KR20160071864A - Apparatus and method for processing wasted powder coating - Google Patents

Apparatus and method for processing wasted powder coating Download PDF

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KR20160071864A
KR20160071864A KR1020140179581A KR20140179581A KR20160071864A KR 20160071864 A KR20160071864 A KR 20160071864A KR 1020140179581 A KR1020140179581 A KR 1020140179581A KR 20140179581 A KR20140179581 A KR 20140179581A KR 20160071864 A KR20160071864 A KR 20160071864A
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powder coating
coating material
waste powder
waste
shaft portion
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KR1020140179581A
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Korean (ko)
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KR101709270B1 (en
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현재규
김병균
이덕원
소병기
김현주
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주식회사 케이씨씨
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J11/00Recovery or working-up of waste materials
    • C08J11/04Recovery or working-up of waste materials of polymers
    • 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
    • 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
    • B29B7/00Mixing; Kneading
    • B29B7/02Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/141Feedstock
    • Y02P20/143Feedstock the feedstock being recycled material, e.g. plastics
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/52Mechanical processing of waste for the recovery of materials, e.g. crushing, shredding, separation or disassembly
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/62Plastics recycling; Rubber recycling

Abstract

According to the present invention, disclosed are a device for treating waste powder coating material and a method for treating waste powder coating material by using the same. The device for treating waste powder coating material comprises: a filtering unit for collecting waste powder coating material from produced powder coating material, and filtering the waste powder coating material; a dispersing unit connected with the filtering unit, and transferring and dispersing the waste powder coating material filtered by the filtering unit; and a pulverizing unit connected with the dispersing unit, and producing the dispersed waste powder coating material into a solid flake. According to the device for treating waste powder coating material and the method for treating waste powder coating material, waste powder coating material is utilized, so costs spent in wasting waste powder coating material are saved. Also, environmental contamination is reduced, and the productivity of powder coating material is improved.

Description

폐분체도료 처리 장치 및 방법{APPARATUS AND METHOD FOR PROCESSING WASTED POWDER COATING}[0001] APPARATUS AND METHOD FOR PROCESSING WASTED POWDER COATING [0002]

본 발명은 폐분체도료 처리 장치 및 방법에 관한 것으로서, 특히, 폐분체도료 제조과정에서 생성된 미분을 재활용할 수 있도록 처리하는 폐분체도료 처리 장치 및 방법에 관한 것이다.The present invention relates to an apparatus and a method for treating waste powder coating, and more particularly, to a waste powder coating processing apparatus and method for treating waste powder that are produced in the process of manufacturing waste powder coating material so as to be recyclable.

일반적으로 분체도료(powder coating)는 액상도료와 달리 용제를 함유하지 않는 친환경 도료이다. 분체도료는 지난 수십 년간 가전제품, 일반철재류 등의 도장에 광범위하게 적용되어 왔고, 액상도료와 달리 용제에 의한 중독이나 화재위험이 적고, 도장작업이 용이한 장점을 갖기에 그 용도가 점차 확대되고 있다. 또한, 분체도료는 그 종류가 다양하나, 수지의 성분에 따라 에폭시-폴리에스터계 도료, 에폭시계 도료, 폴리에스터계 도료, 아크릴계 도료가 주종을 이룬다. 이때, 분체도료는 조성물에 용제를 포함하지 않기에 분말 형태로 이루어지고, 피도장물에 흡인되어 가열되고 용융됨으로써 도막을 형성한다.In general, powder coating is an environmentally friendly paint that does not contain solvents unlike liquid coatings. Powder coatings have been widely applied to home appliances and general steel products for the past decades. Unlike liquid coatings, powder coatings have been used extensively because they have the advantage of being less poisoning by a solvent, have. In addition, powder coatings vary in their types, but epoxy-polyester coatings, epoxy coatings, polyester-based coatings and acrylic-based coatings are predominant, depending on the resin components. At this time, the powder coating material does not contain a solvent in the composition and is formed in powder form, and is attracted to the object to be coated, heated and melted to form a coating film.

분체도료는 배합 - 혼합 - 분산 - 분쇄 단계를 통해 제조된다. 특히, 분쇄 단계에서 대략 30㎛ 내지 50㎛의 평균 입경을 갖는 분말로 형성된다. 이때, 10㎛ 이하의 입경을 갖는 미분이 3% 내지 5%정도 포함된다. 이러한 미분은 분체도료의 작업성을 저해하기에 분쇄 단계에서 포집되는데, 분쇄 단계에서 포집되는 미분은 폐분체도료라 불린다. 한편, 폐분체도료는 분체도료와 동일한 성분을 가짐에도 불구하고, 10㎛ 이하의 입경을 갖는 미분이기에 재활용하는 데에 어려움이 있어 폐기물로서 처리된다. 이로 인해, 폐분체도료는 처리에 따른 비용을 발생시키고, 폐기물로서 환경오염을 유발한다. 또한, 이러한 페분체도료의 생성은 분체도료 제조과정에서 수율 저하를 의미하기도 한다.Powder coatings are prepared through a compounding-mixing-dispersion-grinding step. In particular, it is formed into a powder having an average particle diameter of about 30 탆 to 50 탆 at the pulverizing step. At this time, 3% to 5% of fine particles having a particle size of 10 mu m or less are contained. These fine powders are collected in the pulverizing step in order to inhibit the workability of the powder coating material, and the fine particles collected in the pulverizing step are called pulverulent powder coatings. On the other hand, although the waste powder coating material has the same components as the powder coating material, it is difficult to recycle because it is a fine powder having a particle size of 10 탆 or less and is treated as waste. As a result, the waste powder coating causes the cost of treatment and causes environmental pollution as waste. In addition, the generation of such a powder coating material may also mean a reduction in yield in the process of powder coating production.

한편, 대한민국 특허출원번호 제10-2009-0084328호(발명의 명칭: 폐분체도료의 재처리 방법, 폐분체도료를 포함하는 재생 분체도료 및 재생 분체도료의 제조방법), 및 대한민국 특허출원번호 제10-2005-0044661호(발명의 명칭: 폐분체도료의 재생시스템) 등을 통해 폐분체도료의 재활용 방안이 개시되고 있으나, 여전히 10㎛ 이하의 입경을 갖는 미분 형태의 폐분체도료를 처리하는 데에는 어려움을 겪고 있다.On the other hand, Korean Patent Application No. 10-2009-0084328 (entitled "Reprocessing method of waste powder coating material, recycled powder coating material including waste powder coating material and method of manufacturing recycled powder coating material)", and Korean Patent Application No. 10-2005-0044661 (the name of the invention: a recycling system for waste powder coating), etc. However, in order to treat a pulverulent powder coating material having a particle size of 10 탆 or less still, I am having difficulties.

본 발명은 분체도료 제조 공정에서 생성된 미분 형태의 폐분체도료를 재활용가능하도록 처리하는 폐분체도료 처리 장치 및 방법을 제공하고자 한다.An object of the present invention is to provide a waste powder coating apparatus and method for treating a powder coating material of a fine powder form produced in a powder coating material manufacturing process so as to be recyclable.

본 발명은 제조된 분체도료로부터 폐분체도료를 포집하고, 상기 폐분체도료를 여과시키는 여과부; 상기 여과부에 연결되어, 상기 여과부에 의해 여과된 폐분체도료를 이송 및 분산시키는 분산부; 및 상기 분산부에 연결되어, 상기 분산된 폐분체도료를 고상 플레이크로 형성하는 분쇄부를 포함하는 것을 특징으로 하는 폐분체도료 처리 장치를 개시한다.The present invention relates to a filtration unit for collecting a waste powder coating material from the powder coating material and filtering the waste powder coating material; A dispersion unit connected to the filtration unit to transfer and disperse the waste powder coating material filtered by the filtration unit; And a crushing part connected to the dispersing part to form the dispersed waste powder coating as a solid flake.

또한, 상기 분산부는, 상기 여과부와 상기 분쇄부 사이에 위치되는 하우징부; 상기 하우징부의 내측에서 상기 폐분체도료의 이송방향을 따라 위치된 샤프트부; 상기 여과부에 인접하면서 상기 샤프트부의 일종단부의 외주면 상에서 나선형으로 형성되고, 상기 여과된 폐분체도료를 가열하면서 이송시키는 스크류부; 및 상기 분쇄부에 인접하면서 상기 스크류부에 연결되고, 상기 샤프트부의 직경방향에 대하여 상호 간에 45° 내지 90°를 형성하도록 상기 샤프트부의 외주면 상에 위치되고, 상기 이송된 폐분체도료를 분산시키는 많아야 3개의 패들부들을 포함하는 것을 특징으로 하는 폐분체도료 처리 장치를 개시한다.The dispersing unit may further include: a housing part positioned between the filtering part and the crushing part; A shaft portion located inside the housing portion along a conveyance direction of the waste powder coating material; A screw portion adjacent to the filtration portion and formed in a spiral shape on an outer peripheral surface of a kind of end portion of the shaft portion and transporting the filtered powder coating material while heating; And at least one of a plurality of pulverized powder coating materials disposed adjacent to the crushing portion and connected to the screw portion and positioned on the outer circumferential surface of the shaft portion to form 45 to 90 degrees with respect to the radial direction of the shaft portion, A waste powder coating apparatus characterized by comprising three paddle portions.

또한, 상기 스크류부의 피치에 대응하는 상기 샤프트부의 외주면 상에는 샤프트홈이 함몰형성되는 것을 특징으로 하는 페분체도료 처리 장치를 개시한다.And a shaft groove is formed on an outer circumferential surface of the shaft portion corresponding to the pitch of the screw portion.

또한, 본 발명은 (a) 제조된 분체도료로부터 폐분체도료가 포집되는 단계; (b) 상기 포집된 폐분체도료가 여과되는 단계; (c) 상기 여과된 폐분체도료가 가열되면서 이송되는 단계; (d) 상기 이송된 폐분체도료가 분산되는 단계; 및 (e) 상기 분산된 폐분체도료가 분쇄되어 고상 플레이트로 생성되는 단계를 포함하는 것을 특징으로 하는 폐분체도료 처리 방법을 개시한다.The present invention also provides a method of manufacturing a powder coating material, comprising the steps of: (a) collecting a powdery powder coating material from the powder coating material; (b) filtering the collected waste powder coating material; (c) the filtered pulverulent powder coating is transferred while being heated; (d) dispersing the transferred waste powder coating material; And (e) grinding the dispersed waste powder coating to produce a solid phase plate.

본 발명에 따른 폐분체도료 처리 장치 및 방법은 여과부, 분산부 및 분쇄부를 포함하여, 분체도료 제조 공정 하에서 생성되는 미분 형태의 폐분체도료를 재활용할 수 있도록 처리한다. 미분형태의 폐분체도료는 여과부에 포집되어 여과되고, 분산부에 의해 가열되어 이송되고 분산되며, 분쇄부에 의해 분쇄되어 고상 플레이크로 형성된다. 고상 플레이크가 분체도료의 제조에 있어 원료로서 이용될 수 있다. 따라서, 본 발명에 따른 폐분체도료 처리 장치 및 방법은 폐분체도료를 재활용하여, 폐분체도료의 폐기에 따른 비용을 절감하고 환경오염을 감소시키며, 분체도료의 생산성을 향상시키는 효과를 갖는다.An apparatus and method for treating waste powder coating according to the present invention includes a filtering section, a dispersing section, and a crushing section, and treats the waste powder paint in powder form, which is produced under the powder coating preparation process, for recycling. The pulverized powder coating in the form of fine particles is collected in a filtration part, filtered, heated and transported and dispersed by a dispersing part, and pulverized by a grinding part to form solid phase flakes. Solid phase flakes can be used as raw materials in the preparation of powder coatings. Therefore, the waste powder coating apparatus and method according to the present invention have the effect of reducing the cost of disposal of the waste powder coating, reducing environmental pollution, and improving the productivity of the powder coating by recycling the waste powder coating.

도 1은 본 발명의 바람직한 실시예에 따른 폐분체도료 처리 장치를 도시하는 도면이다.
도 2는 도 1에 도시된 폐분체도료 처리 장치에서 분산부를 도시하는 단면도이다.
도 3은 도 2에 도시된 분산부에서 샤프트부, 스크류부 및 패들부를 도시하는 사시도들이다.
도 4는 본 발명의 바람직한 실시예에 따른 폐분체도료 처리 방법을 도시하는 흐름도이다.
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a view showing a waste powder coating apparatus according to a preferred embodiment of the present invention. FIG.
Fig. 2 is a cross-sectional view showing a dispersing unit in the waste powder coating apparatus shown in Fig. 1. Fig.
3 is a perspective view showing the shaft portion, the screw portion and the paddle portion in the dispersion portion shown in Fig.
4 is a flow chart showing a method of treating waste powder coating according to a preferred embodiment of the present invention.

이하 본 발명의 바람직한 실시예를 첨부된 도면을 참조하여 상세히 설명하면 다음과 같다. 본 발명을 설명함에 있어서, 관련된 공지기능 혹은 구성에 대한 구체적인 설명이 본 발명의 요지를 불필요하게 흐릴 수 있다고 판단되는 경우 그 상세한 설명을 생략한다.Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the accompanying drawings. In the following description of the present invention, a detailed description of known functions and configurations incorporated herein will be omitted when it may make the subject matter of the present invention rather unclear.

도 1은 본 발명의 바람직한 실시예에 따른 폐분체도료 처리 장치(100)를 도시하는 도면이고, 도 2는 도 1에 도시된 폐분체도료 처리 장치(100)에서 분산부(102)를 도시하는 단면도이며, 도 3은 도 2에 도시된 분산부(102)에서 샤프트부(123), 스크류부(125) 및 패들부(127)를 도시하는 사시도들이다.FIG. 1 is a view showing a waste powder coating apparatus 100 according to a preferred embodiment of the present invention, and FIG. 2 shows a dispersion unit 102 in the waste powder coating apparatus 100 shown in FIG. 1 3 is a perspective view showing the shaft portion 123, the screw portion 125 and the paddle portion 127 in the dispersion portion 102 shown in FIG.

도 1 내지 도 3에 도시된 바와 같이, 본 발명의 바람직한 실시예에 따른 폐분체도료 처리 장치(100)는 여과부(101), 분산부(102) 및 분쇄부(103)를 포함하고, 폐분체도료 처리 장치(100)에 의해 처리된 폐분체도료를 분체도료 제조 공정에 이용할 수 있도록 한다. 여기서, 폐분체도료는 분체도료 제조를 통해 생성된 분체도료 중에서 10㎛ 이하의 입경을 갖는 미분의 형태로 이루어져, 분체도료로서 작용하기에 부적합한 분체도료를 의미한다.1 to 3, a waste powder coating apparatus 100 according to a preferred embodiment of the present invention includes a filtration unit 101, a dispersion unit 102, and a crushing unit 103, The waste powder coating material treated by the powder coating material processing apparatus 100 can be used in the powder coating material manufacturing process. Here, the waste powder coating material refers to a powder coating material which is in the form of a fine powder having a particle size of 10 탆 or less in the powder coating material produced through the preparation of the powder coating material, and is unsuitable for functioning as a powder coating material.

여과부(101)는 제조된 분체도료로부터 폐분체도료를 포집하고, 폐분체도료를 여과시킨다. 이로 인해, 폐분체도료에서 이물질의 제거가 이루어지고, 페분체도료는 혼합된다. 이때, 여과부(101)에서 여과가 이루어지는 여과망은 80메쉬 이상 120메쉬 이하로 이루어진다. 여기서 메쉬는 1인치(25.4㎜)인 정사각형에 포함되는 그물눈의 개수를 의미한다. 구체적으로, 여과망이 80메쉬 이하이면, 여과부(101)에서 이물질의 제거가 제대로 이루어지지 않고, 여과망이 120메쉬 이상이면, 여과부(101)에서 폐분체도료의 여과가 이루어지는 데에 어려움을 겪게 되므로, 수율 및 생산성이 저하된다. 따라서, 여과망은 80메쉬 이상 120메쉬 이하로 이루어지는 것이 바람직하다.The filtration unit 101 collects the waste powder coating material from the powder coating material thus prepared, and filters the waste powder coating material. As a result, foreign matter is removed from the waste powder coating material, and the powder coating material is mixed. At this time, the filter network in which the filtration is performed in the filtration unit 101 is 80 mesh or more and 120 mesh or less. Here, the mesh means the number of meshes included in a square of 1 inch (25.4 mm). Specifically, if the filter net is 80 mesh or less, foreign matter can not be properly removed from the filtration unit 101, and if the filter net is 120 mesh or more, filtration of the waste powder coating is difficult in the filtration unit 101 The yield and productivity are lowered. Therefore, it is preferable that the filter network has 80 mesh or more and 120 mesh or less.

한편, 여과부(101)에는 진동부(111)가 설치된다. 진동부(111)는 여과부(101)에 진동을 가하고, 폐분체도료는 진동하는 여과부(101)에서 원활하게 혼합될 수 있다.On the other hand, the filtering part 101 is provided with a vibrating part 111. The vibrating section 111 applies vibration to the filtration section 101, and the waste powder coating material can be mixed smoothly in the vibrating filtration section 101.

분산부(102)는 여과부(101)에 연결되어, 여과된 폐분체도료를 처리한다. 이때, 여과된 폐분체도료는 분산부(102)에서 가열되어 겔 형태로 이루어져 이송되고, 분산된다. 또한, 분산부(102)는 하우징부(121), 샤프트부(123), 스크류부(125) 및 패들부(127)들을 포함한다. The dispersion unit 102 is connected to the filtration unit 101 to treat the filtered powdery coating material. At this time, the filtered pulverized powder coating material is heated in the dispersing part 102 to be formed into a gel form, and is transported and dispersed. The dispersing portion 102 includes a housing portion 121, a shaft portion 123, a screw portion 125, and a paddle portion 127.

하우징부(121)는 여과부(101)와 분쇄부(103) 사이에 위치되어 이들을 연결하고, 여과부(101)로부터 공급된 폐분체도료의 이송 경로를 제공한다.The housing part 121 is positioned between the filtering part 101 and the crushing part 103 to connect them and provide a transport path of the waste powder coating supplied from the filtration part 101. [

샤프트부(123)는 하우징부(121)에 수용되어 폐분체도료의 이송방향을 따라 위치된다. 즉, 샤프트부(123)는 여과부(101)로부터 분쇄부(103)를 향하여 위치된다.The shaft portion 123 is accommodated in the housing portion 121 and positioned along the transport direction of the waste powder coating material. That is, the shaft portion 123 is positioned toward the crushing portion 103 from the filtration portion 101.

스크류부(125)는 여과부(101)에 인접하면서, 샤프트부(123)의 일종단부 외주면 상에서 나선형으로 형성된다. 여과된 폐분체도료는 스크류부(125)에 의해 이송된다. 이때, 하우징부(121)에서 스크류부(125)에 대응하는 이송공간(A)의 온도는 60℃ 내지 80℃인 것이 바람직하다. 만약 이송공간(A)의 온도가 80℃ 이상이면, 폐분체도료의 겔타임이 짧아진다. 여기서, 겔타임은 점성이 증가하면서 유동성을 상실하여 겔화될 때까지의 소요시간으로서, 이송공간(A)의 온도와 밀접한 연관을 갖게 된다. 구체적으로, 이송공간(A)의 온도가 80℃를 초과하면 폐분체도료의 겔타임이 짧아져 레벨링이 많이 떨어지며, 이로부터 제조된 도료는 기계적인 물성이 저하된다. 반면에 이송공간(A)의 온도가 60℃ 미만이면 겔타임이 길어져 광택에 문제가 발생된다.The screw portion 125 is formed in a spiral shape on the outer peripheral surface of a kind of end portion of the shaft portion 123, adjacent to the filtration portion 101. The filtered powdery paint that has been filtered is conveyed by the screw portion 125. At this time, the temperature of the transfer space A corresponding to the screw part 125 in the housing part 121 is preferably 60 ° C to 80 ° C. If the temperature of the transfer space (A) is 80 DEG C or higher, the gel time of the waste powder coating is shortened. Here, the gel time is closely related to the temperature of the transfer space A as the time required until the gelation is lost due to the loss of fluidity due to an increase in viscosity. Specifically, when the temperature of the transfer space (A) exceeds 80 캜, the gel time of the waste powder coating is shortened and the leveling is greatly reduced, and the mechanical properties of the resulting coating are deteriorated. On the other hand, if the temperature of the transfer space (A) is less than 60 캜, the gel time becomes long and a problem of gloss occurs.

또한, 스크류부(125)의 피치에 대응하는 샤프트부(123)의 외주면 상에는 샤프트홈(123a)이 함몰형성된다. 샤프트홈(123a)은 그 크기가 샤프트부(123)의 기능을 저해하지 않는다면 크게 제한되는 것은 아니지만, 바람직하게는 피치 길이의 25% 내지 45%에 상응하는 깊이를 갖는다. 샤프트홈(123a)은, 샤프트부(123)의 외주면에 형성되지 않는 경우에 비해서, 스크류부(125)의 피치에 삽입되는 폐분체도료의 양을 증가시켜 폐분체도료의 이송 효율을 향상시킬 수 있다. A shaft groove 123a is formed on the outer circumferential surface of the shaft portion 123 corresponding to the pitch of the screw portion 125. The shaft groove 123a preferably has a depth corresponding to 25% to 45% of the pitch length, although it is not particularly limited as long as its size does not hinder the function of the shaft portion 123. [ The shaft groove 123a can increase the amount of waste powder paint to be inserted into the pitch of the screw portion 125 to improve the transfer efficiency of the waste powder paint as compared with the case where the shaft groove 123a is not formed on the outer peripheral surface of the shaft portion 123 have.

구체적으로, 스크류부(125)의 피치는 폐분체도료의 이송량 및 샤프트부(123)의 회전력을 고려하여 적절하게 설정될 수 있다. 패들부(127)들은 분쇄부(103)에 인접하면서 스크류부(125)에 연결되고, 샤프트부(123)의 직경방향에 대하여 상호 간에 45° 내지 90°를 형성하여 샤프트부(123)의 외주면 상에 위치된다. 패들부(127)들은 최대 3개이고, 이송된 폐분체도료를 균일한 상태로 분산시킨다. 패들부(127)들이 3개를 초과할 경우 도료의 마찰력이 증대하여 과분산이 발생되며, 이로 인해 도료의 변질이 발생될 수 있다. 보다 바람직하게는, 패들부(127)들은 2 내지 3개일 수 있으며, 가장 바람직하게는 2개일 수 있다. 반면에, 패들부(127)가 형성되지 않을 경우에는 폐분체도료가 균일한 상태로 분산되지 않으므로, 바람직하지 않다.Specifically, the pitch of the screw portion 125 can be appropriately set in consideration of the amount of the waste powder coating material and the rotational force of the shaft portion 123. The paddle portions 127 are connected to the screw portion 125 adjacent to the crushing portion 103 and form 45 to 90 degrees with respect to the radial direction of the shaft portion 123, Lt; / RTI > The maximum number of paddles 127 is three, and the transferred powder coating material is uniformly dispersed. If the number of the paddles 127 exceeds 3, frictional force of the paint increases, resulting in hyperbranched dispersion, which may result in deterioration of the paint. More preferably, the paddles 127 may be two to three, and most preferably two. On the other hand, when the paddle portion 127 is not formed, the waste powder coating material is not dispersed in a uniform state, which is not preferable.

하우징부(121)에서 패들부(127)들에 대응하는 분산공간(B)의 온도는 80℃ 내지 100℃인 것이 바람직하다. 만약 분산공간(B)의 온도가 상기의 온도 범위를 벗어나면, 폐분체도료의 분산이 저하된다.It is preferable that the temperature of the dispersion space B corresponding to the padding portions 127 in the housing portion 121 is 80 占 폚 to 100 占 폚. If the temperature of the dispersion space (B) is out of the above-mentioned temperature range, the dispersion of the waste powder coating is lowered.

분쇄부(103)는 분산부(102)에 연결되어, 분산된 폐분체도료를 분쇄시켜 고상 플레이크(flake)를 형성한다. 이때, 고상 플레이크는 3㎜ 내지 10㎜의 크기를 갖고, 분체도료의 제조에 있어 원료로서 작용할 수 있다.The crushing unit 103 is connected to the dispersing unit 102 to crush the dispersed waste powder coating material to form a solid flake. At this time, the solid flake has a size of 3 mm to 10 mm and can act as a raw material in the production of the powder coating material.

본 실시예에 따른 폐분체도료 처리 장치(100)는 미분 형태의 분체도료를 상기와 같이 처리하고, 처리된 폐분체도료는 분체도료를 제조하는 데에 투입되어 재활용될 수 있다.The waste powder coating material treatment apparatus 100 according to the present embodiment treats the powder powder coating material in the above-described manner, and the treated waste powder coating material can be recycled for preparing the powder coating material.

도 4는 본 발명의 바람직한 실시예에 따른 폐분체도료 처리 방법을 도시하는 흐름도이다. 도 4에 도시된 본 발명의 바람직한 실시예에 따른 폐분체도료 처리 방법은 앞서 서술된 폐분체도료 처리 장치(100)를 이용하여 설명하고자 한다. 4 is a flow chart showing a method of treating waste powder coating according to a preferred embodiment of the present invention. The waste powder coating method according to a preferred embodiment of the present invention shown in FIG. 4 will be described with reference to the powder coating apparatus 100 described above.

우선, 제조된 분체도료로부터 폐분체도료가 포집되는 단계(S101)가 이루어진다. S101 단계에서 폐분체도료는 여과부(101)에 포집된다. 여기서, 폐분체도료는 분체도료 제조를 통해 생성된 분체도료 중에서 10㎛ 이하의 입경을 갖는 미분의 형태로 이루어져 분체도료로서 작용하기에 부적합한 분체도료를 의미한다. 즉, 도료로서 기능을 할 수 있는 분체도료와 그렇지않은 미분 형태의 폐분체도료의 분리가 이루어진다.First, a step (S101) of collecting the powdery powder coating material from the prepared powdery coating material is performed. In step S101, the waste powder coating material is collected in the filtration unit 101. Here, the waste powder coating material refers to a powder coating material which is in the form of a fine powder having a particle size of 10 탆 or less in powder coating material produced through the preparation of powder coating material, and is unsuitable for serving as a powder coating material. That is, the separation of the powder coating material capable of functioning as a coating and the powder coating material of a non-powder form is performed.

다음으로, 포집된 폐분체도료가 여과되는 단계(S102)가 이루어진다. S102 단계에서 폐분체도료는 여과부(101)를 통해 여과되고, 폐분체도료에 포함된 이물질이 제거된다. 이때, 폐분체도료의 혼합이 이루어지기도 한다.Next, a step (S102) in which the collected waste powder coating material is filtered is performed. In step S102, the waste powder coating is filtered through the filtration unit 101 to remove foreign matter contained in the waste powder coating. At this time, the waste powder coating material may be mixed.

다음으로, 여과된 폐분체도료가 가열되면서 이송되는 단계(S103)가 이루어진다. 또한, S103 단계는 분산부(102)의 스크류부(125)에 의해 이루어진다. 이때, 스크류부(125)에 대응하는 이송구간(A)의 온도는 60℃ 내지 80℃인 것이 바람직하다. 만약 이송공간(A)의 온도가 80℃ 이상이면, 폐분체도료의 겔타임이 짧아진다. 이는 폐분체도료의 변질을 유발하여, 폐분체도료의 재활용에 있어 광택의 손실 등과 같은 품질 저하를 유발한다. 반면에, 만약 이송공간(A)의 온도가 60℃ 이하이면, 폐분체도료의 이송속도가 저하된다. 따라서, 이송공간(A)의 온도는 상기 범위를 만족할 때, S103 단계에서, 폐분체도료는 겔 형태로 이루어지면서 안정적으로 이송된다.Next, step S103 is performed in which the filtered powdery paint is heated and transferred. Step S103 is performed by the screw portion 125 of the dispersing portion 102. [ At this time, the temperature of the transfer section A corresponding to the screw section 125 is preferably 60 占 폚 to 80 占 폚. If the temperature of the transfer space (A) is 80 DEG C or higher, the gel time of the waste powder coating is shortened. This causes deterioration of the waste powder coating, which causes deterioration in quality such as loss of gloss in the recycling of the waste powder coating. On the other hand, if the temperature of the transfer space (A) is 60 DEG C or less, the transfer rate of the waste powder coating material is lowered. Therefore, when the temperature of the transfer space A satisfies the above range, the waste powder coating material is transferred in a stable state in step S103.

다음으로, 이송된 폐분체도료가 분산되는 단계(S104)가 이루어진다. 또한, S104 단계는 분산부(102)의 패들부(127)들에 의해 이루어진다. 이때, 분산공간(B)의 온도는 80℃ 내지 100℃인 것이 바람직하며, 폐분체도료는 패들부(127)들에 의해 원활하게 분산된다.Next, a step S104 of dispersing the transferred waste powder coating material is performed. In addition, the step S104 is performed by the paddle portions 127 of the dispersing portion 102. At this time, the temperature of the dispersion space (B) is preferably 80 to 100 ° C, and the waste powder coating material is smoothly dispersed by the paddle portions 127.

다음으로, 분산된 폐분체도료가 분쇄되어 고상 플레이크로 생성되는 단계(S105)가 이루어진다. S105 단계는 분쇄부(103)에 의해 이루어지고, 고상 플레이크는 3㎜ 내지 10㎜의 크기를 갖고, 분체도료의 제조에 원료로서 재활용될 수 있다.Next, a step (S105) is performed in which the dispersed waste powder coating material is pulverized to be solid flakes. Step S105 is performed by the crushing section 103, and the solid flakes have a size of 3 mm to 10 mm and can be recycled as a raw material in the production of the powder coating material.

한편, 본 실시예에 따른 폐분체도료 처리 장치(100) 및 방법을 통해 처리된 폐분체도료가 분체도료의 제조를 위한 원료로서의 성능을 확인하기 위하여 다음과 같은 실험이 실시되었다.
Meanwhile, in order to confirm the performance of the waste powder coating material treated by the waste powder coating material processing apparatus 100 and the method according to this embodiment as a raw material for the preparation of the powder coating material, the following experiment was conducted.

[실시예 1][Example 1]

배합 - 혼합 - 분산 - 분쇄 공정 중에서, 부산물로 나오는 10 ㎛의 미분인 폐분체도료를 포집한다. 포집된 폐분체도료는 본 발명의 폐분체도료 처리 장치(100)에 의해 이물질이 제거되고, 3개의 패들부들 및 스크류부(피치 사이의 공간 30% 증가) 조합에 의해 특정 온도 조건(이송공간: 70℃, 분산공간: 100℃)에서 분산과정을 거쳐 고상 플레이크를 생성하였다.
In the compounding-mixing-dispersion-grinding process, the waste powder coating is collected as a by-product having a particle size of 10 μm. The collected waste powder coating material is removed by the waste powder coating apparatus 100 of the present invention, and a specific temperature condition (transporting space: air) is obtained by a combination of three paddle portions and a screw portion (space of 30% 70 ° C, dispersion space: 100 ° C) to produce solid flakes.

[실시예 2][Example 2]

상기 실시예 1에서, 패들부들의 개수를 2개로 설정한 것을 제외하고는, 실시예 1과 동일한 방법으로 고상 플레이크를 생성하였다.
In Example 1, solid flakes were produced in the same manner as in Example 1, except that the number of paddle portions was set to two.

[실험예 1][Experimental Example 1]

상기 실시예 1에 따라 제조된 고상 플레이크를 80 중량%로 분체도료 원배합에 투입하여, 통상의 분체도료 제조 공정에 따라 제조된 분체도료를 도막으로 형성하였다.
The solid flakes prepared in Example 1 were put into a powder coating material blend at a ratio of 80% by weight, and a powder coating material prepared by a conventional powder coating process was formed into a coating film.

[실험예 2][Experimental Example 2]

상기 실시예 2에 따라 제조된 고상 플레이크를 80 중량%로 분체도료 원배합에 투입한 것을 제외하고는, 실험예 1과 동일한 방법으로 도막을 제조하였다.
A coating film was prepared in the same manner as in Experimental Example 1, except that the solid flakes prepared in Example 2 were added to the powder coating material blend at 80% by weight.

[참조예 1][Reference Example 1]

비교예는 100중량%의 분체도료 원료를 이용하여 제조된 분체도료를 도막으로 형성하였다.
In the comparative example, a powder coating material prepared by using a powder coating material of 100 wt% was formed into a coating film.

[비교 실험예 1][Comparative Experimental Example 1]

상기 실시예 1에 따라 제조된 고상 플레이크 80 중량%를 분체도료 원배합에 투입하고, 상호 간에 90°를 형성하면서 배치된 4개의 패들부들을 이용한 분산 단계가 이루어지는 것을 제외하고는, 실험예 1과 동일한 방법으로 도막을 제조하였다.
Except that 80 weight% of the solid flakes prepared according to Example 1 were put into the powder coating material blend and a dispersing step using four paddles arranged while forming 90 degrees with each other was performed. A coating film was prepared in the same manner.

[비교 실험예 2][Comparative Experimental Example 2]

상기 실시예 1에 따라 제조된 고상 플레이크 80 중량%를 분체도료 원배합에 투입하고, 상호 간에 90°를 형성하면서 배치된 5개의 패들부들, 샤프트부 외주면 상에 샤프트홈이 형성되지 않은 것을 제외하고는, 실험예 1과 동일한 방법으로 도막을 제조하였다.
Except that the shaft pits were not formed on the outer circumferential surface of the shaft portion, while the paddle portions were placed in the powder coating material blend at a rate of 90 ° with respect to the solid phase flake prepared in Example 1, , A coating film was prepared in the same manner as in Experimental Example 1.

실험에 따른 결과는 다음 표 1과 같다.
The results of the experiment are shown in Table 1 below.

실험예 1Experimental Example 1 실험예 2 Experimental Example 2 참조예 1Reference Example 1 비교실험예 1Comparative Experimental Example 1 비교실험예 2Comparative Experimental Example 2 외관Exterior 양호Good 양호Good 양호Good 외관저하Appearance deterioration 외관저하Appearance deterioration 이물질Foreign matter 없음none 없음none 없음none 없음none 없음none 겔타임Gel time 89초89 seconds 96초96 seconds 95초95 seconds 71초71 seconds 67초67 seconds 충격성Impact 양호Good 양호Good 양호Good 양호Good 양호Good 굴곡성Flexibility 양호Good 양호Good 양호Good 양호Good 양호Good 광택Polish 93%93% 93%93% 93%93% 85%85% 85%85% 내황산성Sulfuric acidity 양호Good 양호Good 양호Good 양호Good 양호Good 내식성Corrosion resistance 2.5㎜2.5 mm 2.1㎜2.1 mm 2.3㎜2.3 mm 2.2㎜2.2 mm 2.2㎜2.2 mm 시간당토출량Discharge rate per hour 100㎏100 kg 110㎏110㎏ 110㎏110㎏ 35㎏35 kg 10㎏10 kg 색차값Color difference value 0.40.4 0.40.4 0.40.4 0.20.2 0.20.2

* 외관: 육안평가. 맑고 선명한 경우 양호.Appearance: Visual evaluation. Good if clear and crisp.

* 티/오물: 육안을 통해 확인가능한 티/오물 개수. 3개 이상인 경우 불량* T / Dirt: Number of tees / dirt that can be confirmed through the naked eye. Defects if more than 3

* 겔타임: 180℃ 핫플레이트로 측정* Gel time: Measured with 180 ° C hot plate

* 충격성: 듀폰식 충격성 테스터로 측정 / 1㎏×30㎝ 이상일 때 양호* Impact: measured by DuPont Impact Tester / Good when it is over 1㎏ × 30㎝

* 굴곡성: BYK-가드너식 3/16인치로 측정 / 균열이 발생하지 않을 때 양호Flexibility: Measured by BYK-Gardner formula 3/16 inch / Good when no crack occurs

* 광택: 60° 반사율* Gloss: 60 ° reflectance

* 내황산성: 5% 황산에 48시간 동안 침적 후 육안 평가 / 외관 변화 없을 때 양호* Sulfuric acidity: Good after immersion in 5% sulfuric acid for 48 hours with no visual changes / appearance change

* 내식성: 5% 염수 500시간 동안 분무. 인산아연피막 전처리 조건* Corrosion resistance: 5% brine spray for 500 hours. Pretreatment conditions of zinc phosphate coating

* 분산조건: ZSK-30 기종, 동일한 조건으로 미분을 플레이크화함(색상/Brown)* Dispersion condition: ZSK-30 model, Flakes the powder with the same condition (Color / Brown)

* 색차: 미놀타 색차계/ 색차의 기준은 최종조색시편을 기준으로함
* Color Difference: Minolta Color Difference / Color Difference standard is based on final color sample.

표 1을 살펴보면, 실험예 1 및 실험예 2는 분체도료 100%인 참조예 1과 거의 유사한 결과를 나타내었고, 특히, 실험예 2의 결과는 분체도료 원료와 상당히 유사한 물성을 나타낸 바, 패들이 2개로 형성될 때가 가장 바람직한 것을 확인할 수 있었다. 즉, 본 발명의 폐분체도료 처리 장치를 이용하여 제조된 폐분체도료를 80중량% 이하로 포함시킨다면, 분체도료로서 이용 가능함이 확인되었다.As shown in Table 1, Experimental Example 1 and Experimental Example 2 showed almost the same results as in Reference Example 1 in which the powder coating material was 100%. Particularly, the results of Experimental Example 2 showed properties similar to those of the powder coating material, It was confirmed that it is most preferable to form the two layers. That is, if the waste powder coating material prepared by using the waste powder coating apparatus of the present invention is contained in an amount of 80 wt% or less, it can be used as a powder coating material.

또한, 비교실험예 1의 결과를 참조하면, 패들부들이 3개를초과할 때 패들부들의 증가로 인해, 과분산에 의한 겔타임의 감소 및 외관저하가 초래될 수 있다는 것을 확인하였다.Also, referring to the results of Comparative Experiment Example 1, it was confirmed that, when the number of paddles exceeds 3, the increase of the paddle portions may cause a reduction in gel time and an appearance degradation due to over dispersion.

또한, 비교실험예 2의 결과를 참조하면, 패들부들이 3개를 초과하고 샤프트홈이 형성되지 않을 경우, 실험예들과 비교하여, 겔타임의 감소 및 외관저하가 초래될 뿐만 아니라, 시간당 토출량이 현저히 줄어 생산성이 저하됨을 확인할 수 있었다.Also, referring to the results of Comparative Experiment Example 2, when the number of paddles exceeds 3 and shaft grooves are not formed, not only the gel time is reduced and appearance is lowered as compared with the experimental examples, And the productivity is decreased.

따라서, 본 실시예에 따른 폐분체도료 처리 장치를 통해 처리되는 폐분체도료는, 패들부들이 최대 3개로 형성되고 샤프트부의 외주면 상에 샤프트홈이 형성된 폐분체도료 처리 장치를 통해서 본 발명에서 소망하는 효과를 발휘할 수 있다. Therefore, the waste powder coating material to be treated through the waste powder coating apparatus according to the present embodiment can be obtained through a waste powder coating apparatus in which a maximum of three paddles are formed and a shaft groove is formed on the outer circumferential surface of the shaft, Effect can be exerted.

이상, 구체적인 실시예에 관해서 설명하였으나, 본 발명의 범위에서 벗어나지 않는 한도 내에서 여러 가지 변형이 가능함은 당해 분야에서 통상의 지식을 가진 자에게 있어서 자명하다 할 것이다. 또한, 특허청구범위의 기재 중 괄호 내의 기재는 기재의 불명료함을 방지하기 위한 것이며, 특허청구범위의 권리범위는 괄호 내의 기재를 모두 포함하여 해석되어야 한다.While the present invention has been described in connection with certain exemplary embodiments, it will be understood by those skilled in the art that various changes may be made without departing from the scope of the present invention. In addition, the description in parentheses in the description of the claims is intended to prevent obscuration of the description, and the scope of the claims of the claims should be construed to include all the items in parentheses.

100: 폐분체도료 처리 장치
101: 여과부
102: 분산부
121: 하우징부
123: 샤프트부
123a: 샤프트홈
125: 스크류부
127: 패들부
103: 분쇄부
100: waste powder coating apparatus
101:
102:
121: housing part
123: shaft portion
123a: shaft home
125: screw part
127: Paddle portion
103: Crushing section

Claims (4)

제조된 분체도료로부터 폐분체도료를 포집하고, 상기 폐분체도료를 여과시키는 여과부;
상기 여과부에 연결되어, 상기 여과부에 의해 여과된 폐분체도료를 이송 및 분산시키는 분산부; 및
상기 분산부에 연결되어, 상기 분산된 폐분체도료를 고상 플레이크로 형성하는 분쇄부를 포함하는 것을 특징으로 하는 폐분체도료 처리 장치.
A filtration unit for collecting the waste powder coating material from the powder coating material and filtering the waste powder coating material;
A dispersion unit connected to the filtration unit to transfer and disperse the waste powder coating material filtered by the filtration unit; And
And a crushing portion connected to the dispersing portion to form the dispersed powdery coating material into solid flakes.
제 1 항에 있어서, 상기 분산부는,
상기 여과부와 상기 분쇄부 사이에 위치되는 하우징부;
상기 하우징부의 내측에서 상기 폐분체도료의 이송방향을 따라 위치된 샤프트부;
상기 여과부에 인접하면서 상기 샤프트부의 일종단부의 외주면 상에서 나선형으로 형성되고, 상기 여과된 폐분체도료를 가열하면서 이송시키는 스크류부; 및
상기 분쇄부에 인접하면서 상기 스크류부에 연결되고, 상기 샤프트부의 직경방향에 대하여 상호 간에 45° 내지 90°를 형성하도록 상기 샤프트부의 외주면 상에 위치되고, 상기 이송된 폐분체도료를 분산시키는 많아야 3개의 패들부들을 포함하는 것을 특징으로 하는 폐분체도료 처리 장치.
The apparatus according to claim 1,
A housing part positioned between the filtration part and the crushing part;
A shaft portion located inside the housing portion along a conveyance direction of the waste powder coating material;
A screw portion adjacent to the filtration portion and formed in a spiral shape on an outer peripheral surface of a kind of end portion of the shaft portion and transporting the filtered powder coating material while heating; And
Wherein the pulverized portion is located on the outer circumferential surface of the shaft portion so as to form an angle of 45 DEG to 90 DEG with respect to the radial direction of the shaft portion adjacent to the grinding portion, Wherein the paddle portion includes paddle portions.
제 2 항에 있어서,
상기 스크류부의 피치에 대응하는 상기 샤프트부의 외주면 상에는 샤프트홈이 함몰형성되는 것을 특징으로 하는 페분체도료 처리 장치.
3. The method of claim 2,
And a shaft groove is formed on an outer circumferential surface of the shaft portion corresponding to the pitch of the screw portion.
(a) 제조된 분체도료로부터 폐분체도료가 포집되는 단계;
(b) 상기 포집된 폐분체도료가 여과되는 단계;
(c) 상기 여과된 폐분체도료가 가열되면서 이송되는 단계;
(d) 상기 이송된 폐분체도료가 분산되는 단계; 및
(e) 상기 분산된 폐분체도료가 분쇄되어 고상 플레이트로 생성되는 단계를 포함하는 것을 특징으로 하는 폐분체도료 처리 방법.
(a) collecting a waste powder coating material from the prepared powder coating material;
(b) filtering the collected waste powder coating material;
(c) the filtered pulverulent powder coating is transferred while being heated;
(d) dispersing the transferred waste powder coating material; And
(e) pulverizing the dispersed waste powder coating to produce a solid phase plate.
KR1020140179581A 2014-12-12 2014-12-12 Apparatus and method for processing wasted powder coating KR101709270B1 (en)

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KR20020018834A (en) * 2000-09-04 2002-03-09 조후동 Reprocessing method and device of powder coatings
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Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20020018834A (en) * 2000-09-04 2002-03-09 조후동 Reprocessing method and device of powder coatings
KR20060122306A (en) * 2005-05-26 2006-11-30 (주)인하기연 Regenerated system for waster power coating

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