KR102022023B1 - Method and system manufacturing double extrusion panel for construction - Google Patents

Abstract

The present invention relates to a double extrusion molding device of a synthetic resin, raw material blending feeder → primary and secondary extruder → primary die → primary sizing → primary vacuum cooler → primary water cooling device → air injection device → 1 Primary drawer → heating chamber → 3rd and 4th extruder → 2nd die → 2nd sizing → 2nd vacuum cooler → 2nd water cooler → 2nd draw molding machine → Cutter process Extrude the inner body of the synthetic resin and extruding it so that the outer body of the new synthetic resin is polymerized on the outer surface of the inner body, and again forms a waste synthetic resin layer on the new synthetic resin layer, and forms a waste synthetic resin layer on the new synthetic resin layer. The present invention relates to an apparatus and method for manufacturing a composite extruded panel for building to enable molding of multiple extruded panels having improved strength and durability.

Description

Composite Extrusion Panel Manufacturing Apparatus and Method for Construction {METHOD AND SYSTEM MANUFACTURING DOUBLE EXTRUSION PANEL FOR CONSTRUCTION}

The present invention relates to a double extrusion molding apparatus for synthetic resins that can be used as exterior panels for panels, flooring, container flooring, pedestals of logistics loading floors, flooring of aviation and ships, floors of loading boxes for trucks and the like.

More specifically, the first step of extruding the inner body of the waste synthetic resin, and the second extruding to polymerize the outer body of the new synthetic resin on the inner surface of the second synthetic resin, and again to form a waste synthetic resin layer on the new synthetic resin layer and a new synthetic resin layer on the waste synthetic resin layer It is possible to form multiple extruded panels formed by improving the strength and durability for impact absorption.

In addition, the present invention is to recycle the synthetic resin panel of various forms using waste plastic and waste plastic generated in farming and fishing villages or waste synthetic resin and waste plastic generated in industrial sites, etc. A construction double extrusion panel manufacturing apparatus and method for preventing contamination.

In modern society, various kinds of household goods and industrial goods are newly introduced and delivered to consumers as the industry develops.In particular, exaggerated packaging vinyl, food packaging vinyl, and mulching vinyl used for farming crops in farming and fishing villages are processed. It is one of the most problematic items in the world.

As of 2016, waste plastics, waste synthetic resins, and styrofoam are so low that they do not collect vehicle plastics at collection companies, and they do not collect waste plastics from apartments.

On the other hand, logging is extremely limited in the world, and plastic and synthetic resin products are increasing year by year, and all are used as new materials.

In particular, building materials, civil engineering materials, such as the supply of wood is reduced to meet the demand, the situation is replaced by synthetic resin products, there is a problem that the elasticity, tensile strength, such as wood falls.

  In addition, in order to have durability against impact absorption when molding products using existing waste synthetic resins, there is a problem in that the efficiency of waste synthetic resins is decreased by producing a single product by mixing PVC raw materials with waste synthetic resins, and in particular, conventional waste synthetic resins. In order to produce a molded product using the waste to wash the soil on the collected synthetic resin and then to dry it again because the initial screening work is done by hand manually, there was a problem of managing labor costs as well as people.

Therefore, products recycled using waste synthetic resins cannot be activated in building products and civil engineering products, and very few wastes are mainly used in waste water pipes, sewage pipes, etc., and the remaining wastes are incinerated, thereby increasing the waste disposal cost.

Looking at the prior art in this field, Patent Application Publication No. 10-0789957 (Registration Date: December 21, 2007) "apparatus and method for producing a double extrusion panel using waste synthetic resin" (hereinafter referred to as "prior art") In a manufacturing apparatus for extruding a building member or flooring material using waste synthetic resin, a raw material for mixing raw materials of recycled PE and wood flour, rice hull, vermiculite, glass fiber and foamed material, which are pulverized by a conventional pulverizing device for collecting waste plastic waste vinyl. A mixer 1;

When the raw materials mixed in the raw material mixer 1 are supplied to the hoppers 3 and 3 ', the raw materials are melted by the plate heaters 4 and 4' wound on the outer surface at regular intervals, and the transfer screw 5 ( A first extruder 2 and a second extruder 2 'extruded to the head 6, 6' side by 5 '); The raw material extruded from the head portion 6 of the first extruder 2 is formed by the inner body 8, and the raw material extruded from the head portion 6 ′ of the second extruder 2 ′ is extruded from the outer body 9. A dual extrusion molding machine 7 formed of a plurality of rectangular blocks to form a synthetic resin panel 30 by adjusting the inflow amount of the outer body 9 with a plurality of control bolts 20 horizontally installed on upper and lower surfaces thereof;

A vacuum machine 12 for vacuuming the surface of the synthetic resin panel 30 formed by the double extrusion machine 7 made of the plurality of rectangular blocks is smoothly installed inside the front surface and a plurality of guides 16 on one side of the vacuum machine. A cooler 11 installed with a coolant to fill the coolant;

A drawer (17) having rollers (18) formed on both sides of the cooler (11) to draw and pull out the cured synthetic resin panel (30); Disclosed is an apparatus for producing a double extrusion panel using waste synthetic resin, characterized in that the cutter 19 is configured to cut the synthetic resin panel 30 withdrawn from the extractor 17 while moving a circular saw to a predetermined length.

In the prior art, since the supply of raw materials supplied to the dies is extruded to extrude the inner and outer bodies, a myriad of air layers are formed in the inner body, which is a waste synthetic resin, and the dies are extruded through the dies in a gel-like state. The thickness of the discharged synthetic resin panel is not uniform, and there is a problem in that the seam is generated by partially agglomeration.

In particular, the prior art includes a large amount of air layers because the waste synthetic resin material is supplied to the die in the molten state in the extruder, and the panel extruded from the die is pulled from the sizing to the vacuum due to the coexistence of the dense and unstructured parts of the tissue. In this process, a large amount of air layer is formed and in this process, since the structure is not uniform, the cooling density after vacuum is different, so that the shrinkage density is different. There is a problem.

In other words, even if the inner synthetic waste resin is melted in the extruder, it does not become a liquid state like a new synthetic resin but is formed like a rice cake, and a core is formed during extrusion, and the extrusion speed is slow.

These waste synthetic resins are not melted over a certain concentration even when heated and melted in an extruder, but are burned when the temperature is raised, so they have different physical properties from new synthetic resins. When moving to the extruded into a die by the extrusion force of the extruder in the same state as the lumpy rice cakes, there is a problem that the seam is different from the air layer and the melting point.

The prior art in this field described above is, in addition to the prior art, Patent Registration No. 10-1068947, Patent Registration No. 10-1166899, Patent Registration No. 10-0534050, Patent Registration No. 10-0645935, and the like. There is this. However, the above-listed prior arts also have the same problems described above, so that the production is not continuously made, and in particular, the prior art and the conventional double-extrusion panel forming apparatus using waste synthetic resins have the inner body as the waste synthetic resin and the outside. By using the sieve as a new material to be combined in one die (extrusion mold) to extrude, there is a problem that the extrusion speed is too slow to significantly reduce the productivity of the double extrusion panel.

Republic of Korea Patent Publication No. 10-0789957

The present invention is to solve the above problems, the waste synthetic resin is melted in the extruder to repeat the operation kneading the molten waste synthetic resin when moving in the die to remove the air layer formed in the molten waste synthetic resin and densely structure the resin The purpose of the present invention is to improve the durability of the molded synthetic resin extrusion panel and to minimize defects.

For another purpose, the inner body is made of waste synthetic resin and waste vinyl, and the outer body is made of new materials to enhance the product's appearance by enhancing the appearance of the product and improve elasticity and strength.

In addition, it aims to provide environmentally friendly products that can prevent environmental pollution and reduce waste disposal costs by collecting waste plastics raised as environmental pollution in farming and fishing villages and plastic bags produced in cities. It is done.

 In another aspect, the present invention is to provide a device and method for manufacturing a double extrusion panel for construction aimed at reducing the cost as well as the use of wood by providing a panel made of waste synthetic resin of the inner body and a new material of the outer body as building materials and civil engineering materials. It is about.

A raw material blending feeder 2 which mixes waste synthetic resin raw materials or new synthetic resin raw materials to supply raw materials to the hopper of the primary extruder 13 or the secondary extruder 14;
Primary and secondary extruders (13) and (14) for melting and receiving waste synthetic resin raw materials and new synthetic resins received from the raw material blending feeder from a hopper; After the melted from the primary extruder to the inner synthetic waste material supplied through the feed channel, and the inner side of the second synthetic extruder to melt the synthetic resin supplied through the raw material conveying path to form a double synthetic resin extrusion panel Primary dice 17; A hole forming rod (27) for forming a plurality of holes in the double synthetic resin extrusion panel discharged from the primary die; A primary sizing (21) for forming a flat and smooth outer surface of the panel by vacuum forming a double synthetic resin extrusion panel in which a plurality of holes are formed by the hole forming rods; A primary water cooler 35 for fixing and cooling the shape of the extruded panel smoothed from the primary sizing and a primary water cooler 35 for cooling the extruded panel cooled in the primary vacuum cooler; A primary drawer 37 for pulling and transporting the extruded panel cooled by the water chiller; Tertiary and quaternary extruders (39) (40) connected to secondary dies (41) for supplying resin such that a waste synthetic resin and a new synthetic resin layer are formed on an outer surface of the extruded panel which is pulled from the primary extractor; Secondary dice 41 for adhering the waste synthetic resin and the new synthetic resin supplied from the third and fourth extruders and the extrusion panel to extrude into a multilayer panel; A secondary sizing (42) for vacuuming flat and smoothly the extruded panel formed in multiple layers in said secondary dice; Secondary water cooler 44 for cooling the multi-layered extruded panel cooled by the secondary vacuum cooler 43 and the secondary vacuum cooler 43 to fix the shape of the multilayer extrusion panel smoothed from the secondary sizing 44 )Wow; A draw cooler 45 for pulling and conveying the multi-layered extruded panel cooled by the secondary water cooler and simultaneously cooling the mold; In the building composite extrusion panel manufacturing apparatus comprising a cutter for cutting the multilayer extrusion panel drawn out by the draw-cooling molding machine to a predetermined standard and a banding machine for bending the cut multilayer extrusion panel with a predetermined longevity,
The composite composite panel manufacturing apparatus for construction,
The primary die and the hemispherical protrusions 20 formed in the number of the inner extrusion portion to be kneaded by the waste synthetic resin to flow when inflow;
An air injector (36) for removing water from the surface of the extrusion panel cooled by the primary water cooling device (35);
A heating chamber 38 for drying the moisture of the extruded panel transferred from the primary extractor 37 which pulls the extruded panel from which the water is removed from the air injector, and softens the surface thereof;
The primary sizing 21 and the secondary sizing 42 are inclined portion (C) formed in the upper and lower portions of the inlet;

delete

delete

delete

delete

delete

delete

delete

delete

delete

delete

delete

delete

delete

delete

The raw material blending feeder is connected to the raw material feed hopper and the raw material blending feeder main body installed on one side to the raw material supply conveyor, the conveyor drive motor is installed on the upper end of the raw material supply conveyor, the stirring shaft formed with a stirring blade in the center of the raw material blending feeder main body It is installed vertically to agitate the raw material and a motor for rotating the stirring shaft is installed on the top of the stirring shaft, a heater device having a hot air supply fan is installed on one side of the raw material blending feeder to dry the raw material inside the body with hot air It is configured to be.

The primary die is characterized in that it is possible to knead repeatedly the kneading operation when the waste synthetic resin is introduced into a plurality of hemispherical protrusions are formed therein.

The first and second dice are characterized in that a plurality of air vents are formed in the upper and lower portions.

 The primary die is composed of a plurality of rectangular blocks, and the inside of the primary die is connected to a primary extruder for extruding waste synthetic resin with a plurality of hemispherical protrusions formed therein. Waste extruded resin is supplied to the extruder, and the secondary extruder is connected to another new synthetic resin transfer path of the primary die, and the extruded portion of the primary die has a double overlapped waste synthetic resin and a new synthetic resin, and is connected to the mold die outlet connected to the front side. It is characterized by being extruded.

The primary vacuum cooler and the secondary vacuum cooler is formed in the upper and lower cooling forming plant and the upper cooling forming plant is connected to the cylinder to move up and down, the upper and lower cooling forming plant is characterized in that a plurality of vacuum holes are formed .

The take-out cooling molding machine is characterized in that a plurality of take-out rollers are formed on both sides, and a cold forming machine is installed at a central portion between the take-out roller and the take-out roller to draw and cool the extruded panel.

The primary sizing and the secondary sizing inlet is characterized in that the inclined portion formed by the front light narrow (前 廣 後 俠).

The first die and the second die are characterized in that the mold die outlet of the rear is formed in a convex curved shape with a larger central diameter than both sides diameter size,

The first vacuum cooling molding machine and the second vacuum cooling molding machine are characterized in that the inclined surface is formed in the upper and lower inlet.

The present invention as described above is first formed by extruding the primary panel consisting of the inner body of the waste synthetic resin and the outer body of the new synthetic resin, and the second inner body of the waste synthetic resin and the outer body of the new synthetic resin on the outer surface of the primary panel is laminated and polymerized By forming the synthetic resin panel for building, the strength and durability of the synthetic resin panel can be improved and the exterior of the panel can be provided with a beautiful product.

First, the present invention is to repeat the operation of kneading the molten waste synthetic resin in the process of melting the waste synthetic resin in the extruder to move in the die to remove the air layer formed in the molten waste synthetic resin and densify the structure of the resin panel of the synthetic resin panel It has the effect of improving durability and minimizing product defects,

Second, the inner body of the present invention is made of waste synthetic resin, waste vinyl, and the outer body has the effect of enhancing the productability by enhancing the appearance of the product by using a new material to enhance the merchandise and strength.

Third, the present invention is to collect the waste plastic and the plastic bag produced in the city as the environmental pollution of the farming and fishing villages used as the inner body to prevent environmental pollution and reduce the waste disposal cost effect of providing an environmentally friendly product Has,

 Fourth, the present invention provides a multi-layer panel with the inner synthetic waste plastic and the outer composite as a new synthetic resin as a building material and civil engineering material can be used repeatedly compared to the wood to reduce the cost as well as to replace the forest It has the effect of protecting resources.

1 shows a conventional synthetic resin double panel manufacturing apparatus,
Figure 2 shows a process-specific system for the building composite extrusion panel manufacturing apparatus of the present invention,
Figure 3 shows the raw material blending feeder of the present invention,
Figure 4 is a front configuration diagram showing a primary extruder or a secondary extruder of the present invention,
5 is a plan view showing a primary extruder or a secondary extruder of the present invention,
Figure 6 shows a longitudinal section of the primary die for molding the resin extruded in the primary extruder and the secondary extruder of the present invention into a primary extrusion panel,
Figure 7 shows a front view of the third or fourth extruder according to the present invention,
8 shows a plan view of a third or fourth extruder according to the present invention,
FIG. 9 is a longitudinal sectional view of a secondary die in which the waste synthetic resin and the new synthetic resin supplied from the third and fourth extruders of the present invention are over-extruded on the outer surface of the primary extrusion panel formed from the primary die.
10 is a schematic view showing a connection state in which the primary extrusion panel extruded from the primary die of the present invention is extruded in multiple layers from the secondary die,
11 is a step-by-step view of the primary panel shape extruded from the primary die and the secondary panel shape formed from the secondary die of the present invention,
12 is a cross-sectional view showing a plurality of hemispherical protrusions formed inside the primary die according to the present invention;
Figure 13 shows the primary sizing cross-sectional configuration to form a plurality of holes in the inner body by installing a hole forming rod between the primary die and the primary sizing according to the present invention,
Figure 14 shows a primary vacuum cooler according to the present invention,
Figure 15 shows an upper plate of the primary or secondary vacuum cooler of the present invention,
Figure 16 shows an upper plate of a vacuum cooler as another embodiment of the present invention,
17 is a configuration diagram showing a vacuum cooling plate bottom vacuum hole according to the present invention;
18 shows a secondary vacuum cooler of the present invention,
19 is a front view showing a draw cooling molding machine for drawing out a synthetic resin multilayer panel according to the present invention;
20 is a side view showing the configuration of the take-out roller of the dispenser according to the present invention,
Figure 21 shows a synthetic resin multiple extrusion panel cutter of the present invention,
Figure 22 shows a synthetic resin double extrusion panel extruded from the primary die of the present invention,
Figure 23 shows a synthetic resin extrusion panel extruded from the secondary die of the present invention,
24 is a cross-sectional view showing a state in which a hole forming rod is installed in a primary die as another embodiment of the present invention;
FIG. 25 shows an embodiment of the longitudinal cross-sectional view of FIG. 24;
Figure 26 shows a synthetic resin multilayer panel extruded through the primary and secondary dice of the present invention.

Hereinafter, an embodiment of the present invention will be described in detail.

The present invention relates to a wood substitute building plywood synthetic resin panel having a multilayer structure in which the inner body (A) molded from waste synthetic resin raw materials and the outer body (B) composed of new synthetic resin raw materials are repeatedly polymerized as described above.

In particular, the present invention is to improve the durability by enhancing the productivity efficiency and die air discharge, synthetic resin panel structure emerged as a problem in the conventional double extrusion panel using waste synthetic resin.

It looks at the manufacturing step by step according to the synthetic resin extrusion apparatus 1 having a multilayer structure of the present invention.

Step 1: blending and supplying raw materials

The raw materials used in the present invention are largely classified into two types. It is divided into waste synthetic resin constituting the inner body (A) and new synthetic resin raw material constituting the outer body (B).

The inner body (A) is a waste synthetic resin, made of mulching vinyl and confectionery plastic bags and waste synthetic resin generated after crop cultivation in farming and fishing villages, the outer body (B) is made of new synthetic resin.

Waste vinyl or waste synthetic resin, which is a raw material of the inner body (A) of the present invention, is collected and used as it is, even if soil or wood chips are mixed, without undergoing a separate washing process.

Waste synthetic resin and waste vinyl are dried, collected and pulverized to form a raw material. The waste synthetic resin material thus prepared is dried by hot air blowing from the heat supply fan 8 of the heater device 7 in the raw material blending feeder 2, and then the primary extruder 13 by the discharge conveyor 6. Is supplied.

At this time, in another raw material blending feeder 2, a new synthetic resin raw material is prepared and supplied to the second extruder.

The raw material blending feeder 2 for supplying the waste synthetic resin described in the present invention to the primary extruder 13 and the raw material blending feeder 2 for supplying the new synthetic resin to the secondary extruder 14 are each provided in the same configuration. .

The raw material blending feeder 2 is provided with a mixing hopper 12 provided on one side thereof, and the mixing hopper 12 and the raw material blending feeder 2 are provided with a feeding conveyor 3 and mixed in the mixing hopper 12. The raw material is supplied to the raw material blending feeder 2 by the supply conveyor 3.

The raw material blending feeder (2) is connected to the mixing hopper 12 and the raw material blending feeder (2) main body installed on one side to the raw material feed conveyor (3) and the conveyor drive motor (4) on top of the raw material feed conveyor (3) Installed to drive the feed conveyor (3).

In the center of the main body mixing feeder (2) the main body 11 is provided with a stirring shaft (9) having a stirring blade (10) is installed vertically to enable the stirring of the raw material and the drive motor (11) to rotate the stirring shaft on the stirring shaft (9) ) Is installed.

A heater device 7 having a hot air supply fan 8 is installed at one side of the raw material blending feeder 2 so as to dry the raw material inside the main body with hot air.

The hot air discharged from the heater device 7 is discharged to the inner lower portion of the raw material blending feeder to dry the raw material supplied from the discharge conveyor 6 to each extruder side to remove moisture and the like.

The raw material thus dried is supplied to the primary extruder 13 or the secondary extruder 14 by the discharge conveyor 6.

The raw material discharging conveyor 6 and the raw material supply conveyor 3 are respectively provided with a conveyor driving motor 4, 5 at the top thereof to drive a screw-shaped conveyor to transfer raw materials.

In addition, the mixing hopper 12 provided at one side of the raw material blending feeder 2 is horizontally provided with a stirring blade rotated by a motor at the lower end to stir the raw material contained in the hopper to be supplied to the supply conveyor 3.

Second Process: Raw Material Extrusion Step

The raw material blending feeder 2 is provided in plural, and the raw material blending feeder 2 on one side sends the melted raw synthetic resin material to the primary extruder 13 to melt, and the other raw material blending feeder 2 (shown separately) (Not shown) is sent to the secondary extruder 14 and melted.

The extruder used in the present invention uses an extruder to melt-extrude the synthetic resin, and the control unit is configured to electrically control the driving unit and the heater on one side, and a hopper is formed in the raw material input unit of the extruder, and the synthetic resin introduced from the hopper is transferred. A conveying screw is provided, and a plate-shaped heating device is installed on the outer surface of the screw so as to melt the synthetic resin raw material conveyed by the conveying screw.

The plate heating apparatus installed in each extruder is installed in proportion to the screw length of the extruder, but the heating temperature of the heating apparatus is installed to set the temperature differently for each section. The outer surface of the heating device installed as described above is formed so that a safety accident of the operator is not formed by the cover.

The extruder used in this process is provided with a primary extruder 13 and a secondary extruder 14, the primary extruder 13 to melt the waste synthetic resin to be supplied to the primary die 17, the secondary The extruder 14 can supply the primary die 17 to melt and stack the new synthetic resin.

The primary dice 17 and the secondary dice described later are provided so that the waste synthetic resin raw material and the new synthetic resin raw material can be supplied from the discharge conveyor 6 from each raw material blending feeder.

Third Step: Double Extrusion of Primary Synthetic Resin into Primary Die

The waste synthetic resin introduced from the primary extruder 13 is introduced into the primary die 17 through a transfer path 18 formed on the rear surface of the primary die 17.

The primary die 17 has a transfer path 18 formed on the front surface so that the primary die 17 can be divided into three in one passage.

That is, the discharge port of the primary extruder 13 and the front inlet transfer path 18 of the primary die 17 are connected, and the transfer path 18 thereof is formed as one inlet to the die inner extrusion part 15. The inflow portion is formed to be divided into three inflows.

 In this way, the inlet of the first die 17 connected to the outlet of the primary extruder 13 is introduced into one of the conveying paths 18 and then divided into three pieces. Even though the waste synthetic resin is melted, it is in the form of a rice cake like flour dough. Since the extrusion speed of the panel flows into one passage at the same time, the extrusion speed of the panel is slow and at the same time the primary die 17 is filled with the inner extrusion part 15 so that the extrusion force is received only at the center part during extrusion. There is a problem that different pressures are generated so that the inflow passage of the waste synthetic resin is introduced through the three transfer paths so that the extrusion force inside the die has the same extrusion force as the center and both sides.

At this time, if the difference in the extrusion force of the waste synthetic resin is divided into three can be finely adjusted by using the inflow adjustment bolt 19 installed on the upper and lower portions of the primary die (17).

In this way, the waste synthetic resin introduced into the inner die extruded portion 15 through the primary die 17 through the primary extruder 13 has a plurality of hemispherical protrusions 20 formed on the inner circumferential surface of the extruded portion 15 of the primary die 17. In the process of repeating the tightening and loosening during extrusion, the same action as the dough is prevented, thus preventing the air layer in the waste synthetic resin and making the structure finer to prevent the formation of the core inside the waste synthetic resin.

That is, the inner wall of the primary die 17 forms a plurality of hemispherical protrusions 20 on the slopes to form curved concave-convex portions, so that the waste synthetic resin introduced through the primary extruder 13 is formed inside the primary die 17. In the process of passing, as if the stomach is digested by the human stomach, the air remaining inside the waste synthetic resin is discharged to the outside, and the tissue is luxury and becomes fine particles. It is possible to improve durability without being generated.

The primary die 17 has a configuration in which a plurality of rectangular blocks are coupled, and a heating device having a plate shape is installed at an outer surface thereof.

The inside of the primary die 17 is connected to the primary extruder 13, but divided into three transfer paths 18 in one transfer path 18 so that the waste synthetic resin is supplied into the primary die 13. , The second extruder 14 is connected to another new synthetic resin transfer path 18 ′ of the primary die 17 so that the waste synthetic resin and the new synthetic resin are overlapped in the first die 18 and double-bonded to the front surface. The die 17b is extruded to the discharge port.

The secondary extruder 14 has the same configuration as the primary extruder 13, and receives the raw material from the raw material blending feeder 2 like the primary extruder 13, melts while passing through the screw, and then the primary die ( It is formed inside the primary die 17 in the form of being encapsulated on the outer surface of the waste synthetic resin extruded in 17) is discharged to the mold die 17a of the primary die 17 and flows into the primary sizing 21.

The primary die 17 has a plurality of air vents are formed in the upper and lower to exhaust the air generated therein to the outside.

Fourth step: forming a plurality of hollow parts in the double extrusion panel

The synthetic resin double panel extruded through the mold die 17b of the primary die may be formed without forming a hollow portion, but forms a plurality of hole-shaped hollow portions to increase strength and durability.

In order to form the hollow portion, an elliptical hole-forming rod 27 having a cross section is installed to be fitted into the mold die 17b which is the discharge portion of the primary die 17.

In this case, the hole forming rods 27 are equally disposed laterally equally in the mold die 17b so that a plurality of holes are formed in the inner body A of the double synthetic resin panel, which is the extrudate 34 discharged.

The hole forming rod 27 is fixed so that one end of the hole forming rod 27 is inserted into the inlet opening of the mold die 17b, but the hole forming rod 27 is coupled to be detachable.

The hole forming rod 27 is formed in an elliptical cross section, and is installed so that the larger diameter is located on the vertical line when installed in the mold die 17b discharge port.

The hole forming rod 27 is formed to be coupled to the groove formed in the inlet inlet of the mold die (17b) is formed so that the engaging projection is formed on one side end in order to attach to the discharge port. That is, the protrusions formed at one end of the hole forming rod 27 are inserted into grooves formed in the upper and lower portions of the inlet opening of the mold die 17a, and then rotated to one side to be coupled to each other.

In addition, the hole forming rod may form a pin hole without forming a protrusion at one end thereof and insert the pin hole into a discharge hole of the mold die 17a, and then fix the pin through the pin at an upper surface of the mold die 17a.

As described above, when a plurality of hole forming rods 27 are horizontally installed at the discharge hole of the mold die 17a, a plurality of holes are formed in the double synthetic resin panel that is extruded from the primary die 17.

Fifth Step: Primary Sizing Step of Vacuum Forming

The extrudate of the double synthetic resin extrusion panel in which the plurality of holes are formed by the hole forming rods installed in the mold die discharge port of the primary die is sucked by vacuum in the primary sizing 21 to smooth and smooth the outer surface of the panel. ) Mold.

The primary sizing 21 for vacuum forming has a space such as a tunnel so that the synthetic resin double extrusion panel can be introduced and transported to the other side, and a plurality of vacuum holes are formed therein to form the synthetic resin double extrusion panel at the top and the bottom thereof. Adsorption vacuum to smooth the outer surface.

At this time, the primary sizing 21 for vacuum molding is composed of one unit, but internally, the partition 22 is formed at a half point to be divided into the primary vacuum unit 25 and the secondary vacuum unit 26. Compartment.

The primary sizing 21 is just after the double panel extruded from the primary die 17 is out of the hole-forming rod 27, so that the vacuum pressure is weakened so that the surface vacuum is achieved and the secondary vacuum portion 26 is formed. While passing through the vacuum pressure hard to form the hole and the overall shape is fixed.

Since the shape of the hole formed in the hole forming rod 27 is immediately after leaving the hole forming rod, the egg is placed upright, so that only the surface of the primary vacuum unit 25 is vacuumed weakly, and the second size of the primary sizing 21 is again. A plurality of holes penetrating the inner body (A) of the panel by vacuum is performed in the secondary vacuum section 26 to form the mold.

 That is, when the hole of the panel inner body extruded from the primary die 17 is formed into a circular shape from the beginning, when passing through the primary sizing 21, the shape of the hole is not formed of a garden but is formed as a crushed circle, so that the hole forming rod has a cross section. This elliptical rod is installed so that the larger diameter is located on the vertical line so as to be circular in the vacuum in the primary sizing 21.

In the present invention, when the new synthetic resin is used in the extrusion molding of the panel with the synthetic resin, the holes formed inside are formed without deformation during extrusion, but when the waste synthetic resin is used, the hole is formed like a rice cake, Since the deformation occurs in the shape of the hole, in the case of the waste synthetic resin, it is necessary to install a hole forming rod in consideration of forming a hole such as a circle, a rectangle, a rectangle, and an oval.

In the present invention, forming the partition wall 22 in the primary sizing 21 and dividing it into the primary vacuum unit 25 and the secondary vacuum unit 26 to vacuum forming is well formed in the hole of the panel to be vacuum formed. Although there is a reason to make the waste synthetic resin, the extrusion speed is slowed down, so if the vacuum pressure in the first sizing 21 is weakened and the vacuum pressure is increased in the secondary vacuum part 26, the extrusion speed at which the panel is moved is increased. You can do it faster and increase your productivity.

In addition, the primary sizing inlet is wide in the front and narrow in the back and inclined inward to the upper and lower sides such as " " so that the panel extrudate extruded from the primary die can be easily introduced into the primary sizing 21. Part C was formed to facilitate the inflow of the extruded panel.

  At this time, the panel extrudates extruded from the primary die should be filled in a consolidation form at the inlet when the inlet flows into the primary sizing so as to form a panel during vacuum in the primary sizing to prevent unevenness and unbalance.

When the primary inlet is drawn in a consolidation form at the inlet of the primary sizing, the primary extractor installed at the rear is pulled in and consolidates along the inclined surface at the primary sizing inlet.

The primary sizing is a conduit is formed around the vacuum hole to circulate the refrigerant to cool the sizing.

6th process: primary vacuum cold forming and water cooling step

The shape of the extruded panel smoothed from the primary sizing 21 is passed through the primary vacuum cooler 30 to fix and cool the deformation so that deformation does not occur in the cooling process.

 The primary vacuum cooler 30 is installed at the head of the water cooling device formed in a chamber form to cool the dual panel that is extruded and transferred from the primary size 21.

In this case, as the panel extrudate passes through the first sizing, the external shape is formed by a double extrusion panel, but since the cooling is not completely done, the external shape is completely hardened in the primary vacuum cooler and the primary water cooler to deform the external shape. To prevent them.

The primary vacuum cooler 30 is composed of upper and lower cooling plants 31 and 32 and the upper cooling plant 31 is configured to be moved up and down by a cylinder.

In addition, the upper and lower cooling plants are adsorbed and cooled so that a vacuum hole is formed at the bottom of the synthetic resin double panel which is transported to one side so as not to interfere with movement and deformation does not occur during cooling.

At this time, the vacuum in the primary vacuum cooler 30 is weakened and completely fixed so that deformation does not occur in the shape, and cooling is performed by the refrigerant of the primary vacuum cooler itself.

Maintaining the smoothness in the primary vacuum cooler 30 as described above, the primary cooled synthetic resin double panel is moved in the state submerged by the moving rollers installed in the primary water cooling device (35).

At this time, the primary water cooling device 35 may install a vibrator on one side of the tank to vibrate the water so that the water rumbles like a wave in the tank, thereby further increasing the cooling effect.

In addition, the present invention can be cooled by spraying water by installing a plurality of rollers in the water tank of the primary water cooling apparatus to be moved while being guided by the roller double extrusion panel extruded by the water spray nozzles installed in the upper and lower parts.

When the primary water cooler is cooled by filling with water, the primary vacuum cooler 30 and the primary water cooler 35 are installed by installing a partition so that the primary vacuum cooler installed at the tip does not interfere with the vacuum. Install it.

In this process, the synthetic resin double panel passed through the primary water cooling device 35 is cured to form a complete panel.

That is, since the panel which has passed through the cooling water is completely cooled and no deformation occurs, there is no problem in using the panel or the panel which is not cut to a predetermined standard.

Thus, the panel which passed the primary water cooling apparatus 35 is called primary extrusion panel 34 in this invention.

7th step: moisture removal and withdrawal step

The water sprayed on the surface of the primary extrusion panel 34 cooled by the primary water cooling device is removed by the air spraying device 36.

Since the primary extrusion panel cooled through the primary water cooling device 35 is wetted with water, the external extrusion panel is dried by an air injector 36 because the external water must be dried for a subsequent process.

In addition, the primary ejector 37 is installed on the same line behind the air injector 36 so that the synthetic resin supplied from the primary extruder 13 and the secondary extruder 14 passes through the primary die 17 and is primaryly sized. 21, the primary vacuum cooler 30, the primary water cooler 35, and the air injector 36. At this time, the extrudate is discharged by the extrusion force pushed from the primary extruder and the secondary extruder to the discharge portion of the primary die, and is moved by the pulling force pulled from the primary extractor after the primary sizing.

Step 8: preheating the primary extrusion panel in the heating chamber and forming the multilayer panel in the secondary dice

The primary extrusion panel 34, which is pulled from the primary extractor 37 and transported, is introduced into the heating chamber 38 to dry the moisture remaining on the surface of the primary extrusion panel 34 and soften the surface.

The heating chamber 38 is installed in front of the secondary die 41 to heat and soften the outer surface of the primary extrusion panel 34 which is drawn into the secondary die 41 so that the primary extrusion panel 34 is 2nd. Bonding with the synthetic resin supplied from the 3rd extruder 39 and the 4th extruder 40 in the tea die 41 is made.

In this case, if the surface of the primary extrusion panel 34 is not softened in the heating chamber 38, the adhesive strength is weak when the secondary die 41 is laminated with the synthetic resin, thereby causing a problem in that the multilayer joint of the completed multilayer synthetic panel is opened. As a result, the primary extrusion panel 34 must soften the surface in the heating chamber 38 device.

The primary extrusion panel 34 whose surface is heated from the heating chamber 38 is introduced into the secondary die 41 and the waste synthetic resin supplied from the tertiary extruder 39 is laminated on the outer surface to form a waste synthetic resin layer. And the new synthetic resin supplied from the fourth extruder 40 is laminated on the waste synthetic resin layer to form a multi-layer structure.

As described above, the panel laminated in a multilayer structure in the secondary dice 41 is discharged from the secondary dice 41 and then transferred to the secondary sizing 42.

The tertiary extruder 39 carried out in this step receives waste synthetic resin raw materials from a raw material blending feeder installed on one side, and is melted in the tertiary extruder 39 and injected into the secondary die 41.

In addition, the fourth extruder 40 is supplied with a new synthetic resin raw material from a raw material blending feeder installed on one side, melted in the fourth extruder 40, and injected into the secondary die 41.

Accordingly, when the primary extrusion panel 34 passing through the heating chamber 38 enters the secondary die 41 in the secondary die 41, the waste synthetic resin supplied from the tertiary extruder 39 is the primary extrusion panel. Laminated and extruded on the outer surface, a new synthetic resin supplied from the fourth extruder 40 is laminated on the outer surface of the laminated waste synthetic resin layer is extruded from the secondary die 41 and molded into a multilayer extrusion panel.

The secondary dice 41 need not form hemispherical protrusions 20 like the primary die 17 inner extrusion portion.

The secondary die 41 is formed of a minja inside, so that when the primary extrusion panel 34 is drawn in, the waste synthetic resin layer and the new synthetic resin layer are laminated and extruded on the outer surface.

The secondary dice 41 are coupled to a plurality of blocks like the primary dice 17 and a plate heater is installed on an outer surface thereof.

In addition, synthetic resin inflow adjustment bolts are respectively installed on the upper portion of the secondary dice 41 to adjust the amount of waste synthetic resin and new synthetic resin.

Process 9: second sizing

The secondary sizing 42 vacuums flat and smooth the extruded panel formed in multiple layers in the secondary dice 41.

The secondary sizing 42 carried out in this step smoothes the outer surface of the multilayered synthetic resin panel extruded from the secondary dice 41 with a vacuum.

The secondary sizing 42 is configured to vacuum the multilayer synthetic resin panel at a time without dividing the primary vacuum portion 25 and the secondary vacuum portion 26 like the primary sizing 21.

The secondary sizing 42 is also formed with an inclined surface such as " " " inwardly as the primary sizing 21 so that the multilayered synthetic resin panel extruded from the secondary die 41 can be easily inserted. It was.

10th step: vacuum cooling and water cooling

The multi-layered synthetic resin extrusion panel smoothed from the secondary sizing 42 is cooled in a secondary vacuum cooler 43 and a secondary water cooler 44 which vacuum cool so that the shape is fixed upon cooling.

In this process, the secondary vacuum cooler 43 is installed at the front end of the water tank, and is made up of a plurality of rollers to be filled with water, or spray nozzles are installed at the upper and lower parts to constitute the secondary water cooler 44.

The secondary vacuum cooler 43 has the same configuration as the primary vacuum cooler 30 described above, and the cooling forming plants 31 and 32 are formed in the upper and lower parts, and the upper cooling forming plant 31 is a cylinder. The lower and lower cooling forming plant is connected to the lower and the plurality of vacuum holes are formed.

Therefore, the multilayer synthetic resin panel transferred from the secondary sizing 42 is not completely cooled, but may be deformed upon cooling, thereby cooling while holding the appearance with a vacuum.

The multi-layer synthetic resin extrusion panel passing through the secondary vacuum cooler 43 is precipitated and cooled in water or cooled by water sprayed from a plurality of nozzles in the process of being guided and transported by a roller in the same water tank.

When the multi-layered synthetic resin extrusion panel is moved in a state where water is stored in the water tank of the secondary water cooling device 44, the cooling efficiency may be increased by applying vibration to the water contained therein.

Process 11: Cooling, Cutting and Banding

The multi-layered synthetic resin extrusion panel is cooled in the secondary water cooling device 44 and then drawn out by a draw-cold molding machine installed in the same line and sent to a cutter.

The multi-layered synthetic resin extrusion panel drawn out from the take-out cooling molding machine 45 includes a cutter 49 for cutting to a predetermined standard and a banding machine for bending the cut multi-layer extrusion panel to a predetermined number.

The draw-out cooling molding machine 45 is provided with a secondary drawer 46 on both sides, but the secondary drawer 46 is formed of a plurality of draw rollers 48 and between the secondary drawer 46 and the secondary drawer 46. Cooling molding machine 47 is installed in the center of the extrusion panel to be transported and to be able to cool molding.

The inlet of the primary sizing 21 and the secondary sizing 42 is formed by the inclined portion C of the all-optical rear view.

The primary die 17 and the secondary die 41 are formed in a shape in which the mold die outlets at the rear thereof have a central diameter larger than both side diameters and convexly curved.

The primary vacuum cooler 30 and the secondary vacuum cooler 43 are formed with an inclined portion C on the lower part of the inlet.

Hereinafter, the accompanying drawings of the present invention will be described.

Figure 2 shows a process-specific system for the building composite extrusion panel manufacturing apparatus of the present invention, raw material blending feeder (2) → primary and secondary extruder (13) (14) → primary die (17) → primary Sizing (21) → primary vacuum cooler (30) → primary water cooler (35) → air injector (36) → primary drawer (37) → heating chamber (38) → third and fourth extruders ( 39) (40) → secondary die (41) → secondary sizing (42) → secondary vacuum cooler (43) → secondary water cooler (44) → draw-cooling molding machine (45) → cutting machine (49) The multilayer synthetic resin extrusion panel device which consists of a sequence is shown.

3 shows a raw material blending feeder of the present invention, wherein a mixing hopper 17b is provided on one side of the raw material blending feeder 2 so as to feed raw materials to the raw material blending feeder.

The mixing hopper 12 is provided with a stirring blade on the shaft rotated by a motor at the lower end to agitate the raw material contained in the hopper to be supplied to the supply conveyor (3).

The lower end of the mixing hopper 12 and the upper end of the raw material blending feeder 2 main body is connected to the raw material supply conveyor 3 and the raw material supply conveyor 3 is driven like a screw by a conveyor driving motor 4 installed at the upper end. The raw material of the mixing hopper 12 is transferred to the raw material mix feeder 2, and is supplied.

In addition, a stirring shaft 9 having a stirring blade 10 is vertically installed in the center of the main body of the raw material blending feeder 2 so as to stir the raw materials, and to rotate the stirring shaft 9 at the top of the stirring shaft 9. The drive motor 11 is installed.

A heater device 7 having a hot air supply fan 8 is installed at one side of the main body compound feeder 2 main body to dry the raw material inside the main body with hot air to remove moisture. If moisture remains because the raw material is not dried, an air layer is formed during melting, which causes defects in the product and removes it.

The raw material blending feeder 2 is provided with a new synthetic resin raw material blending feeder and a waste synthetic resin raw material blending feeder, respectively, so that the waste synthetic resin raw material blending feeder 2 may supply waste synthetic resin to the primary extruder 13 and the tertiary extruder 39. The new synthetic resin raw material blending feeder is installed to supply the new synthetic resin raw material to the second extruder 14 and the fourth extruder 40, respectively.

Figure 4 is a front configuration diagram showing the primary and secondary extruders of the present invention, Figure 5 is a plan view showing a primary and secondary extruders of the present invention, the primary extruder 13 is a raw material blending feeder (2) The waste synthetic resin raw material is supplied from the discharge conveyor 6 of the present invention, and the secondary extruder 14 is configured to receive the new synthetic resin raw material from the discharge conveyor 6 of another raw material blending feeder 2.

The primary extruder 13 is melted in the process of conveying the waste synthetic resin raw material supplied from the hopper provided on one side upper portion from the conveying screw of the extruder and injected into the primary die 17. To refer to)

In addition, the secondary extruder 14 has the same configuration as that of the primary extruder 13, and when the waste synthetic resin injected from the primary extruder 13 is extruded from the secondary die 14, a new synthetic resin is laminated and extruded on the upper surface thereof. .

Therefore, the first extruder 13 and the second extruder 14 is provided with a drive unit for driving the screw on one side, and the temperature control unit is installed on the other side to heat the plate heater 16 installed on the screw outer surface. Temperature control section is omitted since it uses a normal one)

The primary and secondary extruders 13 and 14 are formed of a screw having a predetermined length to melt the raw material supplied from the hopper, the screw of which is installed in the casing and the casing outer surface is installed with a plate heater 16. To melt the raw material conveyed along the screw.

 The plate heater 16 installed on the screw outer surface of each extruder is installed to control the temperature differently for each predetermined section.

In addition, a separate cover is formed on the outer surface of the plate heater 16 to protect the plate heater 16 and at the same time protect the worker from safety accidents.

Figure 6 shows a longitudinal section of the primary die for molding the resin extruded from the primary extruder and the secondary extruder of the present invention into a primary extrusion panel, wherein the discharge portion of the primary extruder 13 is the front of the primary die 17 It is connected to the transfer path 18 formed in the center and the transfer path 18 of the primary die 17 is divided into one transfer path 18 into three transfer paths 18 to form the inner body A. Configure.

In addition, the outer surface of the primary die 17 is connected to the discharge portion of the secondary extruder 14 and the new synthetic resin is laminated and extruded on the outer surface of the inner body A of the waste synthetic resin introduced from the primary extruder 13. Form B).

The primary dice 17 are coupled to a plurality of square blocks to form one primary dice 17.

In addition, a mold die 17b is installed at the distal end in the extrusion direction of the primary die 17 to form a primary extruded panel 34 including an inner body A of waste synthetic resin and an outer body B of a new synthetic resin. You can do it.

The primary die 17 may control the inflow of new synthetic resin raw materials introduced from the plurality of inflow adjusting bolts 19 and the second extruder 14 so as to control the inflow of the waste synthetic resin flowing from the primary extruder 13. A plurality of inflow adjustment bolts 19 are provided.

In addition, a plurality of air vents are formed at the upper and lower portions of the primary die 13 to exhaust the gas generated during the extrusion of the inner body and the outer body to the outside air in the primary die. In the present invention, it is not necessary to install the air vent. In the present invention, since the hemispherical protrusion of the primary die is installed and air is not present in the extrudate and a trace amount remains in the extrudate, it is discharged from the die and exhausted to the outside air.

Figure 7 shows a front view of the tertiary and quaternary extruders according to the present invention, Figure 8 shows a plan view of the tertiary and quaternary extruders 39, 40 according to the present invention, the tertiary extruder 39 ) And the fourth extruder 40 have the same configuration as the primary and secondary extruders 13 and 14 described above.

The third extruder 39 melts the waste synthetic resin and supplies it to the secondary die 41, and the fourth extruder 40 melts the new synthetic resin and passes the inside of the secondary die 41 to pass through the secondary die 41. It is laminated on the outer surface of the inner body (A ') consisting of the waste synthetic resin layer laminated on the new synthetic resin layer that is the outer body (B').

The secondary die 41 is also provided with a waste synthetic resin inflow adjusting bolt 19 and a new synthetic resin inflow adjusting bolt 19 are provided to control the amount of resin inflow.

In addition, the secondary die 41 is also provided with a vent for exhausting the gas generated therein to the outside.

9 is a longitudinal cross-sectional view of the secondary die 41 superimposed extrusion molding the outer surface of the primary extrusion panel formed from the primary die 17 and the waste synthetic resin supplied from the third and fourth extruders of the present invention As the secondary die 41 is a primary extruder panel 34 is pulled by the drawer and the surface is softened in the heating chamber 38 and then flows into the secondary die 41, the third extruder 39 installed on one side. Secondary dies are extruded so as to form an inner body A 'by stacking waste synthetic resins supplied from the stack, and a synthetic resin material stacked on the outer surface of the waste synthetic resin layer to form an outer body B'. .

10 is a schematic view showing a connection state in which the primary extrusion panel extruded from the primary die of the present invention is extruded in multiple layers from the secondary die.

FIG. 10 shows the primary extrusion panel 34 by extruding the waste synthetic resin and the new synthetic resin supplied from the primary and secondary extruders 13 and 14 in the primary die 17. In the primary extrusion panel 34, waste synthetic resin constitutes an inner body (A), and new synthetic resin forms an outer body (B) to form a double extrusion panel.

As such, the primary extrusion panel 34 formed in the primary die 17 extrudes the waste synthetic resin and the new synthetic resin supplied from the tertiary extruder 39 and the fourth extruder 40 in the secondary die 41. A resin extrusion panel having a multilayer structure is formed.

10, therefore, omits the steps between the primary and secondary dice and briefly illustrates an embodiment of the primary and secondary dice.

 For reference, in the present invention, the extrudate extruded from the primary die is vacuum extruded in the primary sizing, and the extrudate continuously moved is referred to as a primary extrusion panel 34 for convenience, and the article produced by cutting the double extrusion panel ( 50).

In addition, the panel is completely cooled after passing through the cooling process from the primary die to the binary die is referred to as a multilayer extruded panel (51).

11 is a step-by-step view showing the primary panel shape extruded from the primary die and the secondary panel shape formed from the secondary die of the present invention, the primary extrusion panel constituting the inner body (A) and the outer body (B) Before the 34 is extruded from the primary die 17 and drawn into the primary sizing 21, as shown in FIG. Is formed.

The primary extrusion panel 34 extruded from the primary die 17 has a rectangular cross-section such as ⒝ when drawn into the primary sizing 21 and adsorbed by vacuum in a state having a convex curved portion as shown in Fig. The surface is shaped smoothly.

The primary extrusion panel 34 vacuum-adsorbed in the primary sizing has a primary vacuum cooler 30, a primary water cooling device 35, an air spraying device 36, a drawer 37, and a heating chamber 38. When the waste synthetic resin and the new synthetic resin are laminated from the third extruder 39 and the fourth extruder 40 in the secondary die 41 and discharged from the secondary die 41, the primary extrusion is performed as shown in FIG. The resin laminated on the panel 34 is extruded in a state where a curved portion is formed in a cross section, and then made through a second size 42 to have a rectangular cross section, and the surface is smoothly molded to have a multi-layered synthetic resin extruded panel. Is formed.

  That is, the primary dice 17 and the secondary dice 41 of the present invention are discharged in the shape of convexly convex in the form of curved upper and lower parts and then molded into the correct shape in each sizing.

In concrete terms,

Since the waste synthetic resin raw material is introduced into the die in the primary extruder 13, a foam layer is formed in the raw material due to the gas, and thus the raw material does not uniformly spread in the primary die 13.

Therefore, in order for the product to spread well throughout the die, it is necessary to knead the dough in the dice so that the raw material spreads well in the first die so that the strength of the whole part is the same.

delete

In addition, since the raw material is a waste synthetic resin, when the square product is formed in the die, the product is foamed due to the gas and the product is folded like a steamed bread when it comes out of the first die. Make it slightly curved so that the product is inserted well into the primary sizing (21) without riding the dice.

In addition, in order to make a large number of holes 52 formed in the inner body of the primary extrusion panel 34 in the shape of an egg, a hole forming rod 27 is formed between the primary die 17 and the primary sizing 21. Extrude so that 52 is formed.

In addition, in order to prevent the extruded panel from being swollen like a steamed bread, a plurality of holes 52 may be crushed, the new synthetic resin must be laminated on the product once more to form a rectangular shape, and the strength is formed and the flatness is smooth.

Immediately afterwards, as the extrudate of the panel enters the primary sizing 21, only the surface is weakly formed while the primary vacuum and the primary vacuum section 25 are subjected to the primary cooling and vacuum to form a square shape. A large number of holes (C) are made without sticking to the product, and the hole forming rods 27 are immediately pulled out, gradually vacuuming and cooling in the first vacuum unit 25 and strong cooling and vacuuming in the secondary vacuum unit 26. As the whole square is made, the hole C and the foam layer of the product are formed, and thus the strength is strongly formed in the product.

12 is a cross-sectional view showing a number of hemispherical protrusions formed inside the primary die according to the present invention, and the waste synthetic resin raw material flowing from the primary extruder flows into the central transfer path 18 of the primary die and is divided into three sections. It flows into the primary die 17 through the conveying path 18.

In this way, the waste synthetic resin is divided into three after the waste synthetic resin is introduced into one conveying path 18. Since the waste synthetic resin has a rice cake shape in the molten state as kneading flour, the raw material is injected in one conveying path. When extruding, not only the extrusion speed is lowered but also the space is suddenly widened when entering into the primary die 17 in one narrow passage, so that the extrusion force is applied only to the center portion, and both side portions have an unbalanced extrusion rate.

In order to solve this disadvantage, the present invention forms three divided passages (transfer passages) after being introduced into one passage (transfer passage) to uniformly extrude the raw rice cake-type waste synthetic resin material in the primary die 17. To be possible.

In addition, the primary die 17 of the present invention is to form a plurality of hemispherical protrusions 20 on the upper and lower left and right inner surface to form a waste synthetic resin raw material during extrusion.

That is, the waste synthetic water support material is rubbed by the hemispherical protrusion 20 when extruded from the primary die 17, thereby acting to gelatinize the raw material and release the internal gas.

Particularly, the waste synthetic resin extruded in the primary die 17 serves to improve durability of the molded panel by preventing particles from being broken down and forming cores in the process of kneading, as shown by a hemispherical protrusion 20. .

FIG. 13 is a cross-sectional view of a primary sizing 21 in which a plurality of holes are formed in an inner body by installing a hole forming rod between a primary die and a sizing according to the present invention. It is for forming the hole 52.

According to the present invention, a panel extrudate extruded from the primary die 17 is formed by installing a hole forming rod 27 between the mold die 17a of the primary die 17 and the primary sizing 21. In the process of drawing into the primary sizing 21 in 17b), a plurality of holes 52 are formed in the inner body of the extrusion panel.

One end of the hole forming rod 27 may be fixed to the mold die 17b of the primary die 17 or may be fixed to the pin 29.

The end of the hole forming rod 27 is inserted into the mold die (17b) is formed in a pointed shape so that the extrudate is not disturbed during extrusion, and the other end is located in the primary sizing inlet and fixed with a pin or the like.

The primary sizing 21 has a wall 22 formed therein and is divided into a primary vacuum part 25 and a secondary vacuum part 26, and the primary vacuum part 25 passes through the hole forming rod 27. The vacuum pressure is set weakly so that only the surface of one extrudate is sucked in vacuum, and the secondary vacuum section 26 is set to vacuum in the world than the vacuum pressure of the primary vacuum section 25.

The primary sizing 21 has a plurality of vacuum holes are formed in the upper and lower inner surface and the pipeline is formed inside the body to move the cooling water to cool the heat of the extrudate to prevent sticking during vacuum adsorption and to increase the extrusion movement speed To be able.

Figure 14 shows a primary vacuum cooler according to the present invention, Figure 15 shows a top cooling forming plate of the primary and secondary vacuum cooler of the present invention, Figure 16 is a vacuum cooling molding machine as another embodiment of the present invention The upper cooling molding plate is shown.

17 is a configuration diagram showing a vacuum hole on the bottom surface of the upper cold forming plate according to the present invention.

The vacuum is adsorbed in the primary sizing 21 to form an extrudate in the shape of the primary extruded panel and then cooled while holding the vacuum suction so as not to cause deformation of the shape in the primary vacuum cooler 30.

Process of cooling because the inner body A of the panel molded from the primary sizing 21 to the primary extrusion panel 34 is not completely cooled in a state in which a plurality of holes 52 are formed. Since deformation may occur in the primary vacuum cooler (30) while cooling the first extrusion panel while holding the vacuum.

The primary vacuum cooler 30 is installed in the front end of the primary water cooling device 35 to be cooled while holding the molded primary extrusion panel 34.

The primary vacuum cooler 30 is composed of upper and lower cooling forming plates 31 and 32, and a plurality of vacuum holes are formed on the surface thereof as shown in FIG.

 The upper cabinet forming plate 31 of the primary vacuum cooler can be moved up and down by a cylinder or a motor, and the cooling forming plate is installed in a processed state.

Two or more primary vacuum coolers may be installed to vacuum cold roll the primary extrusion panel.

At this time, the primary extrusion panel 34 vacuum-cooled by the primary vacuum cooler 30 is vacuum-cooled in the process of being pulled and moved by the primary drawer 37 installed on the same line on one side.

As shown in FIG. 15, the primary vacuum cooler 30 has an inlet through which the primary extrusion panel is drawn so that the inclined surface is formed inward so that the primary extrusion panel is not caught.

Figure 15 is to allow the upper cold forming plate of the primary vacuum cooler to move up and down by the cylinder.

Figure 16 is to allow the upper cooling forming plate of the primary vacuum cooler to be moved up and down by a motor in another embodiment of the present invention.

In addition, the primary extrusion panel 34 of the present invention is guided by a roller installed in the primary water cooling device 35 on one side after being primarily cooled in the primary vacuum cooler 30 and then moved into the water of the tank. The primary extrusion panel 34 is cooled.

The primary extrusion panel 34 cooled by the primary water cooling device 35 may provide a 12T plywood standard synthetic plywood when cut to a conventional plywood standard if necessary.

The primary water cooler 35 or the secondary water cooler 44 of the present invention has the same structure, and the primary vacuum cooler 30 is a primary extruded panel or a multilayer that is moved from the secondary vacuum cooler 43. When the synthetic resin panel is cooled in the primary water cooling device 35 or the secondary water cooling device 44, the first pass through the still water as it is, and then the water cools quickly as the water fluctuates like a wave, thereby increasing the moving speed.

In addition, the primary extruded panel cooled by the primary water cooling device removes the water on the surface by an air injector and is pulled by the primary extractor 37 on one side and heated on one side of the primary extractor 37. It is drawn into the chamber 38 and completely dried, while at the same time the surface is softened and drawn into the secondary dice 41.

In addition, the primary drawer 37 and the draw-cooling molding machine 45 control the action of pulling the extrusion panel and the speed at which the primary die 17 and the secondary die 41 are extruded.

18 shows a secondary vacuum cooler of the present invention, in which the primary extrusion panel 43 extruded from the secondary die 41 has the same configuration as that of the primary vacuum cooler. After vacuum adsorption at leveling and smoothing, vacuum cooling is performed in the secondary vacuum cooler 43.

The secondary vacuum cooler 43 cools the secondary vacuum cooler 43 while the heat of the extrudate formed in the secondary sizing 42 is not completely cooled but is held in the secondary vacuum cooler 43.

The secondary vacuum cooler 43 is composed of upper and lower cooling molding plants 31 and 32, and the upper cooling molding plant 31 and 32 has the configuration shown in Figs.

18 shows that the extrudate extruded from the secondary die is initially cooled in a secondary vacuum cooler 43 via a secondary sizing 42 and then cooled in a secondary water cooler 44. After passing through the water, the product cools faster as the water waves like waves.

Fig. 19 is a front view showing a draw cooling molding machine for drawing out a synthetic resin multilayer panel according to the present invention, and Fig. 20 shows a side view showing a drawing roller configuration of a drawer according to the present invention.

In the drawing-out cooling molding machine 45 shown in FIG. 19, the secondary drawing machine 46 and the cooling molding machine 47 are combined.

That is, a secondary drawing machine 46 composed of three drawing rollers 48 is formed at the front part, and a cooling molding machine 47 is formed at the center of the cooling machine, and the three drawing rollers 48 are formed after the cooling molding machine. The secondary drawing machine 46 which consists of these is comprised.

  Therefore, the cooling molding machine 47 which vacuum-cools between the secondary drawing machine 46 which consists of three rollers, and the secondary drawing machine 46 is provided.

Fig. 20 shows the drawing roller configuration of the draw cooling molding machine, in which two rollers are arranged up and down, and a multi-layered synthetic resin extrusion panel, which is an extrudate, is engaged between the upper and lower parts and drawn out as the roller rotates.

The primary drawer 37 and the secondary drawer 46 of the draw cooler 45 are configured to pull the extruded panel.

Figure 21 shows a synthetic resin multi-extrusion panel cutter of the present invention, the cutter shown in Figure 21 is to cut the length of the multi-layer synthetic resin extrusion panel that is an extrudate to a predetermined standard to be commercialized.

The cutter is to be able to adjust the length as needed.

Figure 22 shows a synthetic resin double extrusion panel extruded from the primary die of the present invention, the panel shown in Figure 22 shows a 12T panel as the primary die, primary sizing, primary vacuum cooler, primary water It shows a double extrusion panel 50 produced through a system of a cooling device, a primary air spray device, a primary extractor.

Figure 23 shows a synthetic resin multilayer panel extruded through the primary and secondary dice of the present invention, the multilayer synthetic resin extrusion panel 51 shown in Figure 23 is a panel molded through the system of the previous process of the present invention 24T panel is molded.

In addition, the present invention is to make an uneven protrusion on the inner surface of the inlet of the secondary die to make a small groove in the surface of the primary extrusion panel when the primary extrusion panel enters the secondary die so that the adhesive strength and waste synthetic resin extruded from the tertiary extruder can be improved It was.

24 is a cross sectional view showing a state in which a hole forming rod is installed in a primary die as another embodiment of the present invention, and FIG. 25 shows an embodiment of the longitudinal cross-sectional view of FIG.

24 is shown as another embodiment of the present invention, the primary die is composed of a plurality of rectangular blocks are joined by bolts.

In addition, the inner die extruded portion 15 of the primary die 17a has a plurality of hemispherical protrusions 20 formed therein so as to knead the extruded portion 15 when the waste synthetic resin flowing from both sides from the primary extruder 13 is extruded. Make the dough work.

It is connected to the primary extruder 13 for extruding the waste synthetic resin on both sides of the front end of the primary die 17a, the waste synthetic resin is supplied to the extruded portion 15 from both sides of the primary die 17a so that the inner body (A) And, the second extruder 14 is connected to one side of the middle of the primary die (17a) and the new synthetic resin is introduced to the body synthetic resin layer is laminated on the outer surface of the inner body (A) of the waste synthetic resin layer (B) ).

In addition, as shown in FIGS. 24 and 25, a hole forming rod 28 is installed to penetrate through the inner extruded portion 15 from the outer end surface of the primary die 17a to the inlet of the primary sizing 21. .

The hole forming rod 28 is formed as a hollow portion penetrating therein in the form of a pipe. The hole forming rod 28 fixed to the primary sizing inlet through the primary die 17a is fixed with a pin 29 '.

The hole forming rods 28 allow air to be injected from the outer surface of the distal end of the primary die 17a to be blown to the primary sizing 21 to form a plurality of holes formed in the panel in the primary sizing 21. Prevent 52 from being deformed.

The hole forming rods 28 passing through the inner die extruded portion 15 of the primary die 17a are installed to form a plurality of holes 52 in the inner body of the panel to be extruded.

The hole forming rod 28 is made of a hollow portion like a pipe to inject air into the hole forming rod from the outside of the tip of the primary die 17a to be discharged to the inside of the primary sizing without crushing the hole formed in the panel body. It plays a role.

The extruded portion is formed such that the inflow portion has a larger inner diameter than the discharge side and the inner surface is curved to smoothly flow the waste synthetic resin.

Since the waste synthetic resin supplied from the primary extruder 13 is in the form of rice cake, the extrusion speed is lowered, so that the productivity is lowered, so that the primary die 17a described in another embodiment of the present invention is removed from the primary extruder 13. The diameter of the inlet inside the inlet is larger than that of the discharge port, and the waste synthetic resin flowing from both sides is formed into curved grooves in the upper and lower sides so that the inflow is smooth. After being filled at the inlet 15, it is possible to quickly extrude to the discharge side to improve the productivity.

At this time, in order to make the extrusion pressure of the extrudate uniform, the flow rate adjusting bolt is installed in the upper portion of the primary die 17a so as to penetrate from the upper side to the extruded side.

In addition, the inlet of the primary size 21, the inlet of the primary vacuum cooler 30, the inlet of the secondary size 42, and the inlet of the secondary vacuum cooler 43 of the present invention are inclined inwardly. Was formed to allow the extrudate to be drawn in.

FIG. 26 is a block diagram illustrating a process for manufacturing a composite extruded panel for construction according to the present invention.

① supplying raw materials to the primary and secondary extruders in the raw material blending feeder,

② melt-extruded raw materials supplied in the primary and secondary extruders, respectively, and injected into the primary die,

③ extruding the primary extrusion panel with the waste synthetic resin as the inner body and the new synthetic resin as the outer body in the primary die;

④ forming a plurality of holes in the extrusion panel body discharged from the primary die using a hole forming rod,

(5) vacuuming the extruded panel having a plurality of holes by primary sizing,

⑥ vacuum cooling the extruded panel smoothed in the first sizing using a primary vacuum cooler,

⑦ cooling the vacuum cooled extrusion panel with water in the primary water cooling device,

⑧ to remove water from the surface of the extrusion panel cooled by water with an air spraying device,

⑨ softening the surface by pulling the water-extruded extruded panel into the first drawer into the heating chamber,

(B) extruding in a secondary die so that a waste synthetic resin layer and a new synthetic resin layer are formed on the outer surface of the extruded panel, the surface of which is softened;

(B) vacuuming the extruded panel formed in multiple layers in the secondary dice with secondary sizing,

Vacuum-cooling the extruded panel formed into a multi-layer with a secondary vacuum cooler,

수 water-cooling the vacuum cooled extrusion panel in a secondary water chiller,

당겨 pulling and cooling the cooled multi-layered extruded panel to a draw cooler,

The multi-layer extruded panel drawn out from the draw-cooling molding machine is manufactured in a process including cutting to size.

In addition, the present invention, even if the extrudate is made into a square, the surface is not much, the strength of the product does not come out and the surface is uneven and the extrudate is not foamed to form a square, the inner surface of the waste synthetic resin layer (A) By forming the new synthetic resin layer of the outer body (B) and the waste synthetic resin layer of the inner body (A '), and the new synthetic resin layer of the outer body (B') on the outer surface of the new synthetic resin layer, It is made of square panel smoothly while catching the rising of steamed bread inside

In addition, the present invention forms a layer in the order of the inner body (A), the outer body (B), the inner body (A '), the outer body (B') to prevent breakage even if the panel product is impacted and the strength is increased. There is a hardening feature.

In addition, the present invention is made of a new synthetic resin on the outside, and the inside is made of waste synthetic resin raw material, it is not a substitute for general plywood, it can replace the high-strength apartment slabs, retaining walls, the building used in the European style, coated plywood can be replaced have.

The standard container is 20ft, 20ft container is 5.9m in length, 2.3m in height and 2.4m in height and weighs 2290kg in 20ft container. When the container flooring test is carried out at the weight of 7200kg, container product strength is the most important to pass 7200kg.

Therefore, when the multi-layered synthetic resin extrusion panel of the present invention is used as a container flooring material, the specific gravity is the same as wood, so the fuel cost of the sea is low.

In addition, since the inner body constituting the panel of the present invention is a product in which raw materials are made of waste vinyls and blowing agents, gas is generated, and thus a fine foam layer is formed on the product, so that the product itself is light, and sawing and nailing are performed. Good for you.

It also has the effect of preventing sound, vibration, and ringing. It can be stretched in summer, twisted by sunlight, and even contracted in winter.

In addition, the multi-layer synthetic resin extrusion panel of the present invention is an apartment site, general building, building coating plywood, waterproof plywood, double floors, building floor noise, container floors, train floors, fire floors, building wall soundproofing, European windshield, wood substitute building synthetic resin It can be used in various ways such as plywood.

In addition, the present invention is made by extrusion of the inner body of the waste synthetic resin firstly, and the second body is extruded to polymerize the outer body of the new synthetic resin on the outer surface of the inner body to form an inner layer on the outer surface of the outer body again and the outer surface of the inner body By forming a panel in a multilayer structure in which a sieve layer is formed, it is possible to mold a multi-extruded panel having improved strength and durability against impact absorption.

In addition, the present invention is to recycle the synthetic resin panel of various forms using waste plastic and waste plastic generated in farming and fishing villages or waste synthetic resin and waste plastic generated in industrial sites, etc. A construction double extrusion panel manufacturing apparatus and method for preventing contamination.

1: Synthetic resin extrusion panel manufacturing equipment 2: Raw material blending feeder
3: Supply Conveyor 4, 5: Conveyor Drive Motor
6: Discharge Conveyor 7: Heater Device
8: Heat supply fan 9: Stirring
10: Stirring wing 11: Driving motor
12: mixing hopper 13: 1st extruder
14: 2nd extruder 15: Extruder
16: plate heater 17, 17a: 1st die
18, 18 '; Transport route 19: Flow adjustment bolt
20: Hemispherical protrusion 21: 1 primary sizing
22: bulkhead
25: 1st vacuum part 26: 2nd vacuum part
27,28: Hole forming rod 29,29 ': Hole forming retaining pin
30: 1st vacuum cooler 31: Upper cooling molding plate
32: Lower Cooling Plate 35: 1 Primary Water Chiller
36: Air injector 37: 1 primary drawer
38: heating chamber 39: 3rd extruder
40: 4th Extruder 41: 2nd Die
42: Secondary Sizing 43: Secondary Vacuum Cooler
44: Secondary water chiller 45: Draw-out cooling molding machine
46: secondary drawing machine 47: cooling molding machine
48: withdrawal roller 49: cutter
50: synthetic resin double extrusion panel 51: synthetic resin multilayer extrusion panel
52: hole A, A ': inner body
B, B ': External body C: Inclined part

Claims (16)

A raw material blending feeder 2 which mixes waste synthetic resin raw materials or new synthetic resin raw materials to supply raw materials to the hopper of the primary extruder 13 or the secondary extruder 14;
Primary and secondary extruders (13) and (14) for melting and receiving waste synthetic resin raw materials and new synthetic resins received from the raw material blending feeder from a hopper; After the melted from the primary extruder to the inner synthetic waste material supplied through the feed channel, and the inner side of the second synthetic extruder to melt the synthetic resin supplied through the raw material conveying path to form a double synthetic resin extrusion panel Primary dice 17; A hole forming rod (27) for forming a plurality of holes in the double synthetic resin extrusion panel discharged from the primary die; A primary sizing (21) for forming a flat and smooth outer surface of the panel by vacuum forming a double synthetic resin extrusion panel in which a plurality of holes are formed by the hole forming rods; A primary water cooler 35 for fixing and cooling the shape of the extruded panel smoothed from the primary sizing and a primary water cooler 35 for cooling the extruded panel cooled in the primary vacuum cooler; A primary drawer 37 for pulling and transporting the extruded panel cooled by the water chiller; Tertiary and quaternary extruders (39) (40) connected to secondary dies (41) for supplying resin such that a waste synthetic resin and a new synthetic resin layer are formed on an outer surface of the extruded panel which is pulled from the primary extractor; Secondary dice 41 for bonding the extruded panel and the waste synthetic resin and the new synthetic resin supplied from the third and fourth extruders, and extruded into a multilayer panel; A secondary sizing (42) for vacuuming flat and smoothly the extruded panel formed in multiple layers in said secondary dice; Secondary water cooler 44 for cooling the multi-layered extruded panel cooled by the secondary vacuum cooler 43 and the secondary vacuum cooler 43 to fix the shape of the multilayer extrusion panel smoothed from the secondary sizing 44 )Wow; A draw cooler 45 for pulling and conveying the multi-layered extruded panel cooled by the secondary water cooler and simultaneously cooling the mold; In the building composite extrusion panel manufacturing apparatus comprising a cutter for cutting the multilayer extrusion panel drawn out by the draw-cooling molding machine to a predetermined standard and a banding machine for bending the cut multilayer extrusion panel with a predetermined longevity,
The composite composite panel manufacturing apparatus for construction,
The primary die and the hemispherical protrusions 20 formed in the number of the inner extrusion portion to be kneaded by the waste synthetic resin to flow when inflow;
An air injector (36) for removing water from the surface of the extrusion panel cooled by the primary water cooling device (35);
A heating chamber 38 for drying the moisture of the extruded panel transferred from the primary extractor 37 which pulls the extruded panel from which the water is removed from the air injector, and softens the surface thereof;
The primary sizing (21) and the secondary sizing (42) is a composite extrusion panel manufacturing apparatus for a building, characterized in that it comprises a; delete delete delete The method of claim 1,
The primary die is composed of a plurality of rectangular blocks, and the primary die inner extrusion part is connected to a primary extruder for forming a plurality of hemispherical protrusions to extrude waste synthetic resin, but is divided into three conveying paths in one conveying path and the primary dice. The waste synthetic resin is supplied to the inside, and the second extruder is connected to another new synthetic resin transfer path of the primary die, and the waste synthetic resin and the new synthetic resin are double-overlapping inside the primary die and extruded into a mold die outlet coupled to the front. Composite extrusion panel manufacturing apparatus for construction. The method of claim 1,
The primary vacuum cooler 30 and the secondary vacuum cooler 43 are formed in the upper and lower cooling forming plant and the upper cooling forming plant is connected to the cylinder to move up and down, the upper and lower cooling forming plant is a plurality of vacuum holes Composite extruded panel manufacturing apparatus for building, characterized in that formed. delete delete delete delete The method of claim 1,
The second die has a small protrusion formed on the upper and lower inlet to the primary extrusion panel is introduced to form a plurality of grooves on the upper and lower surfaces of the primary extrusion panel to improve the adhesive strength of the waste synthetic resin flowing from the tertiary extruder. Composite extrusion panel manufacturing apparatus made of. The method of claim 1,
The primary die is composed of a plurality of rectangular blocks, but the primary die inner extrusion portion is formed with a plurality of hemispherical projections, connected to the primary extruder for extruding waste synthetic resin on both sides of the primary die extruded from both sides of the primary die And a secondary extruder connected to the middle one side of the primary die so that the new synthetic resin is introduced, and the hole forming rod having a hollow portion connected to the sizing inlet through the primary die inner extrusion part. And installing the extrusion part, wherein the inlet part has an inner diameter larger than that of the discharge side, and an inner surface thereof is formed in a curved surface, so that the inflow of the waste synthetic resin is smoothly formed. delete delete delete delete

Images