WO2018000552A1 - Method for fabricating greenhouse film - Google Patents

Method for fabricating greenhouse film Download PDF

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Publication number
WO2018000552A1
WO2018000552A1 PCT/CN2016/095911 CN2016095911W WO2018000552A1 WO 2018000552 A1 WO2018000552 A1 WO 2018000552A1 CN 2016095911 W CN2016095911 W CN 2016095911W WO 2018000552 A1 WO2018000552 A1 WO 2018000552A1
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WO
WIPO (PCT)
Prior art keywords
plastic
film
heating
plastic film
laminating
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Application number
PCT/CN2016/095911
Other languages
French (fr)
Chinese (zh)
Inventor
梅未
甘汉南
Original Assignee
伯恩太阳能科技有限公司
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Filing date
Publication date
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Publication of WO2018000552A1 publication Critical patent/WO2018000552A1/en

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    • AHUMAN NECESSITIES
    • A01AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01GHORTICULTURE; CULTIVATION OF VEGETABLES, FLOWERS, RICE, FRUIT, VINES, HOPS OR SEAWEED; FORESTRY; WATERING
    • A01G9/00Cultivation in receptacles, forcing-frames or greenhouses; Edging for beds, lawn or the like
    • A01G9/14Greenhouses
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C65/00Joining or sealing of preformed parts, e.g. welding of plastics materials; Apparatus therefor
    • B29C65/02Joining or sealing of preformed parts, e.g. welding of plastics materials; Apparatus therefor by heating, with or without pressure
    • B29C65/022Particular heating or welding methods not otherwise provided for
    • AHUMAN NECESSITIES
    • A01AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01GHORTICULTURE; CULTIVATION OF VEGETABLES, FLOWERS, RICE, FRUIT, VINES, HOPS OR SEAWEED; FORESTRY; WATERING
    • A01G9/00Cultivation in receptacles, forcing-frames or greenhouses; Edging for beds, lawn or the like
    • A01G9/14Greenhouses
    • A01G9/1438Covering materials therefor; Materials for protective coverings used for soil and plants, e.g. films, canopies, tunnels or cloches
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C65/00Joining or sealing of preformed parts, e.g. welding of plastics materials; Apparatus therefor
    • B29C65/02Joining or sealing of preformed parts, e.g. welding of plastics materials; Apparatus therefor by heating, with or without pressure
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C66/00General aspects of processes or apparatus for joining preformed parts
    • B29C66/40General aspects of joining substantially flat articles, e.g. plates, sheets or web-like materials; Making flat seams in tubular or hollow articles; Joining single elements to substantially flat surfaces
    • B29C66/41Joining substantially flat articles ; Making flat seams in tubular or hollow articles
    • B29C66/45Joining of substantially the whole surface of the articles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B37/00Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding
    • B32B37/06Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding characterised by the heating method
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B37/00Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding
    • B32B37/08Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding characterised by the cooling method
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/25Greenhouse technology, e.g. cooling systems therefor

Definitions

  • the invention relates to a method for manufacturing a greenhouse film, and belongs to the technical field of agricultural materials.
  • the overall performance of the greenhouse film is generally improved by providing a plurality of cable films on the greenhouse film, so that it can be used not only by repeated pulling but also by the greenhouse film.
  • the use area is larger.
  • a Chinese patent application (Publication No.: CN104855178A) discloses a method for heat sealing a cable film, which comprises disposing the bottom plastic film on a working surface; then placing a cable on the bottom plastic film, and then pulling the cable
  • the surface is covered with a plastic film on the surface, and the surface plastic film or the surface plastic film and the bottom plastic film are heated simultaneously on both sides of the cable, and the surface plastic film and the bottom plastic film are pressed, so that the surface plastic film and the bottom plastic film are in the cable.
  • the two sides are in close contact, combined with heat and pressure, and after cooling, they are formed into a unitary structure.
  • the method reinforces the tensile properties of the plastic film to some extent by laminating a plurality of mutually parallel cables on the plastic film, however, since it is only by using two layers of plastic film, the cable is tight. Wrapped, the cable is slidable, pulling the cable At the same time, the plastic film cannot be driven at the same time. If the film of the greenhouse is partially wrinkled or uneven during use, the plastic film itself needs to be pulled to remove the wrinkles or uneven parts. Therefore, the problem of poor pull resistance still exists; Since the overall area of the film is relatively large, it is difficult to convey or pull during the manufacturing process, and the use of the multilayer film makes the processing process more complicated, and the requirements for the setting are correspondingly improved, which is not conducive to practical operation and the like.
  • the present invention is directed to the defects existing in the prior art, and provides a method for fabricating a greenhouse film, which solves the problem of how to simplify the operation and improve the bonding force between the lamination tape and the film and the tear resistance of the film.
  • the object of the present invention is achieved by the following technical solution, a method for manufacturing a greenhouse film, the method comprising the following steps:
  • the plurality of plastic laminating strips and the plastic film are sequentially moved synchronously toward each process under the action of the traction force, the plurality of plastic laminating strips are arranged in parallel, and the plastic laminating strips are flat, so that each strip
  • the plastic laminating tape is thermally composited with the plastic film through a thermal lamination process, and the heating temperature of each plastic laminating tape side is 220 ° C to 240 ° C; the heating temperature of each plastic film side is 160 ° C to 190 °C, so that each plastic laminating tape is thermally combined with the plastic film, and then moved to the next process, so that after cooling, the corresponding greenhouse film is obtained.
  • each plastic laminating tape is directly combined with the plastic film.
  • the overall tensile strength of the plastic film can be effectively improved. Since the plastic laminating tape is relatively fixed to the plastic film, the portion of the plastic laminating tape can be directly pulled during use. To achieve the effect of straightening or flattening the plastic film, there is no damage to the plastic film due to excessive pulling force; at the same time, since the plastic laminating tape is directly laminated on the plastic film, only a single layer of plastic is needed.
  • the film can be used, which greatly simplifies the production process and makes the operation process simpler, since only a single layer is used. Thin also reduces costs to a certain extent.
  • the present invention is directly integrated into one body, since the plastic film is relatively thin and the plastic film tape is relatively thick, if the same heat sealing temperature is used, if the temperature is too high, the plastic film is easily melted during the heat sealing process, and the temperature is high. Too low is likely to cause poor composite effect. Therefore, the inventors have found through research that by using different heating temperatures on both sides of the plastic laminating tape and the plastic film, the heating temperature on the plastic laminating tape side is relatively higher than the heating temperature on the plastic film side, and heating is performed separately. Therefore, the better thermal combination of the two is integrated into one, achieving the effect of high composite strength, achieving a simplified process while ensuring the strength of the product and the yield of the product.
  • the heating temperature on each plastic laminating tape side is heated by a long heating block, and the elongated heating block is attached to each plastic laminating tape.
  • the surface of the plastic film is heated by a cylindrical heating roller or a long heating block, and the cylindrical heating roller or the elongated heating block is attached to the plastic film.
  • a heating surface of the elongated heating block is adjacent to a heating surface of the cylindrical heating roller or the elongated heating block, and each plastic laminating tape is thermally integrated with the plastic film. .
  • the plastic laminating tape can be preheated by heating in advance when entering the long heating block, so that The plastic laminating tape can better soften the state; on the other hand, by using a cylindrical heating roller, the plastic film can be heated relative to the line contact, and at the same time, combined with low-temperature heating, the two can be better.
  • the thermal composite is integrated, and the thermal heating is performed by directly bringing the long heating block into contact with the cylindrical heating roller. By using a cylindrical heating roller, the heating roller can be more effectively rolled.
  • the thermal lamination of the plastic laminating tape and the plastic film can be carried out in the next process, which can also ensure the bonding force of the two after heat sealing.
  • the strip is used.
  • the heating block is heated to achieve a better composite effect.
  • the strip-shaped heating block is attached to the heating surface of each of the plastic lamination belts to have the same width as the corresponding plastic lamination belt.
  • the heating block can be used to heat the plastic laminating tape more effectively, and the heated area of the plastic laminating tape is more uniformly heated, which is advantageous for better bonding with each contact point of the plastic film; meanwhile, due to plastic pressure
  • the heating temperature of the strip-shaped heating pressure on the side of the film strip is relatively high, and by adjusting the size thereof, it is possible to better protect the surrounding plastic film from being damaged.
  • the elongated heating block has a length of 15 cm to 20 cm.
  • the length of the long heating block on the side of the plastic film tape side and the plastic film side may be 15 cm to 20 cm. It can make the heating block heat the plastic laminating tape better, so that it has sufficient preheating time, so that the effect of thermocompression is better.
  • each of the plastic lamination tapes and the plastic film passes between a long heating block and a cylindrical heating roller or a long heating block,
  • Each of the plastic laminating tape and the plastic film are moved in the vertical direction under the action of traction. Since the plastic laminating tape and the plastic film itself have a certain weight, and the present invention is completed by separately heating the plastic laminating tape and the plastic film on both sides, if it is operated in the horizontal direction,
  • the self-gravity action makes it easy for the plastic laminating tape and the plastic film to be pressed down on the heating block or the heating roller below.
  • the underlying material is easily heated to cause melting or damage; on the other hand, the film is added.
  • the friction between the whole and the heating member below may easily cause the film to break during the pulling process, and after the vertical direction is moved, the above problems can be well solved, and the two can be well integrated. Guarantee the quality of the product.
  • each of the plastic laminating tapes and the plastic film simultaneously move at a pulling speed of 10 m/sec to 15 m/sec.
  • the reason that the two in the heating process is more reasonable in the heating part can make the effect of the heat compounding, and at the same time, can also make the plastic film tape and the plastic film have a certain tension. Tightening exists, which can make the heat-sealing between the two smoother, without wrinkles and other phenomena, so that the bonding force of the pressing is better, and it is more favorable for the rapid progress of the pipeline.
  • the plastic laminating tape is prepared by the following method:
  • the twisted polyester thread is subjected to a molten thermoplastic resin, and the twisted polyester thread is combined with the molten thermoplastic resin, and the thermoplastic resin formed by curing the twisted polyester fiber in a molten state is cured.
  • a flat plastic film strip is formed, and the plastic laminating strip is cooled to obtain a corresponding finished plastic laminating strip. Since the twisted polyester thread has a certain spiral state, it is equivalent to making the surface of the polyester thread have a certain roughness, rather than a smooth state, so that the thermoplastic resin coated on the outer layer is in contact with the twisted polyester thread.
  • the surface is formed in a state equivalent to the inlay, which increases the bonding force between the polyester thread and the thermoplastic resin, so that the sliding phenomenon is less likely to occur; at the same time, the heat is softened by first heating the twisted polyester thread for the purpose of
  • the polyester resin is better combined with the molten thermoplastic resin, which is equivalent to a state in which the surface between the two is partially inlaid or staggered, and a synergistic effect can be formed by using a twisted polyester thread.
  • the bonding force between the twisted polyester thread and the thermoplastic resin can be improved, and the bonding force between the polyester thread and the thermoplastic resin coated on the outer layer can be improved as a whole, so that it can be used. It will not fall off during the process.
  • the overall strength property of the laminating tape is improved, and the product is less likely to be broken, thereby improving the composite with the plastic film.
  • the overall strength properties of the film due to the presence of the twisted polyester thread, after thermal compounding with the plastic film, the bonding force between the plastic film and the plastic laminating tape is also increased to some extent, and the bonding fastness performance is improved.
  • the temperature of the heat treatment in the step A in the preparation of the plastic film tape is from 140 ° C to 170 ° C.
  • the polyester wire can be softened at a high temperature to improve the bonding force with the thermoplastic resin, and at least the polyester wire is melted to ensure the strength property, thereby ensuring the overall strength performance of the film.
  • the twisted polyester thread is in a tension state during the heat treatment in the step A. Since the twisted polyester thread is more or less loose during the production process, the filaments are fluffed or fluffed.
  • the polyester yarn can be subjected to a certain reforming process to make the filament Re-stretching, so as to effectively remove the defects of the wool or fluffing, so that the twisting line compounded in the thermoplastic resin and each wire in the twisting line are in a better tension state, effectively ensuring the coated polyester thread
  • the bonding force effect with the thermoplastic resin improves the overall strength properties of the plastic film by increasing the strength of the plastic laminating tape.
  • the molten resin in the molten state in the step B in the preparation of the pressure-coated film tape contains silica gel, and the percentage of the mass of the thermoplastic resin in the molten state is 30% by weight. 40wt%.
  • silica gel the percentage of the mass of the thermoplastic resin in the molten state is 30% by weight. 40wt%.
  • the silica gel accounts for 33% by weight to 35% by weight based on the mass of the thermoplastic resin in a molten state.
  • the molten thermoplastic resin in step B is mainly made up of the following mass percentage components:
  • Polypropylene 30% by weight to 40% by weight
  • Polyethylene 30% by weight to 40% by weight
  • Silica gel 30% by weight to 40% by weight. It can not only improve the bonding force with the polyester thread, but also ensure the good flexibility of the laminating tape. It has better compatibility with the plastic film, and is more beneficial to the plastic laminating tape and the plastic film. Between The combination of fastness.
  • the present invention has the following advantages over the prior art:
  • the plastic laminating tape is directly combined with the plastic film, and the heating temperature of the plastic laminating tape side is much higher than the heating temperature of the plastic film side.
  • the thermal fusion of the two materials with uneven thickness is integrated to improve the strength of the plastic film.
  • the plastic laminating tape is directly laminated on the plastic film, it is only required to pass through the film when pulling or flattening the film. Pulling the plastic laminating tape can achieve the pulling or finishing of the whole film, and the strength of the plastic laminating tape is relatively higher than that of the plastic film, so that the corresponding strength is improved; However, the operation process and the cost reduction effect are greatly simplified.
  • the plastic laminating tape By heating the plastic laminating tape with a long heating block, the plastic laminating tape can be preheated to a better softening state, which is a good solution for the laminating tape.
  • the problem is that the thickness is thick and the heat is uneven or the softening effect cannot be achieved.
  • the plastic film is heated by the cylindrical heating roller which is heated at a low temperature, so that the high bonding force after heat sealing is well realized.
  • the laminating strip can be effectively heated to make the heating uniformity good, thereby
  • the plastic laminating tape has a better softening state, and there is no defect that local heating is caused to cause softening, thereby achieving the bonding fastness with the plastic film, and there is no problem that the partial heat cannot be integrated into one body, as a whole. Improves the bonding fastness between the plastic laminate and the plastic film.
  • the overall strength performance of the laminating tape can be improved, and the phenomenon of cracking and the like is less likely to occur, thereby improving the overall film composited with the plastic film.
  • Strength performance At the same time, due to the presence of the twisted polyester thread, after thermal compounding with the plastic film, the bonding force between the plastic film and the plastic laminating tape is also increased to some extent, and the bonding fastness performance is improved.
  • Figure 1 is a schematic perspective view of the greenhouse film.
  • FIG. 2 is a schematic enlarged perspective view of a plastic laminating tape in the greenhouse film.
  • Fig. 3 is a schematic enlarged perspective view showing the surface of the plastic laminating tape in the greenhouse film partially turned up.
  • Fig. 4 is a schematic enlarged view showing the twisted polyester thread in the plastic lamination belt.
  • plastic laminating tape 11 thermoplastic resin layer; 12, twisted polyester thread, 2, plastic film.
  • the size of the greenhouse film mentioned in the following embodiments can be adjusted according to actual needs, and there is no specific limitation.
  • the number of the heat-sealing plastic laminating strips 1 on the greenhouse film can also be adjusted according to actual needs.
  • the interval between the plastic film strips 1 adjacent to each other on the plastic film 2 is about 6 meters, which can improve the overall strength of the film of the greenhouse, and the plastic film strip 1 on the plastic film 2 can be adjusted according to actual needs.
  • Each of the pieces is thermally composited in turn; of course, it is also possible to use a plurality of plastic laminating strips 1 to perform thermal recombination simultaneously.
  • the greenhouse film comprises a plurality of plastic laminating tapes 1 and a plastic film 2, wherein a plurality of plastic lamination tapes 1 are thermally laminated on the same side of the plastic film 1 , of course,
  • the plastic laminating tape 1 is disposed on both sides of the plastic film 2.
  • the interval between the two adjacent plastic lamination tapes 1 is 1 m, and the interval can be appropriately adjusted according to the strength requirement.
  • plastic laminating strips 1 can be synchronously thermally composited on the plastic film 2, and of course, according to the width of the plastic film 2 4, 5, 8, 10, or even more plastic laminating strips 1 are simultaneously thermally laminated on the plastic film 2, wherein the plastic lamination film
  • the end of the belt 1 may be flush with the edge of the plastic film 2 in the width direction, or the end of the plastic lamination belt 1 may be slightly longer than the edge of the width direction of the plastic film 2, which is advantageous for pulling.
  • the plastic laminating tape 1 includes a twisted polyester thread 12 and a thermoplastic resin layer 11, and the twisted polyester thread 12 is coated in the thermoplastic resin layer 11 by thermal compounding, wherein The polyester threads are arranged in parallel along the length of the plastic laminating strip 1.
  • the plastic laminating tape 1 is flat, and the length can be selected and adjusted according to the needs of the actual plastic film. It is preferable to provide 6-8 twisted polyester threads 12 in the plastic laminating tape for the thermoplastic resin layer.
  • the transparency of 1 can be adjusted according to the materials selected.
  • the twisted polyester thread 12 can also be replaced by other twisted polyester fiber strands, such as twisted nylon thread.
  • the plastic film 2 made of a PE material is not limited to the material.
  • the plastic film 2 can be made of other plastic film 2 made of a PP material or the like.
  • the corresponding plastic laminating tape 1 of the corresponding number of rolls is placed at the unwinding start for unwinding; likewise, the wound PE plastic film 2 is wound.
  • Corresponding placement is performed at the beginning of the unwinding; the plastic laminating tape 1 and the PE plastic film 2 are sequentially moved to the next process by a traction mechanism disposed on the subsequent process, wherein the traction mechanism is preferably placed in the heat
  • the compounding process the thermal lamination process of the plastic laminating tape 1 and the PE plastic film 2 and the cooling treatment process; no matter how many plastic laminating tapes are thermally composited on the PE plastic film 2, each of the production lines can be sequentially
  • the root is subjected to a complete process and then subjected to the next process; a plurality of plastic film tapes 1 can also be simultaneously subjected to simultaneous thermal composite treatment.
  • the thermal composite is performed synchronously, and the plastic film 2 is heated at intervals of 1 meter.
  • a plastic laminating tape 1 is composited, and 7 plastic laminating tapes 1 are thermally composited, and the width of the plastic film 2 is 6 meters, and the length can be adjusted as needed to make the plastic pressure
  • the film tape 1 is thermally composited with a plastic film tape 1 at intervals of 1 meter in the width direction of the plastic film 2.
  • each plastic laminating tape 1 and PE plastic film 2 can be manually guided to the traction mechanism, and then the traction force of each plastic laminating tape 1 and PE plastic film 2 in the traction mechanism can be made.
  • the synchronous movement is sequentially performed to each process, and a plurality of guiding mechanisms can be set for guiding in the middle, and each plastic laminating tape 1 and the PE plastic film 2 that are synchronously moved are subjected to thermal composite processing through thermal compounding, and thermal compounding is performed.
  • each plastic laminating strip 1 side is 240 ° C; the heating temperature of the PE plastic film 2 side is 190 ° C, and the thermocompression is directly performed while heating, so that each plastic laminating strip 1 is After being thermally integrated with the PE plastic film 2, after pulling and moving through the traction mechanism in the next process, each plastic laminating tape 1 and the PE plastic film 2 are simultaneously thermally integrated into one body, and after air cooling through the next process.
  • the winding is performed to obtain a corresponding greenhouse film, wherein the traction after the traction mechanism can be pulled by the power of the winding mechanism.
  • the corresponding plastic laminating tape 1 of the corresponding number of rolls is placed at the unwinding start for unwinding; likewise, the wound PE plastic film 2 is wound.
  • Corresponding placement is performed at the beginning of unwinding; unwinding is carried out by each of the plastic laminating tape 1 and the PE plastic film 2, which are arranged in the subsequent process, wherein the traction mechanism is preferably set.
  • each plastic laminating tape 1 and the PE plastic film 2 are simultaneously thermally composited.
  • the width of the plastic film 2 is 6 meters, the length can be adjusted as needed, so that the plastic laminating tape 1 is thermally composited at intervals of the width of the plastic film 2 with five plastic laminating strips 1, wherein the width of the plastic film 2 The two edges of the direction are each thermally combined with a plastic laminating strip 2.
  • each plastic laminating tape 1 and PE plastic film 2 can be manually guided to the traction mechanism, and then continuous production can be achieved. Then, each plastic laminating tape 1 and PE plastic film 2 are sequentially moved synchronously to each process under the traction force of the traction mechanism, so that the synchronous moving speed is 10 m/s (equivalent to the traction speed).
  • a plurality of conventional guiding mechanisms can be set for guiding, and each plastic laminating strip 1 and the PE plastic film 2 that are synchronously moved are first subjected to thermal lamination processing through a thermal lamination process, and each plastic laminating tape is subjected to thermal composite processing.
  • the heating temperature on the 1 side is 220 ° C.
  • the heating process is performed by heating the strip-shaped heating block, and the long heating block is attached to the outer surface of each plastic laminating strip 1; at the same time, the PE plastic film 2 is made.
  • the heating temperature of the side is 160 ° C, and heating is performed by a cylindrical heating roller during heating, the heating roller can be rolled, and the cylindrical heating roller is attached to the outer surface of the PE plastic film 2, preferably the position of the heating roller.
  • each plastic lamination tape 1 can be combined with the PE plastic film 2
  • the thermal compression is performed while being heated, wherein each of the plastic laminating tape 1 and the PE plastic film 2 are moved between the elongated heating block and the cylindrical heating roller under the traction force, so that each strip
  • the plastic laminating tape 1 and the PE plastic film 2 are both moved in the vertical direction, and the two can enter the thermal recombination process from above by the action of the traction force, and then the thermal composite process is performed from below; Under the action of traction force, the thermal composite process is entered from below, and then the thermal composite process is performed from above, so that each plastic laminating tape 1 is thermally composited with the PE plastic film 2, and then moved to the traction mechanism through the next process.
  • each plastic laminating tape 1 and the PE plastic film 2 are thermally composited into one body, and then air-cooled through the next process, and then wound up to obtain a corresponding greenhouse film, wherein the traction after the traction mechanism can be retracted.
  • the power of the mechanism is towing.
  • the corresponding plastic laminating tape 1 of the corresponding number of rolls is placed at the unwinding start for unwinding; likewise, the wound PE plastic film 2 is wound.
  • Corresponding placement is performed at the beginning of the unwinding; unwinding of each plastic laminating tape 1 and PE plastic is carried out by a traction mechanism disposed on the subsequent process The film 2 is sequentially moved to each process.
  • the traction mechanism between the thermal lamination process (the thermal lamination process of each plastic lamination tape 1 and the PE plastic film 2) and the cooling treatment process;
  • Each plastic laminating strip 1 and PE plastic film 2 are simultaneously thermally composited, and the width of the plastic film 2 is 6 meters, and the length can be adjusted as needed, so that the plastic laminating strips 1 are equally spaced along the width direction of the plastic film 2.
  • the thermal composite has eight plastic laminating strips 1, wherein the plastic film strip 2 is thermally composited at both edges in the width direction. Simultaneously carried out by hot-bonding 8 plastic laminating press belts;
  • each plastic laminating tape 1 and PE plastic film 2 can be manually guided to the traction mechanism, and then the continuous production process can be achieved, and then each plastic lamination tape can be 1 and PE plastic film 2 under the action of the traction mechanism of the traction mechanism to move synchronously to each process, so that the synchronous moving speed is 10m / s (equivalent to the traction speed), a plurality of conventional guiding mechanisms can be set in the middle to guide, first Each of the plastic laminating tape 1 and the PE plastic film 2 that are synchronously moved are subjected to a thermal lamination process through a thermal lamination process, and the heating temperature of each plastic laminating tape 1 side is 230° C., and the heating process is long.
  • the strip-shaped heating block is heated, and a long heating block is attached to the outer surface of each of the plastic laminating strips 1, and a long heating block is attached to the heating of each of the plastic laminating strips 1.
  • the width of the surface is the same as the width of each plastic laminating strip 1 and the length of the elongated heating block is 15 cm; at the same time, the heating temperature of the side of the PE plastic film 2 is 180 ° C, and the heating is performed in a cylindrical manner during heating.
  • the heating roller can roll, and the cylindrical heating roller is attached to the outer surface of the PE plastic film 2, and the position of the heating roller is located in the middle portion of the elongated heating block; wherein, the strip-shaped portion The heating surface of the heating block is close to the heating surface of the cylindrical heating roller, and each plastic laminating tape 1 and the PE plastic film 2 can be directly thermo-compressed while being heated, wherein each plastic laminating tape 1
  • each of the plastic laminating tape 1 and the PE plastic film 2 are moved in the vertical direction, By making the two in traction Under the action, it enters the thermal compounding process from above, and then heats the composite process from below.
  • each plastic laminating strip 1 and the PE plastic film 2 are thermally composited, and air-cooled through the next process. After that, the winding is performed to obtain a corresponding greenhouse film, wherein the traction after the traction mechanism can be pulled by the power of the winding mechanism.
  • the corresponding plastic laminating tape 1 of the corresponding number of rolls is placed at the unwinding start for unwinding; likewise, the wound PE plastic film 2 is correspondingly The placing is performed at the beginning of the unwinding to unwind; the plastic laminating tape 1 and the PE plastic film 2 are sequentially moved to each process by a pulling mechanism disposed on the subsequent process, wherein the traction mechanism is preferably disposed at The thermal compounding process (the thermal lamination process of each plastic laminating tape 1 and the PE plastic film 2) and the cooling treatment process; in this embodiment, each plastic laminating tape 1 and the PE plastic film 2 are simultaneously thermally composited.
  • the width of the plastic film 2 is 6 meters, and the length can be adjusted as needed, so that the plastic laminating tape 1 is thermally composited along the width direction of the plastic film 2 with three plastic laminating tapes 1, wherein the width of the plastic film 2 is made.
  • the two sides of the direction are thermally composited with a plastic laminating strip 2, which is synchronously carried out by thermally laminating three plastic laminating press belts.
  • each plastic laminating tape 1 and PE plastic film 2 can be manually guided to the traction mechanism, and then the continuous production process can be achieved, and then each plastic lamination tape is Under the action of the traction force of the traction mechanism, the PE plastic film 2 is sequentially moved synchronously to each process, so that the synchronous moving speed is 15 m/s (corresponding to the traction speed), and a plurality of conventional guiding mechanisms can be set for guiding in the middle.
  • Each of the plastic laminating tape 1 and the PE plastic film 2 which are synchronously moved are subjected to a thermal lamination process through a thermal lamination process, and the heating temperature of each plastic laminating tape 1 side is 220° C., and the heating process adopts a long strip shape.
  • the width of the film strip is the same and the length of the long heating block is 20 cm; at the same time, the heating temperature of the PE plastic film 2 side is 170 ° C, and the PE plastic film 2 side is also heated by a long heating block during heating.
  • the width of the heating surface of the elongated heating block attached to the side of the plastic film 1 is the same as the width of the plastic laminating tape 2
  • the length of the elongated heating block is 20 cm, and the position of the elongated heating block is located in the middle of the longitudinal direction of the relatively long heating block; wherein the two elongated heating blocks are The heating surfaces are oppositely arranged and close to each other, so that each plastic laminating strip 1 and the PE plastic film 2 can be directly thermo-compressed while being heated, wherein each plastic laminating strip 1 and the PE plastic film 2 are in traction.
  • each plastic laminating tape 1 and the PE plastic film 2 are moved in the vertical direction, and the two can enter the thermal recombination process from above by the traction force, and then move out of the thermal composite from below.
  • the two may enter the thermal recombination process from the bottom under the action of the traction force, and then remove the thermal recombination process from above, so that each plastic lamination tape 1 and the PE plastic film 2 are thermally composited together, and then After the next process is pulled and moved through the traction mechanism, each plastic laminating tape 1 is thermally composited with the PE plastic film 2, and then air-cooled after the next process, and the corresponding greenhouse film is obtained.
  • the traction after the traction mechanism can be pulled by the power of the winding mechanism.
  • the polyester monofilament used in this embodiment can be processed by a conventional method: if the high-viscosity molten polyester raw material is selected first, and then after being metered, the conventional method of spinning, cooling, oiling, stretching and heat setting is adopted. After the process, it is further processed by winding to obtain the corresponding high-strength industrial polyester yarn product.
  • the processing method of the corresponding polyester yarn in the Chinese patent can be processed by other conventional methods, and will not be described herein.
  • the width of the plastic lamination tape 1 in this embodiment can be adjusted according to actual needs. However, for better explanation, the width of the plastic lamination tape 1 in the following embodiments is 1.2 cm, but is not limited to the width range.
  • the polyester yarn is twisted, that is, a plurality of polyester monofilaments are firstly twisted to form a single twisted polyester thread having a specification of 1100 dtex/192f; and then, six single twisted polyester threads are again subjected to twisting treatment.
  • the correspondingly wound twisted polyester thread 12 of the corresponding number of rolls is placed at the beginning of unwinding for unwinding, and at the same time by setting in the successor
  • the traction mechanism in the process drives the twisted polyester thread 12 to move forward, wherein the traction mechanism is disposed between the coating process (the twisting process of the twisted polyester thread 12 and the thermoplastic compound) and the cooling process, and the plastic film is selected in the embodiment.
  • the belt 1 is covered with 8 twisted polyester threads 12 arranged in parallel;
  • the eight twisted polyester threads 12 which are parallel and on the same plane are moved forward by the traction force of the above-mentioned traction mechanism, and a plurality of guiding mechanisms can be provided in the middle of the movement as needed, and then
  • the twisted polyester yarn 12 which is synchronously moved is moved to the heating zone to heat the twisted polyester thread 12, so that the heating temperature when the twisted polyester thread 12 enters the heating zone is 140 ° C, and the twisted polyester thread 12 is removed from the heating zone.
  • the heating temperature is 170 ° C, and the twisted polyester thread 12 is in a tension state when it passes through the heating zone, so that it is in a softened state;
  • the thermoplastic resin raw material can be first placed in the hopper of the twin-screw extruder, and then extruded and melted, and the temperature of the conveying section of the twin-screw extruder is set to 160 ° C to 170 ° C in turn; The temperature is 185 ° C ⁇ 195 ° C; the temperature of the mixing section is 200 ° C ⁇ 220 ° C and the temperature of the homogenization section is 225 ° C ⁇ 235 ° C, at the same time, the head temperature of the twin-screw extruder is set to 245 ° C ⁇ 255 °C, a molten thermoplastic resin is obtained, so that the molten thermoplastic resin is placed in the die of the twin-screw extruder; the processing of the thermoplastic resin in the molten state is in the overall processing line Can be continuously and continuously;
  • the heated polyester resin 12 in the softened state after the heat treatment is passed through the molten thermoplastic resin at the die in the twin-screw extruder to adjust the viscosity of the molten thermoplastic resin to 0.75 dL/g to 0.95 dL.
  • the twisted polyester thread 12 is compounded with the thermoplastic resin, and then moved away from the corresponding outlet at the die as the twisted polyester thread moves forward, wherein the shape of the outlet can be in the shape of the laminating strip
  • the twisted polyester thread 12 is coated in the thermoplastic resin layer 11 formed by curing the molten thermoplastic resin, and a flat plastic lamination tape 1 is formed, and the thickness of the plastic lamination tape 1 is substantially larger than The diameter of the polyester fiber 12 can be twisted.
  • the plastic film tape 1 semi-finished product passes through the traction mechanism, the plastic film tape 1 semi-finished product is first moved through the hot water at a temperature of 40 ° C to 60 ° C for pre-cooling treatment, and then It is cooled by water at normal temperature, and then heat-set by hot air at a temperature of 40 ° C to 60 ° C to remove moisture from the surface, and the movement after the traction mechanism can pass through the winder. Rolling forces on the drive belt that the film is moved forward semifinished product to give the corresponding finished plastic film tape 1. The breaking strength of the obtained plastic laminated tape 1 was 34.5 MPa.
  • thermoplastic resin raw material is made of the following mass percentage components: polypropylene: 30 wt%; polyethylene 40% by weight; silica gel: 30% by weight. After the test, the breaking strength of the plastic laminated tape obtained in the present example was 34.4 MPa.
  • thermoplastic resin raw material is made of the following mass percentage components: polypropylene: 35 wt%; polyethylene : 30 wt%; silica gel: 35 wt%. After the test, the breaking strength of the plastic laminated tape obtained in the present example was 34.00 MPa.
  • thermoplastic resin raw material is made of the following mass percentage components: polypropylene: 30 wt%; polyethylene : 30 wt%; silica gel: 40 wt%. After the test, the breaking strength of the plastic laminated tape obtained in the present example was 34.6 MPa.
  • the polyester yarn is twisted, that is, a plurality of polyester monofilaments are firstly twisted to form a single twisted polyester thread having a specification of 1100 dtex/192f; the twist of the single twisted polyester thread can be 45 degrees per meter; Then, six single twisted polyester threads are again subjected to twisting treatment to form a composite twisted polyester thread 12, which is formed by winding, and the composite twisted polyester thread 12 has a specification of 6000D, so that the twist of the polyester thread is increased. 45 degrees per meter; spare;
  • the correspondingly wound twisted polyester thread 12 of the corresponding number of rolls is placed at the beginning of unwinding for unwinding, and at the same time by setting in the successor
  • the traction mechanism in the process drives the twisted polyester thread 12 to move forward, wherein the traction mechanism is disposed between the coating process (the twisting process of the twisted polyester thread 12 and the thermoplastic compound) and the cooling process, and the plastic film is selected in the embodiment.
  • the belt 1 is covered with 8 twisted polyester threads 12 arranged in parallel along the length of the lamination belt;
  • the eight twisted polyester threads 12 which are parallel and in the same plane are moved forward by the traction force of the above-mentioned traction mechanism, so that the moving speed of the twisted polyester thread 12 is 15 m/s (that is, equivalent to traction Speed), in the process of moving, a plurality of guiding mechanisms can be provided in the middle according to the need, which is beneficial to keep the twisted polyester thread 12 in a relatively tight state, and then move the twisted polyester thread 12 which is synchronously moved to the heating section.
  • the twisted polyester thread 12 is heat treated so that the heating temperature when the twisted polyester thread 12 enters the heating zone is 140 ° C, and the heating temperature when the twisted polyester thread 12 is removed from the heating zone is 170 ° C, the inlet in the heating zone It can also be set between the exit and the exit.
  • the heating temperature is 150 ° C, so that the twisted polyester thread 12 is gradually heated during the heating interval, which is beneficial to more uniform heating, and can effectively remove the phenomenon of hair or burrs, and at the same time, the twisted polyester thread 12 is heated.
  • a tensioning mechanism can be provided to cause the twisted polyester thread 12 to be tensioned by the tensioning mechanism to be in a softened state;
  • the thermoplastic resin raw material can be first placed in the hopper of the twin-screw extruder, and then extruded and melted, and the temperature of the conveying section of the twin-screw extruder is set to 160 ° C in turn; the temperature of the melting section is 195. °C; the temperature of the mixing section is 220 ° C and the temperature of the homogenization section is 235 ° C.
  • the head temperature of the twin-screw extruder is set to 245 ° C to obtain a thermoplastic resin in a molten state, and the thermoplastic resin in a molten state is obtained.
  • thermoplastic resin raw material is made of the following mass percentage components: polypropylene: 30 wt %; polyethylene: 35 wt%; silica gel: 35 wt%.
  • the twisted polyester yarn 12 in the softened state after the heat treatment is passed through a thermoplastic resin in a molten state in the die of the twin-screw extruder, so that the twisted polyester thread 12 is compounded with the thermoplastic resin, and then added.
  • the polyester filament 12 moves forward and is removed from the corresponding outlet at the die, wherein the shape of the outlet can correspond to the shape of the plastic laminating tape, and the twisted polyester thread 12 is coated with the thermoplastic resin in a molten state.
  • the thermoplastic resin layer 11 is formed, and a flat plastic laminating tape 1 semi-finished product is formed.
  • the thickness of the plastic laminating tape 1 is substantially larger than the diameter of the twisted polyester fiber 12, and then the plastic lamination tape is
  • the plastic film lamination 1 semi-finished product is firstly moved through the hot water with a temperature of 40 ° C to 60 ° C for pre-cooling treatment, and then subjected to cooling treatment by water at a normal temperature state, and then the temperature is 40.
  • the hot air is heated at °C ⁇ 60°C to remove the moisture from the surface, and the corresponding finished plastic laminating tape 1 is obtained.
  • the movement can pass through the winding power belt on the winding mechanism. Move the plastic laminating tape 1 semi-finished product forward. After the test, the breaking strength of the finished film laminating tape is 34.3 MPa.
  • the corresponding plastic laminating tape was processed according to the method of Example 9, and the plastic laminating tape 1 and the PE plastic film 2 were thermally composited in the same manner as in the third embodiment, and finally the corresponding greenhouse film was obtained.

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  • Mechanical Engineering (AREA)
  • Life Sciences & Earth Sciences (AREA)
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  • Chemical & Material Sciences (AREA)
  • Materials Engineering (AREA)
  • Soil Sciences (AREA)
  • Lining Or Joining Of Plastics Or The Like (AREA)
  • Laminated Bodies (AREA)
  • Casting Or Compression Moulding Of Plastics Or The Like (AREA)

Abstract

A method for fabricating a greenhouse film, the method comprising: under the action of a traction force, having a plurality of plastic pressing film stripes (1) and plastic films (2) sequentially move synchronously towards each process, the plurality of plastic pressing film stripes (1) being in a parallel arrangement and the plastic pressing film stripes (1) being in a flat shape; each piece of the plastic pressing film stripes (1) and the plastic films (2) are subjected to a thermal composite process to receive a thermal composite treatment, the heating temperature on the side of each piece of the plastic pressing film stripes (1) being between 220℃ and 240℃; the heating temperature on the side of each piece of the plastic films (2) is between 160℃ and 190℃, each piece of the plastic pressing film stripes (1) is thermal composited with the plastic films (2) to form an integral body, which is then subjected to a cooling treatment to obtain a corresponding greenhouse film. The method improves the binding fastness performance between a plastic pressing film and a plastic film, thereby improving the tensile strength performance of a greenhouse.

Description

一种大棚薄膜的制作方法Method for manufacturing greenhouse film 技术领域Technical field
本发明涉及一种大棚薄膜的制作方法,属于农用材料技术领域。The invention relates to a method for manufacturing a greenhouse film, and belongs to the technical field of agricultural materials.
背景技术Background technique
农业大棚技术在我国大部分地区的农业生产中得到广泛的应用,而塑料薄膜则是农业大棚中常用的材料,然而,由于塑料薄膜的材质柔软,抗拉性相对较差,在大棚中使用时由于大棚薄膜的面积较大,很容易造成损坏现象,导致实际使用效果较差。因此,现有的大棚薄膜大多是借助于刚性的骨架来支撑。另一方面,由于大棚薄膜在使用时和搭建过程中经常会被反复拉扯或拉紧使用,而单单塑料薄膜其抗拉性相对也较差和柔软性,很难被拉紧,而用力过大则反而会使大棚薄膜破损。因此,为了提高大棚薄膜的强度和抗拉性,一般是通过在大棚薄膜上设置若干索膜的形式来提高大棚薄膜的整体性能,从而使其不仅能够被反复拉扯使用,也能够使大棚薄膜的使用面积更大。如中国专利申请(公开号:CN104855178A)公开了一种索膜热合制造方法,该方法包括在工作面上设置所述底层塑料膜;再在底层塑料膜上设置拉索,然后,再在拉索的表面覆盖表层塑料膜,通过同步加热靠近拉索两侧的表层塑料膜或表层塑料膜和底层塑料膜,并将表层塑料膜和底层塑料膜按压,令表层塑料膜与底层塑料膜在拉索的两侧紧密接触、受热熔化和受压结合,冷却后,成型为一体状结构。虽然,该方法通过把多条相互平行的拉索复合在塑料膜上,在一定程度上增强了塑料膜的抗拉扯性能,然而,由于其仅是通过采用两层塑料膜层将拉索紧密的包覆起来,其拉索是是可以滑动的,拉动拉索 时并不能同时带动塑料薄膜,在使用过程中如果大棚薄膜局部起皱或不平整,仍需要通过拉扯塑料薄膜本身才能去除起皱或不平整部分,因此,依然存在抗拉扯性差的问题;同时,由于薄膜的整体面积相对较大,加工制作过程中不易输送或牵引,而采用多层薄膜,则使加工工序更加复杂,对于设置的要求也相应的提高,不利于实际操作等问题。Agricultural greenhouse technology has been widely used in agricultural production in most parts of China, and plastic film is commonly used in agricultural greenhouses. However, due to the soft material of plastic film, the tensile strength is relatively poor, when used in greenhouses. Due to the large area of the greenhouse film, it is easy to cause damage, resulting in poor practical use. Therefore, existing greenhouse films are mostly supported by means of a rigid skeleton. On the other hand, since the greenhouse film is often repeatedly pulled or tensioned during use and construction, the single plastic film is relatively inferior in tensile strength and softness, and it is difficult to be tightened, and the force is too strong. On the contrary, the greenhouse film will be damaged. Therefore, in order to improve the strength and tensile strength of the greenhouse film, the overall performance of the greenhouse film is generally improved by providing a plurality of cable films on the greenhouse film, so that it can be used not only by repeated pulling but also by the greenhouse film. The use area is larger. For example, a Chinese patent application (Publication No.: CN104855178A) discloses a method for heat sealing a cable film, which comprises disposing the bottom plastic film on a working surface; then placing a cable on the bottom plastic film, and then pulling the cable The surface is covered with a plastic film on the surface, and the surface plastic film or the surface plastic film and the bottom plastic film are heated simultaneously on both sides of the cable, and the surface plastic film and the bottom plastic film are pressed, so that the surface plastic film and the bottom plastic film are in the cable. The two sides are in close contact, combined with heat and pressure, and after cooling, they are formed into a unitary structure. Although the method reinforces the tensile properties of the plastic film to some extent by laminating a plurality of mutually parallel cables on the plastic film, however, since it is only by using two layers of plastic film, the cable is tight. Wrapped, the cable is slidable, pulling the cable At the same time, the plastic film cannot be driven at the same time. If the film of the greenhouse is partially wrinkled or uneven during use, the plastic film itself needs to be pulled to remove the wrinkles or uneven parts. Therefore, the problem of poor pull resistance still exists; Since the overall area of the film is relatively large, it is difficult to convey or pull during the manufacturing process, and the use of the multilayer film makes the processing process more complicated, and the requirements for the setting are correspondingly improved, which is not conducive to practical operation and the like.
发明内容Summary of the invention
本发明针对以上现有技术中存在的缺陷,提供一种大棚薄膜的制作方法,解决的问题是如何简化操作又能够提高压膜带与薄膜的结合力和薄膜的抗拉扯性。The present invention is directed to the defects existing in the prior art, and provides a method for fabricating a greenhouse film, which solves the problem of how to simplify the operation and improve the bonding force between the lamination tape and the film and the tear resistance of the film.
本发明的目的是通过以下技术方案得以实现的,一种大棚薄膜的制作方法,该方法包括以下步骤:The object of the present invention is achieved by the following technical solution, a method for manufacturing a greenhouse film, the method comprising the following steps:
使若干条塑料压膜带与塑料薄膜在牵引力的作用下依次向着每道工序同步移动,所述若干条塑料压膜带均呈平行设置,且所述塑料压膜带呈扁平状,使每条塑料压膜带均与塑料薄膜经过热复合工序进行热复合处理,且使每条塑料压膜带侧的加热温度为220℃~240℃;使每条塑料薄膜侧的加热温度为160℃~190℃,使每条塑料压膜带均与塑料薄膜热复合为一体后,再向下一道工序牵引移动,使经过冷却处理,得到相应的大棚薄膜。The plurality of plastic laminating strips and the plastic film are sequentially moved synchronously toward each process under the action of the traction force, the plurality of plastic laminating strips are arranged in parallel, and the plastic laminating strips are flat, so that each strip The plastic laminating tape is thermally composited with the plastic film through a thermal lamination process, and the heating temperature of each plastic laminating tape side is 220 ° C to 240 ° C; the heating temperature of each plastic film side is 160 ° C to 190 °C, so that each plastic laminating tape is thermally combined with the plastic film, and then moved to the next process, so that after cooling, the corresponding greenhouse film is obtained.
通过分别对塑料压膜带与塑料薄膜进行加热,直接使每条塑料压膜带与塑料薄膜热复合为一体。一方面,通过复合塑料压膜带后,能够有效的提高塑料薄膜的整体抗拉扯强度,由于塑料压膜带与塑料薄膜相对固定,在使用时直接拉扯复合有塑料压膜带的部位,就能够达到拉直或整平塑料薄膜的效果,也不会出现因拉扯用力过大而使塑料薄膜出现破损现象;同时,由于直接将塑料压膜带热复合在塑料薄膜上,只需采用单层塑料薄膜即可,大大的简化生产操作过程,使操作过程更加简单,由于仅采用单层 薄在一定程度上也降低了成本。另一方面,由于本发明是直接复合为一体,由于塑料薄膜相对较薄以及塑料压膜带相对较厚,如果采用同一热合温度,温度过高则容易导致热合过程中塑料薄膜被熔化,而温度过低则容易导致两者复合效果差。因此,本发明人经过研究发现,通过使塑料压膜带与塑料薄膜两侧采用不同的受热温度,使塑料压膜带侧的加热温度相对远高于塑料薄膜侧的加热温度,通过分别进行受热,从而使两者更好的热复合为一体,达到高复合强度的效果,实现简化工艺的同时又能够保证产品的强度和产品的合格率。By separately heating the plastic laminating tape and the plastic film, each plastic laminating tape is directly combined with the plastic film. On the one hand, after the composite plastic laminating tape, the overall tensile strength of the plastic film can be effectively improved. Since the plastic laminating tape is relatively fixed to the plastic film, the portion of the plastic laminating tape can be directly pulled during use. To achieve the effect of straightening or flattening the plastic film, there is no damage to the plastic film due to excessive pulling force; at the same time, since the plastic laminating tape is directly laminated on the plastic film, only a single layer of plastic is needed. The film can be used, which greatly simplifies the production process and makes the operation process simpler, since only a single layer is used. Thin also reduces costs to a certain extent. On the other hand, since the present invention is directly integrated into one body, since the plastic film is relatively thin and the plastic film tape is relatively thick, if the same heat sealing temperature is used, if the temperature is too high, the plastic film is easily melted during the heat sealing process, and the temperature is high. Too low is likely to cause poor composite effect. Therefore, the inventors have found through research that by using different heating temperatures on both sides of the plastic laminating tape and the plastic film, the heating temperature on the plastic laminating tape side is relatively higher than the heating temperature on the plastic film side, and heating is performed separately. Therefore, the better thermal combination of the two is integrated into one, achieving the effect of high composite strength, achieving a simplified process while ensuring the strength of the product and the yield of the product.
在上述大棚薄膜的制作方法中,作为优选,每条塑料压膜带侧的加热温度采用长条状的加热块进行加热,且所述长条状的加热块贴合在每条塑料压膜带的表面;所述塑料薄膜侧的加热温度采用圆柱状的加热辊或长条状的加热块进行加热,且所述圆柱状的加热辊或长条状的加热块贴合在所述塑料薄膜的表面;所述长条状的加热块的加热面与所述圆柱状的加热辊或长条状的加热块的加热面相靠近,且能够使每条塑料压膜带均与塑料薄膜热复合为一体。由于塑料压膜带的厚度相对较好厚,通过采用长条状的加热块进行高温加热,能够使塑料压膜带在进入长条状的加热块时预先进行加热起到预加热的效果,使塑料压膜带能够更好软化状态;另一方面,通过采用圆柱状的加热辊,使相对于以线接触的方式对塑料薄膜进行加热,同时,结合采用低温加热,从而能够使两者更好的热复合为一体,另外,由于通过直接使长条状的加热块与圆柱状的加热辊相靠近的方式进行热压合的方式,通过采用圆柱状的加热辊,加热辊滚动时能够更有效的使塑料压膜带与塑料薄膜热复合后向下一道工序移动,也能够保证两者热合后的结合力的作用,当然,由于塑料薄膜侧采用的加热温度相对较低,因此,采用长条状的加热块进行加热,同样能够达到较好的复合作用。 In the above method for producing a greenhouse film, preferably, the heating temperature on each plastic laminating tape side is heated by a long heating block, and the elongated heating block is attached to each plastic laminating tape. The surface of the plastic film is heated by a cylindrical heating roller or a long heating block, and the cylindrical heating roller or the elongated heating block is attached to the plastic film. a heating surface of the elongated heating block is adjacent to a heating surface of the cylindrical heating roller or the elongated heating block, and each plastic laminating tape is thermally integrated with the plastic film. . Since the thickness of the plastic laminating tape is relatively thick, by using a long heating block to perform high-temperature heating, the plastic laminating tape can be preheated by heating in advance when entering the long heating block, so that The plastic laminating tape can better soften the state; on the other hand, by using a cylindrical heating roller, the plastic film can be heated relative to the line contact, and at the same time, combined with low-temperature heating, the two can be better. The thermal composite is integrated, and the thermal heating is performed by directly bringing the long heating block into contact with the cylindrical heating roller. By using a cylindrical heating roller, the heating roller can be more effectively rolled. The thermal lamination of the plastic laminating tape and the plastic film can be carried out in the next process, which can also ensure the bonding force of the two after heat sealing. Of course, since the heating temperature of the plastic film side is relatively low, the strip is used. The heating block is heated to achieve a better composite effect.
在上述大棚薄膜的制作方法中,作为优选,所述长条状的加热块贴合在每条塑料压膜带的加热面的宽度与相应塑料压膜带的宽度相同。能够使加热块更有效的加热塑料压膜带,且也使塑料压膜带的受热区域受热更均匀,有利于其与塑料薄膜的每个接触点均能够较好的结合;同时,由于塑料压膜带侧长条状的加热压的加热温度相对较高,通过调整其大小也能够更好的保护周边的塑料薄膜不被破坏。作为进一步的优选,所述长条状的加热块的长度为15cm~20cm。当塑料薄膜侧也采用长条状加热块进行加热时,也可以使塑料压膜带侧与塑料薄膜侧的长条状的加热块的长度均为15cm~20cm。能够使加热块对塑料压膜带更好的加热,使具有充分的预热时间,从而使热压合的效果更好。In the above method for producing a greenhouse film, preferably, the strip-shaped heating block is attached to the heating surface of each of the plastic lamination belts to have the same width as the corresponding plastic lamination belt. The heating block can be used to heat the plastic laminating tape more effectively, and the heated area of the plastic laminating tape is more uniformly heated, which is advantageous for better bonding with each contact point of the plastic film; meanwhile, due to plastic pressure The heating temperature of the strip-shaped heating pressure on the side of the film strip is relatively high, and by adjusting the size thereof, it is possible to better protect the surrounding plastic film from being damaged. Further preferably, the elongated heating block has a length of 15 cm to 20 cm. When the plastic film side is also heated by the elongated heating block, the length of the long heating block on the side of the plastic film tape side and the plastic film side may be 15 cm to 20 cm. It can make the heating block heat the plastic laminating tape better, so that it has sufficient preheating time, so that the effect of thermocompression is better.
在上述大棚薄膜的制作方法中,作为优选,当所述每条塑料压膜带与塑料薄膜通过长条状的加热块与圆柱状的加热辊或长条状的加热块之间时,使所述每条塑料压膜带与塑料薄膜在牵引力的作用下均沿着竖直方向移动。由于塑料压膜带与塑料薄膜本身均有一定的重量,而又由于本发明是通过分别对两侧的塑料压膜带及塑料薄膜进行加热来完成,如果是在水平方向上操作,因各自的自身受重力的作用,容易使塑料压膜带与塑料薄膜均向下压在下方的加热块或加热辊上,一方面容易使下方的材料受热过度导致熔融或破损;另一方面,增加了薄膜整体与下方的加热部件之间的摩擦,容易导致牵引的过程中薄膜破损现象,而通过采用竖直方向移动之后,能够很好的解决上述问题,又能够保证两者很好的复合为一体,保证了产品的质量。In the above method for producing a greenhouse film, preferably, when each of the plastic lamination tapes and the plastic film passes between a long heating block and a cylindrical heating roller or a long heating block, Each of the plastic laminating tape and the plastic film are moved in the vertical direction under the action of traction. Since the plastic laminating tape and the plastic film itself have a certain weight, and the present invention is completed by separately heating the plastic laminating tape and the plastic film on both sides, if it is operated in the horizontal direction, The self-gravity action makes it easy for the plastic laminating tape and the plastic film to be pressed down on the heating block or the heating roller below. On the one hand, the underlying material is easily heated to cause melting or damage; on the other hand, the film is added. The friction between the whole and the heating member below may easily cause the film to break during the pulling process, and after the vertical direction is moved, the above problems can be well solved, and the two can be well integrated. Guarantee the quality of the product.
在上述大棚薄膜的制作方法中,作为优选,所述每条塑料压膜带与塑料薄膜同步移动的牵引速度均为10米/秒~15米/秒。使两者在热复合的过程中在加热部分的时间较合理,能够使热复合的效果,同时,也能够使塑料压膜带与塑料薄膜有一定的张力 拉紧存在,能够使两者之间的热合后较平整,不会出现起皱等现象,使压合的结合力更好,也更有利于流水线的快速进行。In the above method for producing a greenhouse film, preferably, each of the plastic laminating tapes and the plastic film simultaneously move at a pulling speed of 10 m/sec to 15 m/sec. The reason that the two in the heating process is more reasonable in the heating part can make the effect of the heat compounding, and at the same time, can also make the plastic film tape and the plastic film have a certain tension. Tightening exists, which can make the heat-sealing between the two smoother, without wrinkles and other phenomena, so that the bonding force of the pressing is better, and it is more favorable for the rapid progress of the pipeline.
在上述大棚薄膜的制作方法中,作为优选,所述塑料压膜带采用以下方法制备得到:In the above method for producing a greenhouse film, preferably, the plastic laminating tape is prepared by the following method:
A、使若干平行且在同一平面上的加捻涤纶线在牵引力的作用下向前移动,然后,使加捻涤纶线经过加热区间进行加热处理使处于软化状态;A. moving a plurality of twisted polyester threads parallel and on the same plane forward by the traction force, and then heating the twisted polyester thread through the heating zone to be in a softened state;
B、再使加捻涤纶线经过熔融状态的热塑性树脂,使加捻涤纶线与熔融状态的热塑性树脂复合为一体,且使加捻涤纶线包覆在熔融状态的热塑性树脂固化后形成的热塑性树脂层内,形成扁平状的塑料压膜带半成品,再使塑料压膜带经过冷却处理,得到相应的成品塑料压膜带。由于经过加捻后的涤纶线呈一定的螺旋状态,相当于使涤纶线的表面有一定的粗糙性,而不是光滑的状态,从而使包覆在外层的热塑性树脂与加捻后的涤纶线接触的表面之间形成相当于镶嵌的状态,增加了涤纶线与热塑性树脂之间的结合力,使不易出现滑动现象;同时,通过先将加捻涤纶线进行加热处理使处于软化状态,目的是为了使涤纶线更好的与熔融状态的热塑性树脂复合在一起,相当于使两者之间的表面形成部分镶嵌或交错的状态,且与采用加捻涤纶线的方式也能够形成更好的协同作用,而不是简单的包覆状态,从而也能够使加捻涤纶线与热塑性树脂之间的结合力提高,实现整体上提高涤纶线与包覆在外层的热塑性树脂之间的结合力,使在使用过程中不会脱落现象。另外,通过使塑料压膜带内包覆若干平行的加捻涤纶线,是为了提高压膜带的整体强度性能,能够保证产品不易出现断裂等现象,从而也就提高了其与塑料薄膜复合后薄膜的整体强度性能;同时,由于加捻涤纶线的存在,在与塑料薄膜热复合后,也一定程度上增加了塑料薄膜与塑料压膜带之间的结合力,提高结合的牢度性能。 B. Further, the twisted polyester thread is subjected to a molten thermoplastic resin, and the twisted polyester thread is combined with the molten thermoplastic resin, and the thermoplastic resin formed by curing the twisted polyester fiber in a molten state is cured. In the layer, a flat plastic film strip is formed, and the plastic laminating strip is cooled to obtain a corresponding finished plastic laminating strip. Since the twisted polyester thread has a certain spiral state, it is equivalent to making the surface of the polyester thread have a certain roughness, rather than a smooth state, so that the thermoplastic resin coated on the outer layer is in contact with the twisted polyester thread. The surface is formed in a state equivalent to the inlay, which increases the bonding force between the polyester thread and the thermoplastic resin, so that the sliding phenomenon is less likely to occur; at the same time, the heat is softened by first heating the twisted polyester thread for the purpose of The polyester resin is better combined with the molten thermoplastic resin, which is equivalent to a state in which the surface between the two is partially inlaid or staggered, and a synergistic effect can be formed by using a twisted polyester thread. Instead of a simple coating state, the bonding force between the twisted polyester thread and the thermoplastic resin can be improved, and the bonding force between the polyester thread and the thermoplastic resin coated on the outer layer can be improved as a whole, so that it can be used. It will not fall off during the process. In addition, by coating a plurality of parallel twisted polyester threads in the plastic laminating tape, the overall strength property of the laminating tape is improved, and the product is less likely to be broken, thereby improving the composite with the plastic film. The overall strength properties of the film; at the same time, due to the presence of the twisted polyester thread, after thermal compounding with the plastic film, the bonding force between the plastic film and the plastic laminating tape is also increased to some extent, and the bonding fastness performance is improved.
在上述大棚薄膜的制作方法中,作为优选,塑料压膜带的制备过程中的步骤A中所述加热处理的温度为140℃~170℃。能够使涤纶线在高温状态下软化,提高其与热塑性树脂之间的结合力,又不至少使涤纶线出现熔融状态,保证其强度性能,从而保证薄膜的整体强度性能。In the above method for producing a greenhouse film, preferably, the temperature of the heat treatment in the step A in the preparation of the plastic film tape is from 140 ° C to 170 ° C. The polyester wire can be softened at a high temperature to improve the bonding force with the thermoplastic resin, and at least the polyester wire is melted to ensure the strength property, thereby ensuring the overall strength performance of the film.
在上述大棚薄膜的制作方法中,作为优选,步骤A中所述加热处理时使加捻涤纶线处于张紧状态。由于加捻涤纶线在生产过程中或多或少会出现松散而出现毛丝或起毛现象,通过加热状态下使其处理张紧状态,能够对涤纶线起到一定的重整过程,使线丝重新拉整,从而有效去除毛丝或起毛的缺陷,使复合在热塑性树脂内的加捻线以及加捻线内的每根线丝均处于较好的拉紧状态,有效保证包覆后涤纶线与热塑性树脂之间的结合力效果,通过提高塑料压膜带的强度来提高塑料薄膜的整体强度性能。In the above method for producing a greenhouse film, it is preferable that the twisted polyester thread is in a tension state during the heat treatment in the step A. Since the twisted polyester thread is more or less loose during the production process, the filaments are fluffed or fluffed. By heating the state to make it tension, the polyester yarn can be subjected to a certain reforming process to make the filament Re-stretching, so as to effectively remove the defects of the wool or fluffing, so that the twisting line compounded in the thermoplastic resin and each wire in the twisting line are in a better tension state, effectively ensuring the coated polyester thread The bonding force effect with the thermoplastic resin improves the overall strength properties of the plastic film by increasing the strength of the plastic laminating tape.
在上述大棚薄膜的制作方法中,作为优选,料压膜带的制备过程中的步骤B中所述熔融状态的热塑性树脂中含有硅胶,且硅胶占熔融状态的热塑性树脂质量的百分比为30wt%~40wt%。一方面,能够提高涤纶线与热塑性树脂之间的粘结力,使具有更好的结合牢度性能;另一方面,通过加入硅胶还能够使形成的压膜带具有更好的柔韧性能,也能够使塑料压膜带与塑料薄膜之间更好的结合在一起,有利于保证两者的结合力效果。作为更进一步的优选,所述硅胶占熔融状态的热塑性树脂质量的百分比为33wt%~35wt%。作为最优选,步骤B中所述熔融状态的热塑性树脂主要由以下质量百分比的成分制成:In the above method for producing a greenhouse film, preferably, the molten resin in the molten state in the step B in the preparation of the pressure-coated film tape contains silica gel, and the percentage of the mass of the thermoplastic resin in the molten state is 30% by weight. 40wt%. On the one hand, it can improve the adhesion between the polyester thread and the thermoplastic resin, so as to have better bonding fastness performance; on the other hand, by adding silica gel, the formed laminating tape can be made to have better flexibility. It can better combine the plastic laminating tape with the plastic film, which is beneficial to ensure the bonding effect of the two. As a still further preferred, the silica gel accounts for 33% by weight to 35% by weight based on the mass of the thermoplastic resin in a molten state. Most preferably, the molten thermoplastic resin in step B is mainly made up of the following mass percentage components:
聚丙烯:30wt%~40wt%;聚乙烯:30wt%~40wt%;硅胶:30wt%~40wt%。既能够提高其与涤纶线之间的结合力,又能够保证压膜带具有较好的柔韧性能,具其与塑料薄膜之间的相容性更好,更好有利塑料压膜带与塑料薄膜之间 的结合牢度。Polypropylene: 30% by weight to 40% by weight; Polyethylene: 30% by weight to 40% by weight; Silica gel: 30% by weight to 40% by weight. It can not only improve the bonding force with the polyester thread, but also ensure the good flexibility of the laminating tape. It has better compatibility with the plastic film, and is more beneficial to the plastic laminating tape and the plastic film. Between The combination of fastness.
综上所述,本发明与现有技术相比,具有以下优点:In summary, the present invention has the following advantages over the prior art:
1.通过分别对塑料压膜带与塑料薄膜进行加热,直接使塑料压膜带与塑料薄膜热复合为一体,且使塑料压膜带侧的加热温度远高于塑料薄膜侧的加热温度,能够使厚度不均的两种材料之间更好的热复合为一体,从而提高塑料薄膜的强度,同时,由于直接将塑料压膜带直接复合在塑料薄膜上,在拉扯或平整薄膜时只需通过拉扯塑料压膜带处,就能够实现对整体薄膜的拉扯或整理,而由于塑料压膜带的强度相对远远高于塑料薄膜,从而使相应的强度得到的提高;由于只需单层薄膜即可,也大大的简化了操作工序和降低了成本的效果。1. By separately heating the plastic laminating tape and the plastic film, the plastic laminating tape is directly combined with the plastic film, and the heating temperature of the plastic laminating tape side is much higher than the heating temperature of the plastic film side. The thermal fusion of the two materials with uneven thickness is integrated to improve the strength of the plastic film. At the same time, since the plastic laminating tape is directly laminated on the plastic film, it is only required to pass through the film when pulling or flattening the film. Pulling the plastic laminating tape can achieve the pulling or finishing of the whole film, and the strength of the plastic laminating tape is relatively higher than that of the plastic film, so that the corresponding strength is improved; However, the operation process and the cost reduction effect are greatly simplified.
2.通过采用长条形的加热块对塑料压膜带进行加热,能够对塑料压膜带起到一定的预加热过程,使其更好的达到软化的状态,很好的解决因压膜带厚度较厚受热不均或无法达到较好软化效果的问题;同时,结合采用低温加热的圆柱状加热辊对塑料薄膜进行加热,从而很好的实现热合后的高结合力的效果。2. By heating the plastic laminating tape with a long heating block, the plastic laminating tape can be preheated to a better softening state, which is a good solution for the laminating tape. The problem is that the thickness is thick and the heat is uneven or the softening effect cannot be achieved. At the same time, the plastic film is heated by the cylindrical heating roller which is heated at a low temperature, so that the high bonding force after heat sealing is well realized.
3.通过使长条状加热块贴合在塑料压膜带侧的加热面的宽度与塑料压膜带的宽度相同,既能够有效对压膜带进行加热,使其受热均匀性好,从而使塑料压膜带更好的软化状态,不会出现局部受热而导致没有达到软化的缺陷,从而实现了其与塑料薄膜之间的结合牢度,不会出现局部不能热合为一体的问题,整体上提高了塑料压膜与塑料薄膜之间的结合牢度性能。3. By making the length of the heating surface of the strip-shaped heating block attached to the plastic laminating strip side the same as the width of the plastic laminating strip, the laminating strip can be effectively heated to make the heating uniformity good, thereby The plastic laminating tape has a better softening state, and there is no defect that local heating is caused to cause softening, thereby achieving the bonding fastness with the plastic film, and there is no problem that the partial heat cannot be integrated into one body, as a whole. Improves the bonding fastness between the plastic laminate and the plastic film.
4.通过使塑料压膜带内包覆若干平行的加捻涤纶线,能够提高压膜带的整体强度性能,使不易出现断裂等现象,从而也就提高了其与塑料薄膜复合后薄膜的整体强度性能;同时,由于加捻涤纶线的存在,在与塑料薄膜热复合后,也一定程度上增加了塑料薄膜与塑料压膜带之间的结合力,提高结合的牢度性能。 4. By coating a plurality of parallel twisted polyester threads in the plastic laminating tape, the overall strength performance of the laminating tape can be improved, and the phenomenon of cracking and the like is less likely to occur, thereby improving the overall film composited with the plastic film. Strength performance; At the same time, due to the presence of the twisted polyester thread, after thermal compounding with the plastic film, the bonding force between the plastic film and the plastic laminating tape is also increased to some extent, and the bonding fastness performance is improved.
附图说明:BRIEF DESCRIPTION OF THE DRAWINGS:
图1是本大棚薄膜的立体结构示意图。Figure 1 is a schematic perspective view of the greenhouse film.
图2是本大棚薄膜中塑料压膜带的放大立体结构示意图。2 is a schematic enlarged perspective view of a plastic laminating tape in the greenhouse film.
图3是本大棚薄膜中塑料压膜带表层被部分翻起后的放大立体结构示意图。Fig. 3 is a schematic enlarged perspective view showing the surface of the plastic laminating tape in the greenhouse film partially turned up.
图4是塑料压膜带内的加捻涤纶线的放大结构示意图。Fig. 4 is a schematic enlarged view showing the twisted polyester thread in the plastic lamination belt.
图中,1、塑料压膜带;11热塑料树脂层;12、加捻涤纶线、2、塑料薄膜。In the figure, 1, plastic laminating tape; 11 thermoplastic resin layer; 12, twisted polyester thread, 2, plastic film.
具体实施方式detailed description
下面通过具体实施例,对本发明的技术方案作进一步具体的说明,但是本发明并不限于这些实施例。The technical solutions of the present invention are further specifically described below by way of specific embodiments, but the present invention is not limited to the embodiments.
以下实施例中所提及到的大棚薄膜的尺寸大小可以根据实际需要进行调整,并没有具体的限定要求,另外,在大棚薄膜上热合塑料压膜带1的条数同样可以根据实际需要进行调整,一般采用使塑料薄膜2上两两相邻的塑料压膜带1之间的间隔为6米左右,能够提高大棚薄膜的整体强度,且塑料薄膜2上的塑料压膜带1可以根据实际需要依次对每根进行热复合;当然,也可以采用若干根塑料压膜带1同步进行热复合均可。The size of the greenhouse film mentioned in the following embodiments can be adjusted according to actual needs, and there is no specific limitation. In addition, the number of the heat-sealing plastic laminating strips 1 on the greenhouse film can also be adjusted according to actual needs. Generally, the interval between the plastic film strips 1 adjacent to each other on the plastic film 2 is about 6 meters, which can improve the overall strength of the film of the greenhouse, and the plastic film strip 1 on the plastic film 2 can be adjusted according to actual needs. Each of the pieces is thermally composited in turn; of course, it is also possible to use a plurality of plastic laminating strips 1 to perform thermal recombination simultaneously.
具体来说,结合图1所示,本大棚薄膜包括若干塑料压膜带1和塑料薄膜2,其中的若干塑压膜带1等间距的热复合在塑料薄膜1的同一侧,当然,也可以使塑料压膜带1在塑料薄膜2的两侧设置,一般使两两相邻的塑料压膜带1之间的间隔为1米,间隔也可以根据强度的要求,对间隔进行适当的调整,如采用间隔1.5米、2米等等,在实际的生产上加工时,可以使采用3条塑料压膜带1同步进行热复合在塑料薄膜2上,当然也可以根据塑料薄膜2的宽度大小采用4条、5条、8条、10条,甚至更多条的塑料压膜带1同步进行热复合在塑料薄膜2上,其中,塑料压膜 带1的端部可以与塑料薄膜2宽度方向的边缘相齐平,也可以使塑料压膜带1的端部略长于塑料薄膜2宽度方向的边缘,使有利于拉扯Specifically, as shown in FIG. 1 , the greenhouse film comprises a plurality of plastic laminating tapes 1 and a plastic film 2, wherein a plurality of plastic lamination tapes 1 are thermally laminated on the same side of the plastic film 1 , of course, The plastic laminating tape 1 is disposed on both sides of the plastic film 2. Generally, the interval between the two adjacent plastic lamination tapes 1 is 1 m, and the interval can be appropriately adjusted according to the strength requirement. If the interval is 1.5 meters, 2 meters, etc., in the actual production processing, three plastic laminating strips 1 can be synchronously thermally composited on the plastic film 2, and of course, according to the width of the plastic film 2 4, 5, 8, 10, or even more plastic laminating strips 1 are simultaneously thermally laminated on the plastic film 2, wherein the plastic lamination film The end of the belt 1 may be flush with the edge of the plastic film 2 in the width direction, or the end of the plastic lamination belt 1 may be slightly longer than the edge of the width direction of the plastic film 2, which is advantageous for pulling.
如图2-图4所示,其中的塑料压膜带1包括加捻涤纶线12和热塑性树脂层11,且加捻涤纶线12通过热复合包覆在热塑性树脂层11内,其中的加捻涤纶线沿着塑料压膜带1的长度方向呈平行设置。其中的塑料压膜带1呈扁平状,对于长度可以根据实际塑料薄膜的需要进行选择和调整,最好使塑料压膜带内设置有6-8根的加捻涤纶线12,对于热塑性树脂层1的透明度可以根据选用的材料不同进行调整。当然,其中的加捻涤纶线12也可以采用其它的加捻聚酯纤维线,如加捻尼龙线代替。As shown in Figs. 2 to 4, the plastic laminating tape 1 includes a twisted polyester thread 12 and a thermoplastic resin layer 11, and the twisted polyester thread 12 is coated in the thermoplastic resin layer 11 by thermal compounding, wherein The polyester threads are arranged in parallel along the length of the plastic laminating strip 1. The plastic laminating tape 1 is flat, and the length can be selected and adjusted according to the needs of the actual plastic film. It is preferable to provide 6-8 twisted polyester threads 12 in the plastic laminating tape for the thermoplastic resin layer. The transparency of 1 can be adjusted according to the materials selected. Of course, the twisted polyester thread 12 can also be replaced by other twisted polyester fiber strands, such as twisted nylon thread.
为了更好的说明,以下实施例对塑料压膜带1与塑料薄膜2之间的热复合进行具体的说明,同时,采用PE材料制成的塑料薄膜2,但并不限于该材料制成的塑料薄膜2,采用其它如PP材料等制成的塑料薄膜2均可。For better explanation, the following embodiment specifically describes the thermal recombination between the plastic laminating tape 1 and the plastic film 2, and at the same time, the plastic film 2 made of a PE material is not limited to the material. The plastic film 2 can be made of other plastic film 2 made of a PP material or the like.
实施例1Example 1
根据PE塑料薄膜2上设置塑料压膜带1的根数,对应的选用相应卷数的塑料压膜带1放置在放卷起始处进行放卷;同样,将收卷好的PE塑料薄膜2对应的放置在放卷超始处进行放卷;通过设置在后继过程上的牵引机构带动塑料压膜带1与PE塑料薄膜2依次向下一道工序移动,其中,最好使牵引机构设置在热复合工序(塑料压膜带1与PE塑料薄膜2热复合工序)与冷却处理工序之间;不管在PE塑料薄膜2上热复合几根塑料压膜带,在整个生产线过程中均可以依次对每根进行完整的工序处理再进行下一根加工;也可以使多根塑料压膜带1同时进行同步热复合处理,本实施例采用同步进行热复合,且使塑料薄膜2上每间隔1米热复合一条塑料压膜带1,采用热复合7条塑料压膜带1同步进行,且塑料薄膜2的宽度为6米,长度可以根据需要调整,使塑料压 膜带1沿着塑料薄膜2宽度方向上每间隔1米热复合一条塑料压膜带1。According to the number of the plastic laminating tapes 1 disposed on the PE plastic film 2, the corresponding plastic laminating tape 1 of the corresponding number of rolls is placed at the unwinding start for unwinding; likewise, the wound PE plastic film 2 is wound. Corresponding placement is performed at the beginning of the unwinding; the plastic laminating tape 1 and the PE plastic film 2 are sequentially moved to the next process by a traction mechanism disposed on the subsequent process, wherein the traction mechanism is preferably placed in the heat The compounding process (the thermal lamination process of the plastic laminating tape 1 and the PE plastic film 2) and the cooling treatment process; no matter how many plastic laminating tapes are thermally composited on the PE plastic film 2, each of the production lines can be sequentially The root is subjected to a complete process and then subjected to the next process; a plurality of plastic film tapes 1 can also be simultaneously subjected to simultaneous thermal composite treatment. In this embodiment, the thermal composite is performed synchronously, and the plastic film 2 is heated at intervals of 1 meter. A plastic laminating tape 1 is composited, and 7 plastic laminating tapes 1 are thermally composited, and the width of the plastic film 2 is 6 meters, and the length can be adjusted as needed to make the plastic pressure The film tape 1 is thermally composited with a plastic film tape 1 at intervals of 1 meter in the width direction of the plastic film 2.
生产线刚运行时,可以采用人工的方式将每条塑料压膜带1与PE塑料薄膜2引导至牵引机构上,然后,再使每条塑料压膜带1与PE塑料薄膜2在牵引机构的牵引力的作用下依次向着每道工序同步移动,中途可以设置多个引导机构进行引导,先使同步移动的每条塑料压膜带1与PE塑料薄膜2经过热复合工序进行热复合处理,且热复合处理时使每条塑料压膜带1侧的加热温度为240℃;使PE塑料薄膜2侧的加热温度为190℃,直接在加热的同时进行热压合,使每条塑料压膜带1均与PE塑料薄膜2热复合为一体后,再向下一道工序牵引移动通过牵引机构后,同步使每条塑料压膜带1与PE塑料薄膜2热复合为一体,经过下一道工序进行风冷后,进行收卷,得到相应的大棚薄膜,其中,牵引机构后的牵引可以通过收卷机构的动力进行牵引。When the production line is just running, each plastic laminating tape 1 and PE plastic film 2 can be manually guided to the traction mechanism, and then the traction force of each plastic laminating tape 1 and PE plastic film 2 in the traction mechanism can be made. Under the action of the two, the synchronous movement is sequentially performed to each process, and a plurality of guiding mechanisms can be set for guiding in the middle, and each plastic laminating tape 1 and the PE plastic film 2 that are synchronously moved are subjected to thermal composite processing through thermal compounding, and thermal compounding is performed. During the treatment, the heating temperature of each plastic laminating strip 1 side is 240 ° C; the heating temperature of the PE plastic film 2 side is 190 ° C, and the thermocompression is directly performed while heating, so that each plastic laminating strip 1 is After being thermally integrated with the PE plastic film 2, after pulling and moving through the traction mechanism in the next process, each plastic laminating tape 1 and the PE plastic film 2 are simultaneously thermally integrated into one body, and after air cooling through the next process. The winding is performed to obtain a corresponding greenhouse film, wherein the traction after the traction mechanism can be pulled by the power of the winding mechanism.
实施例2Example 2
根据PE塑料薄膜2上设置塑料压膜带1的根数,对应的选用相应卷数的塑料压膜带1放置在放卷起始处进行放卷;同样,将收卷好的PE塑料薄膜2对应的放置在放卷超始处进行放卷;通过设置在后继过程上的牵引机构带动每条塑料压膜带1与PE塑料薄膜2依次向每道工序移动,其中,最好使牵引机构设置在热复合工序(每条塑料压膜带1与PE塑料薄膜2热复合工序)与冷却处理工序之间;本实施例采用使每条塑料压膜带1与PE塑料薄膜2均同步进行热复合,且塑料薄膜2的宽度为6米,长度可以根据需要调整,使塑料压膜带1沿着塑料薄膜2宽度方向上等间隔热复合有5条塑料压膜带1,其中,塑料薄膜2宽度方向上的两边边缘各热复合有一条塑料压膜带2。According to the number of the plastic laminating tapes 1 disposed on the PE plastic film 2, the corresponding plastic laminating tape 1 of the corresponding number of rolls is placed at the unwinding start for unwinding; likewise, the wound PE plastic film 2 is wound. Corresponding placement is performed at the beginning of unwinding; unwinding is carried out by each of the plastic laminating tape 1 and the PE plastic film 2, which are arranged in the subsequent process, wherein the traction mechanism is preferably set. In the thermal compounding process (each plastic laminating tape 1 and the PE plastic film 2 thermal lamination process) and the cooling treatment process; in this embodiment, each plastic laminating tape 1 and the PE plastic film 2 are simultaneously thermally composited. And the width of the plastic film 2 is 6 meters, the length can be adjusted as needed, so that the plastic laminating tape 1 is thermally composited at intervals of the width of the plastic film 2 with five plastic laminating strips 1, wherein the width of the plastic film 2 The two edges of the direction are each thermally combined with a plastic laminating strip 2.
生产线刚运行时,可以采用人工的方式将每条塑料压膜带1与PE塑料薄膜2引导至牵引机构上,接下来即能够达到连续生产 的过程,然后,再使每条塑料压膜带1与PE塑料薄膜2在牵引机构的牵引力的作用下依次向着每道工序同步移动,使同步移动速度为10m/s(相当于牵引速度),中途可以设置多个常规的引导机构进行引导,先使同步移动的每条塑料压膜带1与PE塑料薄膜2经过热复合工序进行热复合处理,且热复合处理时使每条塑料压膜带1侧的加热温度为220℃,加热过程采用长条状的加热块进行加热,且使长条状的加热块贴合在每条塑料压膜带1的外侧表面;同时,使PE塑料薄膜2侧的加热温度为160℃,加热过程中采用圆柱状的加热辊进行加热,加热辊可以滚动,且使圆柱状的加热辊贴合在PE塑料薄膜2的外侧表面,最好使加热辊的位置位于长条状的加热块靠中间的部分;其中,长条状的加热块的加热面与圆柱状的加热辊的加热面相靠近,且能够使每条塑料压膜带1均与PE塑料薄膜2直接在加热的同时进行热压合,其中,每条塑料压膜带1与PE塑料薄膜2在牵引力的作用下移动通过长条状的加热块与圆柱状的加热辊之间时,使每条塑料压膜带1与PE塑料薄膜2均沿着竖直方向移动,可以通过使两者在牵引力的作用下,从上方进入热复合工序,再从下方出热复合工序;当然,也可以使两者在牵引力的作用下从下方进入热复合工序,再从上方出热复合工序,使每条塑料压膜带1与PE塑料薄膜2热复合为一体,再向下一道工序牵引移动通过牵引机构后,使每条塑料压膜带1与PE塑料薄膜2热复合为一体,再经过下一道工序进行风冷后,进行收卷,得到相应的大棚薄膜,其中,牵引机构后的牵引可以通过收卷机构的动力进行牵引。When the production line is just running, each plastic laminating tape 1 and PE plastic film 2 can be manually guided to the traction mechanism, and then continuous production can be achieved. Then, each plastic laminating tape 1 and PE plastic film 2 are sequentially moved synchronously to each process under the traction force of the traction mechanism, so that the synchronous moving speed is 10 m/s (equivalent to the traction speed). In the middle, a plurality of conventional guiding mechanisms can be set for guiding, and each plastic laminating strip 1 and the PE plastic film 2 that are synchronously moved are first subjected to thermal lamination processing through a thermal lamination process, and each plastic laminating tape is subjected to thermal composite processing. The heating temperature on the 1 side is 220 ° C. The heating process is performed by heating the strip-shaped heating block, and the long heating block is attached to the outer surface of each plastic laminating strip 1; at the same time, the PE plastic film 2 is made. The heating temperature of the side is 160 ° C, and heating is performed by a cylindrical heating roller during heating, the heating roller can be rolled, and the cylindrical heating roller is attached to the outer surface of the PE plastic film 2, preferably the position of the heating roller. a portion in the middle of the elongated heating block; wherein the heating surface of the elongated heating block is adjacent to the heating surface of the cylindrical heating roller, and each plastic lamination tape 1 can be combined with the PE plastic film 2 The thermal compression is performed while being heated, wherein each of the plastic laminating tape 1 and the PE plastic film 2 are moved between the elongated heating block and the cylindrical heating roller under the traction force, so that each strip The plastic laminating tape 1 and the PE plastic film 2 are both moved in the vertical direction, and the two can enter the thermal recombination process from above by the action of the traction force, and then the thermal composite process is performed from below; Under the action of traction force, the thermal composite process is entered from below, and then the thermal composite process is performed from above, so that each plastic laminating tape 1 is thermally composited with the PE plastic film 2, and then moved to the traction mechanism through the next process. So that each plastic laminating tape 1 and the PE plastic film 2 are thermally composited into one body, and then air-cooled through the next process, and then wound up to obtain a corresponding greenhouse film, wherein the traction after the traction mechanism can be retracted. The power of the mechanism is towing.
实施例3Example 3
根据PE塑料薄膜2上设置塑料压膜带1的根数,对应的选用相应卷数的塑料压膜带1放置在放卷起始处进行放卷;同样,将收卷好的PE塑料薄膜2对应的放置在放卷超始处进行放卷;通过设置在后继过程上的牵引机构带动每条塑料压膜带1与PE塑料薄 膜2依次向每道工序移动,其中,最好使牵引机构设置在热复合工序(每条塑料压膜带1与PE塑料薄膜2热复合工序)与冷却处理工序之间;本实施例采用使每条塑料压膜带1与PE塑料薄膜2均同步进行热复合,且塑料薄膜2的宽度为6米,长度可以根据需要调整,使塑料压膜带1沿着塑料薄膜2宽度方向上等间隔热复合有8条塑料压膜带1,其中,塑料薄膜2宽度方向上的两边边缘各热复合有一条塑料压膜带2。采用热复合8条塑料压膜压带同步进行;According to the number of the plastic laminating tapes 1 disposed on the PE plastic film 2, the corresponding plastic laminating tape 1 of the corresponding number of rolls is placed at the unwinding start for unwinding; likewise, the wound PE plastic film 2 is wound. Corresponding placement is performed at the beginning of the unwinding; unwinding of each plastic laminating tape 1 and PE plastic is carried out by a traction mechanism disposed on the subsequent process The film 2 is sequentially moved to each process. Among them, it is preferable to arrange the traction mechanism between the thermal lamination process (the thermal lamination process of each plastic lamination tape 1 and the PE plastic film 2) and the cooling treatment process; Each plastic laminating strip 1 and PE plastic film 2 are simultaneously thermally composited, and the width of the plastic film 2 is 6 meters, and the length can be adjusted as needed, so that the plastic laminating strips 1 are equally spaced along the width direction of the plastic film 2. The thermal composite has eight plastic laminating strips 1, wherein the plastic film strip 2 is thermally composited at both edges in the width direction. Simultaneously carried out by hot-bonding 8 plastic laminating press belts;
生产线刚运行时,可以采用人工的方式将每条塑料压膜带1与PE塑料薄膜2均引导至牵引机构上,接下来即能够达到连续生产的过程,然后,再使每条塑料压膜带1与PE塑料薄膜2在牵引机构的牵引力的作用下依次向着每道工序同步移动,使同步移动速度为10m/s(相当于牵引速度),中途可以设置多个常规的引导机构进行引导,先使同步移动的每条塑料压膜带1与PE塑料薄膜2经过热复合工序进行热复合处理,且热复合处理时使每条塑料压膜带1侧的加热温度为230℃,加热过程采用长条状的加热块进行加热,且使长条状的加热块贴合在每条塑料压膜带1的外侧表面,并使长条状的加热块贴合在每条塑料压膜带1的加热面的宽度与每条塑料压膜带1的宽度相同以及使长条状的加热块的长度为15cm;同时,使PE塑料薄膜2侧的加热温度为180℃,加热过程中采用圆柱状的加热辊进行加热,加热辊可以滚动,且使圆柱状的加热辊贴合在PE塑料薄膜2的外侧表面,并使加热辊的位置位于长条状的加热块靠中间的部分;其中,长条状的加热块的加热面与圆柱状的加热辊的加热面相靠近,且能够使每条塑料压膜带1与PE塑料薄膜2直接在加热的同时进行热压合,其中,每条塑料压膜带1与PE塑料薄膜2在牵引力的作用下移动通过长条状的加热块与圆柱状的加热辊之间时,使每条塑料压膜带1与PE塑料薄膜2均沿着竖直方向移动,可以通过使两者在牵引力的 作用下从上方进入热复合工序,再从下方出热复合工序;当然,也可以使两者在牵引力的作用下从下方进入热复合工序,再从上方进行热复合工序,使每条塑料压膜带1与PE塑料薄膜2热复合为一体后,再向下一道工序牵引移动通过牵引机构后,使每条塑料压膜带1与PE塑料薄膜2热复合为一体,经过下一道工序进行风冷后,进行收卷,得到相应的大棚薄膜,其中,牵引机构后的牵引可以通过收卷机构的动力进行牵引。When the production line is just running, each plastic laminating tape 1 and PE plastic film 2 can be manually guided to the traction mechanism, and then the continuous production process can be achieved, and then each plastic lamination tape can be 1 and PE plastic film 2 under the action of the traction mechanism of the traction mechanism to move synchronously to each process, so that the synchronous moving speed is 10m / s (equivalent to the traction speed), a plurality of conventional guiding mechanisms can be set in the middle to guide, first Each of the plastic laminating tape 1 and the PE plastic film 2 that are synchronously moved are subjected to a thermal lamination process through a thermal lamination process, and the heating temperature of each plastic laminating tape 1 side is 230° C., and the heating process is long. The strip-shaped heating block is heated, and a long heating block is attached to the outer surface of each of the plastic laminating strips 1, and a long heating block is attached to the heating of each of the plastic laminating strips 1. The width of the surface is the same as the width of each plastic laminating strip 1 and the length of the elongated heating block is 15 cm; at the same time, the heating temperature of the side of the PE plastic film 2 is 180 ° C, and the heating is performed in a cylindrical manner during heating. Roll Heating, the heating roller can roll, and the cylindrical heating roller is attached to the outer surface of the PE plastic film 2, and the position of the heating roller is located in the middle portion of the elongated heating block; wherein, the strip-shaped portion The heating surface of the heating block is close to the heating surface of the cylindrical heating roller, and each plastic laminating tape 1 and the PE plastic film 2 can be directly thermo-compressed while being heated, wherein each plastic laminating tape 1 When the PE plastic film 2 is moved between the elongated heating block and the cylindrical heating roller under the action of the traction force, each of the plastic laminating tape 1 and the PE plastic film 2 are moved in the vertical direction, By making the two in traction Under the action, it enters the thermal compounding process from above, and then heats the composite process from below. Of course, it is also possible to make the two into the thermal compounding process from the bottom under the action of traction force, and then carry out the thermal compounding process from above to make each plastic lamination film After the belt 1 is thermally composited with the PE plastic film 2, and then pulled through the traction mechanism in the next process, each plastic laminating strip 1 and the PE plastic film 2 are thermally composited, and air-cooled through the next process. After that, the winding is performed to obtain a corresponding greenhouse film, wherein the traction after the traction mechanism can be pulled by the power of the winding mechanism.
实施例4Example 4
根据PE塑料薄膜上设置塑料压膜带1的根数,对应的选用相应卷数的塑料压膜带1放置在放卷起始处进行放卷;同样,将收卷好的PE塑料薄膜2对应的放置在放卷超始处进行放卷;通过设置在后继过程上的牵引机构带动每条塑料压膜带1与PE塑料薄膜2依次向每道工序移动,其中,最好使牵引机构设置在热复合工序(每条塑料压膜带1与PE塑料薄膜2热复合工序)与冷却处理工序之间;本实施例采用使每条塑料压膜带1与PE塑料薄膜2均同步进行热复合,且塑料薄膜2的宽度为6米,长度可以根据需要调整,使塑料压膜带1沿着塑料薄膜2宽度方向上等间隔热复合有3条塑料压膜带1,其中,使塑料薄膜2宽度方向上的两边边缘各热复合有一条塑料压膜带2,采用热复合3条塑料压膜压带同步进行。According to the number of the plastic laminating tapes 1 disposed on the PE plastic film, the corresponding plastic laminating tape 1 of the corresponding number of rolls is placed at the unwinding start for unwinding; likewise, the wound PE plastic film 2 is correspondingly The placing is performed at the beginning of the unwinding to unwind; the plastic laminating tape 1 and the PE plastic film 2 are sequentially moved to each process by a pulling mechanism disposed on the subsequent process, wherein the traction mechanism is preferably disposed at The thermal compounding process (the thermal lamination process of each plastic laminating tape 1 and the PE plastic film 2) and the cooling treatment process; in this embodiment, each plastic laminating tape 1 and the PE plastic film 2 are simultaneously thermally composited. And the width of the plastic film 2 is 6 meters, and the length can be adjusted as needed, so that the plastic laminating tape 1 is thermally composited along the width direction of the plastic film 2 with three plastic laminating tapes 1, wherein the width of the plastic film 2 is made. The two sides of the direction are thermally composited with a plastic laminating strip 2, which is synchronously carried out by thermally laminating three plastic laminating press belts.
生产线刚运行时,可以采用人工的方式将每条塑料压膜带1与PE塑料薄膜2引导至牵引机构上,接下来即能够达到连续生产的过程,然后,再使每条塑料压膜带1与PE塑料薄膜2在牵引机构的牵引力的作用下依次向着每道工序同步移动,使同步移动速度为15m/s(相当于牵引速度),中途可以设置多个常规的引导机构进行引导,先使同步移动的每条塑料压膜带1与PE塑料薄膜2经过热复合工序进行热复合处理,热复合处理时使每条塑料压膜带1侧的加热温度为220℃,加热过程采用长条状的加热块进行 加热,且使长条状的加热块贴合在每条塑料压膜带1的外侧表面,并使长条状的加热块贴合在每条塑料压膜带1的加热面的宽度与塑料压膜带的宽度相同以及使长条状的加热块的长度为20cm;同时,使PE塑料薄膜2侧的加热温度为170℃,加热过程中PE塑料薄膜2侧也采用长条状的加热块进行加热,且使长条状的加热块贴合在PE塑料薄膜2的外侧表面,同时,使贴合在塑料薄膜1侧的长条状加热块的加热面宽度与塑料压膜带2的宽度相同以及使该长条状的加热块的长度为20cm,并使该长条状加热块的位置位于相对长条状的加热块长度方向靠中间的部分;其中,两个长条状的加热块的加热面相对设置且相靠近,能够使每条塑料压膜带1与PE塑料薄膜2直接在加热的同时进行热压合,其中,每条塑料压膜带1与PE塑料薄膜2在牵引力的作用下移动通过长条状的加热块与圆柱状的加热辊之间时使每条塑料压膜带1与PE塑料薄膜2均沿着竖直方向移动,可以通过使两者在牵引力的作用下从上方进入热复合工序,再从下方移动出热复合工序,当然,也可以使两者在牵引力的作用下从下方进入热复合工序,再从上方移出热复合工序,使每条塑料压膜带1与PE塑料薄膜2热复合为一体后,再向下一道工序牵引移动通过牵引机构后,使每条塑料压膜带1与PE塑料薄膜2热复合为一体,再经过下一道工序进行风冷后,进行收卷,得到相应的大棚薄膜,其中,牵引机构后的牵引可以通过收卷机构的动力进行牵引。When the production line is just running, each plastic laminating tape 1 and PE plastic film 2 can be manually guided to the traction mechanism, and then the continuous production process can be achieved, and then each plastic lamination tape is Under the action of the traction force of the traction mechanism, the PE plastic film 2 is sequentially moved synchronously to each process, so that the synchronous moving speed is 15 m/s (corresponding to the traction speed), and a plurality of conventional guiding mechanisms can be set for guiding in the middle. Each of the plastic laminating tape 1 and the PE plastic film 2 which are synchronously moved are subjected to a thermal lamination process through a thermal lamination process, and the heating temperature of each plastic laminating tape 1 side is 220° C., and the heating process adopts a long strip shape. Heating block Heating, and attaching a long heating block to the outer surface of each plastic laminating strip 1, and attaching the elongated heating block to the width of the heating surface of each plastic laminating strip 1 and the plastic pressing The width of the film strip is the same and the length of the long heating block is 20 cm; at the same time, the heating temperature of the PE plastic film 2 side is 170 ° C, and the PE plastic film 2 side is also heated by a long heating block during heating. Heating and laminating the heating block on the outer surface of the PE plastic film 2, and at the same time, the width of the heating surface of the elongated heating block attached to the side of the plastic film 1 is the same as the width of the plastic laminating tape 2 And the length of the elongated heating block is 20 cm, and the position of the elongated heating block is located in the middle of the longitudinal direction of the relatively long heating block; wherein the two elongated heating blocks are The heating surfaces are oppositely arranged and close to each other, so that each plastic laminating strip 1 and the PE plastic film 2 can be directly thermo-compressed while being heated, wherein each plastic laminating strip 1 and the PE plastic film 2 are in traction. Move down through long strips of heating block and cylindrical When the heating roller is between, each plastic laminating tape 1 and the PE plastic film 2 are moved in the vertical direction, and the two can enter the thermal recombination process from above by the traction force, and then move out of the thermal composite from below. In the process, of course, the two may enter the thermal recombination process from the bottom under the action of the traction force, and then remove the thermal recombination process from above, so that each plastic lamination tape 1 and the PE plastic film 2 are thermally composited together, and then After the next process is pulled and moved through the traction mechanism, each plastic laminating tape 1 is thermally composited with the PE plastic film 2, and then air-cooled after the next process, and the corresponding greenhouse film is obtained. The traction after the traction mechanism can be pulled by the power of the winding mechanism.
实施例5Example 5
本实施例中的用到的涤纶单丝可以采用常规的方法加工而成:如先选用高粘熔融涤纶原料,再经过计量之后,通过喷丝、冷却、上油、拉伸和热定型的常规工序后,再经过收卷成型,得到相应的高强度工业涤纶丝产品。如采用中国专利(授权公开号:CN102797055B)中的相应涤纶丝的加工方法,当然,也可以采用其它的常规方法加工而成,这里不再赘述。 The polyester monofilament used in this embodiment can be processed by a conventional method: if the high-viscosity molten polyester raw material is selected first, and then after being metered, the conventional method of spinning, cooling, oiling, stretching and heat setting is adopted. After the process, it is further processed by winding to obtain the corresponding high-strength industrial polyester yarn product. For example, the processing method of the corresponding polyester yarn in the Chinese patent (authorization publication number: CN102797055B) can be processed by other conventional methods, and will not be described herein.
本实施例中塑料压膜带1的宽度可以根据实际需要进行调整,但为了更好的说明,以下实施例中的塑料压膜带1的宽度均为1.2cm,但并不限于该宽度范围。The width of the plastic lamination tape 1 in this embodiment can be adjusted according to actual needs. However, for better explanation, the width of the plastic lamination tape 1 in the following embodiments is 1.2 cm, but is not limited to the width range.
将涤纶丝进行加捻处理,即先采用若干涤纶单丝经过加捻处理,使形成规格为1100dtex/192f的单加捻涤纶线;然后,再采用6根单加捻涤纶线再次经过加捻处理,形成复合加捻涤纶线,收卷成型,备用;且复合的加捻涤纶线的规格达到6000D;The polyester yarn is twisted, that is, a plurality of polyester monofilaments are firstly twisted to form a single twisted polyester thread having a specification of 1100 dtex/192f; and then, six single twisted polyester threads are again subjected to twisting treatment. Forming a composite twisted polyester thread, winding and forming, and standby; and the composite twisted polyester thread has a specification of 6000D;
根据塑料压膜带1内设置加捻涤纶线12的根数,对应的选用相应卷数的以上收卷好的加捻涤纶线12放置在放卷起始处进行放卷,同时通过设置在后继过程上的牵引机构带动加捻涤纶线12向前移动,其中,牵引机构设置在包覆工序(加捻涤纶线12与热塑性塑料复合工序)与冷却处理之间,本实施例中选用塑料压膜带1内包覆有8根平行设置的加捻涤纶线12;According to the number of twisted polyester threads 12 disposed in the plastic laminating tape 1, the correspondingly wound twisted polyester thread 12 of the corresponding number of rolls is placed at the beginning of unwinding for unwinding, and at the same time by setting in the successor The traction mechanism in the process drives the twisted polyester thread 12 to move forward, wherein the traction mechanism is disposed between the coating process (the twisting process of the twisted polyester thread 12 and the thermoplastic compound) and the cooling process, and the plastic film is selected in the embodiment. The belt 1 is covered with 8 twisted polyester threads 12 arranged in parallel;
具体来说,使8根平行且在同一平面上的加捻涤纶线12在上述牵引机构的牵引力作用下向前移动,移动的过程中可以根据需要在中途设有多个引导机构,然后,使同步行进的加捻涤纶线12移动到加热区间对加捻涤纶线12进行加热处理,使加捻涤纶线12进入加热区间时的加热温度为140℃,且使加捻涤纶线12移出加热区间时的加热温度为170℃,且使加捻涤纶线12经过加热区间时处于张紧状态,使处于软化状态;Specifically, the eight twisted polyester threads 12 which are parallel and on the same plane are moved forward by the traction force of the above-mentioned traction mechanism, and a plurality of guiding mechanisms can be provided in the middle of the movement as needed, and then The twisted polyester yarn 12 which is synchronously moved is moved to the heating zone to heat the twisted polyester thread 12, so that the heating temperature when the twisted polyester thread 12 enters the heating zone is 140 ° C, and the twisted polyester thread 12 is removed from the heating zone. The heating temperature is 170 ° C, and the twisted polyester thread 12 is in a tension state when it passes through the heating zone, so that it is in a softened state;
另一方面,可以先将热塑性树脂原料放入双螺杆挤出机的料斗中,然后,进行挤出熔融,依次设定双螺杆挤出机的输送段温度为160℃~170℃;熔融段的温度为185℃~195℃;混炼段的温度为200℃~220℃和均化段的温度为225℃~235℃,同时,设定双螺杆挤出机的机头温度为245℃~255℃,得到熔融状态的热塑性树脂,使熔融状态的热塑性树脂处于双螺杆挤出机的口模处;对于熔融状态的热塑性树脂的加工过程在整体加工流水线 中可以是同步连续进行的;On the other hand, the thermoplastic resin raw material can be first placed in the hopper of the twin-screw extruder, and then extruded and melted, and the temperature of the conveying section of the twin-screw extruder is set to 160 ° C to 170 ° C in turn; The temperature is 185 ° C ~ 195 ° C; the temperature of the mixing section is 200 ° C ~ 220 ° C and the temperature of the homogenization section is 225 ° C ~ 235 ° C, at the same time, the head temperature of the twin-screw extruder is set to 245 ° C ~ 255 °C, a molten thermoplastic resin is obtained, so that the molten thermoplastic resin is placed in the die of the twin-screw extruder; the processing of the thermoplastic resin in the molten state is in the overall processing line Can be continuously and continuously;
然后再使经过加热处理后的软化状态的加捻涤纶线12再经过双螺杆挤出机中口模处的熔融状态的热塑性树脂,使熔融状态的热塑性树脂的粘度为0.75dL/g~0.95dL/g,使加捻涤纶线12与热塑性树脂复合为一体,再随着加捻涤线向前移动,从口模处的相应出口处移出,其中,出口的形状可以与压膜带的形状相对应,且使加捻涤纶线12包覆在熔融状态的热塑性树脂固化后形成的热塑性树脂层11内,并且形成扁平状的塑料压膜带1半成品,塑料压膜带1的厚度基本上略大于加捻涤纶线12的直径即可,然后,使塑料压膜带1半成品经过牵引机构后,先使塑料压膜带1半成品移动经过温度为40℃~60℃热水进行预冷却处理,再使其经过常温状态的水进行冷却处理,然后,再采用温度为40℃~60℃热风进行热定型处理,除去表面的水分风干,牵引机构之后的移动可以通过收卷机构上的收卷动力带动使压膜带半成品向前移动,得到相应的成品塑料压膜带1。得到的塑料压膜带1的破断强度为34.5MPa。Then, the heated polyester resin 12 in the softened state after the heat treatment is passed through the molten thermoplastic resin at the die in the twin-screw extruder to adjust the viscosity of the molten thermoplastic resin to 0.75 dL/g to 0.95 dL. /g, the twisted polyester thread 12 is compounded with the thermoplastic resin, and then moved away from the corresponding outlet at the die as the twisted polyester thread moves forward, wherein the shape of the outlet can be in the shape of the laminating strip Correspondingly, the twisted polyester thread 12 is coated in the thermoplastic resin layer 11 formed by curing the molten thermoplastic resin, and a flat plastic lamination tape 1 is formed, and the thickness of the plastic lamination tape 1 is substantially larger than The diameter of the polyester fiber 12 can be twisted. Then, after the plastic film tape 1 semi-finished product passes through the traction mechanism, the plastic film tape 1 semi-finished product is first moved through the hot water at a temperature of 40 ° C to 60 ° C for pre-cooling treatment, and then It is cooled by water at normal temperature, and then heat-set by hot air at a temperature of 40 ° C to 60 ° C to remove moisture from the surface, and the movement after the traction mechanism can pass through the winder. Rolling forces on the drive belt that the film is moved forward semifinished product to give the corresponding finished plastic film tape 1. The breaking strength of the obtained plastic laminated tape 1 was 34.5 MPa.
实施例6Example 6
本实施例的塑料压膜带1的具体制备方法同实施例5一致,这里不再赘述,区别仅在于,其中的热塑性树脂原料由以下质量百分比的成分制成:聚丙烯:30wt%;聚乙烯:40wt%;硅胶:30wt%。经过检测之后,本实施例得到的塑料压膜带的破断强度为34.4MPa。The specific preparation method of the plastic laminating tape 1 of the present embodiment is the same as that of the embodiment 5, and is not described herein again. The only difference is that the thermoplastic resin raw material is made of the following mass percentage components: polypropylene: 30 wt%; polyethylene 40% by weight; silica gel: 30% by weight. After the test, the breaking strength of the plastic laminated tape obtained in the present example was 34.4 MPa.
实施例7Example 7
本实施例的塑料压膜带1的具体制备方法同实施例1一致,这里不再赘述,区别仅在于,其中的热塑性树脂原料由以下质量百分比的成分制成:聚丙烯:35wt%;聚乙烯:30wt%;硅胶:35wt%。经过检测之后,本实施例得到的塑料压膜带的破断强度为34.00MPa。 The specific preparation method of the plastic laminating tape 1 of the present embodiment is the same as that of the embodiment 1, and will not be described herein again. The only difference is that the thermoplastic resin raw material is made of the following mass percentage components: polypropylene: 35 wt%; polyethylene : 30 wt%; silica gel: 35 wt%. After the test, the breaking strength of the plastic laminated tape obtained in the present example was 34.00 MPa.
实施例8Example 8
本实施例的塑料压膜带1的具体制备方法同实施例1一致,这里不再赘述,区别仅在于,其中的热塑性树脂原料由以下质量百分比的成分制成:聚丙烯:30wt%;聚乙烯:30wt%;硅胶:40wt%。经过检测之后,本实施例得到的塑料压膜带的破断强度为34.6MPa。The specific preparation method of the plastic laminating tape 1 of the present embodiment is the same as that of the embodiment 1, and will not be described herein again. The only difference is that the thermoplastic resin raw material is made of the following mass percentage components: polypropylene: 30 wt%; polyethylene : 30 wt%; silica gel: 40 wt%. After the test, the breaking strength of the plastic laminated tape obtained in the present example was 34.6 MPa.
实施例9Example 9
将涤纶丝进行加捻处理,即先采用若干涤纶单丝经过加捻处理,使形成规格为1100dtex/192f的单加捻涤纶线;可以使单加捻涤纶线的捻度为每米45捻度;然后,再采用6根单加捻涤纶线再次经过加捻处理,形成复合加捻涤纶线12,收卷成型,且复合的加捻涤纶线12的规格达到6000D的要求,使加捻涤纶线的捻度为每米45捻度;备用;The polyester yarn is twisted, that is, a plurality of polyester monofilaments are firstly twisted to form a single twisted polyester thread having a specification of 1100 dtex/192f; the twist of the single twisted polyester thread can be 45 degrees per meter; Then, six single twisted polyester threads are again subjected to twisting treatment to form a composite twisted polyester thread 12, which is formed by winding, and the composite twisted polyester thread 12 has a specification of 6000D, so that the twist of the polyester thread is increased. 45 degrees per meter; spare;
根据塑料压膜带1内设置加捻涤纶线12的根数,对应的选用相应卷数的上述收卷好的加捻涤纶线12放置在放卷起始处进行放卷,同时通过设置在后继过程上的牵引机构带动加捻涤纶线12向前移动,其中,牵引机构设置在包覆工序(加捻涤纶线12与热塑性塑料复合工序)与冷却处理之间,本实施例中选用塑料压膜带1内包覆有8根沿着压膜带长度方向呈平行设置的加捻涤纶线12;According to the number of twisted polyester threads 12 disposed in the plastic laminating tape 1, the correspondingly wound twisted polyester thread 12 of the corresponding number of rolls is placed at the beginning of unwinding for unwinding, and at the same time by setting in the successor The traction mechanism in the process drives the twisted polyester thread 12 to move forward, wherein the traction mechanism is disposed between the coating process (the twisting process of the twisted polyester thread 12 and the thermoplastic compound) and the cooling process, and the plastic film is selected in the embodiment. The belt 1 is covered with 8 twisted polyester threads 12 arranged in parallel along the length of the lamination belt;
具体来说,使8根平行且在同一平面上的加捻涤纶线12在上述牵引机构的牵引力作用下向前移动,使加捻涤纶线12的移动速度为15m/s(也就是相当于牵引速度),移动的过程中可以根据需要在中途设有多个引导机构,有利于使加捻涤纶线12始终处于较张紧的状态,然后,使同步行进的加捻涤纶线12移动到加热区间对加捻涤纶线12进行加热处理,使加捻涤纶线12进入加热区间时的加热温度为140℃,且使加捻涤纶线12移出加热区间时的加热温度为170℃,在加热区间的进口与出口之间还可以设置中间 加热温度150℃,使加捻涤纶线12经过加热区间时呈逐步加热的过程,有利于更均匀的受热,且能够有效除去毛丝或毛边的现象,同时,使加捻涤纶线12经过加热区间时处于张紧状态,可以设置张紧机构,使加捻涤纶线12经过张紧机构达到张紧状态,使处于软化状态;Specifically, the eight twisted polyester threads 12 which are parallel and in the same plane are moved forward by the traction force of the above-mentioned traction mechanism, so that the moving speed of the twisted polyester thread 12 is 15 m/s (that is, equivalent to traction Speed), in the process of moving, a plurality of guiding mechanisms can be provided in the middle according to the need, which is beneficial to keep the twisted polyester thread 12 in a relatively tight state, and then move the twisted polyester thread 12 which is synchronously moved to the heating section. The twisted polyester thread 12 is heat treated so that the heating temperature when the twisted polyester thread 12 enters the heating zone is 140 ° C, and the heating temperature when the twisted polyester thread 12 is removed from the heating zone is 170 ° C, the inlet in the heating zone It can also be set between the exit and the exit. The heating temperature is 150 ° C, so that the twisted polyester thread 12 is gradually heated during the heating interval, which is beneficial to more uniform heating, and can effectively remove the phenomenon of hair or burrs, and at the same time, the twisted polyester thread 12 is heated. When the tension is in a state of tension, a tensioning mechanism can be provided to cause the twisted polyester thread 12 to be tensioned by the tensioning mechanism to be in a softened state;
另一方面,可以先将热塑性树脂原料放入双螺杆挤出机的料斗中,然后,进行挤出熔融,依次设定双螺杆挤出机的输送段温度为160℃;熔融段的温度为195℃;混炼段的温度为220℃和均化段的温度为235℃,同时,设定双螺杆挤出机的机头温度为245℃,得到熔融状态的热塑性树脂,使熔融状态的热塑性树脂处于双螺杆挤出机的口模处;对于熔融状态的热塑性树脂的加工过程在整体加工流水线中可以是同步连续进行的;上述的热塑性树脂原料由以下质量百分比的成分制成:聚丙烯:30wt%;聚乙烯:35wt%;硅胶:35wt%。On the other hand, the thermoplastic resin raw material can be first placed in the hopper of the twin-screw extruder, and then extruded and melted, and the temperature of the conveying section of the twin-screw extruder is set to 160 ° C in turn; the temperature of the melting section is 195. °C; the temperature of the mixing section is 220 ° C and the temperature of the homogenization section is 235 ° C. At the same time, the head temperature of the twin-screw extruder is set to 245 ° C to obtain a thermoplastic resin in a molten state, and the thermoplastic resin in a molten state is obtained. At the die of the twin-screw extruder; the processing of the thermoplastic resin in the molten state can be carried out synchronously and continuously in the entire processing line; the above-mentioned thermoplastic resin raw material is made of the following mass percentage components: polypropylene: 30 wt %; polyethylene: 35 wt%; silica gel: 35 wt%.
然后再使经过加热处理后的软化状态的加捻涤纶线12再经过双螺杆挤出机中口模处熔融状态的热塑性树脂,使加捻涤纶线12与热塑性树脂复合为一体,再随着加捻涤线12向前移动,从口模处的相应出口处移出,其中,出口的形状可以与塑料压膜带的形状相对应,使加捻涤纶线12包覆在熔融状态的热塑料性树脂固化后形成的热塑性树脂层11内,并且形成扁平状的塑料压膜带1半成品,塑料压膜带1的厚度基本上略大于加捻涤纶线12的直径即可,然后,使塑料压膜带1半成品经过牵引机构后,先使塑料压膜带1半成品移动经过温度为40℃~60℃热水进行预冷却处理,再使其经过常温状态的水进行冷却处理,然后,再采用温度为40℃~60℃热风进行热定型处理,除去表面的水分风干,得到相应的成品塑料压膜带1,牵引机构之后的移动可以通过收卷机构上的收卷动力带动使塑料压膜带1半成品向前移动。经过检测之后,本成品大棚压膜带的破断强度为34.3MPa。 Then, the twisted polyester yarn 12 in the softened state after the heat treatment is passed through a thermoplastic resin in a molten state in the die of the twin-screw extruder, so that the twisted polyester thread 12 is compounded with the thermoplastic resin, and then added. The polyester filament 12 moves forward and is removed from the corresponding outlet at the die, wherein the shape of the outlet can correspond to the shape of the plastic laminating tape, and the twisted polyester thread 12 is coated with the thermoplastic resin in a molten state. After curing, the thermoplastic resin layer 11 is formed, and a flat plastic laminating tape 1 semi-finished product is formed. The thickness of the plastic laminating tape 1 is substantially larger than the diameter of the twisted polyester fiber 12, and then the plastic lamination tape is After the semi-finished product passes through the traction mechanism, the plastic film lamination 1 semi-finished product is firstly moved through the hot water with a temperature of 40 ° C to 60 ° C for pre-cooling treatment, and then subjected to cooling treatment by water at a normal temperature state, and then the temperature is 40. The hot air is heated at °C~60°C to remove the moisture from the surface, and the corresponding finished plastic laminating tape 1 is obtained. After the traction mechanism, the movement can pass through the winding power belt on the winding mechanism. Move the plastic laminating tape 1 semi-finished product forward. After the test, the breaking strength of the finished film laminating tape is 34.3 MPa.
实施例10Example 10
本实施例中的大棚薄膜的具体制作方法如下:The specific manufacturing method of the greenhouse film in this embodiment is as follows:
先按照实施例9的方法加工制备得到相应的塑料压膜带,再按照实施例3的方法将塑料压膜带1与PE塑料薄膜2热复合为一体,最终得到相应的大棚薄膜。First, the corresponding plastic laminating tape was processed according to the method of Example 9, and the plastic laminating tape 1 and the PE plastic film 2 were thermally composited in the same manner as in the third embodiment, and finally the corresponding greenhouse film was obtained.
本发明中所描述的具体实施例仅是对本发明精神作举例说明。本发明所属技术领域的技术人员可以对所描述的具体实施例做各种各样的修改或补充或采用类似的方式替代,但并不会偏离本发明的精神或者超越所附权利要求书所定义的范围。The specific embodiments described in the present invention are merely illustrative of the spirit of the invention. A person skilled in the art can make various modifications or additions to the specific embodiments described or in a similar manner, without departing from the spirit of the invention or as defined by the appended claims. The scope.
尽管对本发明已作出了详细的说明并引证了一些具体实施例,但是对本领域熟练技术人员来说,只要不离开本发明的精神和范围可作各种变化或修正是显然的。 While the invention has been described in detail and shown in the embodiments of the embodiments

Claims (11)

  1. 一种大棚薄膜的制作方法,其特征在于,该方法包括以下步骤:A method for manufacturing a greenhouse film, characterized in that the method comprises the following steps:
    使若干条塑料压膜带(1)与塑料薄膜(2)在牵引力的作用下依次向着每道工序同步移动,所述若干条塑料压膜带(1)均呈平行设置,且所述塑料压膜带(1)呈扁平状,使每条塑料压膜带(1)均与塑料薄膜(2)经过热复合工序进行热复合处理,且使每条塑料压膜带(1)侧的加热温度为220℃~240℃;使每条塑料薄膜(2)侧的加热温度为160℃~190℃,使每条塑料压膜带(1)均与塑料薄膜(2)热复合为一体后,再向下一道工序牵引移动,使经过冷却处理,得到相应的大棚薄膜。The plurality of plastic laminating tapes (1) and the plastic film (2) are sequentially moved synchronously toward each process under the action of the traction force, and the plurality of plastic laminating tapes (1) are arranged in parallel, and the plastic pressing is performed. The film strip (1) is flat, so that each plastic laminating strip (1) is thermally composited with the plastic film (2) through a thermal lamination process, and the heating temperature of the side of each plastic laminating strip (1) is made. It is 220 ° C ~ 240 ° C; the heating temperature of each plastic film (2) side is 160 ° C ~ 190 ° C, so that each plastic laminating tape (1) is thermally combined with the plastic film (2), and then Pulling the movement in the next process, after cooling, the corresponding greenhouse film is obtained.
  2. 根据权利要求1所述大棚薄膜的制作方法,其特征在于,每条塑料压膜带(1)侧的加热温度采用长条状的加热块进行加热,且所述长条状的加热块贴合在每条塑料压膜带(1)的表面;所述塑料薄膜(2)侧的加热温度采用圆柱状的加热辊或长条状的加热块进行加热,且所述圆柱状的加热辊或长条状的加热块贴合在所述塑料薄膜(2)的表面;所述长条状的加热块的加热面与所述圆柱状的加热辊或长条状的加热块的加热面相靠近,且能够使每条塑料压膜带(1)均与塑料薄膜(2)热复合为一体。The method for producing a greenhouse film according to claim 1, wherein the heating temperature on the side of each of the plastic film strips (1) is heated by a long heating block, and the strip-shaped heating block is attached On the surface of each plastic lamination tape (1); the heating temperature on the side of the plastic film (2) is heated by a cylindrical heating roller or a long heating block, and the cylindrical heating roller or long a strip-shaped heating block is attached to the surface of the plastic film (2); the heating surface of the elongated heating block is close to the heating surface of the cylindrical heating roller or the elongated heating block, and It is possible to thermally combine each of the plastic laminating strips (1) with the plastic film (2).
  3. 根据权利要求2所述大棚薄膜的制作方法,其特征在于,所述长条状的加热块贴合在每条塑料压膜带(1)的加热面的宽度与相应塑料压膜带(1)的宽度相同。The method for manufacturing a greenhouse film according to claim 2, wherein the strip-shaped heating block is attached to the width of the heating surface of each plastic laminating tape (1) and the corresponding plastic laminating tape (1) The width is the same.
  4. 根据权利要求2或3所述大棚薄膜的制作方法,基特征在于,所述长条状的加热块的长度为15cm~20cm。The method for producing a greenhouse film according to claim 2 or 3, characterized in that the length of the elongated heating block is 15 cm to 20 cm.
  5. 根据权利要求2或3所述大棚薄膜的制作方法,其特征在于,当所述每条塑料压膜带(1)与塑料薄膜(2)通过长条状的加热块与圆柱状的加热辊或长条状的加热块之间时,使所述每条塑料压膜带(1)与塑料薄膜(2)在牵引力的作用下均沿着竖直方向移动。 The method for manufacturing a greenhouse film according to claim 2 or 3, wherein each of the plastic laminating tapes (1) and the plastic film (2) passes through a long heating block and a cylindrical heating roller or When the strips are between the heating blocks, each of the plastic laminating tapes (1) and the plastic film (2) are moved in the vertical direction under the action of the traction force.
  6. 根据权利要求1所述大棚薄膜的制作方法,其特征在于,所述每条塑料压膜带(1)与塑料薄膜(2)同步移动的牵引速度均为10米/秒~15米/秒。The method for manufacturing a greenhouse film according to claim 1, wherein the pulling speed of each of the plastic laminating tapes (1) and the plastic film (2) is 10 m/sec to 15 m/sec.
  7. 根据权利要求1所述大棚薄膜的制作方法,其特征在于,所述塑料压膜带(1)采用以下方法制备得到:The method for fabricating a greenhouse film according to claim 1, wherein the plastic laminating tape (1) is prepared by the following method:
    A、使若干平行且在同一平面上的加捻涤纶线(12)在牵引力的作用下向前移动,然后,使加捻涤纶线(12)经过加热区间进行加热处理使处于软化状态;A. moving a plurality of twisted polyester threads (12) parallel and on the same plane forward by the traction force, and then heating the twisted polyester thread (12) through the heating zone to be in a softened state;
    B、再使加捻涤纶线(12)经过熔融状态的热塑性树脂,使加捻涤纶线(12)与熔融状态的热塑性树脂复合为一体,且使加捻涤纶线(12)包覆在熔融状态的热塑性树脂固化后形成的热塑性树脂层(11)内,形成扁平状的压膜带半成品,再使压膜带经过冷却处理,得到相应的成品塑料压膜带1。B. The twisted polyester thread (12) is subjected to a molten thermoplastic resin, and the twisted polyester thread (12) is integrated with the molten thermoplastic resin, and the twisted polyester thread (12) is coated in a molten state. In the thermoplastic resin layer (11) formed by curing the thermoplastic resin, a flat semi-finished film is formed, and the laminating tape is subjected to a cooling treatment to obtain a corresponding finished plastic laminating tape 1.
  8. 根据权利要求7所述大棚薄膜的制作方法,其特征在于,步骤A中所述加热处理的温度为140℃~170℃。The method for producing a greenhouse film according to claim 7, wherein the temperature of the heat treatment in the step A is from 140 ° C to 170 ° C.
  9. 根据权利要求8所述大棚薄膜的制作方法,其特征在于,步骤A中所述加热处理时使加捻涤纶线(12)处于张紧状态。The method for producing a greenhouse film according to claim 8, wherein the twisted polyester thread (12) is in a tensioned state during the heat treatment in the step A.
  10. 根据权利要求7-9任意一项所述大棚薄膜的制作方法,其特征在于,步骤B中所述熔融状态的热塑性树脂中含有硅胶,且硅胶占熔融状态的热塑性树脂质量的百分比为30wt%~40wt%。The method for producing a greenhouse film according to any one of claims 7 to 9, wherein in the step B, the molten thermoplastic resin contains silica gel, and the percentage of the mass of the thermoplastic resin in the molten state is 30% by weight. 40wt%.
  11. 根据权利要求9所述大棚薄膜的制作方法,其特征在于,步骤B中所述熔融状态的热塑性树脂主要由以下质量百分比的成分制成:The method for producing a greenhouse film according to claim 9, wherein the molten thermoplastic resin in the step B is mainly made of the following mass percentage components:
    聚丙烯:30wt~40wt%;聚乙烯:30wt~40wt;硅胶:30wt~40wt。 Polypropylene: 30 wt to 40 wt%; polyethylene: 30 wt to 40 wt; silica gel: 30 wt to 40 wt.
PCT/CN2016/095911 2016-06-29 2016-08-18 Method for fabricating greenhouse film WO2018000552A1 (en)

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