizer and 0.1-1 part of a lubricant.
2. The biodegradable antistatic graphene in-situ polymerized copolyester cast film according to claim 1, characterized in that: the graphene in-situ polymerization biodegradable copolyester has the following chemical structural formula:
3. the biodegradable antistatic graphene in-situ polymerized copolyester cast film according to claim 1, characterized in that: the graphene in-situ polymerization biodegradable copolyester has the number average molecular weight of 100000-120000, the intrinsic viscosity of 0.6-1.2 dL/g and the acid value of 15-25.
4. The biodegradable antistatic graphene in-situ polymerized copolyester cast film according to claim 1, characterized in that: the polylactic acid is one or more of Ingeo 4032D, Ingeo 4043D, Ingeo 4060D manufactured by Natureworks, USA; the filler is one or more of talcum powder, calcium carbonate, titanium dioxide and white carbon black; the antioxidant is one or more of hindered phenol heat stabilizer and phosphite heat stabilizer; the compatilizer is a polyepoxy group compatilizer; the lubricant is one or more of erucamide, oleamide, stearic acid and calcium stearate.
5. A preparation process of a biodegradable antistatic graphene in-situ polymerization copolyester cast film is characterized by comprising the following steps:
s1: uniformly mixing the graphene in-situ polymerization biodegradable copolyester, polylactic acid, a filling material, an antioxidant, a compatilizer and a lubricant, putting the mixture into a double-screw extruder, and carrying out melt blending at 140-180 ℃;
s2: extruding and granulating, and air-cooling and granulating to obtain the special material for the biodegradable cast film;
s3: putting the prepared special material for the biodegradable cast film into a twin-screw casting forming device, and performing cast forming to prepare the biodegradable antistatic graphene in-situ polymerization copolyester cast film;
the preparation method of the graphene in-situ polymerization biodegradable copolyester sequentially comprises the steps of raw material preparation, esterification, polycondensation, chain extension and discharging, wherein the reaction raw materials comprise graphene, two dibasic acids and one dihydric alcohol, and the graphene accounts for 0.1-1 wt% of the copolyester; the dibasic acid is 2 of purified terephthalic acid, adipic acid and succinic acid, the dibasic alcohol is butanediol, and the molar ratio of the alkyd is (1.05-1.15): 1.
6. the process according to claim 5, characterized in that: the graphene is hydroxyl graphene oxide; the particle size of the hydroxyl graphene oxide is 2-6 microns.
7. The process according to claim 5, characterized in that: in the preparation process of the graphene in-situ polymerization biodegradable copolyester, reaction raw materials further comprise a reaction auxiliary agent, wherein the reaction auxiliary agent comprises 0.01-0.05 wt% of a catalyst, 0.05-0.2 wt% of an antioxidant, 0.05-0.2 wt% of a stabilizer and 0.05-0.2 wt% of a lubricant;
the catalyst is one or more of titanium catalysts and tin catalysts such as tetrabutyl titanate, stannous zincate and the like;
the antioxidant is a complex of a phosphite antioxidant and a hindered amine antioxidant, and the complex mass ratio is (0.9-1.2): 1;
the stabilizer is hindered phenol stabilizer;
the lubricant is an amide lubricant.
8. The process according to claim 5, characterized in that: the preparation of the raw materials comprises the steps of graphene dispersion, auxiliary agent preparation and pulping, wherein,
the graphene dispersion comprises the steps of adding graphene into dihydric alcohol, and simultaneously performing pre-dispersion treatment by using a high-speed stirrer and an ultrasonic disperser to obtain graphene dispersion liquid, wherein the content of the graphene in the graphene dispersion liquid is 4-8 wt%, the power of the ultrasonic disperser is 10-15 KW, and the dispersion time is 10-40 min;
the preparation method of the auxiliary agent comprises the steps of adding a reaction auxiliary agent into dihydric alcohol, and performing pre-dispersion treatment by using a high-speed stirrer to obtain an auxiliary agent dispersion liquid, wherein the auxiliary agent content in the auxiliary agent dispersion liquid is 5-10 wt%;
the pulping comprises the steps of adding two dibasic acids and one dihydric alcohol in a certain ratio into a pulping kettle, maintaining the temperature of the pulping kettle at 65-75 ℃, enabling the rotating speed of a stirrer to be 100-120 r/min, pulping for 1 hour, adding a graphene dispersion liquid and an auxiliary dispersion liquid, and continuously pulping for 0.5-1 hour.
9. The process according to claim 5, characterized in that: the esterification step also comprises a pre-esterification step, wherein the pre-esterification step comprises the step of conveying the mixture slurry in the pulping kettle to a pre-esterification kettle through a screw pump, maintaining the temperature of the pre-esterification kettle at 165-175 ℃, and carrying out pre-esterification reaction for 1 hour;
the esterification comprises the steps of conveying materials in a pre-esterification kettle into a tower plate type continuous esterification reactor through a metering pump, maintaining the temperature of the reactor at 215-225 ℃, enabling the materials to flow downwards along a tower plate in sequence under the action of self gravity, keeping a high dispersion effect of graphene under the dispersion of ultrasonic waves built in the reactor, and enabling the materials to reach a high esterification degree when flowing to the bottom of the reactor by calculating the height and the distance of the tower plate.
10. The process according to claim 9, characterized in that: the plate-type continuous esterification reactor comprises:
the reactor body is provided with a plurality of reaction chambers,
the material inlet is arranged at the upper end of the side wall of the reactor body;
the material outlet is arranged at the lower end of the reactor body;
a gas phase outlet provided at an upper end of the reactor body,
the tower plate is arranged in the inner cavity of the reactor body, and the cross section of the tower plate is arranged in an inverted V shape;
the ultrasonic dispersion part comprises ultrasonic dispersion probes, a plurality of ultrasonic dispersion probes are arranged on the inner side wall of the reactor body, the ultrasonic dispersion probes are matched with the tower plate to enable materials entering from the material inlet to fall on the center of the right upper side of the tower plate, and the materials flow downwards along the tower plate and are dispersed under the action of the ultrasonic dispersion probes.
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| CN115637026A (en) * | 2021-07-19 | 2023-01-24 | 中国石油化工股份有限公司 | Degradable copolyester composition, antistatic biodegradable film material, antistatic biodegradable film and application |
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| US20180043656A1 (en) * | 2017-09-18 | 2018-02-15 | LiSo Plastics, L.L.C. | Oriented Multilayer Porous Film |
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| CN115637026A (en) * | 2021-07-19 | 2023-01-24 | 中国石油化工股份有限公司 | Degradable copolyester composition, antistatic biodegradable film material, antistatic biodegradable film and application |
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