OA16892A - A method for recycling waste thermoplastic materials and using this recycled thermoplastic in composite material production. - Google Patents

Abstract

This invention is related to a method for production of high strength and low cost thermoplastic composite materials by processing and treating waste plastic materials with some minerals. The object of the invention is to embody a recycling method wherein it contains high amounts of additives and therefore composite materials with high strength properties are obtained. Another object of the invention is to embody a recycling method wherein high amounts of additives are used in the production and the machines used in the production are not damaged.

Description

A METHOD FOR RECYCLING WASTE THERMOPLASTIC . MATERIALS AND USING THIS RECYCLED THERMOPLASTIC IN . COMPOSITE MATERIAL PRODUCTION

Field of the Invention

This invention is related to a method for production of high strength and low cost thermoplastic composite materials by processing and treating waste plastic materials with some minerais.

Background of the invention '

Nowadays, since the cost of materials such as wood, métal, iron, gypsum etc. is high, composite materials that can be substituted for the above mentioned materials arc produced.

Thermoplastic composite materials are mainly produced by processing plastic materials and adding various chemical and other additives into the plastics. The aim of these additions is to improve the mechanical and chemical properties of the thermoplastic materials without increasing costs. Ncvertheless, the manufactured thermoplastics do not hâve the desired cost. This situation also makes it barder to use these materials in construction and building industries. .

Now recycling methods are also used in obtaining thermoplastic composite materials. Il is more préférable to obtain plastic materials thaï will be used in the thermoplastic composite materials from the waste plastics collected from the garbage, both from an economical and an environmental point of view. However, when materials on the waste plastics such as dirt, oil, chemicals etc. can not be removed completcly, the quality of the obtained thermoplastic composite material gets lower.

The recycling methods of the waste plastic materials mainly consist of the following steps; séparation of the waste plastics from the foreign materials, cutting the plastic materials into small pièces, melting and casting into desired 5 molds, cooling and obtainîng the desired producL Besidcs, various thermoplastic composite materials are produced by adding additives to plastic materials during this above mentioned melting process.

In the Japanese patent document No. JP 2007130885 of the known state of the art, 10 a high strength, good endurance and long life composite material production system is disclosed. In this method, the emphasized process is primarily to déterminé the amount and size of the additive that will be given to the plastic..

Secondly, the amount and type of the additive is determined. The 3* step is about melting the mixture and controllîng the predetermined amount and type of the 15 additive of the mixture formed in the mold.

In the Japanese patent document No. JP 2009132939 of the known state of the art, a durable composite material production technique is disclosed wherein waste plastic materials are used as raw material and additives arc mixed in. The 20 recyclable plastic first contains polymer and secondly polymer and résiduel additives.

In the Japanese patent document No. JP 2010234812 of the known state of the art, u high strength, good endurance and long life plastic mold production method is 25 disclosed by employing various techniques and melhods. For recycling waste plastic materials that contains 2 or more additives, the waste material is separated from the foreign materials, then melted and molded, respectively. The métal is separated from the plastic by mixture filtration method and after détermination of the type and amount of additive, the separated mêlai and the additives are added 30 to the recydabl e pl astic.

t ln the Japanese patent document No. JP 2004042461 ofthe known state ofthe art, the management of the processes such as washing off lhe dirt, oil, earth, undesired . chemicals and food wastes on the waste plastics that contain foreign materials, séparation and drying is disclosed. The recyclable plastic material is powdcred in a liquid by cutting into small pièces. Then the plastic material is adhered or the materials contained within are separated from the plastic. The materials that indicate their positions are separated by liquid séparation, plastic or plastic melting.

However, the amount of additives that will be mixed into the plastic materials is ' very important for the strength of the products to be obtained. When more additives (chemicals or minerais) can be added, the strength of the obtained material becomesproportionally higher. BuL as high amounts of additives are mixed into the waste plastics, the melting of this mixture becomes more problematic. Usually thèse procedures are performed in extrader machines. In extraders, plastic waste materials and additives are fed in and composite material in dough form is obtained. ln this situation, when a high amount of additive is mixed into the mixture, wearing and break downs occur in the machines, when the additives are used in low amounts the materials can not achîeve the desired 20 strength properties. '

In the plastic processing machines that are used in the known state of the art that run by Systems such as Injection and extrusion, the working principle is forcing the melted material under pressure to exit through a hole. In lhe system, there is a 25 feeding zone (a cône or a side feeding screw), a worm gear (also called as an · Archimedes screw, it has compression and pushtng tasks) and a cylindrical body (shell) where ‘the gear moves inside and that can rcsist high pressures and températures up to 500 C. This situation increases the production and operation costs ofthe machine.

Moreover, in the plastic processing machines that are used in the known state of the art that run by Systems such as injection and extrusion, more wearing occurs on the machines since the filler materials that hâve hard and abrasive properties arc fed starting from the thermoplastic feeding zone. This situation increases the maintenance and repairment costs of the machine.

Furthermore, in the plastic processing machines that arc used în the known state of the art that nin by Systems such as injection and extrusion, when the melted mixture reaches the compression zone, it can not be compressed since the 10 minerais are not compressible and it causes the gear to be jammed or broken by generating very high counter torque forces. Therefore, high amounts of minerais are not used in melted thermoplastic mixtures and the mixture can not reach the desired strength value.

Moreover, in the plastic processing machines that are used tri the known state of the art that run by Systems such as injection and extrusion, very spécial molds need to be used. The price of these molds is very high. ·

Furthermore, In the plastic processing machines that tire used in the known state 20 of the art that run by Systems such as injection and extrusion, the material is injected into the mold by the machine itself and also the required pressure is generated by the machine itself. Therefore, these machines are very complicatcd and ex pensive.

Moreover, in the plastic processing machines that are used in the known state of the art that run by Systems such as injection and extrusion, since the molds are attached to the machine, the machines should not work while the material is cooling in the mold. As a resuit, these system runs by a start and stop principlc and their production capacity is low.

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Another problem is waiting the cool*down period after pressing the plastic material in dough form into a mold. In this situation, the machines can not run until the composite material in the mold cools.

Brief description of the invention

The object of the invention is to embody a recycling method for waste plastics of which the production costs are decreased.

Another object of the invention is to embody a recycling method wherein the 10 waste plastics are cleaned from the materials on them such as dirt, oil, chemicals ‘ etc.

Yet another object of the invention is to embody a recycling method wherein it . contains high amounts of additives and therefore composite materials with high 15 stren gth properties are obtained.

Yet another object of the invention is to embody a recycling method wherein high amounts of additives are used in the production and the machines used in the production are not damaged.

Yet another object of the invention is to embody a recycling method that provides low energy consumption.

The method of recycling waste plastic materials and using these recycled plastics 25 in composite material production which is performed în order to achieve the objects of the invention comprises the steps of;

- Rclcasing a number of types of baledthermoplastic waste materials by feeding into a baie opening machine (110),

- Feeding the waste plastic materials into a séparation unit and in there

0 séparation from rocks, earth, sand and other coarse foreign materials ( 120), • Fecding the waste plastic material into the cutting machine, cutting the waste plastic material into small pièces through high speed blades and at the same time washing by injecting water into the machine (130), , - Fecding the waste plastic materials eut into small pièces to a muddy water séparation machine and séparation of slîmed material from the muddy water by centrifugal forces (140),

- Transferring the material into a pool fîllcd with water, rinsing in there and at the same time précipitation of sand and other heavy materials that may hâve left on it (150), .

* Transferring the material into the organic contamination séparation machine and here eleaning ofthe oil and other organic foretgn materials on the material that can not be removed in the previous processes by centriftiga] forces (160),

- Transferring the material to the water séparation machine and there separating the water and moisture on the maieria] by centrifugal forces (170),

- Storing the material by transferring to storage silos (180),

- Transferring the material into the drying machine and here drying the material by healing and at the same time powdering it by crinkling for easy fecding to machines in the future processes (190),

- Storing the dried and crinkled material by transferring to storage silos (200), · ' - Transferring the material to the horizontal reactor (210),

- Heating the material in the horizorilal reactor under pressure up to 350 °C température (220),

- Adding the painter and the compatibilizer chemical materials to the material heated in the horizontal reactor through a side feeding unit (230),

- Adding minerai materials, through another side feeding unit, to the material in which painter and compatibilizer chemical materials hâve been added and which is being heated in the horizontal reactor (240),

- Heating the plastic material untîl linear links are broken, cross links are cstablishcd and materials are rclinked to each other at the molecular level (250),

- Immediately pouring the melted composite material exiting from the horizontal reactor into the molds before it cools down and cooling under pressure by compression inside the mold (260).

Detailed description of the invention

The method of recycling waste plastic materials and using these recycled plastic materials in composite material production which is performed In order to achieve the object of the invention is illustrated In appended figure, wherein;

FIGURE-1 Is the flow chart ofthe method.

First, a number of types of thermoplastic waste plastic material are fed into a baie opening machine and the comprcssed waste plastic malerial is released. (110) .

The waste plastic materials is fed Info a séparation unit and in there separated from rocks, earth, sand and other coarsc forei gn materials. (120)

The waste plastic material ts fed into the cutting machine, the waste plastic material is eut into small pièces through high speed blades and at the same time washed by injecting water into the machine. (130)

The waste plastic materials eut Into small pièces are fed to a muddy water séparation machine and the slimed material is separated from the muddy water by centrifiigal forces. (140)

Then the material is transfencd into a pool filled with water, rinsed in there and at the same time sand and other heavy materials that may hâve left on it is precipitated. (150)

The material is transferred into the organic contamination séparation machine and here the oil and other organic forci gn materials on the material that can not be removed in the previous processes are cleaned off by centrifugal forces. (160)

The material is transferred to the water séparation machine and there the water and moisture on the material is separated by centrifugal forces. (170)

Then the material is stored by transferring to storage silos. (180)

I

The mQterial is transferred Into the drying machine and here the material is dried by heating and at the same time powdered by crinklîng for easy feeding to machines tn the future processes. (190)

The dried and crinkled material is stored by transferring to storage silos. (200)

The material is transferred to the horizontal reactor. (210)

The material is heated in the horizontal reactor under pressure up to 350 °C i

température. (220)

The pointer and the compatibilizer chemical materials are injected to the material heated in the horizontal reactor through a side feeding unit. (230)

The minerai materials are injected to the system through another side feeding unit. 25 (240)

The mixture is continuously mixed and heated until the linear links of the plastic material is broken and branched, cross links form and materials are rclinked to each other at molecular level and the réaction is waîted to end. (250)

The melted composite material exiting from the horizontal reactor is immedîately poured into the molds before it cools down and cooled under pressure by .

compression inside the molds. (260) ' .

In the method according to the Invention, a high amount of additives can be added to the thermoplastics since there is no compression after the filler material ls added and no large countcr torques arc generated.

In the system according to the invention, the loss of energy for heating is prevented by adding the filler material in the reaction stage after the plastic materials arc melted and unnecessary energy consumptton for the filler materials is prevented.

In the system according to the invention, the wearing on the machines is mlnimized since the filler materials and the minerais are fed Into the reactor after the plastic materials arc melted.

The method according to the invention provides a huge amount of energy snving. In the plastic processing machines that are currently in use that work by Systems such as injection and extrusion, the filler material is inilially fed into the machines with the thermoplastic materials and the mixture is required to be heated up to the melting température of the thermoplaslics. Here energy must be consumcd for heating both the thermoplastics and the filler materials. In the system according to the invention, no energy must be consumed for heating the filler materials since the filler materials are fed into the system ai a later stage.

In the method according to the invention, the melted composite material exiting from the horizontal reactor is immedîately poured Into the molds and cooled under pressure by compression. A multiple-mold system is employed depending on the capacity of the horizontal reactor and the cooling time of the melted composite material in the mold. The molds are piaced sequentially, one mold is filled and left to cool and the ncxt molds is processed. The compression in the molds is performed by hydraulic presses. Non flooding compression molding method is used in the system. By this method, the plastic material that has a large volume with a certain weight is compressed in the mold by pressure into the molding 5 cavity with a smallcr volume. In the non flooding compression molds, the driving punch is matched to the mold cavity as in a cylinder-piston system.

In the method according to the invention, the molds are simple and produced very cheapty since the non flooding compression molding method is used.

ln the method according to the invention, since the pressure required for compressing the molds is provided by the hydraulic presses which are separate parts of the system, the machines tn the system are not required to bc very complîcated and thus the investment costs are low.

In the method according to the invention, since the molds that are used are not attached to the machine and a multiple mold system is employed, the other machines continue to run while the material is cooling in the mold. As a resuit, the method according to the invention nuis by continuous working principle and the 20 production capacity is high.

Claims (4)

1. A method for recycling waste plastic materials and using this recycled plastic in composite material production, comprises the steps of;

- Releasing a number of types of compressed thermoplastic waste materials by feeding into a baie opening machine (110), • Feeding the waste plastic materials into a séparation unit and in there séparation from rocks, earth, sand and other coarsc foreign materials (120),

- Feeding the waste plastic material into the cutting machine, cutting the waste plastic material into small pièces through high speed blades and at the same time washing by injecting water into the machine (130),

- Feeding the waste plastic materials cul into small pièces to a muddy water séparation machine and séparation of slimed material from the muddy water by centrifugal forces (140),

- Transferring the waste plastic material into a pool filled with water, rinsing in there and at the same time précipitation of sand and other heavy materials that may hâve left on it (150),

- Transferring the waste plastic material into the organic contamination séparation machine and here cleanîng of the oil and other organic foreign materials on the waste plastic material that can not be removed in the previous processes by centrifugal forces (160),

- Transferring the waste plastic material to the water séparation machine and there separating the water and moisture on the material by centrifugal forces (170),

- Storing the waste plastic material by transferring to storage silos (180),

- Transferring the waste plastic material into the drying machine and here drying the waste plastic material by heating and at the same time powdering it by crinkling for easy feeding to machines in the future processcs (190),

- Storing the dried and crinkled waste plastic material by transferring to storage silos (200),

- Transferring the waste plastic material to the horizontal reactor (210),

- Heating the waste plastic material in the horizontal reactor until it melts under pressure up to 350 °C température (220), characterized ln that, the method also comprises the steps of;

5 - Adding the painter and the compatibilizer chemical materials to the waste plastic material melted in the horizontal reactor through a side feeding unit (230),

- Adding minerai materials, through another side feeding unit in the horizontal reactor, to the melted waste plastic material in which painter and

10 compatibilizer chemical materials hâve been added (240),

- Further heating and mixing the melted waste plastic material with the additives (250),

- Immediately pouring the melted composite material free flowing from the horizontal reactor into the independent detached molds before it cools

15 down and cooling under pressure by compression inside the molds by means of individual hydraulie presses. (260)