KR102599800B1 - Manufacturing method of recycled PET chip using waste PET - Google Patents

Manufacturing method of recycled PET chip using waste PET Download PDF

Info

Publication number
KR102599800B1
KR102599800B1 KR1020210134694A KR20210134694A KR102599800B1 KR 102599800 B1 KR102599800 B1 KR 102599800B1 KR 1020210134694 A KR1020210134694 A KR 1020210134694A KR 20210134694 A KR20210134694 A KR 20210134694A KR 102599800 B1 KR102599800 B1 KR 102599800B1
Authority
KR
South Korea
Prior art keywords
pet
flakes
waste pet
recycled
transparent
Prior art date
Application number
KR1020210134694A
Other languages
Korean (ko)
Other versions
KR20230052320A (en
Inventor
이경희
김혁태
김동현
김민재
Original Assignee
이경희
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 이경희 filed Critical 이경희
Priority to KR1020210134694A priority Critical patent/KR102599800B1/en
Publication of KR20230052320A publication Critical patent/KR20230052320A/en
Application granted granted Critical
Publication of KR102599800B1 publication Critical patent/KR102599800B1/en

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B9/00Making granules
    • B29B9/02Making granules by dividing preformed material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B11/00Making preforms
    • B29B11/02Making preforms by dividing preformed material, e.g. sheets, rods
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B11/00Making preforms
    • B29B11/06Making preforms by moulding the material
    • B29B11/10Extrusion moulding
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/0026Recovery of plastics or other constituents of waste material containing plastics by agglomeration or compacting
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/0026Recovery of plastics or other constituents of waste material containing plastics by agglomeration or compacting
    • B29B17/0047Compacting complete waste articles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/02Separating plastics from other materials
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/04Disintegrating plastics, e.g. by milling
    • B29B17/0412Disintegrating plastics, e.g. by milling to large particles, e.g. beads, granules, flakes, slices
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B9/00Making granules
    • B29B9/02Making granules by dividing preformed material
    • B29B9/06Making granules by dividing preformed material in the form of filamentary material, e.g. combined with extrusion
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/001Combinations of extrusion moulding with other shaping operations
    • B29C48/0022Combinations of extrusion moulding with other shaping operations combined with cutting
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/022Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the choice of material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/50Details of extruders
    • B29C48/69Filters or screens for the moulding material
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G63/00Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/78Preparation processes
    • C08G63/80Solid-state polycondensation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B9/00Making granules
    • B29B9/16Auxiliary treatment of granules
    • B29B2009/165Crystallizing granules
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • B29B2017/001Pretreating the materials before recovery
    • B29B2017/0015Washing, rinsing
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/02Separating plastics from other materials
    • B29B2017/0203Separating plastics from plastics
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/02Separating plastics from other materials
    • B29B2017/0213Specific separating techniques
    • B29B2017/0217Mechanical separating techniques; devices therefor
    • B29B2017/0231Centrifugating, cyclones
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/04Disintegrating plastics, e.g. by milling
    • B29B2017/0424Specific disintegrating techniques; devices therefor
    • B29B2017/0468Crushing, i.e. disintegrating into small particles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2067/00Use of polyesters or derivatives thereof, as moulding material
    • B29K2067/003PET, i.e. poylethylene terephthalate
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/20Waste processing or separation
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/52Mechanical processing of waste for the recovery of materials, e.g. crushing, shredding, separation or disassembly
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/62Plastics recycling; Rubber recycling

Abstract

본 발명은 고유점도(IV)가 낮은(0.72dl/g) 저급의 폐PET로부터 투명한 폐PET만의 선별 및 용융에 의한 정제공정으로 순도를 높이고, 고상중합에 의해 고유점도(IV)가 높은(8 ~ 1.02dl/g) 리싸이클 PET 칩 제조방법에 관한 것이다.
본 발명의 제조방법은 투명 폐PET병만을 선별한 후, 플레이크 형상으로 분쇄하고 저온에서 습식으로 재차 분쇄한 다음, 원심분리에 의해 순수한 투명 폐PET만을 수득하는 정선공정 및 용융에 의한 정제공정과, 수분에 의한 가수분해 방지를 위해 결정화 및 고상중합공정과, 리싸이클 PET 칩을 제조하는 공정으로 이루어진다.
본 발명은 복수의 정선공정 및 용융에 의한 정제공정에 의해 순도를 향상시키서 고상중합으로 고품위의 리싸이클 PET 칩을 제조하는 효과를 나타내므로 보다 고품질의 PET 성형제품을 생산할 수 있어 부가가치가 높은 다양한 제품을 제조하는데 적합하여 상업적으로 매우 유리한 장점을 지니고 있다.
The present invention improves purity through a purification process by selecting and melting only transparent waste PET from low-grade waste PET with low intrinsic viscosity (IV) (0.72 dl/g), and produces high intrinsic viscosity (IV) (8 ~ 1.02dl/g) Regarding the manufacturing method of recycled PET chips.
The manufacturing method of the present invention includes selecting only transparent waste PET bottles, pulverizing them into flakes, grinding them again in a wet manner at low temperature, and then centrifuging to obtain only pure transparent waste PET bottles, a selection process and a purification process by melting, It consists of crystallization and solid-state polymerization processes to prevent hydrolysis due to moisture, and a process to manufacture recycled PET chips.
The present invention has the effect of producing high-quality recycled PET chips through solid-state polymerization by improving purity through multiple selection processes and refining processes by melting, so that higher quality PET molded products can be produced, and various products with high added value can be produced. It is suitable for manufacturing and has a very commercially advantageous advantage.

Description

폐PET를 활용한 고품위 리싸이클 PET 칩의 제조방법{Manufacturing method of recycled PET chip using waste PET}Manufacturing method of recycled PET chip using waste PET}

본 발명은 폐PET를 활용한 리싸이클 PET 칩의 제조방법에 관한 것이며 보다 구체적으로는 폐PET 폐기물로부터 투명한 폐PET의 순도 및 고유점도를 향상시킨 고품위 리싸이클 PET 칩을 제조하는 방법에 관한 것이다.The present invention relates to a method of manufacturing recycled PET chips using waste PET, and more specifically, to a method of manufacturing high-quality recycled PET chips with improved purity and intrinsic viscosity of transparent waste PET from waste PET waste.

폴리에틸렌테레프탈레이트(polyethylene terephthalate; PET)는 결정성이 크고 용융점이 높아 섬유뿐만 아니라 필름 , 음료용기, 사출형 재료 등 다양한 용도에 사용되고 있으며, PET는 무게가 가볍고 강도가 커서 깨지지 않으며, 우수한 투명성 및 가스에 대한 저투과성, 높은 광투과율의 특성 때문에 유리용기 대체물로 탄산음료, 생수, 과즙음료 등의 음료용기로 많이 사용되고 있다.Polyethylene terephthalate (PET) has large crystallinity and a high melting point, so it is used in a variety of applications such as fibers, films, beverage containers, and injection molding materials. PET is light in weight, has high strength, does not break, has excellent transparency, and is resistant to gases. Due to its characteristics of low transmittance and high light transmittance, it is widely used as a substitute for glass containers as beverage containers for carbonated drinks, bottled water, and juice drinks.

PET는 열가소성 수지이므로 사용된 폐PET는 용융에 의해 재생이 가능하며 현재 폐PET 재활용 기술로는 기계적 재활용 방법과 화학적 재활용방법 및 소각에 의한 에너지 회수 등의 재활용방법이 있으며, 화학적 재활용방법이 고품질의 제품을 얻을 수 있으나, 기술적인 접근이 어렵고, 처리시설 등 비용이 높은 문제가 있고, 소각에 의한 에너지 회수 등의 재활용방법은 소각시 다이옥신 등 유해한 화합물이 생성되기 때문에 환경을 오염시키는 문제가 있으므로 비용이 적게 들고 공해문제가 없는 기계적 재활용 방법을 이용하는 것이 적절한 방법이라 하겠다.Since PET is a thermoplastic resin, used waste PET can be recycled by melting. Current waste PET recycling technologies include mechanical recycling, chemical recycling, and energy recovery through incineration. Chemical recycling is a high-quality recycling method. The product can be obtained, but there are problems such as difficult technical access, high costs such as treatment facilities, and recycling methods such as energy recovery through incineration have the problem of polluting the environment because harmful compounds such as dioxin are generated during incineration. The appropriate method would be to use a mechanical recycling method that costs less and does not cause pollution problems.

폐PET 폐기물로부터 고품질의 재생 PET의 생산을 위해서는 폐PET의 화학적 재활용 방법이나 기계적 재활용 방법의 구분없이 폐PET 폐기물로부터 순수한 폐PET를 선별하는 것이 중요하며, 폐PET의 선별이 적절하지 못하여 이종의 합성수지 또는 폐PET 폐기물에 부착된 라벨 등이 혼입되면 재생 PET의 성형작업시에 가수분해 등에 의한 분자량 감소로 물성이 저하되어 재생 PET 제품의 품질에 문제가 발생한다.In order to produce high-quality recycled PET from waste PET waste, it is important to select pure waste PET from waste PET waste regardless of whether it is a chemical recycling method or a mechanical recycling method. Since the selection of waste PET is not appropriate, heterogeneous synthetic resins are produced. Alternatively, if labels attached to waste PET waste are mixed, the physical properties deteriorate due to a decrease in molecular weight due to hydrolysis during the molding process of recycled PET, causing problems in the quality of recycled PET products.

폐PET의 재활용 방법과 관련한 선행기술로 예를 들면, 특허문헌1에 고유점도(Ⅳ)가 0.95dl/g으로 높고, 분포 범위가 주로 0.60 내지 0.80dl/g으로 넓은 PET재를 수집하는 단계, 수집한 재료를 혼합하고 이를 사실상 다수의 불균일한 플레이크형 및 토막(chunk)형 단편을 포함하는 이종 Ⅳ 재료 혼합물로 재형성시키는 단계 및 이종 혼합물을 직접 고체 상태 중합(SSP)시켜 평균 Ⅳ가 0.90dl/g 이상인 이종재료를 형성시키는 단계를 포함하는, 고성능 플라스틱 스트랩의 제조에 사용하기에 적합한 PET재의 제조방법은 고유점도(IV)가 다소 높은 재활용 PET병 플레이크를 고성능 PET 스트랩을 제조하고 있으며, 특허문헌2에는 압축된 페트병을 투입하는 투입단계와, 상기 투입단계에서 압축되어 투입된 페트병을 해체하고, 페트병에 부착된 이물질을 분리시킴과 동시에 페트병의 색상별로 선별 분리하는 선별단계와, 상기 선별단계에서 선별이 완료된 후 일정 크기로 분쇄하여 PET칩이 형성되는 분쇄단계와, 상기 분쇄단계에서 분쇄된 PET칩을 냉수와 온수를 이용하여 이물질 및 라벨용 본드, 약품을 제거하는 세척단계와, 상기 세척단계에서 세척된 PET칩에 잔류하는 습기 및 이물질을 제거하는 건조단계와, 상기 선별단계, 분쇄단계, 세척단계, 건조단계에서 발생되는 오염물질을 포집제거하는 집진부로 이루어진 것을 특징으로 하는 페트병 재생방법을 개시하고 있다.For example, in the prior art related to the recycling method of waste PET, Patent Document 1 includes the steps of collecting PET material with a high intrinsic viscosity (IV) of 0.95 dl/g and a wide distribution range of mainly 0.60 to 0.80 dl/g; mixing the collected materials and reforming them into a heterogeneous IV material mixture comprising substantially a plurality of heterogeneous flake-like and chunk-like fragments and subjecting the heterogeneous mixture to direct solid state polymerization (SSP) such that the average IV is 0.90 dl. A method of manufacturing a PET material suitable for use in the manufacture of a high-performance plastic strap, which includes the step of forming a dissimilar material having a weight of more than /g, involves manufacturing a high-performance PET strap using recycled PET bottle flakes with a somewhat high intrinsic viscosity (IV), and the patented method is Document 2 includes an input step of injecting compressed PET bottles, a sorting step of dismantling the compressed PET bottles and injecting them in the input step, separating foreign substances attached to the PET bottles, and sorting the PET bottles by color, and the sorting step. A pulverizing step in which PET chips are formed by pulverizing them to a certain size after the selection is completed, a washing step in which foreign substances, label bonds, and chemicals are removed from the PET chips pulverized in the pulverizing step using cold water and hot water, and the washing step. A PET bottle recycling method comprising a drying step for removing moisture and foreign substances remaining in the washed PET chips, and a dust collection section for collecting and removing contaminants generated in the selecting, grinding, washing, and drying steps. It is starting.

또 특허문헌 3에 폐 폴리에스테르 제품을 분쇄하여 플레이크(flake)를 제조하는 공정; 잔류 수분율이 0.1 중량% 이하가 되도록 상기 플레이크를 건조하는 공정; 및 상기 건조된 플레이크를 녹여 재생 폴리에스테르 용융액을 제조하는 공정을 포함하되 상기 플레이크를 건조하는 공정은 60 내지 200 ℃의 온도 및 1 내지 24 시간 동안 수행되는 것을 특징으로 하는 재생 폴리에스테르 중합체의 제조방법을 개시하고 있다.Additionally, Patent Document 3 discloses a process for producing flakes by pulverizing waste polyester products; A process of drying the flakes so that the residual moisture content is 0.1% by weight or less; And a process for preparing a recycled polyester melt by melting the dried flakes, wherein the process of drying the flakes is performed at a temperature of 60 to 200 ° C. for 1 to 24 hours. A method for producing a recycled polyester polymer. is starting.

본 발명의 발명자는 폐PET 폐기물로부터 투명한 폐PET의 정선 및 정제와 기계적 재활용 기술을 이용하여 순도 및 점도를 향상시켜 고품위의 리싸이클 PET 칩을 제조하는 방법을 개발하고 본 발명을 완성하였다.The inventor of the present invention developed a method for manufacturing high-quality recycled PET chips from waste PET waste by improving purity and viscosity using transparent waste PET selection and purification and mechanical recycling technology, and completed the present invention.

KRKR 10-0257284 10-0257284 B1B1 KRKR 10-0895529 10-0895529 B1B1 KRKR 10-1417193 10-1417193 B1B1

본 발명에서 해결하려는 과제는 폐PET(polyethylene terephthalate; PET)로부터 투명한 폐PET만의 정밀한 정선 및 용융에 의한 정제로 순도를 높이고, 고상중합에 의해 고유점도를 향상시킨 고품위 리싸이클 PET 칩의 제조방법을 제공하는 것이며, 보다 상세하게는 고유점도(IV)가 낮은(0.72dl/g) 저급의 폐PET로부터 투명한 폐PET만의 정밀한 정선 및 용융에 의한 정제에 의해 순도를 높이고, 고상중합에 의해 고유점도(IV)가 높은(8 ~ 1dl/g) 리싸이클 PET 칩을 제조하는 방법의 제공을 목적으로 하는 것이다.The problem to be solved in the present invention is to provide a method for manufacturing high-quality recycled PET chips that improve the purity of waste PET (polyethylene terephthalate; PET) by precise selection and melting of transparent waste PET and improve intrinsic viscosity through solid-state polymerization. In more detail, the purity is increased by precise selection and melting purification of transparent waste PET only from low-grade waste PET with low intrinsic viscosity (IV) (0.72 dl/g), and the intrinsic viscosity (IV The purpose is to provide a method of manufacturing recycled PET chips with high (8 ~ 1 dl/g).

본 발명에 따른 과제의 해결수단으로 폐PET를 활용한 리싸이클 PET 칩의 제조방법은 수집된 폐PET 폐기물로부터 투명 폐PET만을 선별한 후, 플레이크 형상으로 분쇄하고, 저온에서 습식으로 재차 분쇄한 다음, 원심분리에 의해 순수한 투명 폐PET만을 수득하는 복수의 정선공정, 용융에 의한 정제공정, 가수분해 방지를 위한 결정화공정, 고상중합공정 및 고상중합물을 용융압출하여 리싸이클 PET 칩을 제조하는 공정을 포함하는 것으로 이루어진다.As a means of solving the problem according to the present invention, the method of manufacturing recycled PET chips using waste PET is to select only transparent waste PET from the collected waste PET waste, crush it into flakes, and crush it again in a wet manner at low temperature, A plurality of selection processes to obtain only pure transparent waste PET by centrifugation, a purification process by melting, a crystallization process to prevent hydrolysis, a solid phase polymerization process, and a process of melting and extruding the solid polymer to produce recycled PET chips. It is made up of

본 발명의 폐PET를 활용한 리싸이클 PET 칩의 제조방법에 따른 일 실시형태는 a). 수집된 폐PET로부터 투명 폐PET만을 선별한 다음, 투명 폐PET를 압착하는 선별공정, b). 압착된 폐PET를 플레이크 형태로 분쇄한 다음, 투명 PET 플레이크만을 분리하는 제1차 정선공정, c). 투명 폐PET 플레이크를 습식분쇄하고 분쇄물을 원심분리하여 이물질을 제거하고 투명 폐PET 분쇄물을 얻는 제2차 정선공정, d). 투명 폐PET 분쇄물을 제습 및 건조하는 건조공정, e). 건조된 투명 폐PET 분쇄물을 용융온도에서 용융압출 및 용융상태에서 필터링하여 냉각한 다음, 플레이크 형태로 분쇄하여 재생 PET플레이크를 제조하는 정제공정, f). 재생 PET 플레이크를 결정화하는 결정화공정, g). 결정화된 재생 PET 플레이크를 고상중합시키는 고상중합공정 및 h). 고상중합물을 용융온도 조건에서 압출하고 커팅하여 칩으로 성형하는 리싸이클 PET칩 제조공정을 포함하는 것으로 이루어진다.One embodiment of the method for manufacturing recycled PET chips using waste PET of the present invention is a). A sorting process that selects only transparent waste PET from the collected waste PET and then compresses the transparent waste PET, b). The first sorting process c) crushes the compressed waste PET into flakes and then separates only the transparent PET flakes. The second sorting process, d), where transparent waste PET flakes are wet-grinded and the grinded product is centrifuged to remove foreign substances and obtain transparent waste PET flakes. Drying process to dehumidify and dry transparent waste PET pulverized material, e). A refining process, f), in which the dried transparent waste PET pulverized material is melt-extruded at the melting temperature, filtered and cooled in the molten state, and then pulverized into flakes to produce recycled PET flakes. Crystallization process to crystallize recycled PET flakes, g). Solid-state polymerization process and h) for solid-state polymerization of crystallized recycled PET flakes. It consists of a recycled PET chip manufacturing process in which the solid polymer is extruded under melting temperature conditions, cut, and molded into chips.

본 발명의 폐PET를 활용한 리싸이클 PET 칩의 제조방법에 따른 보다 구체적인 또 다른 실시형태는 a). 수집된 폐PET로부터 오염물질을 제거하고 투명 폐PET만을 선별한 다음, 선별된 투명 폐PET를 압착하는 선별공정, b). 압착된 폐PET를 5 ~ 10㎜ 크기의 플레이크 형태로 분쇄한 다음, 투명 PET 플레이크만을 분리하는 제1차 정선공정, c). 투명 폐PET 플레이크를 5 ~ 10℃에서 습식분쇄하고 분쇄물을 원심분리하여 투명 폐PET 분쇄물을 얻는 제2차 정선공정, d). 투명 폐PET 분쇄물을 잔류수분이 0.1중량% 이하로 제습 및 건조하는 건조공정, e). 건조된 폐PET 분쇄물을 용융온도에서 용융압출 및 용융상태에서 필터링하고 냉각하여 3 ~ 5㎜ 크기의 플레이크 형태로 분쇄하여 재생 PET 플레이크를 제조하는 정제공정, f). 재생 PET 플레이크를 140 ~ 165℃에서 일정시간 결정화하는 결정화공정, g). 결정화된 재생 PET 플레이크를 진공조건에서 질소가스를 충진하고 180 ~ 220℃에서 고상중합시키는 고상중합공정 및 h) 고상중합물을 용융온도 조건에서 압출하고, 커팅하여 PET 칩으로 성형하는 리싸이클 PET 칩 제조공정을 포함하는 것으로 이루어진다.Another more specific embodiment according to the manufacturing method of recycled PET chips using waste PET of the present invention is a). A sorting process that removes contaminants from the collected waste PET, selects only the transparent waste PET, and then compresses the selected transparent waste PET, b). The first sorting process c) crushes the compressed waste PET into flakes with a size of 5 to 10 mm and then separates only the transparent PET flakes. Second selection process, d), where transparent waste PET flakes are wet-grinded at 5 to 10°C and centrifuged to obtain transparent waste PET flakes. Drying process of dehumidifying and drying transparent waste PET pulverized material to a residual moisture of 0.1% by weight or less, e). A refining process to produce recycled PET flakes by melt-extruding the dried waste PET pulverized material at the melting temperature, filtering the molten state, cooling, and pulverizing it into flakes with a size of 3 to 5 mm, f). Crystallization process in which recycled PET flakes are crystallized at 140 ~ 165℃ for a certain period of time, g). a solid-state polymerization process in which crystallized recycled PET flakes are filled with nitrogen gas under vacuum conditions and subjected to solid-state polymerization at 180 to 220°C; and h) a recycled PET chip manufacturing process in which the solid polymer is extruded under melting temperature conditions, cut, and formed into PET chips. It consists of including:

본 발명에 따른 리싸이클 PET 칩의 제조방법은 순도가 향상되고, 8 ~ 1dl/g의 높은 고유점도(IV)를 갖는 리싸이클 PET 펠릿이 제조되므로 높은 고유점도가 요구되는 PET용기, 건축자재, 탄산수용기, 고강력 폴리에스터 장섬유 등 부가가치가 높은 다양한 제품을 제조하는데 적합하다.The manufacturing method of recycled PET chips according to the present invention improves purity and produces recycled PET pellets with a high intrinsic viscosity (IV) of 8 to 1 dl/g, so it can be used in PET containers, building materials, and carbonate receptors that require high intrinsic viscosity. It is suitable for manufacturing a variety of products with high added value, such as high-strength polyester long fibers.

본 발명에 따른 폐PET를 활용한 리싸이클 PET 칩의 제조방법은 복수의 정선공정 및 용융에 의한 정제공정에 의해 순도를 향상시킨 후 고상중합에 의해 고품위의 리싸이클 PET 펠릿을 제조하는 효과를 나타내므로 보다 고품질의 PET 성형제품을 생산할 수 있어 부가가치가 높은 다양한 제품을 제조하는데 적합하므로 상업적으로 매우 유리한 장점을 지니고 있다.The manufacturing method of recycled PET chips using waste PET according to the present invention has the effect of improving purity through a plurality of selection processes and a purification process by melting and then manufacturing high-quality recycled PET pellets through solid-state polymerization. It has a very commercial advantage as it can produce high-quality PET molded products and is suitable for manufacturing a variety of products with high added value.

도 1은 본 발명의 폐PET를 활용한 고품위 리싸이클 PET 칩의 제조공정을 개략적으로 나타낸 도면Figure 1 is a diagram schematically showing the manufacturing process of high-quality recycled PET chips using waste PET of the present invention.

이하에서는 본 발명을 실시하기 위하여 보다 구체적으로 설명하지만 아래 기재 내용에 의해 본 발명이 한정되는 것은 아니다.Hereinafter, the present invention will be described in more detail for carrying out the present invention, but the present invention is not limited by the contents described below.

첨부한 도 1은 본 발명의 폐PET를 활용한 고품위 리싸이클 PET 칩의 제조공정을 개략적으로 나타낸 도면으로 도 1을 참고하면서 본 발명을 구체적으로 설명하기로 한다.The attached Figure 1 is a diagram schematically showing the manufacturing process of high-quality recycled PET chips using waste PET of the present invention. The present invention will be described in detail with reference to Figure 1.

본 발명에 따른 폐PET를 활용한 리싸이클 PET 칩의 제조방법은 a). 수집된 폐PET로부터 투명 폐PET만을 선별한 다음, 투명 폐PET를 압착하는 선별공정, b). 압착된 폐PET를 플레이크 형태로 분쇄한 다음, 투명 PET 플레이크만을 분리하는 제1차 정선공정, c). 투명 폐PET 플레이크를 습식분쇄하고 분쇄물을 원심분리하여 이물질을 제거하고 투명 폐PET 분쇄물을 얻는 제2차 정선공정, d). 투명 폐PET 분쇄물을 제습 및 건조하는 건조공정, e). 건조된 투명 폐PET 분쇄물을 용융온도에서 용융압출 및 용융상태에서 필터링하여 냉각한 다음, 플레이크 형태로 분쇄하여 재생 PET 플레이크를 제조하는 정제공정, f). 재생 PET 플레이크를 결정화하는 결정화공정, g). 결정화된 재생 PET 플레이크를 고상중합시키는 고상중합공정 및 h) 고상중합물을 용융온도 조건에서 압출하고 커팅하여 칩으로 성형하는 리싸이클 PET칩 제조공정을 포함하는 것으로 이루어진다.The manufacturing method of recycled PET chips using waste PET according to the present invention is a). A sorting process that selects only transparent waste PET from the collected waste PET and then compresses the transparent waste PET, b). The first sorting process c) crushes the compressed waste PET into flakes and then separates only the transparent PET flakes. The second sorting process, d), where transparent waste PET flakes are wet-grinded and the grinded product is centrifuged to remove foreign substances and obtain transparent waste PET flakes. Drying process to dehumidify and dry transparent waste PET pulverized material, e). A refining process in which the dried transparent waste PET pulverized material is melt-extruded at the melting temperature, filtered and cooled in the molten state, and then pulverized into flakes to produce recycled PET flakes, f). Crystallization process to crystallize recycled PET flakes, g). It includes a solid-state polymerization process of solid-state polymerization of crystallized recycled PET flakes, and h) a recycled PET chip manufacturing process of extruding and cutting the solid-state polymer at a melting temperature and forming it into chips.

본 발명에 따른 상기 선별공정은 수집된 폐PET로부터 투명 폐PET을 선별한 후 오염물질, 라벨 등을 제거하고, 압착하여 투명 폐PET만을 얻는 공정이며, 수집된 폐PET는 다양한 형태의 폐기되는 PET제품이며, 특별하게 한정되는 것은 아니지만 회수작업 및 정선작업에 유리한 폐PET 병을 수집하는 것이 바람직하다.The sorting process according to the present invention is a process of selecting transparent waste PET from the collected waste PET, removing contaminants, labels, etc., and compressing to obtain only transparent waste PET. The collected waste PET is disposed of in various forms. It is a product, and although it is not particularly limited, it is desirable to collect waste PET bottles, which are advantageous for recovery and sorting operations.

상기 선별공정의 투명 폐PET의 선별은 광학선별기를 이용하여 육안으로 구분이 어려운 유색 폐PET 등을 분리 및 제거하고, 투명 폐PET만을 선별하며, 선별된 투명 폐PET는 분쇄효율을 높이기 위하여 압착한다.The selection of transparent waste PET in the above sorting process uses an optical sorter to separate and remove colored waste PET that is difficult to distinguish with the naked eye, select only transparent waste PET, and press the selected transparent waste PET to increase grinding efficiency. .

본 발명에 따른 상기 제1차 정선공정은 압착된 투명 폐PET를 플레이크 형상으로 절단 및 분쇄하고 세척하여 투명 폐PET 플레이크를 얻는 공정으로 정선공정은 재생과정에서 PET의 물성변화를 최소화하고 순도를 향상시키는 공정이다.The first selection process according to the present invention is a process of obtaining transparent waste PET flakes by cutting, crushing, and washing compressed transparent waste PET into flakes. The selection process minimizes changes in physical properties of PET during the recycling process and improves purity. It is a process that is done.

상기 제1차 정선공정은 압착된 투명 폐PET병을 5 ~ 10㎜ 크기의 폐PET 플레이크로 절단 및 분쇄한 후, 폐PET 플레이크를 가열수단이 설치된 세척조에 투입하여 70 ~ 80 ℃의 온수로 세척한 다음, 스크린하여 투명 폐PET 플레이크만을 분리하는 것으로 이루어진다.In the first selection process, the compressed transparent waste PET bottle is cut and crushed into waste PET flakes of 5 to 10 mm in size, and then the waste PET flakes are placed in a washing tank equipped with a heating means and washed with hot water at 70 to 80 ° C. Then, it is screened to separate only transparent waste PET flakes.

상기 제1차 정선공정에 의해 투명 폐PET에 부착된 라벨, 점착제 등이 온수에 의해 분리되어 세척조 상부로 부유하므로 세척수를 유월시켜 부유물을 제거하고, 폐PET 플레이크 보다 입자가 작고, 무거운 금속 등의 이물질은 스크린 작업으로 분리되어 투명 폐PET 플레이크 만으로 분리된다.Through the first selection process, labels, adhesives, etc. attached to transparent waste PET are separated by hot water and float to the top of the washing tank, so the washing water is passed through to remove floating matter, and the particles are smaller than waste PET flakes and heavy metals, etc. Foreign substances are separated by screen work and separated into only transparent waste PET flakes.

본 발명에 따른 상기 제2차 정선공정은 투명 폐PET 플레이크를 저온에서 습식분쇄에 의해 분쇄한 분쇄물을 원심분리하여 투명 폐PET 분쇄물을 얻는 2차적인 정선공정이며, 습식분쇄기를 이용하여 5 ~ 10℃에서 상기 제1차 정선공정의 플레이크 보다 작은 크기로 분쇄하는 것으로 이루어진다.The secondary sorting process according to the present invention is a secondary sorting process in which transparent waste PET flakes are centrifuged by wet grinding at low temperature to obtain transparent waste PET flakes. Using a wet grinder, 5 It consists of pulverizing at ~10°C to a size smaller than the flakes of the first selection process.

상기 제2차 정선공정의 습식분쇄기는 본 발명이 속하는 기술 분야에서 널리 이용되고 있으며, 투명 폐PET 플레이크에 부착된 점착제는 저온에서 경도가 높아져 보다 쉽게 분리시킬 수가 있으며, 상기 제1차 정선공정의 플레이크 보다 작은 크기의 입자로 분쇄된 습식분쇄물은 원심분리에 의해 침강되어 투명 폐PET 분쇄물로 얻어진다.The wet grinder of the second sifting process is widely used in the technical field to which the present invention belongs, and the adhesive attached to the transparent waste PET flakes increases in hardness at low temperatures and can be separated more easily. Wet pulverized material pulverized into particles smaller than flakes is sedimented by centrifugation to obtain transparent waste PET pulverized material.

본 발명에 따른 상기 건조공정은 PET가 가수분해에 의해 중합도가 감소되어 PET의 물성 저하를 초래하므로 이를 방지하기 위하여 투명 폐PET 분쇄물로부터 수분을 제거하는 공정이며, 제습기 등을 이용하여 잔류수분이 0.1중량% 이하가 되도록 제습 및 건조하는 것으로 이루어진다. The drying process according to the present invention is a process of removing moisture from transparent waste PET pulverized material in order to prevent the decrease in the degree of polymerization of PET due to hydrolysis, resulting in a decrease in the physical properties of PET, and removing residual moisture using a dehumidifier, etc. It consists of dehumidifying and drying to less than 0.1% by weight.

본 발명에 따른 상기 정제공정은 최종생성물인 리싸이클링 PET 펠릿의 순도를 향상시키기 위하여 상기 건조된 투명 폐PET 분쇄물을 용융압출하고, 용융상태에서 필터링하여 용융물에 함유된 이물질을 제거하고, 상온으로 냉각한 후 일정크기로 절단한 압출물을 일정크기의 플레이크 형태로 분쇄하여 순도가 향상된 재생 PET 플레이크를 얻는 예비 재생공정이다. In the purification process according to the present invention, in order to improve the purity of the final product, recycled PET pellets, the dried transparent waste PET pellets are melt-extruded, filtered in the molten state to remove foreign substances contained in the melt, and cooled to room temperature. This is a preliminary recycling process to obtain recycled PET flakes with improved purity by crushing the extruded product cut to a certain size into flakes of a certain size.

상기 정제공정은 건조된 투명 폐PET 분쇄물을 압출기를 이용하여 용융온도 275 ~ 280℃, 최대압력 110bar으로 용융압출하며, 용융상태의 PET를 진공도 10mbar에서 20미크론의 스테인레스스틸 필터로 통과시켜 용융물 내에 함유된 이물질을 제거하여 고순도의 재생 PET 압출물을 얻으며, 상온으로 냉각한 후 일정하게 절단하고, 플레이크 형태로 분쇄하여 재생 PET를 얻는 것으로 이루어진다.In the purification process, dried transparent waste PET pulverized material is melted and extruded using an extruder at a melt temperature of 275 to 280°C and a maximum pressure of 110 bar, and the molten PET is passed through a 20 micron stainless steel filter at a vacuum degree of 10 mbar to be contained in the melt. This consists of removing the contained foreign substances to obtain high-purity recycled PET extrudate, cooling it to room temperature, cutting it into pieces, and pulverizing it into flakes to obtain recycled PET.

또 상기 재생 PET는 후속하는 결정화공정 및 고상중합공정에서 반응효율을 향상시키기 위해 중합반응의 면적을 넓히는 것이 바람직하며, 3 ~ 5㎜크기의 플레이크 형태로 분쇄하여 재생 PET 플레이크로 얻는 것이 바람직하다.In addition, it is desirable to expand the polymerization area of the recycled PET in order to improve reaction efficiency in the subsequent crystallization process and solid-state polymerization process, and it is preferable to obtain recycled PET flakes by pulverizing them into flakes with a size of 3 to 5 mm.

본 발명에 따른 상기 결정화공정은 상기 재생 PET 플레이크를 예열 및 건조하여 결정화하는 공정이며, 결정화공정은 재생 PET 플레이크의 투입량 및 결정화온도에 따라 결정화 시간이 다를 수 있으나 일반적으로 140 ~ 165℃에서 1 ~ 2시간정도 결정화하는 것으로 이루어진다. The crystallization process according to the present invention is a process of preheating and drying the recycled PET flakes to crystallize them. The crystallization time may vary depending on the input amount of recycled PET flakes and the crystallization temperature, but is generally 1 ~ 1 at 140 ~ 165 ℃. It consists of crystallization for about 2 hours.

상기 결정화공정은 로타리 방식의 결정화 설비 내지 고속교반기가 장착된 가열호퍼에서 유동시키면서 결정화하는 방식의 결정화설비 등을 채용하며, 결정화 공정이 없이 단순히 고상중합반응을 위하여 예열한 후 고상중합반응을 수행할 경우 원료의 고착현상이 일어날 수 있어 고상중합반응의 효율에 바람직하지 못한 영향을 준다.The crystallization process employs a rotary-type crystallization facility or a crystallization facility that crystallizes while flowing in a heating hopper equipped with a high-speed stirrer. The solid-state polymerization reaction can be performed simply after preheating for the solid-state polymerization reaction without a crystallization process. In this case, sticking of raw materials may occur, which has an undesirable effect on the efficiency of the solid-state polymerization reaction.

본 발명에 따른 상기 고상중합공정은 고상중합반응에 의해 높은 고유점도(IV)의 리싸이클 PET를 제조하는 공정이며, 결정화된 재생 PET 플레이크를 200 ~ 210℃ 반응온도에서 진공상태 및 질소분위기 하에 고상중합시키는 것으로 이루어진다.The solid-state polymerization process according to the present invention is a process for producing recycled PET with high intrinsic viscosity (IV) through solid-state polymerization reaction, and solid-state polymerization of crystallized recycled PET flakes is carried out under vacuum and nitrogen atmosphere at a reaction temperature of 200 to 210°C. It is done by doing what you are told.

상기 고상중합공정은 재생 PET 플레이크를 반응기에서 반응온도를 200 ~ 210℃ 유지하고, 5mbar 미만의 진공상태 및 질소를 2000ℓ/hr의 유속으로 반응기에 투입하여 질소분위기 하에서 고상중합시키는 것으로 이루어진다.The solid-state polymerization process consists of maintaining the reaction temperature of the recycled PET flakes in a reactor at 200 to 210°C, introducing nitrogen into the reactor at a vacuum of less than 5 mbar and a flow rate of 2000 L/hr, and performing solid-state polymerization under a nitrogen atmosphere.

또 고상중합공정은 고상중합반응이 종료되면 반응생성물을 반응기 내의 하부에서 교반 하에 5 ~ 6시간 체류시키는 것으로 이루어지며, 반응생성물을 교반 하에 5 ~ 6시간 체류시키는 것은 고상중합반응이 종료된 후, PET 플레이크의 브릿지 현상을 방지하여 배출을 용이하게 한다.In addition, the solid phase polymerization process consists of allowing the reaction product to remain in the lower part of the reactor under stirring for 5 to 6 hours after the solid phase polymerization reaction is completed. The reaction product is allowed to remain for 5 to 6 hours under stirring after the solid phase polymerization reaction is completed. Prevents the bridging phenomenon of PET flakes and facilitates discharge.

상기 본 발명에 따른 상기 리싸이클 PET칩 제조공정은 고상중합공정의 종료후 배출되는 고상중합물을 용융압출하고, 커팅하여 리싸이클 PET 칩을 제조하는 공정이며, 상기 고상중합물을 280℃의 용융온도에서 용융압출한 다음 커팅하여 고유점도(IV) 0.8 ~ 1.dl/g의 리싸이클 PET 칩을 제조한다.The recycled PET chip manufacturing process according to the present invention is a process of manufacturing recycled PET chips by melt-extruding and cutting the solid polymer discharged after completion of the solid polymerization process, and melt-extruding the solid polymer at a melt temperature of 280°C. Then, it is cut to produce recycled PET chips with an intrinsic viscosity (IV) of 0.8 to 1.dl/g.

상기 본 발명의 방법에 따라 제조된 고유점도(IV) 0.8 ~ 1.dl/g의 리싸이클 PET 칩은 일반적인 PET용기 외에 높은 고유점도를 요구하는 고강력 폴리에스터 장섬유의 제조에 적합하며 예를 들면, 건축자재(고유점도 0.8dl/g), 탄산수용기(고유점도 0.85dl/g), 고강력사(고유점도 0.90dl/g)등 부가가치가 높은 제품을 제조하는데 적합하여 상업적을 매우 유리한 장점이 있다.The recycled PET chip with an intrinsic viscosity (IV) of 0.8 to 1.dl/g manufactured according to the method of the present invention is suitable for the production of high-strength polyester long fibers that require high intrinsic viscosity in addition to general PET containers, for example. , It is suitable for manufacturing products with high added value such as building materials (intrinsic viscosity 0.8dl/g), carbonate receptors (intrinsic viscosity 0.85dl/g), and high-strength yarn (intrinsic viscosity 0.90dl/g), which is very commercially advantageous. .

Claims (5)

a). 수집된 폐PET로부터 투명 폐PET만을 선별한 다음, 투명 폐PET을 압착하는 선별공정,
b). 압착된 폐PET를 5 ~ 10㎜ 크기의 플레이크 형태로 절단 및 분쇄한 후, 폐PET 플레이크를 70 ~ 80℃의 온수로 세척한 다음, 스크린하여 투명 폐PET 플레이크만을 선별하는 제1차 정선공정,
c). 투명 폐PET 플레이크를 5 ~ 10℃에서 상기 제1차 정선공정의 PET 플레이크 보다 작은 크기로 습식분쇄하고 분쇄물을 원심분리하여 투명 폐PET 분쇄물을 얻는 제2차 정선공정,
d). 투명 폐PET 분쇄물을 잔류수분이 0.1중량% 이하가 되도록 제습 및 건조하는 건조공정,
e). 건조된 투명 폐PET 분쇄물을 용융온도에서 용융압출하고, 용융상태에서 필터링하고 상온으로 냉각하면서 일정크기로 절단한 다음 3 ~ 5㎜ 크기의 플레이크 형태로 분쇄하여 재생 PET플레이크를 제조하는 정제공정,
f). 재생 PET 플레이크를 140 ~ 165℃에서 1 ~ 2시간 결정화하는 결정화공정,
g). 결정화된 재생 PET 플레이크를 200 ~ 210℃ 반응온도에서 5mbar 미만의 진공상태 및 질소를 2000ℓ/hr의 유속으로 반응기에 투입하여 질소분위기 하에 고상중합시키는 고상중합공정 및
h). 고상중합물을 용융온도 조건에서 압출하고 커팅하여 PET 칩으로 성형하는 리싸이클 PET 칩 제조공정을 포함하는 것을 특징으로 하는 폐PET를 활용한 고품위 리싸이클 PET 칩의 제조방법.
a). A sorting process that selects only transparent waste PET from the collected waste PET and then compresses the transparent waste PET,
b). The first sorting process involves cutting and pulverizing the compressed waste PET into flakes with a size of 5 to 10 mm, washing the waste PET flakes with hot water at 70 to 80°C, and then screening to select only transparent waste PET flakes;
c). A second sorting process in which transparent waste PET flakes are wet-grinded at 5 to 10°C to a smaller size than the PET flakes in the first sorting process and centrifuged to obtain transparent waste PET flakes,
d). Drying process of dehumidifying and drying transparent waste PET pulverized material so that the residual moisture is less than 0.1% by weight,
e). A refining process in which dried transparent waste PET pulverized material is melt-extruded at the melting temperature, filtered in the molten state, cooled to room temperature, cut to a certain size, and then pulverized into flakes of 3 to 5 mm in size to produce recycled PET flakes;
f). A crystallization process in which recycled PET flakes are crystallized at 140 to 165°C for 1 to 2 hours,
g). A solid-state polymerization process in which crystallized recycled PET flakes are solid-phase polymerized under a nitrogen atmosphere by adding them to a reactor at a reaction temperature of 200 to 210°C under a vacuum of less than 5 mbar and nitrogen at a flow rate of 2000 ℓ/hr.
h). A method for manufacturing high-quality recycled PET chips using waste PET, comprising a recycled PET chip manufacturing process of extruding and cutting solid polymers at melt temperature conditions and forming them into PET chips.
삭제delete 삭제delete 청구항 1에 있어서, 정제공정은 건조된 투명 폐PET 분쇄물을 용융온도 275 ~ 280℃에서 용융압출한 다음, 용융상태에서 20미크론의 스테인레스스틸 필터로 필터링하는 것을 특징으로 하는 폐PET를 활용한 고품위 리싸이클 PET 칩의 제조방법.According to claim 1, the purification process involves melting and extruding dried transparent waste PET pulverized material at a melting temperature of 275 to 280°C, and then filtering the molten state through a 20 micron stainless steel filter. Manufacturing method of recycled PET chips. 삭제delete
KR1020210134694A 2021-10-12 2021-10-12 Manufacturing method of recycled PET chip using waste PET KR102599800B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR1020210134694A KR102599800B1 (en) 2021-10-12 2021-10-12 Manufacturing method of recycled PET chip using waste PET

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR1020210134694A KR102599800B1 (en) 2021-10-12 2021-10-12 Manufacturing method of recycled PET chip using waste PET

Publications (2)

Publication Number Publication Date
KR20230052320A KR20230052320A (en) 2023-04-20
KR102599800B1 true KR102599800B1 (en) 2023-11-08

Family

ID=86143683

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1020210134694A KR102599800B1 (en) 2021-10-12 2021-10-12 Manufacturing method of recycled PET chip using waste PET

Country Status (1)

Country Link
KR (1) KR102599800B1 (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100578766B1 (en) 1999-05-01 2006-05-11 김용재 Method for recycling of PET bottles
KR100866819B1 (en) 2001-10-16 2008-11-04 데이진 가부시키가이샤 Method for recycling pet bottle
KR102163351B1 (en) * 2019-11-08 2020-10-08 이경희 Manufacturing method of recycled PET chip for manufacturing high strength polyester long fiber

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE69727650T2 (en) * 1996-12-31 2004-07-29 M&G Polimeri Italia S.P.A., Patrica Process for the recovery of solid microporous polyester from a recycling stream and products from it
US5886058A (en) 1997-02-03 1999-03-23 Illinois Tool Works Inc. Inline solid state polymerization of pet flakes for manufacturing plastic strap
KR100895529B1 (en) 2008-08-08 2009-04-30 박용익 A pet bottle revival method
KR20110075097A (en) * 2009-12-28 2011-07-06 주식회사 효성 Method for preparing the recycled polyester chip and the polyester filament fiber with modified cross-section using the same
KR101417193B1 (en) 2010-09-30 2014-07-09 코오롱인더스트리 주식회사 Recycled polyester polymer and Method for manufacturing the same, Spun bond nonwoven fabric using the same

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100578766B1 (en) 1999-05-01 2006-05-11 김용재 Method for recycling of PET bottles
KR100866819B1 (en) 2001-10-16 2008-11-04 데이진 가부시키가이샤 Method for recycling pet bottle
KR102163351B1 (en) * 2019-11-08 2020-10-08 이경희 Manufacturing method of recycled PET chip for manufacturing high strength polyester long fiber

Also Published As

Publication number Publication date
KR20230052320A (en) 2023-04-20

Similar Documents

Publication Publication Date Title
KR102163351B1 (en) Manufacturing method of recycled PET chip for manufacturing high strength polyester long fiber
CN111138641B (en) Method for preparing bottle-grade slices by recycling waste polyester bottles
AU777435C (en) Process for preparing food contact grade polyethylene terephthalate resin from waste pet containers
US4033907A (en) Reclaiming waste plastics
CN1192998C (en) Method of chemical recycling of polyethylene terephthalate waste
JP4719217B2 (en) Recycled polyethylene terephthalate and method for producing the same
EP0994146A1 (en) Solid state polymerization of PET flakes
JP3613198B2 (en) Flake foreign matter removal method in PET bottle recycling
KR102599800B1 (en) Manufacturing method of recycled PET chip using waste PET
KR102339830B1 (en) Manufacturing of high-viscosity recycled PET chips using low-viscosity PET flakes
KR20220119020A (en) Optimized process for depolymerization of polyesters comprising polyethylene terephthalate
JP3711794B2 (en) Manufacturing method of recycled polyester resin sheet.
KR102508241B1 (en) Manufacturing method of monofilament yarn using recycled PET
Fadlalla Management of PET plastic bottles waste through recycling Khartoum state
KR20120068373A (en) Process for preparing recycled polyester chip and process for preparing recycled polyester filament with modified cross-section
CN112776208B (en) Preparation method for regenerating and processing ABS particles by using waste refrigerator material
US20220324140A1 (en) Process for joint recycling of composite items based on a thermoplastic polymer matrix
KR20220097568A (en) Manufacturing method of recycled PET pellets using waste PET bottles
KR20220119054A (en) Improved process for depolymerization of polyesters comprising polyethylene terephthalate
CN112390999A (en) HDPE reclaimed material, preparation method thereof and HDPE pipe
KR20220097567A (en) Manufacturing method of recycled PET pellets using waste PET bottles
KR102611943B1 (en) Pet chip regeneration method capable of enhancing intrinsic viscosity and purity and regeneration apparatus using the same
CN100516113C (en) Method and device for reusing waste polyester in continuous polyester producing apparatus
CN220008888U (en) Recovered heat shrinkage film preparation system
CN116175808A (en) Physical method production system and process of food-grade regenerated polyethylene terephthalate

Legal Events

Date Code Title Description
E701 Decision to grant or registration of patent right
GRNT Written decision to grant