WO2023171862A1 - Method for regenerating everyday film sheet-shaped waste plastic - Google Patents
Method for regenerating everyday film sheet-shaped waste plastic Download PDFInfo
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- WO2023171862A1 WO2023171862A1 PCT/KR2022/012172 KR2022012172W WO2023171862A1 WO 2023171862 A1 WO2023171862 A1 WO 2023171862A1 KR 2022012172 W KR2022012172 W KR 2022012172W WO 2023171862 A1 WO2023171862 A1 WO 2023171862A1
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- waste plastic
- film sheet
- plastic
- recycling
- compatibilizer
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B08—CLEANING
- B08B—CLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
- B08B3/00—Cleaning by methods involving the use or presence of liquid or steam
- B08B3/04—Cleaning involving contact with liquid
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B13/00—Conditioning or physical treatment of the material to be shaped
- B29B13/06—Conditioning or physical treatment of the material to be shaped by drying
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B13/00—Conditioning or physical treatment of the material to be shaped
- B29B13/06—Conditioning or physical treatment of the material to be shaped by drying
- B29B13/065—Conditioning or physical treatment of the material to be shaped by drying of powder or pellets
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
- B29B17/04—Disintegrating plastics, e.g. by milling
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B9/00—Making granules
- B29B9/02—Making granules by dividing preformed material
- B29B9/06—Making granules by dividing preformed material in the form of filamentary material, e.g. combined with extrusion
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/022—Extrusion 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
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/285—Feeding the extrusion material to the extruder
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
- B29B2017/001—Pretreating the materials before recovery
- B29B2017/0015—Washing, rinsing
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
- B29B17/04—Disintegrating plastics, e.g. by milling
- B29B2017/0424—Specific disintegrating techniques; devices therefor
- B29B2017/0468—Crushing, i.e. disintegrating into small particles
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING 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
- B29K2023/00—Use of polyalkenes or derivatives thereof as moulding material
- B29K2023/04—Polymers of ethylene
- B29K2023/06—PE, i.e. polyethylene
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING 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
- B29K2023/00—Use of polyalkenes or derivatives thereof as moulding material
- B29K2023/10—Polymers of propylene
- B29K2023/12—PP, i.e. polypropylene
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING 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
- B29K2025/00—Use of polymers of vinyl-aromatic compounds or derivatives thereof as moulding material
- B29K2025/04—Polymers of styrene
- B29K2025/06—PS, i.e. polystyrene
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING 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
- B29K2077/00—Use of PA, i.e. polyamides, e.g. polyesteramides or derivatives thereof, as moulding material
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/20—Waste processing or separation
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/52—Mechanical processing of waste for the recovery of materials, e.g. crushing, shredding, separation or disassembly
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
Definitions
- the present invention relates to a method for recycling film sheet-type waste plastic from living environments, and in particular, to a method for recycling randomly collected composite waste plastic without undergoing material selection.
- 'film sheet-type household waste plastic refers to film-type and sheet-type plastics that are used and discarded for the purchase of goods or convenience of life in the real life of the general consumer, regardless of the specific material, and are commonly found in the surrounding environment. It should be understood to include all film-type and sheet-type plastics discarded after being used for commercial, industrial, and agricultural purposes. Hereinafter, for convenience, this will be referred to as ‘waste plastic’.
- waste plastic is made into recycled plastic and used through the following processes: collection/sorting, crushing/crushing, washing/drying, and melting/extrusion.
- the waste plastic collected in this way In order for the waste plastic collected in this way to be used as a recycled raw material, it must first be sorted. If it is melted without being sorted, the melting point is different for each material, so for example, if the temperature is set to a high melting point, it must be melted to a low melting point. Materials with a high melting point cannot be used because they will be carbonized, and conversely, if the temperature is set to a low melting point, materials with a high melting point cannot be used because they will be processed without melting.
- these different materials are not compatible with each other and the affinity between the resin polymers is low, so not only do they have poor physical properties when mixed, but they are also weak against impact, making it difficult to use them as recycled raw materials.
- the present invention proposes a method of producing recycled plastic by pulverizing waste plastic, washing and drying it, adding a compatibilizer in a fixed amount to create recycled raw materials, and extruding the recycled material at high temperature.
- the present invention relates to a method for recycling film sheet-type waste plastic from living quarters, which method includes:
- the waste plastic input into the extruder hopper is tentatively molded in a brittle state in a molding machine after the drying step.
- the waste plastic recycling method of the present invention includes:
- the washing step is:
- the living waste plastics include polyethylene, polypropylene, polystyrene, polyamide and printed film;
- the compatibilizer is a powder made of a mixture of an inorganic material and a transition metal or a master batch containing the powder;
- the pseudo-molded waste plastic is:
- the lump is in the form of a lump in a brittle state, and the lump is preferably in the form of a diameter of 2 cm to 5 cm and a length of 5 cm to 10 cm.
- the recycled plastic can be post-processed into pellet form.
- composite waste plastics are recycled through a continuous process of crushing, washing, and drying, then adding a compatibilizer in a fixed amount to create recycled raw materials, and extruding them at high temperature. Therefore, it can facilitate the handling and quantification of waste plastic during the process, and is also effective in terms of homogenization of recycled plastic. In particular, this effect is preferably doubled as the waste plastic undergoes a preforming step.
- the composite waste plastic is washed and dried, pre-molded in a temporary brittle state in a molding machine, and then recycled through processes such as transport, mixing of compatibilizer, stirring, disassembly of pre-molding, and extrusion.
- the physical stability of recycled plastic can be improved by ensuring that it is distributed homogeneously in the recycled plastic
- FIG. 1 is a flowchart of a waste plastic recycling method according to a preferred embodiment of the present invention.
- Figures 2a and 2b are views showing each cutter and shredder.
- Figure 3 is a diagram showing a water washing device.
- Figure 4 is a diagram showing a molding machine.
- Figures 5a and 5b are views showing each powder and masterbatch.
- Figure 6 is a view showing an extruder
- Figure 7 is a view showing recycled plastic processed into pellet form.
- the living waste plastics include polyethylene (PE), polypropylene (PP), polystyrene (PS), polyamide (PA), polyester (PET), polyurethane (PU), printed film, etc. It should be understood to include all obtainable waste plastic materials, and the subject of the 'recycling method' of the present invention is premised on the fact that these materials are composite waste plastics collected randomly without selection.
- This step is a process of cutting and crushing the collected waste plastic to an appropriate size.
- cutting and disassembly reduces the volume of the collected waste plastic, facilitates the post-processing process, and contaminates the metal, stones, and dirt contained therein. Substances can be removed primarily.
- a typical shearing cutter 10 and a waste vinyl shredder 11 shown in FIGS. 2A and 2B can be used, and the waste plastic is ultimately pulverized into a size of 10 cm to 20 cm in length.
- the above-mentioned metallic contaminants are components that must be removed first when recycling waste plastic.
- a metal separator may be used in advance, but this is not explained separately here.
- This step is a process of removing contaminants by washing the waste plastic cut and pulverized in the previous process (S11) with water.
- the pulverized waste plastic is washed as it passes through a water tank, and only the washed waste plastic is transferred to the next process, excluding contaminants that settle during washing or waste plastic that contains a large amount of such contaminants.
- This water washing and water tank can be provided in plurality as needed.
- Figure 3 illustrates the water washing device 20, where a plurality of rotating presses 21 are installed in a longitudinal water tank so that the waste plastic 22 is pressed against the press, submerged in water, and moved forward while being washed.
- a chlorine washing step is preferably further included after the water washing step. Collected household waste plastics are contaminated with various bacteria and bad odors, and when recycled, the bad smell is especially severe in the recycled plastics, making it very difficult to use them as actual household goods. Accordingly, in this embodiment, we attempt to expand the usability of recycled plastic by sterilizing and deodorizing it by washing it with chlorine in advance.
- chlorine is added and mixed in an amount of 0.4 to 1.0 mg per 1L of water, and at this stage, chlorine cleaning can be performed using a water tank method such as water washing, spraying, or water spraying.
- This step is a process of drying waste plastic containing moisture through a washing step (S12). It would also be possible to dry in a high temperature atmosphere after washing in a general way. However, since there is a possibility that the physical properties of the plastic may be modified, in this embodiment, natural conditions are used in a dry house. At this time, the moisture content of the waste plastic after drying is less than 20%.
- This step is a process of temporarily molding the waste plastic dried through the drying step (S13) into a brittle state.
- the waste plastic that is put into the molding machine after drying is compression molded, but is temporarily temporarily molded and discharged in a brittle state that is easily broken by external forces.
- Figure 4 illustrates the molding machine 30 used in this process and is designed to discharge a brittle molding 31 in the form of a lump with a diameter of 2 cm to 5 cm and a length of 5 cm to 10 cm. At this time, the discharged molding is placed on the lower conveyor 32. It is taken off and transported to the right place.
- waste plastics that have not been sorted are not evenly distributed among the recycled plastics but are grouped together by material. Accordingly, in this embodiment, the waste plastic is temporarily temporarily molded in a brittle state in this process and the temporary mold is easily dismantled in the post-process, thereby making it easier to handle and quantify the waste plastic during the process, and also to measure the waste plastic by material. This ensures homogeneous distribution in the recycled plastic.
- This step is to prepare recycled raw materials by adding a fixed amount of compatibilizer to the dried or caustic waste plastic in the previous step.
- a compatibilizer is added to the brittle molded product and then stirred to prepare a recycled raw material mixed with the dismantled waste plastic and the compatibilizer.
- the waste plastic that has been preformed into a brittle lump in the previous process is mixed with a compatibilizer while the preform is broken up by a stirrer in this preparation stage, thereby preparing the recycled raw material.
- the stirring process is not necessarily necessary, but is much more advantageous in terms of even mixing and distribution of materials and compatibilizers.
- the stirrer Since the above molded product is in a brittle state that is easily broken by external force, the stirrer does not need to have special power, and a normal rotary stirrer is sufficient. However, a rotating blade-type stirrer can be effectively used to quickly dismantle the molded product and mix the waste plastic material and the compatibilizer.
- the compatibilizer is a filling material that allows various waste plastic materials to melt and combine with each other. Referring to FIG. 5A, it is a material in the form of a powder 40 made of a mixture of an inorganic material and a transition metal. More specifically, the compatibilizer:
- Transition metals including aluminum oxide, iron oxide, titanium oxide, magnesium chloride, and aluminum chloride
- the compatibilizer is added to the extruder hopper together with the waste plastic in an amount of 3 to 8% by weight based on 100% by weight of the waste plastic dried above.
- the components of the compatibilizer are disclosed in the prior art and are not special to the present invention, nor are the present invention limited to the specific components of the compatibilizer. Meanwhile, powder-type compatibilizers are difficult to handle and quantify. Therefore, as the compatibilizer, as illustrated in FIG. 5B, masterbatch (MB) 41 obtained by mixing the powder and liquid plastic and solidifying it may be used.
- MB masterbatch
- This step is a process in which the recycled raw materials prepared above are put into the hopper of an extruder with a temperature of 210°C or higher and extruded to obtain solid recycled plastic.
- Figure 5 illustrates a plastic extruder 50 used in this process, which is no different from a typical extruder for plastic recycling. Meanwhile, the recycled plastic 51 may be post-processed into a pellet form (see symbol 52 in FIG. 7) that is convenient to transport, use, and handle.
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Abstract
Description
본 발명은 필름 시트형 생활계 폐플라스틱 재생방법에 관한 것으로 특히, 무작위 수집된 복합 폐플라스틱을 재질 선별작업을 거치지 않은 상태로 재생하는 방법에 관한 것이다.The present invention relates to a method for recycling film sheet-type waste plastic from living environments, and in particular, to a method for recycling randomly collected composite waste plastic without undergoing material selection.
본 발명에서 말하는 '필름 시트형 생활계 폐플라스틱'이란, 구체적인 재질을 불문하고, 일반 소비대중의 실생활에서 물품의 구입이나 생활의 편의 등을 위하여 사용되고 버려진 필름형 및 시트형 플라스틱 외에, 주변 환경에서 흔히 볼 수 있는 상업용·공업용·농업용으로 사용된 후 폐기된 필름형 및 시트형 플라스틱 등을 모두 포함하는 것으로 이해되어야 한다. 이하에서는, 이를 편의상 '폐플라스틱'이라고 한다.In the present invention, 'film sheet-type household waste plastic' refers to film-type and sheet-type plastics that are used and discarded for the purchase of goods or convenience of life in the real life of the general consumer, regardless of the specific material, and are commonly found in the surrounding environment. It should be understood to include all film-type and sheet-type plastics discarded after being used for commercial, industrial, and agricultural purposes. Hereinafter, for convenience, this will be referred to as ‘waste plastic’.
일반적으로 폐플라스틱은 수집·선별, 분쇄·파쇄, 세척·건조, 용융·압출의 공정을 거쳐 재생 플라스틱으로 만들어져 사용되고 있다. 이와 같이 수집된 폐플라스틱이 재생원료로 사용되기 위하여는 먼저 선별작업이 선행되어야 하는데, 만약 선별되지 않은 채 용융을 할 경우 재질별 용융점이 상이해 예컨대, 높은 용융점에 온도를 맞출 경우에는 낮은 용융점을 가진 재료는 탄화될 것이므로 사용할 수 없고 반대로 낮은 용융점에 온도를 맞출 경우에는 높은 용융점을 가진 재료는 용융되지 않은 채 가공될 것이므로 사용할 수 없다.In general, waste plastic is made into recycled plastic and used through the following processes: collection/sorting, crushing/crushing, washing/drying, and melting/extrusion. In order for the waste plastic collected in this way to be used as a recycled raw material, it must first be sorted. If it is melted without being sorted, the melting point is different for each material, so for example, if the temperature is set to a high melting point, it must be melted to a low melting point. Materials with a high melting point cannot be used because they will be carbonized, and conversely, if the temperature is set to a low melting point, materials with a high melting point cannot be used because they will be processed without melting.
또한, 이와 같이 상이한 재료들은 서로 상용성을 갖지 않으며 수지 중합체간 친화도가 떨어져, 혼합시 물리적 성질이 떨어질 뿐만 아니라 충격에 약해 재생원료로 사용하기가 어렵다.In addition, these different materials are not compatible with each other and the affinity between the resin polymers is low, so not only do they have poor physical properties when mixed, but they are also weak against impact, making it difficult to use them as recycled raw materials.
특히, 생활계 폐플라스틱의 경우 통계에 의하면 90% 이상 재활용되는 것으로 나타나 있지만, 사실상으로는 SRF(Solid Refuse Fuel)로 만들어져 소각되는 비율이 전체의 85%에 육박할 뿐만 아니라 일부 재활용되는 것도 물리적으로 내충격성, 내마모성 등이 거의 요구되지 않는 제수변밸브, 가로수보호관, 오수관 덮개 등 일부에 한정적으로 사용되는 실정이다.In particular, in the case of household waste plastic, statistics show that more than 90% of it is recycled, but in reality, not only is the rate of being made into SRF (Solid Refuse Fuel) and incinerated close to 85% of the total, but some of it is also recycled physically. It is only used in some applications such as water control valves, street tree protection pipes, and sewage pipe covers that require little impact or wear resistance.
이는 무작위 수집된 생활계 폐플라스틱의 경우 폴리에틸렌, 폴리프로필렌, 폴리스티렌, 폴리아미드, 폴리에스테르, 폴리우레탄 등 다양한 재질이 복합되어 이루어져 있으며, 그 중에는 다층구조를 가지고 심지어 그 표면에 인쇄용 수지 혼합물이 포함되었거나 알루미늄 박막층이 코팅되어 있는 것, 음식물이나 흙 등으로 오염된 것 등이 포함되어 있어서 재생원료로서의 활용이 극히 제한될 수밖에 없기 때문이다.In the case of randomly collected household waste plastic, it is made up of a combination of various materials such as polyethylene, polypropylene, polystyrene, polyamide, polyester, and polyurethane, and some of them have a multi-layer structure and even contain a printing resin mixture on the surface or aluminum. This is because its use as a recycled raw material is extremely limited because it contains materials that are coated with a thin film layer and are contaminated with food or dirt.
결국, 수집된 폐플라스틱을 효과적으로 재생할 수 있기 위하여는 먼저, 재질별로 선별될 것이 필요하다고 할 수 있다. 그러나 이 선별은 기계적으로 불가능하기 때문에 여기에 많은 인력, 비용, 시간이 필요하며, 이는 매우 비경제적이고 비합리적이어서 많은 사업장에서 생활계 필름 시트형 물질의 재활용을 포기하는 원인이 되고 있다.In the end, in order to effectively recycle the collected waste plastic, it must first be sorted by material. However, since this sorting is mechanically impossible, it requires a lot of manpower, money, and time, and is very uneconomical and unreasonable, causing many businesses to give up recycling of household film sheet-type materials.
이에 제안된 것이 등록특허 제10-0623157호, 등록특허 제10-1463400호 등에 개시된 소위 '상용화성 충전재'이다. 이 특허들은 분쇄한 무기물계 혼합물과 전이금속 첨가물을 혼합하여 폐플라스틱 재생용 상용화성(相溶化性) 충전재를 제조한다는 것이며, 수집 후 선별되지 않은 채의 복합 폐플라스틱에 이 분말 충전재를 첨가 및 혼합한 후 용융 압출함으로써 원하는 물리적 특성의 재생 플라스틱을 제조할 수 있다는 것이다. 이들 특허 이후에, 같은 목적을 갖는 유사 충전재들이 많은 특허에서 다양하게 제안되어 왔다.What has been proposed is the so-called 'commercial chemical filler' disclosed in Patent Registration No. 10-0623157, Patent No. 10-1463400, etc. These patents are about producing a compatible filler for waste plastic recycling by mixing pulverized inorganic mixtures with transition metal additives, and adding and mixing this powder filler to composite waste plastics that have not been collected and sorted. This means that recycled plastic with desired physical properties can be manufactured by melting and extruding the material. After these patents, similar fillers with the same purpose have been variously proposed in many patents.
이러한 충전재가 폐플라스틱을 재생함에 있어 상용화제로서 유효하게 작용한다는 것은 여러 실험 또는 테스트를 통하여 확인된 바 있다.It has been confirmed through various experiments or tests that these fillers effectively act as compatibilizers in recycling waste plastic.
<선행기술문헌><Prior art literature>
한국 등록특허공보 제10-0623157호Korean Patent Publication No. 10-0623157
한국 등록특허공보 제10-1107584호Korean Patent Publication No. 10-1107584
한국 등록특허공보 제10-1463400호Korean Patent Publication No. 10-1463400
한국 등록특허공보 제10-1583305호Korean Patent Publication No. 10-1583305
그러나 종래의 폐플라스틱 재생기술에 의하면, 상기 충전재를 사용하는 것과 무관하게, 건조된 필름형 및 시트형 재료는 그 경량성·분산성으로 인하여 이송·투입·혼합 등 공정 작업에 있어 취급이 어려운 문제가 있으며 한편, 선별을 거치지 않은 복합 폐플라스틱이 재생 플라스틱에 골고루 분포되지 않고 재질별로 뭉쳐져 있게 되는 - 애초에 그렇게 폐기 및 수집되기 때문 - 문제가 있다.However, according to the conventional waste plastic recycling technology, regardless of the use of the above filler, dried film-type and sheet-type materials are difficult to handle in process operations such as transport, input, and mixing due to their lightness and dispersibility. On the other hand, there is a problem in that composite waste plastic that has not been sorted is not evenly distributed among the recycled plastics but is lumped together by material - because that is how they are disposed of and collected in the first place.
본 발명은:The invention:
주요하게, 복합 폐플라스틱의 공정상 취급을 용이하게 하고 또한 재생 플라스틱에서 균질하도록 함으로써, 재생 플라스틱의 생산성 및 물리적 안정성을 개선할 수 있는 폐플라스틱 재생방법을 제공하는 것;Mainly, providing a waste plastic recycling method that can improve the productivity and physical stability of recycled plastic by facilitating the process handling of composite waste plastic and ensuring homogeneity in recycled plastic;
한편으로, 폐플라스틱이 가진 악취를 제거함으로써 재생 플라스틱이 실생활에 적극적으로 활용될 수 있는 폐플라스틱 재생방법을 제공하는 것;On the one hand, providing a waste plastic recycling method that allows recycled plastic to be actively used in daily life by removing the bad smell of waste plastic;
을 목적으로 한다.For the purpose.
상기한 목적을 달성하기 위하여 본 발명은, 폐플라스틱을 분쇄하여 세척·건조한 후 상용화제를 정량 투입하여 재생원료를 만들고 이를 고온에서 압출함으로써 재생 플라스틱을 만드는 방법을 제시한다.In order to achieve the above object, the present invention proposes a method of producing recycled plastic by pulverizing waste plastic, washing and drying it, adding a compatibilizer in a fixed amount to create recycled raw materials, and extruding the recycled material at high temperature.
구체적으로, 본 발명은 필름 시트형 생활계 폐플라스틱 재생방법에 관한 것으로서, 상기 재생방법은:Specifically, the present invention relates to a method for recycling film sheet-type waste plastic from living quarters, which method includes:
필름 시트형 생활계 폐플라스틱을 절단 및 분쇄하는 단계;Cutting and pulverizing film sheet-type household waste plastic;
분쇄된 폐플라스틱을 세척한 후 수분 함량 20% 미만으로 건조하는 단계;Washing the pulverized waste plastic and drying it to a moisture content of less than 20%;
상기 건조된 폐플라스틱 100 중량%에 대하여 전이금속과 무기물의 혼합물로 이루어진 상용화제 3 ~ 8 중량%와 함께 210℃ 이상의 온도를 갖는 압출기의 호퍼에 투입하는 단계;Injecting 3 to 8 wt% of a compatibilizer consisting of a mixture of transition metals and inorganic materials with respect to 100 wt% of the dried waste plastic into the hopper of an extruder having a temperature of 210°C or higher;
상기 압출기에서 재생 플라스틱을 수득하는 단계;Obtaining recycled plastic from the extruder;
를 포함한다.Includes.
바람직하게, 상기 압출기 호퍼에 투입되는 폐플라스틱은, 상기 건조단계 후 성형기에서 취성(脆性) 상태로 가성형된 것이다. 더욱 바람직하게, 이때 본 발명의 상기 폐플라스틱 재생방법은:Preferably, the waste plastic input into the extruder hopper is tentatively molded in a brittle state in a molding machine after the drying step. More preferably, the waste plastic recycling method of the present invention includes:
가성형된 폐플라스틱에 상용화제를 첨가한 후 교반함으로써, 가성형이 해체되는 폐플라스틱과 상용화제가 혼합된 재생원료를 준비하는 단계;Adding a compatibilizer to the temporarily molded waste plastic and then stirring it to prepare a recycled raw material mixed with the waste plastic from which the temporary mold is dismantled and the compatibilizer;
를 더 포함할 수 있으며,may further include,
이때 상기 재생원료가 압출기 호퍼에 투입되는 것;At this time, the recycled raw material is input into the extruder hopper;
을 특징으로 한다.It is characterized by .
구체적으로, 상기 세척단계는:Specifically, the washing step is:
물 세척 단계와 탈취용 염소 세척 단계를 차례로 포함하는 것;sequentially including a water washing step and a deodorizing chlorine washing step;
을 특징으로 한다.It is characterized by .
바람직하게,Preferably,
상기 생활계 폐플라스틱은 폴리에틸렌, 폴리프로필렌, 폴리스티렌, 폴리아미드 및 인쇄된 필름을 포함하며;The living waste plastics include polyethylene, polypropylene, polystyrene, polyamide and printed film;
상기 상용화제는 무기물과 전이금속의 혼합물로 이루어진 파우더 또는 그 파우더를 포함하는 마스터배치(master batch)인 것;The compatibilizer is a powder made of a mixture of an inorganic material and a transition metal or a master batch containing the powder;
을 특징으로 한다.It is characterized by .
상기 가성형 폐플라스틱은:The pseudo-molded waste plastic is:
취성 상태의 덩어리 형태이며, 상기 덩어리는 바람직하게 지름 2cm ~ 5cm, 길이 5cm ~ 10cm 형태인 것으로 한다.It is in the form of a lump in a brittle state, and the lump is preferably in the form of a diameter of 2 cm to 5 cm and a length of 5 cm to 10 cm.
상기 재생 플라스틱은 펠릿(pellet) 형태로 후가공될 수 있다.The recycled plastic can be post-processed into pellet form.
본 발명에 의하면, 복합 폐플라스틱은 분쇄 및 세척·건조한 후 상용화제를 정량 투입하여 재생원료를 만들고 이를 고온에서 압출하는 연속공정을 거쳐 재생된다. 따라서 폐플라스틱의 공정상 취급 및 정량화 작업을 용이하게 할 수 있으며, 재생 플라스틱의 균질화 측면에서도 효과적이다. 특히, 이러한 효과는 바람직하게 폐플라스틱의 가성형 단계를 거침에 따라 배가된다.According to the present invention, composite waste plastics are recycled through a continuous process of crushing, washing, and drying, then adding a compatibilizer in a fixed amount to create recycled raw materials, and extruding them at high temperature. Therefore, it can facilitate the handling and quantification of waste plastic during the process, and is also effective in terms of homogenization of recycled plastic. In particular, this effect is preferably doubled as the waste plastic undergoes a preforming step.
본 발명의 바람직한 실시 예에서, 복합 폐플라스틱은 세척·건조 후 성형기에서 임시 취성상태로 가성형된 이후 이송, 상용화제 혼합, 교반, 가성형 해체, 압출 등의 공정을 거쳐 재생된다. 따라서,In a preferred embodiment of the present invention, the composite waste plastic is washed and dried, pre-molded in a temporary brittle state in a molding machine, and then recycled through processes such as transport, mixing of compatibilizer, stirring, disassembly of pre-molding, and extrusion. thus,
폐플라스틱의 공정상 취급 및 정량화 작업을 용이하게 할 수 있으며;It can facilitate the process handling and quantification of waste plastic;
또한, 재생 플라스틱에서 균질하게 분포되도록 함으로써 재생 플라스틱의 물리적 안정성을 개선할 수 있는;In addition, the physical stability of recycled plastic can be improved by ensuring that it is distributed homogeneously in the recycled plastic;
각별한 효과가 있다.It has a special effect.
한편, 상기 염소 세척을 통하여 재생원료가 가질 수 있는 악취를 사전에 제거해줌으로써 재생 플라스틱이 실생활에 적극적으로 활용될 수 있는;On the other hand, through the chlorine washing, the odor that the recycled raw material may have is removed in advance, so that the recycled plastic can be actively used in daily life;
추가적 효과가 있다.There is an additional effect.
도 1은 본 발명의 바람직한 실시 예에 따른 폐플라스틱 재생방법의 순서도.1 is a flowchart of a waste plastic recycling method according to a preferred embodiment of the present invention.
도 2a, 2b는 각 절단기 및 분쇄기를 보인 도면.Figures 2a and 2b are views showing each cutter and shredder.
도 3은 물 세적 장치를 보인 도면.Figure 3 is a diagram showing a water washing device.
도 4는 성형기를 보인 도면.Figure 4 is a diagram showing a molding machine.
도 5a, 5b는 각 파우더 및 마스터배치를 보인 도면.Figures 5a and 5b are views showing each powder and masterbatch.
도 6은 압출기를 보인 도면Figure 6 is a view showing an extruder
도 7은 재생 플라스틱이 펠릿 형태로 가공된 것을 보인 도면.Figure 7 is a view showing recycled plastic processed into pellet form.
[부호의 설명][Explanation of symbols]
S10. 재생방법S10. How to play
S11. 절단/분쇄단계S11. Cutting/crushing stage
S12. 세척단계S12. Washing step
S13. 건조단계S13. drying stage
S14. 성형단계S14. Molding stage
S15. 준비단계S15. Preparation stage
S16. 압출단계S16. Extrusion step
10. 절단기10. Cutter
11. 분쇄기11. Grinder
20. 물 세척 장치20. Water washing device
21. 프레스21. Press
22. 폐플라스틱22. Waste plastic
30. 성형기30. Molding machine
31. 성형물31. Molding
32. 컨베이어32. Conveyor
40. 파우더40. Powder
41. 마스터배치41. Masterbatch
50. 압출기50. Extruder
51. 재생 플라스틱51. Recycled plastic
52. 펠릿52. Pellets
이상에 기재된 또는 기재되지 않은 본 발명의 '필름 시트형 생활계 폐플라스틱 재생방법'(이하 '재생방법'이라 함)은, 이하에서 첨부도면을 참조하여 설명하는 바람직한 실시 예 기재를 통하여 더욱 명백해질 것이다. 도 1에서 부호 'S10'은 본 발명의 실시 예에 따른 재생방법을 나타낸 것으로, 여기에서는 이를 순서대로 설명하되 필요한 부분에서 다른 도면을 참고하기로 한다.The 'film sheet type waste plastic recycling method' (hereinafter referred to as 'recycling method') of the present invention, which may or may not be described above, will become more clear through the preferred embodiments described below with reference to the accompanying drawings. In Figure 1, symbol 'S10' indicates a playback method according to an embodiment of the present invention, and herein, it will be described in order, with reference to other drawings where necessary.
본 발명에서 상기 생활계 폐플라스틱은 폴리에틸렌(PE), 폴리프로필렌(PP), 폴리스티렌(PS), 폴리아미드(PA), 폴리에스테르(PET), 폴리우레탄(PU), 인쇄된 필름 기타 생활 주변에서 쉽게 얻을 수 있는 폐플라스틱 재료들을 모두 포함하는 것으로 이해되어야 하며, 본 발명 '재생방법'의 대상은 이 재료들이 선별됨이 없이 무작위 수집된 상태의 복합 폐플라스틱인 것을 전제로 한다.In the present invention, the living waste plastics include polyethylene (PE), polypropylene (PP), polystyrene (PS), polyamide (PA), polyester (PET), polyurethane (PU), printed film, etc. It should be understood to include all obtainable waste plastic materials, and the subject of the 'recycling method' of the present invention is premised on the fact that these materials are composite waste plastics collected randomly without selection.
[절단/분쇄(S11)][Cutting/Crushing (S11)]
이 단계는 수집된 폐플라스틱을 적당한 크기로 절단 및 분쇄하는 공정으로, 여기에서 절단 및 분해는 수집 폐플라스틱의 부피를 감소시키고 후처리 공정을 원활하게 하며 거기에 포함된 금속, 돌, 흙 등 오염물질을 일차적으로 제거할 수 있다. 이 공정에서는 예컨대 도 2a 및 2b에 예시된 통상의 샤링 절단기(10) 및 폐비닐 분쇄기(11) 등이 사용될 수 있으며, 상기한 폐플라스틱이 결과적으로는 길이 10cm ~ 20cm 크기로 분쇄된다.This step is a process of cutting and crushing the collected waste plastic to an appropriate size. Here, cutting and disassembly reduces the volume of the collected waste plastic, facilitates the post-processing process, and contaminates the metal, stones, and dirt contained therein. Substances can be removed primarily. In this process, for example, a
특히 상기한 금속성 오염물질은 폐플라스틱을 재생함에 있어 우선적으로 제거되어야 할 성분이다. 이 제거를 위하여 사전에 금속 선별기를 사용할 수도 있으나 여기에서는 따로 설명하지 않는다.In particular, the above-mentioned metallic contaminants are components that must be removed first when recycling waste plastic. To remove this, a metal separator may be used in advance, but this is not explained separately here.
[세척(S12)][Washing (S12)]
이 단계는 이전 공정(S11)에서 절단 및 분쇄된 폐플라스틱을 물 세척하여 오염물질을 제거하는 공정이다. 상기 분쇄된 폐플라스틱은 수조를 통과하면서 세척되며, 세척 중 가라앉는 오염물질 또는 그 오염물질을 다량 포함한 폐플라스틱을 제외하고 세척된 폐플라스틱만 다음 공정으로 이송된다. 이 물 세척 및 수조는 필요에 따라 복수로 구비될 수 있다. 도 3은 물 세척 장치(20)를 예시한 것으로, 장-방향 수조에 복수의 회전 프레스(21)를 설치하여 폐플라스틱(22)이 프레스에 눌려 물속에 잠기면서 세척되면서 전방으로 이동되도록 한다.This step is a process of removing contaminants by washing the waste plastic cut and pulverized in the previous process (S11) with water. The pulverized waste plastic is washed as it passes through a water tank, and only the washed waste plastic is transferred to the next process, excluding contaminants that settle during washing or waste plastic that contains a large amount of such contaminants. This water washing and water tank can be provided in plurality as needed. Figure 3 illustrates the
이때 수조 바닥에 가라앉는 금속 등 오염물질 또는 그 오염물질을 다량 포함한 폐플라스틱은 별도의 장치에 의하여 제거될 것이다.At this time, contaminants such as metals that settle to the bottom of the tank or waste plastic containing large amounts of such contaminants will be removed by a separate device.
이상에서 세척(S12) 단계로서 물 세척에 관하여 설명하였지만, 바람직하게는 물 세적 단계 후 염소 세척 단계를 더 포함한다. 수집된 생활계 폐플라스틱은 각종 세균 및 악취로 오염되어 있으며, 이를 그대로 재생할 경우 그 재생 플라스틱에서 특히 악취의 정도가 심하여 실제 생활용품으로 사용하기는 매우 어렵다. 이에 본 실시 예에서는 사전에 염소 세척을 하여 살균 및 탈취를 함으로써 재생 플라스틱의 활용성을 확대하고자 한다.Although water washing has been described as the washing (S12) step above, a chlorine washing step is preferably further included after the water washing step. Collected household waste plastics are contaminated with various bacteria and bad odors, and when recycled, the bad smell is especially severe in the recycled plastics, making it very difficult to use them as actual household goods. Accordingly, in this embodiment, we attempt to expand the usability of recycled plastic by sterilizing and deodorizing it by washing it with chlorine in advance.
바람직하게 이때 염소는 물 1L 대비 0.4~1.0mg을 투입하여 혼합하며, 이 단계에서는 물 세척과 같은 수조 방식, 분무 또는 살수 방식으로 염소 세척을 수행할 수 있을 것이다.Preferably, chlorine is added and mixed in an amount of 0.4 to 1.0 mg per 1L of water, and at this stage, chlorine cleaning can be performed using a water tank method such as water washing, spraying, or water spraying.
[건조(S13)][Drying (S13)]
이 단계는 세척단계(S12)를 통하여 수분이 함유된 폐플라스틱을 건조시키는 공정이다. 일반적인 방법으로 세척 후 고온 분위기에서 건조하는 것도 가능할 것이다. 다만, 플라스틱의 물성이 변형될 가능성이 있으므로 본 실시 예에서는 건조 하우스에서 자연조건을 이용하는 것으로 한다. 이때 건조 후 폐플라스틱의 수분 함량은 20% 미만으로 한다.This step is a process of drying waste plastic containing moisture through a washing step (S12). It would also be possible to dry in a high temperature atmosphere after washing in a general way. However, since there is a possibility that the physical properties of the plastic may be modified, in this embodiment, natural conditions are used in a dry house. At this time, the moisture content of the waste plastic after drying is less than 20%.
[가성형(S14)][Provisional molding (S14)]
이 단계는 건조단계(S13)를 통하여 건조된 폐플라스틱을 취성(脆性) 상태로 가성형하는 공정이다. 이 공정에서는 건조 후 성형기에 투입된 폐플라스틱을 압축 성형하되 외부 힘에 의하여 쉽게 부서지는 상태 즉, 취성 상태로 임시 가성형하여 배출한다. 도 4는 이 공정에서 이용되는 성형기(30)를 예시한 것으로 지름 2cm ~ 5cm 길이 5cm ~ 10cm 덩어리 형태의 취성 성형물(31)을 배출하도록 설계되어 있으며, 이때 배출된 성형물은 하부 컨베이어(32)에 떨어져 적소로 이송된다.This step is a process of temporarily molding the waste plastic dried through the drying step (S13) into a brittle state. In this process, the waste plastic that is put into the molding machine after drying is compression molded, but is temporarily temporarily molded and discharged in a brittle state that is easily broken by external forces. Figure 4 illustrates the
참고로, 상기 성형물의 사이즈가 더 크면 취급 및 이송이 불편할 뿐 아니라, 이후 공정에서 교반기에 투입되고 교반되는 과정이 원활하지 못할 수 있다.For reference, if the size of the molded product is larger, not only is it inconvenient to handle and transport, but the process of putting it into the stirrer and stirring it in the subsequent process may not be smooth.
일반적으로 건조된 필름형 또는 시트형 재료는 그 경량성·분산성으로 인하여 이송·투입·혼합 등의 작업 공정에서 정량 취급이 어렵다. 한편, 선별을 거치지 않은 복합 폐플라스틱은 재생 플라스틱에 골고루 분포되지 않고 재질별로 뭉쳐져 있게 된다. 이에 본 실시 예에서는 이 공정에서 폐플라스틱을 취성 상태로 임시 가성형하고 후공정에서 그 가성형이 쉽게 해체되도록 함으로써, 폐플라스틱의 공정상 취급 및 정량화 작업을 더욱 용이하게 하고, 또한 재질별 폐플라스틱이 재생 플라스틱에서 균질하게 분포되도록 한다.In general, dried film-type or sheet-type materials are difficult to handle in quantitative quantities during work processes such as transport, input, and mixing due to their lightness and dispersibility. Meanwhile, composite waste plastics that have not been sorted are not evenly distributed among the recycled plastics but are grouped together by material. Accordingly, in this embodiment, the waste plastic is temporarily temporarily molded in a brittle state in this process and the temporary mold is easily dismantled in the post-process, thereby making it easier to handle and quantify the waste plastic during the process, and also to measure the waste plastic by material. This ensures homogeneous distribution in the recycled plastic.
[준비(S15)][Preparation (S15)]
이 단계는 전 단계에서 건조된 또는 가성형 폐플라스틱에 정량의 상용화제를 첨가하여 재생원료를 준비하는 단계이다. 본 실시 예에서는 상기 취성 성형물에 상용화제를 첨가한 후 교반하여, 성형이 해체된 폐플라스틱과 상용화제가 혼합된 재생원료를 준비한다. 즉 전 공정에서 취성 덩어리 형태로 가성형된 폐플라스틱은 이 준비단계에서 교반기에 의하여 가성형이 해체되면서 상용화제와 혼합되며, 이에 재생원료가 준비되는 것이다. 이때 상기 교반공정이 반드시 필요한 것은 아니지만, 재료 및 상용화제의 고른 혼합 및 분포의 측면에서 훨씬 유리하다.This step is to prepare recycled raw materials by adding a fixed amount of compatibilizer to the dried or caustic waste plastic in the previous step. In this embodiment, a compatibilizer is added to the brittle molded product and then stirred to prepare a recycled raw material mixed with the dismantled waste plastic and the compatibilizer. In other words, the waste plastic that has been preformed into a brittle lump in the previous process is mixed with a compatibilizer while the preform is broken up by a stirrer in this preparation stage, thereby preparing the recycled raw material. At this time, the stirring process is not necessarily necessary, but is much more advantageous in terms of even mixing and distribution of materials and compatibilizers.
상기한 성형물은 외부 힘에 의하여 쉽게 부서지는 취성 상태이므로 상기 교반기가 특별한 힘을 가질 필요는 없으며, 통상의 회전식 교반기로 충분하다. 다만, 성형물의 빠른 해체 및 폐플라스틱 재료와 상용화제 간 혼합을 위하여 회전 칼날식 교반기가 유효하게 사용될 수 있다.Since the above molded product is in a brittle state that is easily broken by external force, the stirrer does not need to have special power, and a normal rotary stirrer is sufficient. However, a rotating blade-type stirrer can be effectively used to quickly dismantle the molded product and mix the waste plastic material and the compatibilizer.
본 실시 예에서는 건조된 폐플라스틱이 가성형 및 교반되는 것을 전제로 하지만, 건조된 폐플라스틱이 그대로 적용될 수도 있다. 상기 상용화제는 각종 폐플라스틱 재료가 서로 용융 결합할 수 있도록 하는 충전재료로서, 도 5a를 참조하면, 무기물과 전이금속의 혼합물로 이루어진 파우더(40) 형태의 재료이다. 더욱 구체적으로, 상기 상용화제는:In this embodiment, it is assumed that the dried waste plastic is temporarily molded and stirred, but the dried waste plastic may be applied as is. The compatibilizer is a filling material that allows various waste plastic materials to melt and combine with each other. Referring to FIG. 5A, it is a material in the form of a
백운석, 제올라이트, 탄산칼슘을 적정 포함하는 무기물과;minerals containing dolomite, zeolite, and calcium carbonate;
산화알루미늄, 산화철, 산화티타늄, 염화마그네슘, 염화알루미늄을 적정 포함하는 전이금속;Transition metals including aluminum oxide, iron oxide, titanium oxide, magnesium chloride, and aluminum chloride;
으로 구성된 것이다.It is composed of.
상기 상용화제는 위에서 건조된 폐플라스틱 100 중량%에 대하여 3 ~ 8 중량%의 분량으로 폐플라스틱과 함께 압출기 호퍼에 투입된다.The compatibilizer is added to the extruder hopper together with the waste plastic in an amount of 3 to 8% by weight based on 100% by weight of the waste plastic dried above.
이상에서 상기 상용화제의 구성요소는 종래 기술에도 개시되어 있는바 본 발명에서 특별한 것은 아니며, 본 발명이 상용화제의 구체적인 구성요소에 한정되는 것도 아니다. 한편, 파우더 형태의 상용화제는 그 취급 및 정량화가 어렵다. 따라서 그 상용화제로서, 도 5b에 예시한 바와 같이, 상기 파우더와 액상 플라스틱을 혼합하여 고형화한 마스터배치(MB)(41)를 이용할 수도 있다.As described above, the components of the compatibilizer are disclosed in the prior art and are not special to the present invention, nor are the present invention limited to the specific components of the compatibilizer. Meanwhile, powder-type compatibilizers are difficult to handle and quantify. Therefore, as the compatibilizer, as illustrated in FIG. 5B, masterbatch (MB) 41 obtained by mixing the powder and liquid plastic and solidifying it may be used.
[압출(S16)][Extrusion (S16)]
이 단계는 위에서 준비된 재생원료를 210℃ 이상의 온도를 갖는 압출기의 호퍼에 투입하고 압출하여 고형의 재생 플라스틱을 수득하는 공정이다. 도 5는 이 공정에 이용되는 플라스틱 압출기(50)를 예시한 것이며, 이는 통상의 플라스틱 재생용 압출기와 다르지 않다. 한편, 상기 재생 플라스틱(51)은 운반, 사용, 취급이 편리한 펠릿(도 7의 부호 52 참조) 형태로 후가공될 수 있을 것이다.This step is a process in which the recycled raw materials prepared above are put into the hopper of an extruder with a temperature of 210°C or higher and extruded to obtain solid recycled plastic. Figure 5 illustrates a
이상의 단계를 거쳐 재생 플라스틱을 수득한다.Recycled plastic is obtained through the above steps.
Claims (9)
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002103329A (en) * | 2000-10-03 | 2002-04-09 | Taiyo Denko Kk | Method for reproducing agricultural used waste vinyl film into electric wire sheath material molding material |
| KR20030002657A (en) * | 2001-06-29 | 2003-01-09 | 학교법인 수원대학교 | Method for recycling mixed waste plastics using inorganic filler |
| KR20160069818A (en) * | 2014-12-09 | 2016-06-17 | 이종국 | Filler compound for recycling waste mixing synthetic resin |
| KR20160104586A (en) * | 2015-02-26 | 2016-09-05 | 한남대학교 산학협력단 | Method for recovering polypropylene by washing waste sediment filter for water-purifier |
| KR102122851B1 (en) * | 2019-09-11 | 2020-06-15 | 하태근 | Filler for recycling waste mixing synthetic resin |
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- 2022-03-07 KR KR1020220028773A patent/KR20230132007A/en active Pending
- 2022-08-16 WO PCT/KR2022/012172 patent/WO2023171862A1/en not_active Ceased
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002103329A (en) * | 2000-10-03 | 2002-04-09 | Taiyo Denko Kk | Method for reproducing agricultural used waste vinyl film into electric wire sheath material molding material |
| KR20030002657A (en) * | 2001-06-29 | 2003-01-09 | 학교법인 수원대학교 | Method for recycling mixed waste plastics using inorganic filler |
| KR20160069818A (en) * | 2014-12-09 | 2016-06-17 | 이종국 | Filler compound for recycling waste mixing synthetic resin |
| KR20160104586A (en) * | 2015-02-26 | 2016-09-05 | 한남대학교 산학협력단 | Method for recovering polypropylene by washing waste sediment filter for water-purifier |
| KR102122851B1 (en) * | 2019-09-11 | 2020-06-15 | 하태근 | Filler for recycling waste mixing synthetic resin |
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