KR101749334B1 - Apparatus and method for recycling nylon wasted yarns - Google Patents
Apparatus and method for recycling nylon wasted yarns Download PDFInfo
- Publication number
- KR101749334B1 KR101749334B1 KR1020150103540A KR20150103540A KR101749334B1 KR 101749334 B1 KR101749334 B1 KR 101749334B1 KR 1020150103540 A KR1020150103540 A KR 1020150103540A KR 20150103540 A KR20150103540 A KR 20150103540A KR 101749334 B1 KR101749334 B1 KR 101749334B1
- Authority
- KR
- South Korea
- Prior art keywords
- nylon
- strand
- extruder
- extruded
- molten
- Prior art date
Links
- 229920001778 nylon Polymers 0.000 title claims abstract description 208
- 239000004677 Nylon Substances 0.000 title claims abstract description 205
- 238000000034 method Methods 0.000 title claims abstract description 64
- 238000004064 recycling Methods 0.000 title description 5
- 238000001125 extrusion Methods 0.000 claims abstract description 50
- 238000005520 cutting process Methods 0.000 claims abstract description 28
- 238000001035 drying Methods 0.000 claims abstract description 25
- 238000001816 cooling Methods 0.000 claims abstract description 22
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 20
- 239000000126 substance Substances 0.000 claims abstract description 19
- 238000010298 pulverizing process Methods 0.000 claims abstract description 18
- 239000000155 melt Substances 0.000 claims abstract description 11
- 238000011045 prefiltration Methods 0.000 claims description 15
- 239000000843 powder Substances 0.000 claims description 10
- 238000005086 pumping Methods 0.000 claims description 8
- 238000002844 melting Methods 0.000 claims description 4
- 230000008018 melting Effects 0.000 claims description 4
- 239000002245 particle Substances 0.000 claims description 3
- 238000010438 heat treatment Methods 0.000 claims description 2
- 229910001220 stainless steel Inorganic materials 0.000 claims description 2
- 239000010935 stainless steel Substances 0.000 claims description 2
- 235000012438 extruded product Nutrition 0.000 claims 1
- 102100026827 Protein associated with UVRAG as autophagy enhancer Human genes 0.000 abstract description 9
- 101710102978 Protein associated with UVRAG as autophagy enhancer Proteins 0.000 abstract description 9
- 239000002994 raw material Substances 0.000 abstract description 8
- 238000011069 regeneration method Methods 0.000 abstract description 8
- 230000001172 regenerating effect Effects 0.000 abstract description 6
- 238000004519 manufacturing process Methods 0.000 abstract description 5
- 230000008929 regeneration Effects 0.000 abstract description 3
- 238000007380 fibre production Methods 0.000 abstract 1
- 239000007788 liquid Substances 0.000 description 16
- 239000000835 fiber Substances 0.000 description 9
- 229920002994 synthetic fiber Polymers 0.000 description 6
- 239000012209 synthetic fiber Substances 0.000 description 6
- 238000010586 diagram Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000008188 pellet Substances 0.000 description 3
- 241001442654 Percnon planissimum Species 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 229920000728 polyester Polymers 0.000 description 2
- 238000006424 Flood reaction Methods 0.000 description 1
- 229920003188 Nylon 3 Polymers 0.000 description 1
- 239000004952 Polyamide Substances 0.000 description 1
- -1 acryl Chemical group 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 229920006351 engineering plastic Polymers 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000010309 melting process Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000012188 paraffin wax Substances 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 229920002647 polyamide Polymers 0.000 description 1
- 239000011164 primary particle Substances 0.000 description 1
- 229920001059 synthetic polymer Polymers 0.000 description 1
Images
Classifications
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
- D01D1/00—Treatment of filament-forming or like material
- D01D1/04—Melting filament-forming substances
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D35/00—Filtering devices having features not specifically covered by groups B01D24/00 - B01D33/00, or for applications not specifically covered by groups B01D24/00 - B01D33/00; Auxiliary devices for filtration; Filter housing constructions
- B01D35/02—Filters adapted for location in special places, e.g. pipe-lines, pumps, stop-cocks
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C23/00—Auxiliary methods or auxiliary devices or accessories specially adapted for crushing or disintegrating not provided for in preceding groups or not specially adapted to apparatus covered by a single preceding group
- B02C23/08—Separating or sorting of material, associated with crushing or disintegrating
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
- D01D5/00—Formation of filaments, threads, or the like
- D01D5/08—Melt spinning methods
- D01D5/088—Cooling filaments, threads or the like, leaving the spinnerettes
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F6/00—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
- D01F6/58—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products
- D01F6/60—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products from polyamides
Landscapes
- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Mechanical Engineering (AREA)
- Food Science & Technology (AREA)
- General Chemical & Material Sciences (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Abstract
The present invention relates to a regeneration apparatus and a regeneration method of a nylon pascal which can uniformly pulverize and extrude nylon filaments generated in the course of fiber production by nylon yarn so as to be reused as raw materials for production of nylon filament.
To this end, the present invention provides a nylon pacer reproducing apparatus comprising: a pulverizer which cuts and crushes nylon pulses into a predetermined size; a pulverizing feeder which supplies the pulverized pulses at a constant rate; an extruder which melts and extrudes pulverized pulses; A first and a second filter for removing foreign substances in the nylon melt extruded in the extruder; a gear pump for compensating the extrusion pressure of the melt extruded nylon and volumetically feeding the melt to maintain a constant flow rate; and a molten nylon, A cooling unit for water cooling the nylon strand extruded in the extrusion die in a water tank; a drying unit for drying the nylon strand cooled in the cooling unit; and a drying unit for drying the nylon strand dried by the drying unit A cutting section for cutting a predetermined length into nylon chips and a controller for controlling the operation of the above- And a regenerating method and a regenerating method of the nylon panel constructed.
Description
The present invention relates to a regeneration apparatus and regeneration method of nylon pascal, and more particularly, to a regeneration apparatus and regeneration method of nylon pascal, which comprises cutting and pulverizing nylon papermas produced in the course of producing fibers by nylon yarn, melt extruding the extruded nylon fibers, And then recycled as a raw material for production of nylon. BACKGROUND OF THE INVENTION
In general, Nylon is a synthetic polymer polyamide, a synthetic fiber developed by DuPont in 1935, in an attempt to substitute synthetic plastic for a substitute for natural silk. In 1938, it was the world's first full- It was sold as synthetic fiber.
Such synthetic fibers, nylon, are used in various fields such as tire cords, automobile parts, and the like, which are manufactured from yarn of fabric, that is, yarn, for women's stockings, military parachutes, armor, fire extinguisher, underwear and socks.
On the other hand, nylon, which is a synthetic fiber, is spun by fibers made of nylon yarn, and nylon yarns such as fibers are produced during the production of fibers by nylon yarns. And is recycled.
Conventional mixed-paced reproduction apparatuses for reproducing various synthetic fiber materials such as nylon and polyester are disclosed in Patent Registration No. 10-0355004 (published on Oct. 10, 2002).
Such conventional reproducing apparatus of the mixed-pacer is for making fibers by mixing fibers of various kinds of synthetic fiber materials, polyester, nylon, acryl, etc., and recycling the remaining pa- per, so that the reproducing apparatus of the mixed- So that the molten liquid in the molten chamber 18 is discharged into the discharge port 16 by means of the rotary tool 17. In this case,
However, since the above-described conventional mixing-type regenerating apparatus merely mixes and melts the mixture to be discharged, it is difficult to reuse the original recycled material because it contains foreign substances.
Conventionally, there is a device for regenerating nylon filament. However, since there is a problem as described below, the nylon filament regenerated by a conventional apparatus is merely recycled as an engineering plastic, Has not been reused.
First, the conventional nylon-pacer reproducing apparatus has a problem in that the melting time of the nylon pacer is not constant since the uneven nylon pacer raw material mixed in a lump form or the like is manually introduced into the regenerating apparatus.
Second, in the conventional nylon-pacer reproducing apparatus, since the diameter of the extruding die for extruding the liquid nylon in which the nylon pascals are melted is large and the strand of extruded nylon is not constant because the extrusion pressure is not constant, There is a problem that the size is not uniform.
Third, the conventional nylon-pacer reproducing apparatus has a problem that nylon chips are not in good quality due to foreign substances mixed in the nylon pads.
Therefore, there is a demand for development of a recycling apparatus and a regeneration method of nylon pacer in order to solve the above problems and reuse the nylon papa as a raw material for the original nylon company.
Disclosure of Invention Technical Problem [8] Accordingly, the present invention has been made in order to solve the above problems, and it is an object of the present invention to provide a nylon filament yarn which is produced by cutting nylon filaments, It is an object of the present invention to provide a nylon pacifier reproducing apparatus which minimizes foreign matter in molten nylon and uniformizes the size of nylon chips so that the nylon chips can be reused as raw materials for producing original nylon yarns.
It is another object of the present invention to provide a method for regenerating nylon papa which can be reused as a raw material for producing original nylon yarn produced in the process of producing fibers by nylon yarn.
The present invention relates to a pulverizer for pulverizing nylon pulp to a predetermined size; A crushing feeder for uniformly feeding the pulverized powder to the extruder by means of a screw conveyor; An extruder which melts and extrudes the supplied pulverized powder by an electric heater; A pre-filter for primarily removing foreign matters from melt-extruded molten nylon; A gear pump for compensating an extruding pressure of the molten nylon melt extruded by the extruder and performing a volume feed to maintain a constant flow rate; A fine filter for secondarily removing foreign matter from molten nylon which is pressure-fed by the gear pump; An extrusion die for extruding molten nylon into a strand having a thickness of 2.5 mm; A strand cooling unit for water-cooling the nylon strand extruded from the extrusion die in a water tank; A strand drying unit for drying the nylon strand cooled in the strand cooling unit; A strand cutting unit for cutting a nylon strand dried by the strand drying unit into a predetermined length and processing the nylon strand into a nylon chip; And a controller for controlling the operation of the above-described configuration.
In the present invention, an extrusion pressure sensor is further provided between the extruder and the pre-filter to control the rotation speed of the motor of the extruder in accordance with the pressure of the molten nylon to be extruded.
In addition, the present invention provides a method for producing a nylon filament yarn, A pulverized powder supplying step of uniformly supplying pulverized powder to the extruder by means of a screw conveyor; A melt extrusion process in which the supplied pulverized powder is melted and extruded by an electric heater; A primary foreign matter removing process for removing foreign substances in the extruded molten nylon; A volumetric pumping process for volumetrically feeding the molten nylon by a gear pump to back up the discharge pressure; A second foreign matter removing process for removing foreign substances in the molten nylon to be volume pumped; A nylon strand extrusion process for extruding the extruded molten nylon into a strand having a thickness of 2.5 mm; A strand cooling process for submerging the nylon strand in a water tank; Strand drying process for drying nylon strands; And a strand cutting process for cutting the nylon strand into a predetermined length and processing the strand into a regenerated nylon chip.
In the present invention, the melt extrusion process further includes a pressure interlocking extrusion control process for controlling the rotation speed of the motor of the extruder in conjunction with the pressure of the molten nylon extruded from the extruder.
The present invention has the following effects by means of solving the above-mentioned problems.
First, according to the present invention, nylon paraffin raw material is pulverized into a predetermined size and shape by a pulverizer which cuts and pulverizes nylon pulp to a predetermined size, and the pulverized pulp is uniformly supplied to an extruder by a pulverizer feeder, which is a screw conveyor, There is an effect that the melting of the nylon layer can be performed uniformly and quickly.
Secondly, since the volume pumping is performed by the gear pump that compensates the extrusion pressure of the molten nylon melt-extruded in the extruder and performs volume-pushing so as to maintain a constant flow rate, extrusion in the extrusion die is constantly performed, A pre-filter is provided at the front end and a fine filter is provided at the rear end of the gear pump to remove foreign matter in a first and a second order, thereby minimizing the foreign matter content of the regenerated nylon chip.
Thirdly, the present invention has an extrusion die having a nozzle of 2.5 mm so that the thickness of the extruded nylon strand is reduced by extruding the molten nylon so that the size of the regenerated nylon chip becomes uniform, and the extruder and the pre- the pressure of the molten nylon extruded from the extruder controls the rotation speed of the motor of the extruder in accordance with the pressure of the molten nylon extruded by the extruder so that the flow rate of the molten nylon extruded from the extruder is kept constant, The nylon strand is uniformly maintained.
Brief Description of the Drawings Fig. 1 is a diagram showing a main configuration example of an embodiment of a nylon-pacer reproducing apparatus according to the present invention. Fig.
BACKGROUND OF THE INVENTION 1. Field of the Invention [0001] The present invention relates to a nylon-
3 is a diagram illustrating an example of a process of a method for reproducing a nylon layer according to an embodiment of the present invention.
Fig. 4 is a process example of another embodiment of the nylon pacer reproducing method according to the present invention. Fig.
Hereinafter, embodiments of the present invention will be described in detail with reference to the accompanying drawings.
FIG. 1 is a view showing a main configuration of an embodiment of a reproducing apparatus for a nylon panel according to the present invention, and FIG. 2 is a diagram illustrating a configuration of a nylon panel reproducing apparatus according to another embodiment of the present invention.
The main point of the present invention is to regenerate the fiber so that the remaining nylon fiber can be reused as a raw material for producing nylon fiber during production of fiber by nylon yarn.
That is, the present invention provides a pellet mill for cutting and pulverizing nylon pellets to a predetermined size, a crushing
In the present invention, the pulverizer (10) cuts nylon particles mixed in a lump shape or the like into a predetermined size and shape to be crushed.
The pulverizing
The
The molten nylon melt-extruded in the
Here, a pre-filter 41 that primarily removes foreign matter contained in the molten nylon in the liquid state and a fine-
The
On the other hand, a heat insulating layer may be formed on the outer surface of the extrusion die 50 in order to maintain a constant temperature in the extrusion process of the nylon strand.
The
The
Also, in the present invention, a pre-filter 41 for protecting the
Between the
Hereinafter, a method of reproducing a nylon layer according to the present invention will be described.
FIG. 3 is a flowchart illustrating a method of reproducing a nylon layer according to an exemplary embodiment of the present invention. FIG. 4 is a flowchart illustrating an exemplary method of reproducing a nylon layer according to an exemplary embodiment of the present invention. Referring to FIG.
That is, the present invention relates to a process for producing a pulverized pulp which comprises a pulverizing
In the present invention, the
The
The primary foreign
The nylon
In the present invention, the regeneration method of the nylon pascal is a pressure interlocking
Meanwhile, the regenerated nylon chip manufactured through the above process is transferred to a silo (not shown) to be stored.
Hereinafter, the operation of the nylon pacer reproducing apparatus and the reproducing method according to the present invention will be described.
As described above, in the nylon pacer reproducing apparatus, there is provided a
In the present invention, the extrusion die (50) is pumped through a volume pumping process (140) by a gear pump (40) which compensates the extrusion pressure of molten nylon melted and extruded in the extruder (30) The extrusion molding of the nylon strand at a constant speed is achieved.
In the present invention, a pre-filter 41 provided at the front end of the
In addition, in the present invention, the nylon
In the present invention, the pressure of the molten nylon extruded from the
10: crushing mill 20: crushing crushing feeder
30: extruder 40: gear pump
41: pre-filter 42: fine filter
50: extrusion die 60: strand cooling section
70: strand drying section 80: strand cutting section
90: Controller 91: Extrusion pressure sensor
110: crushing process 120: crushing process
130: extrusion melting process 131: pressure interlocking extrusion control process
140: Volume pumping process 141: Primary particle removal process
142: Secondary foreign matter removal process 150: Nylon strand extrusion process
160: Strand cooling process 170: Strand drying process
180: Strand cutting process
Claims (6)
An extrusion pressure sensor 91 is provided between the extruder 30 and the pre-filter 41 to control the rotational speed of the motor M of the extruder 30 according to the pressure of the molten nylon to be extruded ; The pre-filter 41 and the fine filter 42 are made of stainless steel and each mesh has a mesh size of 150 to 400 meshes.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1020150103540A KR101749334B1 (en) | 2015-07-22 | 2015-07-22 | Apparatus and method for recycling nylon wasted yarns |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1020150103540A KR101749334B1 (en) | 2015-07-22 | 2015-07-22 | Apparatus and method for recycling nylon wasted yarns |
Publications (2)
Publication Number | Publication Date |
---|---|
KR20170011250A KR20170011250A (en) | 2017-02-02 |
KR101749334B1 true KR101749334B1 (en) | 2017-06-21 |
Family
ID=58151441
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
KR1020150103540A KR101749334B1 (en) | 2015-07-22 | 2015-07-22 | Apparatus and method for recycling nylon wasted yarns |
Country Status (1)
Country | Link |
---|---|
KR (1) | KR101749334B1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20220117936A (en) | 2021-02-17 | 2022-08-25 | 하이테크필라(주) | Manufacturing method of monofilament yarn using recycled nylon |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107675277A (en) * | 2017-10-20 | 2018-02-09 | 新凤鸣集团股份有限公司 | The recycling equipment and its reuse method of a kind of polyester waste silks |
CN108453926B (en) * | 2018-02-06 | 2023-10-31 | 瑞安市君诚塑胶制造有限公司 | Processing equipment for preparing nylon particles from nylon return materials |
CN108842197B (en) * | 2018-08-21 | 2020-03-27 | 深圳市友邦工程塑料有限公司 | Polyamide fiber production process |
KR101954223B1 (en) * | 2018-09-12 | 2019-03-05 | 한국화학연구원 | Flat type melt-electro spinning apparatus for mass production of Nano-fiber and the method of Solvent-free Melt-electro spinning |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR200314928Y1 (en) * | 2003-01-07 | 2003-06-02 | 김우성 | Manufacturing system using used chemical fiber |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100355004B1 (en) | 2000-07-11 | 2002-10-05 | 이귀영 | Device of restoration melting an mixing fiber |
-
2015
- 2015-07-22 KR KR1020150103540A patent/KR101749334B1/en active Search and Examination
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR200314928Y1 (en) * | 2003-01-07 | 2003-06-02 | 김우성 | Manufacturing system using used chemical fiber |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20220117936A (en) | 2021-02-17 | 2022-08-25 | 하이테크필라(주) | Manufacturing method of monofilament yarn using recycled nylon |
Also Published As
Publication number | Publication date |
---|---|
KR20170011250A (en) | 2017-02-02 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
KR101749334B1 (en) | Apparatus and method for recycling nylon wasted yarns | |
KR101448824B1 (en) | Method for recycling plastic materials | |
TWI658921B (en) | Device and method for the production of a filled polymeric composite material | |
EP0638017B1 (en) | Process and device for recycling blown plastics | |
KR101679322B1 (en) | Manufacturing device of filamant for 3d printer using waste plastics | |
CN110552085A (en) | polyester waste cloth and waste silk recycling system and recycling method thereof | |
KR20120065881A (en) | Meting and extruding unit for recycling resin | |
KR100411955B1 (en) | The automatically regenerated apparatus of polystyrene plastic foam and the method thereof | |
JP2010030176A (en) | Method for manufacturing thermoplastic resin composition pellet | |
EP3835347A1 (en) | A device to increase intrinsic viscosity of recycling polyester waste | |
JP2001088196A (en) | Pellet making apparatus | |
KR100866308B1 (en) | A film recycling machine | |
KR20220122883A (en) | Extruder for Recycling of Vinyl Waste | |
KR200282691Y1 (en) | Device for manufacturing synthetic wood | |
JPS62167012A (en) | Granulating equipment | |
JPH04301409A (en) | Manufacture of polyvinyl alcohol base molded form | |
JP2002178388A (en) | Method for manufacturing extrusion by extruder | |
KR200250216Y1 (en) | The automatically regenerated apparatus of polystyrene plastic foam | |
WO2024048485A1 (en) | Method for producing polycarbonate resin molded product | |
CN213830316U (en) | Plastic film blowing machine with waste recovery mechanism | |
JP7376139B2 (en) | Manufacturing method of recycled composite material | |
KR101938594B1 (en) | Extruder | |
EP3835346A1 (en) | A method to increase intrinsic viscosity of recycling polyester waste | |
JP2000044808A (en) | Aggregate for asphalt mixture | |
JP2000000848A (en) | Injection molding machine, device for manufacture of recycled resin, method for injection molding, manufacture of recycled resin, injection molding article, and recycled resin |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A201 | Request for examination |