JPH081095A - Method for separately recovering plastic from glass fiber-reinforced plastic article and equipment therefor - Google Patents

Abstract

PURPOSE:To recover a pulverized resin by pulverizing the waste of a glass fiber-reinforced resin, forming a separated mixture by a superhigh-speed eddy current or pressure vibration, blowing the ionized air against the mixture by a vibrating feeder to separate the mixture into glass fiber and resin and dropping the glass fiber by a wire net. CONSTITUTION:The formed waste is coarsely crushed, and the coarsely crushed material 4 is recovered (A) through a cyclone 3. The material 4 is introduced into a pulverizer 6 and pulverized, and a pulverized material 7 is obtained (B) as a mixture of the glass fiber and resin by the superhigh-speed eddy current generated at the rear of an impeller and the high-frequency pressure vibration. A vibrating screening machine 13 is provided with a vibrating screen 13a consisting of a 6-mesh wire net, while the oversize 14 contg. the glass fiber in the pulverized material 7, fine glass fiber and primary fraction 15 are sieved by the wire net, the glass fiber is positively charged and the resin is negatively charged. The materials are destaticized (C) by blowing the air ionized by a corona discharge in a destaticizer 12 and separated (D) by a vibrating feeder 18.

Description

Detailed Description of the Invention

[0001]

BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention separates and collects plastic components in waste products such as defective products and ear trimming products that are generated during the manufacturing process of plastic products containing glass fibers such as corrugated plates made of vinyl chloride containing glass mesh. The present invention relates to a method for separately collecting and recovering plastics from glass fiber-reinforced plastic products.

[0002]

2. Description of the Related Art Plastic products such as corrugated plates made of vinyl chloride inevitably generate waste products such as defective products and ear trimming products obtained by trimming the ears during the manufacturing process. Of these wastes, the wastes of plastic products made of only a single plastic are crushed as they are and mixed with new plastic raw materials to be reused. In the case of glass-fiber-containing plastic products such as those provided with, it is impossible to reuse unless the glass fibers are removed, and most of them are currently disposed of.

Therefore, after wastes of these glass fiber-containing plastic products are finely pulverized by a cutter type pulverizer composed of a rotary blade and a fixed blade (for example, a pulverizer disclosed in Japanese Patent Publication No. 47-18819). Attempts have been made to throw the finely pulverized material into a sorting machine 100 as shown in FIG. 5 to sort and collect only plastic. That is, this sorter 100 is configured such that the finely pulverized product is fed to the first sort tank 101
The air from the blower 102 to the first separation tank 10
1 is blown into 1 to form an air flow in the first sorting tank 101 to blow up the glass fiber, which is a light weight component in the finely pulverized material, to the upper side of the first sorting tank 101, and from a suction port 103 leading to a dust collector. Aspirate the glass fibers. And the first
The second collection tank 1 is used to collect the primary recovery product accumulated at the bottom of the separation tank 101.
04, and again blows air from the blower 105 into the second separation tank 104, forms an air flow in the second separation tank 104, and blows up the glass fiber, which is a light weight component remaining in the primary recovery product, upward. The glass fiber is sucked and removed from the suction port 106 provided in the upper part of the second separation tank 104 and connected to the dust collector, and only the finely pulverized plastic material can be taken out from the extraction port 107 provided in the lower part of the second separation tank 104. .

[0004]

However, the wastes of plastic products containing glass fibers, if not sufficiently pulverized, remain in a sandwich state in the pulverized plastic products, and the glass fibers are completely removed from the pulverized plastic products. It is impossible to separate. On the other hand, if the waste of the plastic product containing glass fiber is crushed with the above cutter type crusher until the plastic is sufficiently fine, the glass fiber and the plastic are completely separated. When it is rotated at a high speed, it contacts the cutting blade and is crushed, so if it is crushed too much, the plastic component will be burned and the color tone will change. Therefore, there is a problem in that it cannot be used when molding a product that requires decorativeness.

Further, in the case where the sorting process is performed by the sorting machine 100, pill-like fibers are produced during the sorting process, and the sorting is required again, and there is a problem that the recovery rate is poor. Further, due to friction during pulverization, the plastic is charged (-) and the glass fiber is charged (+).
Even if the plastic is burnt and can be finely crushed and separated from the glass fiber without changing the color tone, there is also a problem that the plastic and the glass fiber are re-attached due to the electric suction force, and it is difficult to separate and collect them.

In view of such circumstances, the present invention makes it possible to make a plastic product containing glass fibers into a fine powder without burning the plastic content and discoloring the color tone.
Moreover, it is an object of the present invention to provide a method and a facility for separately collecting and recovering a plastic component from a glass fiber-reinforced reinforced plastic product capable of efficiently recovering only the plastic component by removing glass fiber from the fine powder material. .

[0007]

In order to achieve the above object, the separation of plastics from a glass fiber-reinforced reinforced plastic product according to the invention of claim 1 (hereinafter referred to as "first invention"). The recovery method is to roughly crush a glass fiber reinforced plastic product and obtain a coarsely crushed product, which is subjected to the impact of a high-speed rotating blade, the numerous ultra-high-speed vortices generated behind this blade, and the high-frequency pressure vibration generated by this. A fine pulverization process in which it is put into a fine pulverizer and pulverized into a finely pulverized product, and this finely pulverized product is sieved, and the non-sieving fraction containing most of the glass fibers remaining on the sieve and the primary fractionation through the sieve. The primary separation treatment process to separate the product into products and the primary separation product is supplied to one end of the diaphragm, moved to the other end of the diaphragm while vibrating, and ionized from the upper part of the diaphragm by corona discharge. did Spraying, and neutralizing static electricity charged to the glass fibers and plastic in the primary fractionation products,
In addition, air is blown through the wire mesh to the primary separated product that passes through the wire mesh part provided in the middle part of the vibration plate, the light weight component in the primary separated product is blown above the diaphragm, and the light weight component blown up is sucked by the dust collector. A secondary sorting process of removing and discharging the secondary sorted product from which the light weight component is removed from the primary sorted product from the other end of the diaphragm, and the secondary sorted product in a vertical passage having a wire mesh on one side. , While diffusing the secondary fractionated product by the airflow generated toward the metal mesh side by suction from the metal mesh side, remove the fine glass fiber in the secondary fractionated product passing through the metal mesh,
A collecting step of collecting the finely pulverized plastic material that does not pass through the wire mesh.

According to the invention of claim 2 (hereinafter referred to as "second invention"), a method for separating and recovering a plastic component from a glass fiber-reinforced reinforced plastic product comprises fine grinding in addition to the constitution of the first invention. During the transfer step of the finely pulverized material from the process to the first separation processing step, and at least one of the transfer steps from the primary separation processing step of the primary separation product to the secondary separation processing step, glass fiber and It is configured to remove static electricity from the plastic.

On the other hand, the facility for separating and collecting plastics from glass fiber-reinforced reinforced plastic products according to the invention of claim 3 (hereinafter, referred to as "third invention") roughly crushes the glass fiber-containing plastic products. The coarsely crushed product obtained by
A fine pulverizer for fine pulverization by the impact of a high-speed rotating blade, a large number of ultra-high-speed vortexes behind this blade, and the high-frequency pressure vibration generated by this, and the finely pulverized material obtained by this fine pulverizer is sieved. A vibrating sieving machine that separates the non-passed fraction containing most of the glass fibers into a primary fractionated product that passes through the sieve, and moves the primary fractionated product that has been introduced into one end toward the other end by vibration, and an intermediate Plate provided with a wire mesh part in the part, and below the wire mesh part of this diaphragm, wind blows over the wire mesh to the primary separated product passing through the wire mesh part, and blows up the light weight part of the primary separated product The vibrating feeder consisting of a blower and the primary fractionated product charged in the vibrating feeder were blown with the air ionized by corona discharge to blow the glass fiber component and plastic A static elimination blower for removing static electricity charged in the finely pulverized product, a dust collector for sucking and collecting the light weight component blown up by the wire mesh portion of the vibrating feeder, and a primary separated product discharged from the other end of the vibrating feeder. It has a vertical passage through which the secondary separated product excluding the lightweight component passes, and the fine glass fiber remaining in the secondary separated product passes through one side wall surface of this passage, but the size of the plastic fine pulverized product does not pass through. A wire mesh is provided, and fine glass fibers in the secondary sorted product passing through the wire net are removed while diffusing the secondary sorted product by the airflow generated toward the wire net side by suction from the wire net side, and the wire net is A collection device that collects the finely crushed plastic that does not pass through the lower part of the passage by collecting it.
It is configured to have.

According to the invention described in claim 4 (hereinafter, referred to as "the fourth invention"), the equipment for separating and collecting the plastics from the glass fiber-reinforced reinforced plastic product, in addition to the configuration of the third invention, is provided with A tank for storing the primary fractionated product is provided under the sieve through the discharge pipe, and the glass fiber and the plastic in the primary fractionated product were charged in the middle of the discharge pipe by friction in the vibrating screener. A configuration is provided in which a static eliminator that eliminates static electricity is provided.

According to the invention of claim 5 (hereinafter referred to as "fifth invention"), the facility for separately collecting plastics from a glass fiber-reinforced reinforced plastic product has the structure of the third invention or the fourth invention. In addition, the finely pulverized material finely pulverized by the fine pulverizer is sent to the vibrating screener via the air transport pipeline, and the inner wall surface of the air transport pipeline is a mirror surface with a maximum roughness of μm or less. In addition, the minimum radius of the curved portion is 1.5 m or more.

[0012]

According to the configurations of the first and third inventions,
The waste of plastic products containing glass fiber is first roughly crushed, and this coarsely crushed product is put into a fine crusher to be finely crushed. It is subjected to crushing and peeling action due to shock and a large number of ultra high-speed vortices generated behind this wing, and high-frequency pressure vibrations generated thereby, and is finely crushed without changing the color tone of the plastic component due to burning. That is, a finely pulverized product which is a mixture of glass fibers and a finely pulverized product of plastics is obtained.

The finely pulverized product thus obtained is introduced into a vibrating screener in the first fractional recovery step, and is separated into a glass fiber component which does not pass through the sieve and a primary fractionated product which passes through the sieve. That is, most of the glass fibers are separated and removed in the primary separation and collection process. On the other hand, the primary separated products that have been separated and collected in the first separated collection process are put into a vibration feeder that is a second separated collection process. In the vibrating feeder, the primary separated product put into one end of the diaphragm vibrates and is dispersed by the diaphragm and moves toward the other end. The light weight in the primary separation product, that is, the glass fiber component is separated and blown up by the wind supplied from the blower installed on the side of the dust collector, and the blown glass fiber component is passed through the duct connected to the dust collector. Will be recovered and removed.

Moreover, since the ionized wind by the corona discharge is blown from the static elimination blower to the primary separated product put into the vibrating feeder from above, the finely pulverized plastic material and (+) which are charged to (-) by friction. Since the electrically charged glass fiber is discharged, the finely pulverized plastic material and the glass fiber are not electrically adsorbed. Therefore, it is easier to separate and blow up.

Next, the secondary fractionated product that has passed through the vibrating feeder is put into a collection device. In the collection device, a very small amount of the glass fiber component left in the secondary fractionated product that has entered the vertical passage is wire mesh. The finely pulverized plastics containing almost no glass fiber are recovered from the recovery device outlet by being removed through the wire mesh while falling downward by being sucked over.

According to the configurations of the second and fourth inventions,
The charge is removed even before the primary separated product is sent to the second separated collection process, and the separation in the second separated collection process is performed more accurately. According to the configuration of the fifth invention, the finely pulverized material is smoothly sent to the vibration sieving machine without being jammed in the air transportation pipeline.

[0017]

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described in detail below with reference to the drawings showing the embodiments thereof. FIG. 1 shows one embodiment of a separation and recovery facility for plastics from a plastic product containing glass fiber according to the present invention. This separation / recovery facility is divided into a coarse crushing step A, a fine crushing step B, a first separation processing step C, a second separation processing step D, and a recovery step E, which are sequentially processed from the coarse crushing step A to the recovery step E. , Recyclable resin components are collected from waste products such as defective molding products of glass fiber-filled vinyl chloride corrugated plates and ear trimming products.

That is, in the coarse crushing process A, defective molding products are treated by a coarse crusher (a turbo cutter manufactured by Turbo Industry Co., Ltd.) 1
In addition, the ear trimming products are respectively put into the ear crusher 2 for coarse crushing treatment, and the coarsely crushed product 4 is collected through the cyclone 3. The coarsely pulverized product 4 coarsely pulverized by the coarse pulverizer 1 or the ear pulverizer 2 includes a large number of glass fibers partially sandwiched between the coarsely pulverized products of vinyl chloride.

In the fine pulverizing step B, the coarse pulverized product 4 obtained in the coarse pulverizing step A carried by the hopper pallet truck 5 is fed to the fine pulverizer (turbo mill manufactured by Turbo Industry Co., Ltd.) 6 via the supply feeder 6a. Then, the coarsely pulverized product 4 is finely pulverized. That is, this fine crusher 6
Is designed to finely pulverize the coarsely pulverized material 4 by causing an impact by a blade rotating at a high speed, a large number of ultra-high-speed vortices generated behind the blade, and a high-frequency pressure vibration generated by the vortex. The coarsely pulverized product 4 having a sandwich structure in which glass fibers are sandwiched is put into the fine pulverizer 6 to mix the plastic component and the glass fiber component, but the glass fiber is completely mixed with the plastic. A finely pulverized product 7 that has been peeled off is obtained.

In addition, the vinyl chloride resin content in the finely pulverized product 7 has no discoloration. Next, the finely pulverized material 7 is transferred to the pneumatic transportation line 8, the cyclone 9, the rotary feeder 1
Oscillating sieving machine 11 as the first fractional recovery process C
To Since glass fibers are mixed in the finely pulverized material 7, if the inner wall surface of the air transportation pipeline 8 has irregularities or is bent suddenly, the glass fibers will adhere to that portion. , The pipe 8 is completely blocked, and the air transport pipe 8
Maintenance of is very troublesome. Therefore, in this separation / collection facility, the air transport pipe 8 is formed of a stainless steel pipe having a diameter of 150 mm and an inner wall surface buffed to a maximum roughness μm, and the minimum radius of the bend is 1.5.
The length is set to m so that the glass fibers do not adhere to block the inside of the air transportation pipeline 8.

Vibratory sieving machine 13 as the primary separation and collection step C
Is equipped with a vibrating screen 13a made of a 6-mesh wire net, and the screen non-passing part 14 containing most of the fluffy glass fibers in the finely pulverized product 7 and the remaining fine glass fiber part. The primary fractionation product 15 in which the vinyl chloride resin finely pulverized product is mixed is sieved. by the way,
Static electricity is generated due to friction during sieving by the vibration sieving machine 13, and the glass fiber and the vinyl chloride resin finely pulverized product in the primary fractionated product 15 are glass fiber (+) and vinyl chloride resin finely pulverized product, respectively. The glass fiber and the vinyl chloride resin finely pulverized product are electrically adsorbed and become difficult to be separated because they are each charged to (-). However, in this separation and collection facility, as shown in FIGS. A neutralization device 12 is provided in the middle of.

That is, the static eliminator 12 is sent from an air compressor (not shown) to the static elimination electrode 12b through the air pipe 12a so as to surround the discharge pipe 13b from all sides, and the air ionized by the static elimination electrode 12b is discharged to the discharge pipe. 13b
Is sprayed onto the falling primary fractionated product 15 to eliminate static electricity from the charged glass fiber and vinyl chloride resin finely pulverized material to prevent electrical adsorption between the glass fiber and vinyl chloride resin finely pulverized material as much as possible. ing.

As shown in FIG. 3, the static elimination electrode 12b is provided so that the air jet direction thereof is inclined with respect to the falling direction of the primary separated product 15. On the other hand, the sieved primary fractionated product 15 is stored in a tank 16 disposed below the vibrating screener 13 via a discharge pipe 13b, and then transferred by a screw conveyor 17 to perform a second fractionation treatment step. It is put into the vibration feeder 18 as D.

As shown in FIG. 4, the vibrating feeder 18 includes a hopper 18a, a vibrating plate 18b having a frame, and a blower 18c. Further, a neutralization blower 19 is provided diagonally above the diaphragm 18b. The vibrating plate 18b is configured such that the primary separated product 15 supplied to one end of the diaphragm 18a from the hopper 18a is dispersed by vibration on the vibrating plate 18b, and can be discharged as a secondary separated product 20 from an outlet provided at the other end. At the same time, a 60-mesh wire mesh portion 18e is provided in the middle portion, and the blower 18c blows air from the lower side of the wire mesh portion 18e. Further, a wire netting 18f is arranged above the diaphragm 18b so as to face the diaphragm 18b.

That is, when the primary separated product 15 that moves in the outlet direction while being dispersed by the vibration of the vibrating plate 18b reaches the wire mesh portion 18e, it is lightened by the wind supplied from the blower 15 from the lower side of the wire mesh portion 18e. Minutes,
That is, fine glass fibers having a small apparent specific gravity (single fiber glass fibers) mixed in the primary separated product 15 are blown up, and the suction duct 21 provided above the wire mesh portion 18e.
To be collected by suction to a dust collector (not shown), and the secondary fractionated product 20 containing the remaining weight, that is, the vinyl chloride resin finely pulverized product and a very small amount of glass fiber, is discharged from the outlet to the collection process E side. It has become.

On the other hand, the static elimination blower 19 includes a diaphragm 18b.
The ionized wind by corona discharge is blown from the wire mesh portion 18e to the portion from the hobber 18a. That is, the glass fiber and the vinyl chloride resin finely pulverized product in the primary sorted product 15 charged into the vibrating feeder 18 have glass fiber (+) and vinyl chloride resin finely pulverized product (-), respectively, due to static electricity due to friction. Each of them is electrically charged and electrically adsorbed, but by blowing the ionized air by the static elimination blower 19, the static electricity is eliminated, and the glass fiber portion is separated and blown up by the wire mesh portion 18e from the finely pulverized vinyl chloride resin material. Making it easier.

Finally, the secondary fractionated product 20 is put into the powder collecting device 22 (blower shifter) in the collecting step E. As shown in FIG. 4, the powder recovery device 22 includes a hopper 23, an intake pipe line 24, and a vertical pipe line 25. Hopper 23
Has an upper opening 23a provided below the outlet of the vibrating feeder 18 and a lower end opening in the middle of the intake pipe line 24.

The intake conduit 24 has one end open and the other end connected to the vertical conduit 25. The vertical pipe line 25 is provided with a 28-mesh wire netting 26 on its tube wall, and a decompression chamber 27 connected to a dust collector is provided on the opposite side with the wire netting 26 in between. In addition, the lower end of the vertical pipe line 25 faces the upper inlet of the collection tank 28, as shown in FIG.

That is, in the powder collecting device 22, the decompression chamber 27 is decompressed by the suction from the dust collector, so that the outside air is sucked from the open end of the intake pipe 24 toward the vertical pipe 24. Therefore, in the intake pipe line 24, an airflow is constantly generated from the open end toward the vertical pipe line 25, and the secondary separated product 20 supplied in the middle of the intake pipe line 24 via the hopper 23 is It is blown away in the direction of the vertical pipeline 25 while being diffused by the air flow.

The secondary sorted product 20 that has entered the vertical conduit 25 is
The glass fiber component diffused by the air flow and slightly remaining in the secondary fractionated product 20 floats while being completely separated from the vinyl chloride resin finely pulverized product. Then, only the finely pulverized product of the vinyl chloride resin falls as the recovered product 29 into the recovered product tank 28 and is stored therein. On the other hand, the glass fiber component floating in the vertical conduit 25 enters the decompression chamber 27 side through the metal net 26 and is further collected by the dust collector.

The recovered product 29 thus recovered is
The total amount of the vinyl chloride resin finely pulverized product is 8 times the total amount of the vinyl chloride resin component contained in the coarsely pulverized product 4 put into the recovery facility.
At 0%, it contained 0.02% fine glass fibers.
Further, in 15 of the primary fractionated products, the total amount of the vinyl chloride resin finely pulverized product was 89% of the total amount of the vinyl chloride resin component contained in the coarsely pulverized product 4 charged into the recovery facility.

The recovered product 29 obtained as described above is mixed with 10% of a new raw material to form a vinyl chloride resin corrugated plate,
The total light transmittance (%), the haze (%), and the amount of deflection (mm), which were molded using only new raw materials, were examined, and the results are shown in Table 1. The total light transmittance and the haze were measured using a haze meter, and the amount of deflection was examined according to the method according to JIS.

[0033]

[Table 1] As shown in Table 1 above, even if the recovered product 29 is mixed with 10% of new raw material, the obtained vinyl chloride resin corrugated sheet is obtained by molding only the new raw material, and the total light transmittance (%), Haze (%) and deflection (mm) were almost unchanged. Further, the tensile strength, impact strength, and weather resistance did not change at all.

Incidentally, the finely pulverized product 7 is separated by a sorter 10 shown in FIG.
The recovered product obtained by sorting by 0 contains 0.5% of glass fiber, and 10% of the recovered product obtained by this sorting machine 100 is added to a new raw material to form a vinyl chloride resin corrugated sheet in the same manner. In that case, the glass fibers appeared to be irregularly dispersed inside the molded product, and the appearance was very poor. As described above, if this separate collection method and separate collection equipment are used,
It is possible to efficiently collect a finely pulverized plastic product that does not contain glass fibers and has no discoloration.

The separation and recovery equipment according to the present invention is not limited to the above embodiment. For example, in the above embodiment, the primary sorted product 15 is fed from the tank 16 to the vibrating feeder 18 above the tank 16 via the screw conveyor 17.
However, the tank 16 and the screw conveyor 17 may not be provided as long as the building has a sufficient height and the vibrating screener 13 can be arranged above the vibrating feeder 18. .

Further, in the above embodiment, the static eliminator 12 was provided in the middle of the discharge pipe 13b, but it may be provided in the outlet of the screw conveyor 17 or in the middle of the air transport pipe 8. Further, in the above-mentioned embodiment, the air transport pipeline 8 is made of a stainless steel pipe whose inner wall surface is buffed, but the maximum roughness of the inner wall surface is 5
If it is not more than μm, it may be plated with chromium or the like.

[0037]

As described above, according to the configurations of the first and third inventions, plastics are produced by finely pulverizing collectable defective products generated during the manufacturing process and waste products such as ear trimming products that are inevitably generated. The finely pulverized product can be separated and recovered from the glass fiber in good yield. Moreover, the recovered finely pulverized plastic is not discolored by burning, and can be reused like a new raw material.

According to the configurations of the second and fourth inventions,
In addition to the effects of the first invention and the third invention, it becomes possible to more reliably and efficiently collect only the finely pulverized plastic material. According to the configuration of the fifth invention, the third invention or the fourth invention described above.
In addition to the effect of the invention, there is an effect that the maintenance of the facility becomes easy.

[Brief description of drawings]

FIG. 1 is a system diagram schematically showing an embodiment of a separate collection facility according to the present invention.

FIG. 2 is a cross-sectional view of a discharge pipe of the vibrating screener of the separation and recovery facility of FIG.

FIG. 3 is a vertical cross-sectional view of a discharge pipe of the vibrating screener of the separation and recovery facility of FIG.

FIG. 4 is a cross-sectional view showing an enlarged view of a vibrating feeder and a collecting device portion of FIG. 1.

FIG. 5 is a cross-sectional view of a conventional sorting machine.

[Explanation of symbols]

 B Fine Grinding Process C First Fractional Recovery Process D Second Fractional Recovery Process E Recovery Process 4 Coarse Grinded Product 6 Fine Grinding Machine 7 Finely Grinded Product 8 Air Transport Pipeline 12 Electrification Device 13 Vibrating Screening Machine 13a Wire Mesh 13b Discharge Pipe 14 Non-sieving component 15 Primary separation product 18 Vibration feeder 18b Vibration plate 18c Blower 18e Wire mesh part 19 Static eliminator blower 20 Secondary separation product 22 Powder recovery device 25 Vertical pipe line 29 Recovery product

Claims (5)

[Claims] 1. A coarsely pulverized product obtained by coarsely pulverizing a glass fiber-reinforced reinforced plastic product, an impact of a blade rotating at high speed, a large number of ultra-high-speed vortices generated behind the blade, and a high-frequency pressure vibration generated thereby. The fine pulverization step of throwing into a fine pulverizer to pulverize it into a finely pulverized product, sieving this finely pulverized product, and passing through the sieve and the non-sieving part containing most of the glass fibers remaining on the sieve. A primary separation process that separates the separated product into the separated product, and the primary separated product is supplied to one end of the diaphragm, moved to the other end of the diaphragm while vibrating, and corona discharge is applied from the upper part of the diaphragm. Ionized wind is blown to remove static electricity charged on the glass fiber and plastic in the primary separated product, and air is blown over the primary separated product passing through the wire mesh part provided in the middle part of the vibration plate, The light weight component of the primary separated product is blown up above the diaphragm, the blown up lightweight component is sucked and removed by a dust collector, and the secondary separated product from which the light weight component is removed from the primary separated product is discharged from the other end of the diaphragm. The second separation treatment step and the secondary separation product is introduced into a vertical passage provided with a wire mesh on one side surface, while the secondary separation product is diffused by an airflow generated from the wire mesh side toward the wire mesh side by suction, A method for separating and collecting plastics from glass fiber-reinforced reinforced plastic products, characterized by comprising a recovery step of removing fine glass fibers in the secondary separated product that passes through the wire net and recovering finely pulverized plastic products that do not pass through the wire net. Method. 2. A transfer process of at least one of a finely pulverized product from a fine pulverization process to a primary separation treatment process and a transfer process from a primary separation treatment process of a primary separation product to a secondary separation treatment process. The method for separating and collecting plastics from a reinforced plastic product containing glass fibers according to claim 1, wherein static electricity charged on the glass fibers and plastics is removed during the process. 3. A coarsely pulverized product obtained by coarsely pulverizing a glass fiber-containing plastic product is subjected to impact by a blade rotating at a high speed, a large number of ultra-high-speed vortices generated behind the blade, and high-frequency pressure vibration generated thereby. A fine pulverizer for fine pulverization, and a vibrating screener for separating the fine pulverized product obtained by the fine pulverizer into a sieve non-passing component containing most of the glass fibers and a primary fractionated product passing through the sieve, While moving the primary sorted product charged to one end in the direction of the other end by vibration, a diaphragm provided with a wire mesh portion in the middle portion, and provided below the wire mesh portion of this diaphragm, over the wire mesh, By blowing wind to the primary separated product passing through the wire mesh part and blowing up the light weight component in the primary separated product, a vibrating feeder consisting of a blower and the primary separated product put in the vibrating feeder are corona-discharged. A static neutralization blower that removes the static electricity charged in the glass fiber component and the finely pulverized plastic material in the primary separation product by blowing ionized wind, and a dust collector that sucks and collects the light weight component blown up by the wire mesh portion of the vibrating feeder. A vertical passage through which the secondary separated product excluding the light weight component passes from the primary separated product discharged from the other end of the vibrating feeder, and the fine particles remaining in the secondary separated product on one side wall surface of the passage. There is a wire mesh of a size that allows the glass fibers to pass but does not allow the finely pulverized plastic to pass, and passes through the wire net while diffusing the secondary separated product with the airflow generated from the wire net side toward the wire net by suction. A recovery device that removes the fine glass fibers in the secondary fractionated product and collects the finely crushed plastic that does not pass through the wire net by dropping it to the lower side of the passage. Plastic content of the separation and collection equipment from fiber-filled reinforced plastic products. 4. A tank for storing the primary fractionated product is provided below the vibrating screener through a discharge pipe, and the glass fiber in the primary sorted product is provided in the middle of the discharge pipe due to friction in the vibrating screener. 4. A facility for separately collecting and recovering a plastic component from a glass fiber-reinforced reinforced plastic product according to claim 3, further comprising a static eliminator for removing static electricity charged in the plastic and the plastic. 5. A finely pulverized material finely pulverized by a fine pulverizer is sent to a vibrating screener via an air transport pipeline, and the inner wall surface of this air transport pipeline has a maximum roughness of 5 μm or less. 5. The facility for separating and collecting plastics from glass fiber reinforced plastic products according to claim 3 or 4, wherein the curved surface has a minimum radius of 1.5 m or more.