DEVICE TO INCREASE INTRINSIC VISCOSITY OF RECYCLING POLYESTER WASTE

Abstract

The present invention relates to a device to increase intrinsic viscosity of recycling polyester waste, first, shredding the recycled polyester waste, pouring the shredded polyester waste into a melting unit for smelting for achieving melting status, after filtration, pouring the semi-finished pellet into a reactor tank, the molecular chain of the melting polyester will depolymerize to a shorter molecular chain and further repolymerize to a molecular chain fitting the requirement, and using a vacuum unit to remove the organic impurity, moisture and dirt for increasing the intrinsic viscosity of the semi-finished pellet to make intrinsic viscosity be higher than 0.65 dl/g; by processing with the reactor tank, the present invention increases intrinsic viscosity of recycling polyester waste by changing the I.V. of the RPET and the structure of the molecular chain, enhancing the quality of the RPET for increasing applicability and economic benefits of RPET.

Claims

1. A device to increase intrinsic viscosity of recycling polyester waste, comprising: a shredding unit shredding the recycled polyester waste; a melting unit, pouring the shredded polyester waste into said melting unit for smelting for achieving melting status; a filtration unit, pouring the melting polyester into said filtration unit for removing the inorganic impurity to form a semi-finished pellet; wherein a reactor tank, the reactor tank is linked to a vacuum unit and a control unit for controlling the heating temperature and time of the reactor tank; pouring the semi-finished pellet into the reactor tank under final temperature 250° C.-300° C., the molecular chain of the melting polyester will depolymerize to a shorter molecular chain, said shorter molecular chain further repolymerize to a molecular chain fitting the requirement, and using the vacuum unit to remove the organic impurity, moisture and dirt for increasing the intrinsic viscosity of the semi-finished pellet to make intrinsic viscosity be higher than 0.65 dl/g; and a cutting unit, pouring the semi-finished pellet into said cutting unit to form polyester chips.

2. The device to increase intrinsic viscosity of recycling polyester waste as claimed in claim 1, said shredding unit can be an impact breaker or a shredding machine.

3. The device to increase intrinsic viscosity of recycling polyester waste as claimed in claim 1, wherein said melting unit includes a screw type extruder.

4. The device to increase intrinsic viscosity of recycling polyester waste as claimed in claim 1, wherein said filtration unit includes a polyester melt filter.

5. The device to increase intrinsic viscosity of recycling polyester waste as claimed in claim 1, wherein said reactor tank is composed of a tank body, a tank lid, a jacket, an agitator and a driving unit, and the heating methods include electric heating, double boiling, heat transfer oil heating, far infrared heating and coil heating.

6. The device to increase intrinsic viscosity of recycling polyester waste as claimed in claim 1, wherein said vacuum unit can be a vacuum pump.

7. The device to increase intrinsic viscosity of recycling polyester waste as claimed in claim 1, wherein said control unit can be a processor or a controller.

8. The device to increase intrinsic viscosity of recycling polyester waste as claimed in claim 1, wherein the intrinsic viscosity of the semi-finished pellet is between 0.65-0.9 dl/g.

9. The device to increase intrinsic viscosity of recycling polyester waste as claimed in claim 1, wherein said cutting unit can be a slicer or a granulator.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0017] FIG. 1 is a schematic diagram illustrating a polyester waste recycling system according to the prior art;

[0018] FIG. 2 is a flow diagram of an applicable embodiment of the recycling steps of the present invention;

[0019] FIG. 3 is a schematic diagram illustrating the structure of the polyester waste recycling device of the present invention;

[0020] FIG. 4 is a schematic diagram illustrating the structure of the reactor tank of the present invention.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT

[0021] For better understanding of present invention, I provide the embodiment and drawing enclosed for detailed description. Those who skilled in the art can understand purpose, feature and benefit of the present invention from the contents disclosed in this specification. Kindly noted that the present invention can be implemented or applied through other different specific embodiments and based on different viewpoints various details in this specification can be various changed without departing from the spirit of the present invention. In addition, the drawings attached to the present invention are merely a schematic illustration and they are not depicted in actual dimensions. The following embodiments will further describe the related technical content of the present invention in detail, but the disclosed content is not intended to limit the technical scope of the present invention.

[0022] Referring to FIGS. 2-4, FIG. 2 disclosed a flow diagram of an applicable embodiment of the recycling steps of the present invention, FIG. 3 is a schematic diagram illustrating the structure of the polyester waste recycling device 80 of the present invention. Said polyester waste recycling device 80 comprises: a shredding unit 10, shredding the recycled polyester waste; the polyester waste includes: PET waste cloth, waste PET fiber and PET flake, these materials need to be shredded base on their own characteristic before melting process, wherein the PET flake do not need to be shredded. In this embodiment have a shredding unit 10 for shredding PET waste, said shredding unit 10 can be an impact breaker or a shredding machine. The impact breaker and the shredding machine can be conventional products, so I won't mention its details in the specification.

[0023] a melting unit 20, pouring the shredded polyester waste into said melting unit 20 for smelting for achieving melting status; in this embodiment, the melting unit 20 includes a screw type extruder.

[0024] a filtration unit 30, pouring the melting polyester into the filtration unit 30 for removing the inorganic impurity to from a semi-finished pellet; in this embodiment, the filtration unit 30 includes a polyester melt filter, when the melting PET material came out from the screw type extruder 20 and going into the filtration unit 30, when the melt fill up the filtration chamber, under the influence of pressure, the melt went through the filter disc, the filter disc blocks the impurity and the gel particles with larger grain size, the filtered melt went through the filter disc and mixed via the core cube, and further came out from the outlet.

[0025] The technology of the equipment above mentioned are belonged to prior art, so I won't mention its details in the specification.

[0026] A reactor tank 40, said reactor tank 40 is connected to a vacuum unit 50 and a control unit 60, said control unit 60 controls the heating temperature and time of said reactor tank 40, said reactor tank 40 adjusts the process detail based on the characteristics of different kinds recycled polyester; in this embodiment, said control unit 60 can be a processor or a controller.

[0027] Referring to FIG. 4, in this embodiment, the reactor tank 40 is composed of a tank body 41, a tank lid 42, a jacket 43, a agitator 44 and a driving unit 45, and the heating methods include electric heating, double boiling, heat transfer oil heating, far infrared heating and coil heating.

[0028] Pouring the semi-finished pellet into the reactor tank 40 under final temperature 250° C.-300° C., depolymerizing the molecular chain of the melting polyester and repolymerizing the homogeneous molecular chain, using a vacuum unit 50 to remove the organic impurity, moisture and dirt for increasing the intrinsic viscosity of the semi-finished pellet to make intrinsic viscosity be higher than 0.65 dl/g; In this embodiment, the intrinsic viscosity characterizes the molecular chain, the higher the intrinsic viscosity is, the stronger the molecular chain is, by processing with the reactor tank 40, the polyester will depolymerize to a shorter molecular chain, said shorter molecular chain further repolymerize to a molecular chain fitting the requirement, and achieve changing the intrinsic viscosity, the melting point, and the structure of molecular chain to enhance the quality. The intrinsic viscosity of said semi-finished pellet is higher than 0.65 dl/g, and to deal with the different kinds of PET waste and requirements, using the processing method of the present invention can make the intrinsic viscosity to be between 0.65-0.9 dl/g or 0.7-0.8 dl/g.

[0029] A cutting unit 70, pouring the semi-finished pellet into the cutting unit 70 to form RPET chips. In this embodiment, the cutting unit 70 can be a slicer or a granulator. However, the technology of the slicer and the granulator are belonged to prior art, so I won't mention its details in the specification.

[0030] With the feature above mentioned, by processing with the reactor tank 40, the present invention increases intrinsic viscosity of recycling polyester waste by changing the I.V. of the RPET and the structure of the molecular chain, works suitable for RPET, and solves the problems application limit problems of RPET and increased the economic benefits.

[0031] Although particular embodiments of the invention have been described in detail for purposes of illustration, various modifications and enhancements may be made without departing from the spirit and scope of the invention. Accordingly, the invention is not to be limited except as by the appended claims.