KR102505591B1 - Waste Synthetic Resin Regenerative Extrusion Unit with two Mixing Zone and Vents - Google Patents

Waste Synthetic Resin Regenerative Extrusion Unit with two Mixing Zone and Vents Download PDF

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KR102505591B1
KR102505591B1 KR1020210052129A KR20210052129A KR102505591B1 KR 102505591 B1 KR102505591 B1 KR 102505591B1 KR 1020210052129 A KR1020210052129 A KR 1020210052129A KR 20210052129 A KR20210052129 A KR 20210052129A KR 102505591 B1 KR102505591 B1 KR 102505591B1
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base material
screw
synthetic resin
waste synthetic
mixing
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KR1020210052129A
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Korean (ko)
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KR20220145966A (en
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안병학
안병록
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안병학
안병록
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    • 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
    • B29C48/375Plasticisers, homogenisers or feeders comprising two or more stages
    • 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
    • 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
    • B29C48/375Plasticisers, homogenisers or feeders comprising two or more stages
    • B29C48/38Plasticisers, homogenisers or feeders comprising two or more stages using two or more serially arranged screws in the same barrel
    • 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
    • B29C48/501Extruder feed section
    • 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
    • B29C48/505Screws
    • B29C48/535Screws with thread pitch varying along the longitudinal axis
    • 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
    • B29C48/505Screws
    • B29C48/64Screws with two or more threads
    • B29C48/655Screws with two or more threads having three or more threads
    • 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
    • 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
    • B29C48/76Venting, drying means; Degassing means
    • 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
    • B29C48/76Venting, drying means; Degassing means
    • B29C48/765Venting, drying means; Degassing means in the extruder apparatus
    • B29C48/766Venting, drying means; Degassing means in the extruder apparatus in screw extruders
    • 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
    • B29B2017/0464Solid state shear extrusion pulverisation
    • 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

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Environmental & Geological Engineering (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)

Abstract

본 발명을 폐합성수지 재생 압출장치에 관한 것으로서, 폐합성수지를 이송시키면서 분쇄하고 믹스하기 위한 스크류, 스크류가 내부에 위치하는 스크류 하우징, 용융된 폐합성수지에 이물질을 걸러내는 미세필터가 내장된 필터하우징으로 구성되며, 스크류에 폐합성수지를 분쇄하고 믹스하기 위한 믹싱구간이 2개로 나뉘어지고, 스크류 하우징에는 이송되면서 가열되어 발생하는 수증기와 가스를 배출하기 위한 환기구가 각각 형성되고 용융된 폐합성수지에서 이물질을 걸러내는 미세필터의 세척 또는 교체가 쉬운 것을 특징으로 한다.
이에 따라 스크류의 플라이트가 받는 부하를 분산해 내구도를 향상시키고 두차례 반복되는 분쇄와 믹스작업으로 개선된 결과물을 얻을 수 있고, 가열되어 발생하는 수증기와 가스를 바로 배출하여 재료의 역류와 안전사고를 방지하며 남아있는 이물질을 여과하기 위한 미세필터의 교체가 간단하여 생산성과 작업성이 좋다.
The present invention relates to an extrusion device for recycling waste synthetic resin, which includes a screw for grinding and mixing waste synthetic resin while transporting it, a screw housing in which the screw is located, and a filter housing with a built-in fine filter for filtering out foreign substances from molten waste synthetic resin. The mixing section for crushing and mixing the waste synthetic resin is divided into two on the screw, and the screw housing is formed with a ventilation hole to discharge steam and gas generated by being heated while being transported, respectively, and filters out foreign substances from the melted waste synthetic resin. It is characterized in that it is easy to clean or replace the fine filter.
As a result, durability is improved by distributing the load on the flight of the screw, and improved results can be obtained through repeated grinding and mixing work twice, and steam and gas generated by heating are immediately discharged to prevent backflow of materials and safety accidents. It is easy to replace the fine filter to filter the remaining foreign substances, so productivity and workability are good.

Figure R1020210052129
Figure R1020210052129

Description

각 2개의 믹싱존과 환기구를 가지는 폐합성수지 재생 압출장치{Waste Synthetic Resin Regenerative Extrusion Unit with two Mixing Zone and Vents}Waste Synthetic Resin Regenerative Extrusion Unit with two Mixing Zone and Vents}

본 발명은 한번 사용되어 버려진 폐합성수지를 재활용하기 위한 폐합성수지 재생 압출장치에 관한 것으로, 좀 더 구체적으로는 모재가 되는 폐합성수지가 재생 압출장치의 내부에서 회전하는 스크류로 인해 이송되는 동안 히터에 의해 가열되면서 수분이 증발한 수증기와 모재가 용융되는 과정에서 남아있는 이물질과 함께 발생하는 가스를 효율적으로 배출시켜 모재가 안정적으로 용융되어 이송되게 하며, 압출과정에서 발생하는 부하를 줄이면서도 생산효율을 높일 수 있도록 하려는 것이다.The present invention relates to a waste synthetic resin regeneration extrusion apparatus for recycling waste synthetic resin once used and discarded, and more specifically, waste synthetic resin as a base material is transferred by a screw rotating inside the regeneration extrusion apparatus by a heater. Efficiently discharges water vapor from which moisture evaporates while being heated and gas generated along with foreign substances remaining in the process of melting the base material so that the base material is stably melted and transported, while reducing the load generated during the extrusion process and increasing production efficiency. is to make it possible.

주지된 바와 같이 합성수지는 열을 가해 반복적인 성형이 가능하므로 자원절감과 환경보호 차원에서 소각하거나 폐기하지 않고 최대한 재생공정을 통하여 재활용한다.As is well known, since synthetic resin can be repeatedly molded by applying heat, it is recycled through a recycling process as much as possible without incineration or disposal in terms of resource saving and environmental protection.

재활용에 사용되는 수지는 주로 한번 사용되어 버려진 플라스틱등의 폐합성수지로 종류별로 수거한 다음에 선별장소에서 재생할 수지 이외의 폐기물을 선별하며, 절단을 통하여 일정 크기 이하의 플레이크 상태로 만든다. 그러나 이러한 재생을 위한 재료 준비상태에서도 수분 및 이물질이 포함될 수 밖에 없다.The resin used for recycling is mainly waste synthetic resin such as plastic that has been used once and discarded, and is collected by type, then sorted out waste other than resin to be recycled at a sorting site, and made into flakes of a certain size or less through cutting. However, even in the material preparation state for such regeneration, moisture and foreign substances are inevitably included.

준비된 폐합성수지는 호퍼를 통하여 재생 압출장치로 투입되어 장치 내부에 회전하는 스크류에 의해 이송됨과 동시에 첨가제가 투입된 상태로 가열장치에 의해 가열되면서 혼련을 거치면서 점차 반용융 상태가 되며, 스크류 통로 끝에 위치한 필터에서 남아있는 이물질을 걸러내어 재사용이 가능하게 만든다.The prepared waste synthetic resin is injected into the regeneration extrusion device through the hopper and transported by the screw rotating inside the device. At the same time, it is heated by the heating device in the state of adding additives and gradually becomes a semi-melted state through kneading. It filters out the foreign matter remaining in the filter and makes it reusable.

그러나, 종래의 폐합성수지 재생 압출장치는 폐합성수지를 가열하여 수분이 증발되어 발생하는 수증기와 용융되는 과정에 이물질과 함께 발생하는 가스는 폐합성수지를 투입하는 호퍼로 역류하게 되므로 투입되는 폐합성수지의 이송을 방해하여 작업속도를 늦춰 생산성을 저하시킨다.However, in the conventional extrusion apparatus for regenerating waste synthetic resin, water vapor generated by evaporating water by heating waste synthetic resin and gas generated together with foreign substances during melting flow back to the hopper into which the waste synthetic resin is injected, so that the injected waste synthetic resin is transported. It slows down work and lowers productivity.

또한, 스크류가 위치한 통로에 잔류하는 수증기는 통로 내부의 온도를 낮춰 폐합성수지가 용융되는 것을 방해하고, 가스는 통로에 잔류하는 시간이 길어질수록 계속된 가열로 큰 폭발음을 내거나 심한경우에는 가스폭발과 같은 안전사고를 유발하는 문제가 있다.In addition, the vapor remaining in the passage where the screw is located lowers the temperature inside the passage to prevent the waste synthetic resin from melting, and the longer the time remaining in the passage, the longer the gas remains in the passage, the louder the explosion or the worse the gas explosion. There is a problem that causes the same safety accident.

또한, 폐합성수지에 첨가제가 균등하게 섞이기 위해서는 스크류의 플라이트가 짧게 배치되어 있는 좁은 공간의 혼련구간(또는 믹스구간)을 통과해야하는데, 이러한 혼련구간에서 높은 열마찰과 전단력으로 압출장치 전체의 부하가 증대되고 플라이트의 마모가 빠르게 일어나게 되어 내구성이 저하되는 문제도 있고, 모재의 열가소화가 발생하고 열분해에 의한 탄화현상도 발생하는 문제가 있다.In addition, in order to evenly mix the additives in the waste synthetic resin, it is necessary to pass through a kneading section (or mixing section) in a narrow space where the flights of the screw are arranged short. There is also a problem that durability is lowered due to increased and rapid abrasion of the flight, and there is also a problem that thermoplasticization of the base material occurs and carbonization by thermal decomposition also occurs.

그리고 종래의 압출장치에서 스크류 통로 끝에 설치되는 필터장치는 용융된 소재가 압출되어 배출되는 직선방향으로 필터를 통과하도록 설계되어 있고 모터와 변속기 및 필터와 스크래퍼가 모두 장착된 필터 하우징이 스크류 통로 끝단으로부터 이격되면서 열리는 형태로 구성되어 있다. 따라서 필터 하우징 내부를 청소하거나 미세필터를 교체하려면, 모터와 변속기, 미세필터와, 스크래퍼가 모두 장착되어 매우 무게가 무거운 필터 하우징을 크레인으로 걸은 상태로 개방을 시켜야 하는 방식으로 유지보수를 하였다.And in the conventional extrusion device, the filter device installed at the end of the screw passage is designed to pass through the filter in the straight direction in which the molten material is extruded and discharged, and the filter housing equipped with the motor, transmission, filter, and scraper are all removed from the end of the screw passage. It is configured in an open form while being spaced apart. Therefore, in order to clean the inside of the filter housing or replace the fine filter, maintenance was performed in such a way that the motor, transmission, fine filter, and scraper were all mounted and the filter housing, which was very heavy, had to be opened while hanging with a crane.

결국, 이러한 문제에 따라 필터 하우징 내부를 청소하거나 미세필터를 교체하는 등의 작업이 매우 어렵고 시간이 많이 걸리면서 위험한 작업이 될 수밖에 없었던 것이다.As a result, due to these problems, tasks such as cleaning the inside of a filter housing or replacing a fine filter have to be very difficult, time-consuming, and dangerous tasks.

대한민국 등록특허공보 제10-1985373호Republic of Korea Patent Registration No. 10-1985373

상기와 같은 문제점을 해결하고자 안출된 본 발명은 폐합성수지를 분쇄하고 용융하는 과정이 개선된 폐합성수지 재생 압출장치를 제공함으로써, 용융되는 폐합성수지에서 발생하는 수증기와 가스가 역류되거나 통로 내부에 남지않게 배출하고, 용융되는 모재의 흐름을 원활하게 하면서도 충분한 혼련과 생산성이 향상되도록 하는 것을 목적으로 한다.The present invention, which has been made to solve the above problems, provides a waste synthetic resin regeneration extrusion apparatus in which the process of crushing and melting the waste synthetic resin is improved, so that water vapor and gas generated from the melted waste synthetic resin do not flow backward or remain inside the passage. Its purpose is to improve sufficient kneading and productivity while facilitating the flow of the base material being discharged and melted.

또한, 스크류와 모터의 부하를 줄여 내구성을 개선하여 에너지 소모를 줄이면서 생산작업이 안전하면서도 생산성이 크게 향상되는 것을 목적으로 한다.In addition, an object of the present invention is to significantly improve productivity while reducing energy consumption by reducing the load of the screw and the motor and improving durability.

아울러 본 발명은 필터 하우징을 유지보수하는 작업이, 안전하면서도 편리하고 신속하게 이루어질 수 있도록 함을 목적으로 한다.In addition, an object of the present invention is to ensure that maintenance of the filter housing can be performed safely, conveniently and quickly.

상기 목적을 달성하기 위한 본 발명의 2개의 환기구와 나뉘어져 있는 믹싱존을 가지는 폐합성수지 재생 압출장치는, 폐합성수지를 이송시키고 분쇄 및 믹스작업을 하기 위한 스크류에 2개로 나뉘어진 믹싱구간과 믹싱구간 끝에 환기구를 형성하여 폐합성수지의 분쇄와 믹스 작업에서 발생하는 플라이트의 부하를 분산해 내구도는 향상시키고 작업으로 체류되는 폐합성수지에서 발생하는 수증기와 가스는 환기구로 배출하여 폐합성수지가 역류되는 것과 안전사고를 방지하는 것을 특징으로 한다.In order to achieve the above object, the extrusion apparatus for recycling waste synthetic resin having a mixing zone divided from two vents of the present invention has a mixing section divided into two and an end of the mixing section on a screw for conveying waste synthetic resin and performing crushing and mixing operations. Ventilation holes are formed to distribute the load of the flight generated from crushing and mixing of waste synthetic resin to improve durability, and vapor and gas generated from waste synthetic resin remaining during work are discharged through the ventilation holes to prevent backflow of waste synthetic resin and safety accidents. characterized by preventing

또한, 분쇄 및 믹스작업을 거치면서 용융된 폐합성수지에 남아있는 이물질을 걸러내는 미세필터는 하우징 본체가 스크류 끝단에 고정된 상태에서 문짝만을 열어 내부를 개방할 수 있도록 함으로써 유지보수 작업을 크레인과 같은 대형장치 없이 안전하게 진행할 수 있는 것을 특징으로 한다.In addition, the fine filter, which filters out foreign substances remaining in the melted waste synthetic resin through crushing and mixing, allows maintenance work to be performed like a crane by opening only the door while the housing body is fixed to the end of the screw. It is characterized in that it can proceed safely without a large device.

본 발명의 폐합성수지 재생 압출장치는, 폐합성수지가 이송되게 스크류가 위치하는 통로에 소정의 거리를 가지는 2개의 환기구와 분할되어 구분되는 믹싱존이 형성된 재생 압출장치를 제공함으로써 모재의 안정적인 용융과 이송이 가능하며, 분할된 혼련으로 균일하고 충분한 체류시간에 의해 가소화와 탄화를 낮추어 품질향상을 도모할 수 있고, 플라이트 피치를 넓게 설계하여 생산성도 향상시킬 수 있다.The waste synthetic resin regeneration extrusion device of the present invention provides a regeneration extrusion device in which a mixing zone is divided and distinguished from two vents having a predetermined distance in a passage where a screw is located to transport waste synthetic resin, thereby stably melting and transporting the base material. This is possible, and quality improvement can be promoted by lowering plasticization and carbonization by uniform and sufficient residence time through divided kneading, and productivity can be improved by designing a wide flight pitch.

또 수증기와 가스는 환기구로 신속하고 효과적으로 배출되어 생산성의 저하와 안전사고를 예방하게 된다.In addition, water vapor and gas are quickly and effectively discharged through the vent to prevent a decrease in productivity and safety accidents.

또한, 폐합성수지와 첨가제를 믹싱하는 과정을 2단계로 나누어 균등하게 섞이게 작업하며 스크류의 플라이트가 받는 부하는 줄어들어 내구성이 향상되며, 전기 사용도 줄일 수 있게 된다.In addition, the process of mixing waste synthetic resin and additives is divided into two stages to mix them evenly, and the load on the flight of the screw is reduced, improving durability and reducing electricity consumption.

그리고 미세필터를 교체하는 등 필터 하우징을 유지보수 하는 작업이 매우 안전하고 신속하게 이루어지게 된다.In addition, maintenance of the filter housing, such as replacing the fine filter, can be performed very safely and quickly.

도 1은 본 발명의 전체측면도
도 2는 본 발명의 전체단면도
도 3은 본 발명의 일부단면도
도 4는 본 발명의 또 다른 일부단면도
도 5는 도 4의 평면단면도
1 is an overall side view of the present invention
2 is an overall cross-sectional view of the present invention
3 is a partial cross-sectional view of the present invention
4 is another partial cross-sectional view of the present invention
5 is a cross-sectional plan view of FIG. 4

이하, 본 발명의 2개의 믹싱존과 환기구를 가지는 폐합성수지 재생 압출장치에 대하여 상세히 설명하고자 하는바, 이러한 설명은 본 발명을 구현하기 위한 실시 예를 기준으로 한 것으로서, 본 발명이 추구하는 기술적 사상을 본 문서에 기재된 실시 예에 기재된 형태로 한정하려는 것이 아니며, 본 발명의 실시 예의 다양한 변경(modifications), 균등물(equivalents) 및/또는 대체물(alternatives)을 포함하는 것으로 이해되어야 할 것이다.Hereinafter, the waste synthetic resin regeneration extrusion apparatus having two mixing zones and a ventilation hole of the present invention will be described in detail. This description is based on an embodiment for implementing the present invention, and the technical idea pursued by the present invention It is not intended to be limited to the form described in the embodiments described in this document, and it will be understood to include various modifications, equivalents and / or alternatives of the embodiments of the present invention.

아울러, 본 발명의 실시 예를 설명하면서 본 발명의 구성에 따른 작용 효과를 명시적으로 기재하여 설명하지 않았을지라도, 해당 구성에 의해 예측 가능한 효과 또한 인정되어야 함은 당연하다.In addition, even if the operational effects according to the configuration of the present invention are not explicitly described and described while describing the embodiments of the present invention, it is natural that the effects predictable by the corresponding configuration should also be recognized.

본 발명의 폐합성수지 재생 압출장치(1)는 길이방향으로 길게 형성되는데, 스크류(10)는 스크류 하우징(20) 내부의 통로(21)에 위치해 한쪽 끝에는 회전을 위한 동력수단으로 스크류 모터(23)가 연결되고 반대쪽 끝에는 스크류(10)를 지탱하기 위한 스크류 지지대(22)가 조립되고 스크류 하우징(20) 외부에는 가열장치(도면 미도시)가 구비된다.The waste synthetic resin extrusion apparatus 1 of the present invention is formed long in the longitudinal direction, and the screw 10 is located in the passage 21 inside the screw housing 20, and at one end is a screw motor 23 as a power means for rotation. is connected, and at the opposite end, a screw support 22 for supporting the screw 10 is assembled, and a heating device (not shown) is provided outside the screw housing 20.

스크류(10)는 소정의 직경을 가지고 몸체가 되는 회전축(11)과, 회전축(11)을 중심으로 통로(21)의 직경보다 작고 나선형으로 이어져서 폐합성수지를 이송, 분쇄, 믹스하는 플라이트(12)를 포함한다.The screw 10 has a rotational shaft 11 having a predetermined diameter and becomes a body, and a flight 12 that is smaller than the diameter of the passage 21 around the rotational shaft 11 and spirally connected to transfer, crush, and mix the waste synthetic resin. ).

나선형의 플라이트(12)는 플라이트(12)간의 간격(거리)에 따라서 폐합성수지(이하 '모재')를 이송, 분쇄, 믹스하는 작업의 비율(효율)이 달라지는데, 동일한 길이의 축에 형성되는 설정하에 넓은 간격(12-1)은 플라이트(12)간의 사이가 멀어져 모재와의 접촉이 줄어 분쇄와 믹스작업의 효율은 떨어지나 내구성이 높아 모재의 이송에 효과적이고, 좁은 간격(12-2)은 플라이트(12)간의 사이가 가까워지는 만큼 모재와의 접촉이 잦아 내구성은 떨어지나 분쇄와 믹스작업이 효과적이다.In the spiral flight 12, the ratio (efficiency) of the work of transporting, crushing, and mixing the waste synthetic resin (hereinafter referred to as 'base material') varies according to the distance (distance) between the flights 12. Under the wide gap (12-1), the distance between the flights (12) is reduced and the contact with the base material is reduced, reducing the efficiency of grinding and mixing work, but is effective in transferring the base material due to high durability, and the narrow gap (12-2) is (12) As the distance between them increases, the contact with the parent material is frequent, so the durability is reduced, but the grinding and mixing work is effective.

종래의 폐합성수지 재생 압출장치에서 사용한 스크류는 시작점에서 필요한 만큼 넓은 간격의 플라이트로 형성된 이송구간과 나머지에는 모재를 분쇄하고 믹스하는 좁은 간격의 플라이트로 형성된 믹싱구간으로 나누었는데, 믹싱구간이 짧으면 모재의 분쇄와 믹스가 제대로 되지않고 믹싱구간이 길면 모재가 플라이트 사이에서 체류하는 시간이 길어져 탄화되고 플라이트의 마모가 빨라져 내구도가 급격하게 떨어지는 문제가 있다.The screw used in the conventional waste synthetic resin regeneration extrusion device is divided into a transfer section formed of flights at a wide interval as needed at the starting point and a mixing section formed with flights at a narrow interval to crush and mix the base material in the rest. If the mixing section is short, the base material If the grinding and mixing are not done properly and the mixing section is long, the length of time the base material stays between the flights is lengthened and carbonized, and the wear of the flights is accelerated, resulting in a rapid drop in durability.

이러한 문제를 해결하기 위해 본 발명의 스크류(10)는 모재가 이송되는 동안 가열장치로 적당한 온도까지 가열되는 제1 이송구간(31), 가열된 모재를 분쇄하고 믹스하는 제1 믹싱구간(34), 1차 작업된 모재를 이송하는 제2 이송구간(32), 1차 작업된 모재를 다시 분쇄 및 믹스하는 제2 믹싱구간(35), 2차 작업을 마친 모재를 이송하는 제3 이송구간(33)을 차례대로 구성해 믹싱구간(34,35)에서 플라이트(12)가 받는 부하를 나누어 내구성을 향상시키고 모재에 사용하는 첨가제가 충분히 섞이게 한다.In order to solve this problem, the screw 10 of the present invention is a first transfer section 31 in which the base material is heated to an appropriate temperature by a heating device while being transported, and a first mixing section 34 for grinding and mixing the heated base material , the second transfer section 32 for transporting the first worked base material, the second mixing section 35 for crushing and mixing the first worked base material again, the third transfer section for transferring the second worked base material ( 33) in order to divide the load received by the flight 12 in the mixing sections 34 and 35 to improve durability and sufficiently mix the additives used in the base material.

상기 제1 이송구간(31)은 플라이트(12)가 넓은 간격(12-1)을 가지면서 회전축(11)의 직경이 작았다가 점차 커지는 형태로 구성하여 최초에 공간이 많고 부피가 큰 상태의 폐합성수지가 유입되어 점차 압축되면서 이송하는 역할을 하며, 제1 믹싱구간(34)은 플라이트(12)가 좁은 간격(12-2)을 유지하면서 회전축(11)의 직경은 제1 이송구간(31) 최대의 직경이 유지되어 용해되는 모재를 교반과 동시에 강한 힘으로 압착하면서 밀어내게 된다. The first transfer section 31 is configured in such a way that the diameter of the rotating shaft 11 is small and then gradually increases while the flights 12 have a wide interval 12-1, so that the lungs in a large space and bulky state are initially formed. It plays a role in transporting synthetic resin while being gradually compressed, and in the first mixing section 34, the flight 12 maintains a narrow gap 12-2, and the diameter of the rotating shaft 11 is the first conveying section 31 The maximum diameter is maintained and the dissolving base material is pushed out while stirring and compressing with strong force at the same time.

제2 이송구간(32)은 다시 플라이트(12)가 넓은 간격(12-1)을 가지면서 회전축(11)의 직경이 작았다가 점차 커지는 형태로 구성하여 상기 제1 믹싱구간(34)을 통과한 모재의 압축정도를 이완시켜주는 기능을 하면서 이송속도를 느리게 하여 재질의 응력을 줄이면서 가스를 배출시키는 작용을 도와주게 된다.The second transfer section 32 is formed in such a way that the diameter of the rotating shaft 11 is small and gradually increases while the flights 12 have a wide interval 12-1, and passes through the first mixing section 34 While functioning to relax the degree of compression of the base material, it slows down the transfer speed to reduce the stress of the material and help to release the gas.

제2 이송구간(32) 다음에 구성되는 제2 믹싱구간(35)은 다시 플라이트(12)가 좁은 간격(12-2)을 유지하면서 회전축(11)의 직경은 제2 이송구간(32) 최대의 직경이 유지되어 용해되는 모재를 교반과 동시에 강한 힘으로 압착하면서 밀어내게 된다. 상기 제2 믹싱구간(35)의 후단에는 역회전 플라이트부를 형성하여 혼련을 강화할 수 있다.In the second mixing section 35, which is composed after the second conveying section 32, the diameter of the rotating shaft 11 is the maximum of the second conveying section 32 while the flight 12 maintains the narrow gap 12-2. The diameter of is maintained and the dissolving base material is pushed out while stirring and compressing with strong force. Kneading may be enhanced by forming a counter-rotating flight unit at the rear end of the second mixing section 35.

또, 제3 이송구간(33) 역시 다시 플라이트(12)가 넓은 간격(12-1)을 가지면서 회전축(11)의 직경이 작았다가 점차 커지는 형태로 구성하여 상기 제2 믹싱구간(35)을 통과한 모재의 압축정도를 이완시켜주는 기능을 하면서 이송속도를 느리게 하여 재질의 응력을 줄이면서 가스를 배출시키는 작용을 하게 된다.In addition, the third transfer section 33 is also configured in such a way that the diameter of the rotating shaft 11 is small and gradually increases while the flights 12 have a wide interval 12-1, so that the second mixing section 35 It has the function of relaxing the degree of compression of the parent material that has passed through it and slows down the transfer speed to reduce the stress of the material and to release the gas.

그리고 제1 믹싱구간(34)과 제2 믹싱구간(35)에서의 플라이트(12) 간격을 서로 다르게 하여 분쇄 및 믹스의 작업비율을 30:70, 40:60 등으로 원하는 작업비율의 설정이 가능하다.In addition, by making the flight 12 intervals in the first mixing section 34 and the second mixing section 35 different from each other, the working ratio of grinding and mixing can be set to 30:70, 40:60, etc. do.

스크류 하우징(20)에는 믹싱구간(34,35)이 끝나고 제2 이송구간(32) 및 제3 이송구간(33)이 시작되는 위치에 각각 환기구(24)를 형성하여 모재가 용융되어 발생하는 수증기와 가스가 역류하거나 남지 않게 배출시키고, 필요에 따라 환기필터(24-1), 집진기(24-2) 등을 사용한다.Ventilation ports 24 are formed in the screw housing 20 at the positions where the mixing sections 34 and 35 end and the second conveying section 32 and the third conveying section 33 start, respectively, so that water vapor generated by melting the base material and gas are discharged so that they do not flow back or remain, and use a ventilation filter (24-1), a dust collector (24-2), etc. as necessary.

스크류(10)가 조립된 스크류 하우징(20)의 끝에는 이송되면서 용융된 모재에 남아있는 이물질을 걸러내기 위해 미세필터(42)가 내장되어 있는 필터 하우징(40)이 위치한다.At the end of the screw housing 20 to which the screw 10 is assembled, a filter housing 40 having a built-in fine filter 42 is positioned to filter out foreign substances remaining in the molten base material while being transported.

필터 하우징(40)의 본체(40') 내부 중앙에는 모재의 진입방향과 직각이 되는 방향으로 미세필터(42)를 설치하고, 본체(40')의 외부에도 모재의 진입방향과 직각이 되는 방향으로 스크래퍼 모터(44)를 설치한 후 스크래퍼 모터(44)의 축이 미세필터(42)를 관통하게 한 다음 끝단에 미세필터(42)의 표면에 밀착되는 스크래퍼(43)를 설치하였다. A fine filter 42 is installed in the inner center of the main body 40' of the filter housing 40 in a direction perpendicular to the entry direction of the base material, and a direction perpendicular to the entry direction of the base material also outside the main body 40'. After installing the scraper motor 44, the shaft of the scraper motor 44 penetrates the fine filter 42, and then the scraper 43 adhered to the surface of the fine filter 42 is installed at the end.

또한, 스크류 하우징(20)은 미세필터(42) 앞쪽의 본체(40')에 모재가 공급되도록 연결하여 모재가 진입한 다음 직각방향으로 이송이 전환되면서 미세필터(42)를 통과하도록 구성하였고, 필터 하우징(40)을 통과한 모재가 배출되는 이송관(60)은 미세필터(42)의 후방에서 다시 측방향으로 연결하여 미세필터(42)를 통과한 모재는 다시 직각으로 이송방향이 전환되면서 배출되도록 구성한 것이다.In addition, the screw housing 20 is connected to the main body 40 'in front of the fine filter 42 so that the base material is supplied so that the base material enters and then passes through the fine filter 42 while being transferred in a right angle direction, The transport pipe 60 through which the base material passing through the filter housing 40 is discharged is connected laterally again from the rear of the fine filter 42, and the base material passing through the fine filter 42 is converted to a right angle again, It is designed to be released.

또한, 필터 하우징(40)의 일측 즉, 본체(40')의 스크래퍼(43)가 설치된 쪽에는 개폐도어(41)를 설치하여 본체(40') 사이에 설치된 경첩으로 개폐가 가능하도록 설치된다. 개폐도어(41)는 본체(40') 내부 공간의 청소나 장시간 사용한 미세필터(42)를 세척 및 교체할 때 사용된다.In addition, an opening/closing door 41 is installed on one side of the filter housing 40, that is, on the side of the main body 40' on which the scraper 43 is installed, so that it can be opened and closed by a hinge installed between the main bodies 40'. The opening and closing door 41 is used to clean the inner space of the main body 40' or to wash and replace the fine filter 42 that has been used for a long time.

이러한 구성으로 인하여 무게가 무거운 필터 하우징(40)이 스크류 하우징(20)에 직접 연결고정된 상태가 되므로 개폐도어(41)만 개방하면 내부 청소나 미세필터(42) 교체가 가능하게 되는 것이다.Due to this configuration, since the heavy filter housing 40 is directly connected and fixed to the screw housing 20, it is possible to clean the inside or replace the fine filter 42 by opening only the opening and closing door 41.

상기와 같이 구성된 본 발명의 작용을 살펴보면 다음과 같다.Looking at the operation of the present invention configured as described above is as follows.

수거한 폐합성수지에서 분류하기 쉬운 이물질을 우선적으로 제거한 다음, 폐합성수지 재생 압출장치(1)에 넣어 재활용이 가능한 상태로 만든다.Foreign substances that are easy to classify are preferentially removed from the collected waste synthetic resin, and then put into the waste synthetic resin recycling extrusion device 1 to make it recyclable.

더욱 상세하게는, 모재를 호퍼(50)에 넣으면 스크류 하우징(20)의 통로(21)로 들어가 회전하고 있는 스크류(10)에 의해 접차 압축되면서 이송된다.More specifically, when the base material is put into the hopper 50, it enters the passage 21 of the screw housing 20 and is transported while being compressed by the rotating screw 10.

모재는 제1 이송구간(31)에서 가열장치로 서서히 가열되는 상태로 이송되고 제1 믹싱구간(34)에서 좁은 간격(12-2)을 가지는 플라이트(12)에 분쇄되고 첨가제가 균등하게 섞이도록 믹스작업하며, 작업을 위해 체류되는 동안 모재는 조금씩 용융되어 남아있는 수분이 증발해 생기는 수증기와 모재와 가스에서 발생하는 가스가 끝에 위치한 환기구(24)로 배출된다.The base material is transferred in a state of being slowly heated by a heating device in the first transfer section 31 and pulverized on the flight 12 having a narrow gap 12-2 in the first mixing section 34, and the additives are mixed evenly While mixing and staying for work, the base material melts little by little and the remaining moisture evaporates, resulting in water vapor and gas generated from the base material and gas are discharged through the ventilation port 24 located at the end.

제1 믹싱구간(34)에서 1차작업된 모재는 제2 이송구간(32)을 지나서 제2 믹싱구간(35)으로 넘어와 다시 한번 분쇄 및 믹스작업을 진행하면서 수증기와 가스는 환기구(24)로 배출시키고 좀 더 용융되어 있는 상태가 되어 제3 이송구간(33)을 통해서 필터 하우징(40)으로 이송된다.The primary material in the first mixing section 34 passes through the second transfer section 32 and passes to the second mixing section 35, where it is crushed and mixed once again while steam and gas are discharged through the ventilation port 24 It is discharged to a more molten state and is transferred to the filter housing 40 through the third transfer section 33.

필터 하우징(40)에 도달한 모재는 뒤에서 밀려오는 모재에 의해 압출방식처럼 계속해서 밀려나 미세필터(42)를 통과하게 되고 용융된 모재가 미세필터(42)를 통과하면서 남아있는 이물질을 걸러내고 다음공정을 위해 이송관(60)을 통하여 이송된다.The base material that has reached the filter housing 40 is continuously pushed like an extrusion method by the base material pushed from behind and passes through the fine filter 42, and the molten base material passes through the fine filter 42 to filter out the remaining foreign substances and then It is transported through the transfer pipe 60 for the process.

이렇게 두개로 나뉘어진 믹싱구간(34,35)으로 인해 좁은 간격(12-2)을 가지는 플라이트(12)가 받는 부하를 분산시켜 내구도를 향상시키고 분쇄 및 믹스작업을 두차례에 걸쳐 진행해 좀더 개선된 모재를 얻을 수 있고, 모재가 용융되어 발생하는 수증기와 가스는 환기구(24)로 배출되어 통로(21)에서 모재가 역류하여 작업속도를 지연시키거나 가스폭발 등의 안전사고를 예방한다.Due to the mixing section (34, 35) divided into two, the load on the flight (12) having a narrow gap (12-2) is distributed to improve durability, and the crushing and mixing work is carried out twice to achieve more improved The base material can be obtained, and steam and gas generated when the base material is melted are discharged through the ventilation hole 24, and the base material flows backward in the passage 21 to delay the work speed or prevent safety accidents such as gas explosion.

또한, 필터 하우징(40)의 경우도 본체(40')가 스크류 하우징(20)에 고정된 상태가 되므로 무게가 비교적 가벼운 개폐도어(41)만 열면 내부 청소나 미세필터(42)의 세척 및 교환을 편리하고 간단하게 할 수 있다는 장점이 있다.In addition, in the case of the filter housing 40, since the main body 40' is fixed to the screw housing 20, opening the door 41, which is relatively light in weight, cleans the inside or cleans and replaces the fine filter 42. It has the advantage of being convenient and simple to do.

1: 폐합성수지 재생 압출장치
10: 스크류
11: 회전축
12: 플라이트
12-1: 넓은 간격
12-2: 좁은 간격
20: 스크류 하우징
21: 통로
22: 스크류 지지대
23: 스크류 모터
24: 환기구
24-1: 환기필터
24-2: 집진기
31: 제1 이송구간
32: 제2 이송구간
33: 제3 이송구간
34: 제1 믹싱구간
35: 제2 믹싱구간
40: 필터 하우징
40': 본체
41: 개폐도어
42: 미세필터
43: 스크래퍼
44: 스크래퍼 모터
50: 호퍼
60: 이송관
1: Waste synthetic resin recycling extrusion device
10: screw
11: axis of rotation
12: Flight
12-1: wide spacing
12-2: narrow spacing
20: screw housing
21: aisle
22: screw support
23: screw motor
24: ventilation hole
24-1: ventilation filter
24-2: dust collector
31: 1st transfer section
32: 2nd transfer section
33: 3rd transfer section
34: 1st mixing section
35: 2nd mixing section
40: filter housing
40': body
41: opening and closing door
42: fine filter
43: scraper
44: scraper motor
50: Hopper
60: transfer pipe

Claims (3)

플라이트(12)가 형성되어 있는 스크류(10)가 스크류 하우징(20)의 통로(21)에 조립되고, 스크류 하우징(20)에 조립된 스크류(10)의 이송방향 끝에는 미세필터(42)가 내장되며 미세필터(42)에 붙어있는 이물질을 긁어내는 스크래퍼(43)를 가지는 필터 하우징(40)이 연결되는 폐합성수지 재생 압출장치에 있어서,
상기 스크류(10)는,
플라이트(12)가 넓은 간격(12-1)을 가지면서 회전축(11)의 직경이 작았다가 점차 커지는 형태로 구성하여 최초에 공간이 많고 부피가 큰 상태의 폐합성수지가 유입되어 점차 압축되면서 이송하는 역할을 하는 제1 이송구간(31);
플라이트(12)가 좁은 간격(12-2)을 유지하면서 회전축(11)의 직경은 제1 이송구간(31) 최대의 직경이 유지되어 용해되는 모재를 교반과 동시에 강한 힘으로 압착하면서 밀어내게 하는 제1 믹싱구간(34);
다시 플라이트(12)가 넓은 간격(12-1)을 가지면서 회전축(11)의 직경이 작았다가 점차 커지는 형태로 구성하여 상기 제1 믹싱구간(34)을 통과한 모재의 압축정도를 이완시켜주는 기능을 하면서 이송속도를 느리게 하여 재질의 응력을 줄이면서 가스를 배출시키는 작용을 도와주게 하는 제2 이송구간(32);
다시 플라이트(12)가 좁은 간격(12-2)을 유지하면서 회전축(11)의 직경은 제2 이송구간(32) 최대의 직경이 유지되어 용해되는 모재를 교반과 동시에 강한 힘으로 압착하면서 밀어내게 하며, 후단에는 역회전 플라이트부를 형성하여 혼련을 강화할 수 있게하는 제2 믹싱구간(35);
다시 플라이트(12)가 넓은 간격(12-1)을 가지면서 회전축(11)의 직경이 작았다가 점차 커지는 형태로 구성하여 상기 제2 믹싱구간(35)을 통과한 모재의 압축정도를 이완시켜주는 기능을 하면서 이송속도를 느리게 하여 재질의 응력을 줄이면서 가스를 배출시키는 작용을 하는 제3 이송구간(33);으로 구분되며,
스크류 하우징(20)의 끝에는 필터 하우징(40)이 위치하되, 필터 하우징(40)의 본체(40') 내부 중앙에는 모재의 진입방향과 직각이 되는 방향으로 미세필터(42)와 스크래퍼(43)를 설치하며,
스크류 하우징(20)은 미세필터(42) 앞쪽의 본체(40')에 모재가 공급되도록 연결하여 모재가 진입한 다음 직각방향으로 이송이 전환되면서 미세필터(42)를 통과하도록 구성하였고, 필터 하우징(40)을 통과한 모재가 배출되는 이송관(60)은 미세필터(42)의 후방에서 다시 측방향으로 연결하여 미세필터(42)를 통과한 모재는 다시 직각으로 이송방향이 전환되면서 배출되도록 구성하며,
필터 하우징(40)의 일측 즉, 본체(40')의 스크래퍼(43)가 설치된 쪽에는 개폐도어(41)를 설치하여 본체(40') 사이에 설치된 경첩으로 개폐가 가능하도록 설치하여 개폐도어(41)만 개방하면 내부 청소나 미세필터(42) 교체가 가능하게 되는 것을 특징으로 하는 각 2개의 믹싱존과 환기구를 가지는 폐합성수지 재생 압출장치.
The screw 10 on which the flight 12 is formed is assembled to the passage 21 of the screw housing 20, and a fine filter 42 is built-in at the end of the screw 10 assembled to the screw housing 20 in the transport direction. In the waste synthetic resin regeneration extrusion device connected to the filter housing 40 having a scraper 43 that scrapes foreign substances attached to the fine filter 42,
The screw 10,
The flight 12 has a wide interval 12-1 and the diameter of the rotation shaft 11 is small and gradually increases, so that the waste synthetic resin with a lot of space and a large volume is introduced and gradually compressed and transported. A first transfer section 31 serving as a role;
While the flight 12 maintains a narrow gap 12-2, the diameter of the rotating shaft 11 maintains the maximum diameter of the first transfer section 31 to push the dissolving base material while stirring and pressing with strong force at the same time. a first mixing section 34;
Again, the flight 12 has a wide interval 12-1, and the diameter of the rotating shaft 11 is configured in a form where the diameter of the rotating shaft 11 is small and then gradually increases to relax the degree of compression of the base material passing through the first mixing section 34 A second conveying section 32 that assists the action of discharging gas while reducing the stress of the material by slowing down the conveying speed while functioning;
Again, while the flight 12 maintains a narrow gap 12-2, the diameter of the rotating shaft 11 is maintained at the maximum diameter of the second transfer section 32 to push the dissolving base material while stirring and pressing with strong force at the same time. And, a second mixing section 35 for strengthening kneading by forming a counter-rotating flight part at the rear end;
Again, the flight 12 has a wide interval 12-1 and the diameter of the rotating shaft 11 is configured in a form where the diameter of the rotating shaft 11 is small and then gradually increases to relax the degree of compression of the base material passing through the second mixing section 35 It is divided into a third conveying section 33 that functions to discharge gas while reducing the stress of the material by slowing the conveying speed while performing the function,
The filter housing 40 is located at the end of the screw housing 20, but the fine filter 42 and the scraper 43 are placed in the center of the inside of the main body 40' of the filter housing 40 in a direction perpendicular to the entry direction of the base material. install,
The screw housing 20 is connected to the main body 40' in front of the fine filter 42 so that the base material is supplied so that the base material enters and passes through the fine filter 42 while being transferred in a right angle direction. The transfer pipe 60 through which the base material passing through 40 is discharged is connected laterally again from the rear of the fine filter 42 so that the base material passing through the fine filter 42 is discharged while the transfer direction is converted to a right angle again. make up,
An opening/closing door 41 is installed on one side of the filter housing 40, that is, on the side where the scraper 43 of the main body 40' is installed, so that it can be opened and closed by a hinge installed between the main bodies 40'. Waste synthetic resin regeneration extrusion apparatus having two mixing zones and ventilation holes, characterized in that when only 41) is opened, internal cleaning or replacement of the fine filter 42 is possible.
제1항에 있어서,
상기 제1 믹싱구간(34)과 제2 믹싱구간(35)은 플라이트(12)를 동일한 치수의 좁은 간격(12-2) 외에도 각기 다른 치수의 간격을 가지게 하여 모재의 분쇄와 믹스작업비율을 다르게 설정할 수 있는 것을 특징으로 하는 각 2개의 믹싱존과 환기구를 가지는 폐합성수지 재생 압출장치.
According to claim 1,
In the first mixing section 34 and the second mixing section 35, the flights 12 have different dimensions apart from the narrow spacing 12-2 of the same dimension, so that the grinding and mixing ratio of the base material is different. Waste synthetic resin regeneration extrusion apparatus having two mixing zones and ventilation holes, characterized in that it can be set.
제1항에 있어서,
상기 필터 하우징(40)은 본체(40')의 일측에 스크류 하우징과 이송관이 모두 연결된 것을 특징으로 하는 각 2개의 믹싱존과 환기구를 가지는 폐합성수지 재생 압출장치.
According to claim 1,
The filter housing (40) has two mixing zones and a ventilation hole, characterized in that both the screw housing and the transfer pipe are connected to one side of the main body (40').
KR1020210052129A 2021-04-22 2021-04-22 Waste Synthetic Resin Regenerative Extrusion Unit with two Mixing Zone and Vents KR102505591B1 (en)

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