JPH0323909A - Separately recovering method for refuse of composite material - Google Patents
Separately recovering method for refuse of composite materialInfo
- Publication number
- JPH0323909A JPH0323909A JP1158514A JP15851489A JPH0323909A JP H0323909 A JPH0323909 A JP H0323909A JP 1158514 A JP1158514 A JP 1158514A JP 15851489 A JP15851489 A JP 15851489A JP H0323909 A JPH0323909 A JP H0323909A
- Authority
- JP
- Japan
- Prior art keywords
- pvc
- urethane
- waste
- matters
- crushed
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 238000000034 method Methods 0.000 title claims description 19
- 239000002131 composite material Substances 0.000 title abstract description 13
- 239000000463 material Substances 0.000 claims abstract description 52
- 239000002245 particle Substances 0.000 claims abstract description 13
- 238000003756 stirring Methods 0.000 claims abstract description 4
- 239000010786 composite waste Substances 0.000 claims description 7
- 238000010298 pulverizing process Methods 0.000 claims description 7
- 238000011084 recovery Methods 0.000 claims description 6
- 238000000926 separation method Methods 0.000 claims description 6
- JOYRKODLDBILNP-UHFFFAOYSA-N Ethyl urethane Chemical compound CCOC(N)=O JOYRKODLDBILNP-UHFFFAOYSA-N 0.000 abstract description 14
- 238000010008 shearing Methods 0.000 abstract description 6
- 238000009775 high-speed stirring Methods 0.000 abstract description 3
- 238000002156 mixing Methods 0.000 abstract description 3
- 238000009966 trimming Methods 0.000 abstract description 3
- 239000006260 foam Substances 0.000 abstract description 2
- 239000000843 powder Substances 0.000 abstract 1
- 239000002699 waste material Substances 0.000 description 27
- 239000004800 polyvinyl chloride Substances 0.000 description 19
- 229920000915 polyvinyl chloride Polymers 0.000 description 19
- 235000019589 hardness Nutrition 0.000 description 9
- 230000005484 gravity Effects 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 230000000704 physical effect Effects 0.000 description 4
- 238000004064 recycling Methods 0.000 description 4
- 239000000470 constituent Substances 0.000 description 3
- 238000000227 grinding Methods 0.000 description 3
- 238000010998 test method Methods 0.000 description 3
- 206010001497 Agitation Diseases 0.000 description 2
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- 238000013019 agitation Methods 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 229920001875 Ebonite Polymers 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 1
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 230000006698 induction Effects 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229920002635 polyurethane Polymers 0.000 description 1
- 239000004814 polyurethane Substances 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 238000007873 sieving Methods 0.000 description 1
- 229920005992 thermoplastic resin Polymers 0.000 description 1
- 229920001187 thermosetting polymer Polymers 0.000 description 1
- 238000010333 wet classification Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
- B03B9/00—General arrangement of separating plant, e.g. flow sheets
- B03B9/06—General arrangement of separating plant, e.g. flow sheets specially adapted for refuse
- B03B9/061—General arrangement of separating plant, e.g. flow sheets specially adapted for refuse the refuse being industrial
-
- 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
-
- 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
Landscapes
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
Abstract
Description
【発明の詳細な説明】
〈産業上の利用分野〉
本発明は、複数の材料が接着した複合材の廃棄物(スク
ラップ、不良品等)から、1種又はそれ以上の材料を分
離回収する方法に関する。[Detailed Description of the Invention] <Industrial Application Field> The present invention provides a method for separating and recovering one or more materials from composite waste (scrap, defective products, etc.) in which multiple materials are bonded together. Regarding.
〈従来の技術〉
最近では資源の有限性、原材料価格の高騰又は公害防止
の観点から、廃棄物の再生利用が一段と強く要請される
ようになってきている。単一の材料からなる廃棄物であ
ればその再生利用は容易である。しかし複数の材料が接
着した複合材につぃては、それを構成する各材料を採算
性よく分離回収することが不可能であることが多く、再
生利用が殆どの場合行なわれていない。<Prior Art> Recently, there has been a strong demand for the recycling of waste from the viewpoints of limited resources, rising prices of raw materials, and prevention of pollution. If waste is made of a single material, it is easy to recycle it. However, in the case of composite materials in which a plurality of materials are bonded together, it is often impossible to separate and recover the constituent materials in a profitable manner, and recycling is not carried out in most cases.
そのような複合材の廃棄物の一例として、ポリウレタン
とPVC (ポリ塩化ビニル)が積層した廃棄物(以下
、ウレタン付着PVc廃棄物という)がある。これは自
動車内装部品等の製造工場で多量に発生するものである
が、通常焼却又は埋立処分されている。しかしウレタン
付着PVc廃棄物を焼却処分すると、PVc中に含まれ
ている塩素が塩化水素となり、それが焼却炉やその付帯
設備を腐食させるので設備の寿命が短くなるうえに公害
問題を引き起こし易い。An example of such composite material waste is waste in which polyurethane and PVC (polyvinyl chloride) are laminated (hereinafter referred to as urethane-adhered PVc waste). A large amount of this is generated in factories manufacturing automobile interior parts, etc., and it is usually incinerated or disposed of in a landfill. However, when urethane-adhered PVc waste is incinerated, the chlorine contained in the PVc turns into hydrogen chloride, which corrodes the incinerator and its auxiliary equipment, shortening the life of the equipment and easily causing pollution problems.
そのため一部でウレタン付着PVc廃棄物の分離回収が
試みられている。その方法はウレタン付着PVC廃棄物
をカッターミル等で破砕することによりPVCからウレ
タンを剥離させ、その破砕集合物を多段の分級装置で分
級ずることにょりPVCとウレタンを分離回収する方法
である。Therefore, some attempts have been made to separate and recover urethane-adhered PVc waste. The method involves crushing urethane-adhered PVC waste with a cutter mill or the like to peel off the urethane from the PVC, and separating and recovering the PVC and urethane by classifying the crushed aggregate using a multi-stage classification device.
く発明が解決しようとする課題〉
上記のウレタン付着PVC廃棄物の分離回収方法には次
のような問題点がある:
■カッターミルによる粉砕はマクロ的にはPVCからウ
レタンを剥離することであるが、ミクロ的にはカッター
によりウレタン付着I) V C廃棄物を純ウレタン片
、幾らかのウレタンが付着したPVC片、及び純PVC
片の3種に切断することであり、PVC層の薄い廃棄物
では前2片の生成が主であるから、回収されたPVCに
はその物性低下の主因となるウレタンの混入が避けられ
なり\:■カッターミルによる粉砕ではウレタンとPV
Cがほぼ同等の大きさで粉砕されるため、フルイによる
分級が行なえず、比重差による分級が必要となるが、そ
の場合、気流中での飛散距離の差を利用する簡便な乾式
分級方法では各粉砕片がどの方向を向くかで受ける風力
が左右されるのでウレタンとPVCを十分に分級できず
、湿式分級方法では操作が非常に面倒となる。Problems to be Solved by the Invention> The above method for separating and recovering urethane-adhered PVC waste has the following problems: ■Crushing with a cutter mill macroscopically means peeling off urethane from PVC. However, microscopically, urethane is attached using a cutter.
The method is to cut the PVC into three types of pieces, and since the first two pieces are mainly produced in waste with a thin PVC layer, it is possible to avoid contamination of the recovered PVC with urethane, which is the main cause of deterioration of its physical properties. : ■Urethane and PV are crushed by cutter mill.
Since the C particles are crushed to approximately the same size, they cannot be classified using a sieve, and classification based on the difference in specific gravity is required. Since the wind force received depends on which direction each crushed piece faces, urethane and PVC cannot be adequately classified, and the wet classification method is very troublesome to operate.
以上のように、複数の異なる材料が接着した複合材から
分離回収された材料は、一般的に不純物を含むために新
品の材料に比較して物性的に劣るという問題があり、一
方高純度に分離回収しJ:つとすれば極めて低収率で企
業の採算ベースに乗りにくいという問題がある。これら
の問題が複合材廃棄物の分離回収・再生利用を困難にし
ている。As mentioned above, materials separated and recovered from composite materials made by bonding multiple different materials generally contain impurities and therefore have inferior physical properties compared to new materials. The problem with separation and recovery is that the yield is extremely low, making it difficult for companies to make a profit. These problems make it difficult to separate, collect, and recycle composite waste.
本発明は上記諸問題を解決する目的でなされたものであ
り、その解決しようとする課題は、複数の材料が接着し
た複合材の廃棄物から、その構成材料を簡便なる手段を
以って高純度且っ高収率に分離回収する方法を提供する
ことである。The present invention was made for the purpose of solving the above-mentioned problems, and the problem to be solved is to increase the constituent materials of waste composite materials made of multiple materials by simple means. It is an object of the present invention to provide a method for separating and recovering with high purity and high yield.
く課題を解決するための手段〉
上記課題を解決できる本発明の複合材廃棄物の分離回収
方法は、硬さの異なる複数の材料が接着した複合材の廃
棄物を粗粉砕し、次いでそれを高速撹拌機で撹拌するこ
とにより各材料毎に異なる平均粒度に粉砕した後、分級
することを特徴とする。Means for Solving the Problems> The method for separating and recovering composite material waste of the present invention capable of solving the above problems coarsely crushes composite material waste in which a plurality of materials with different hardnesses are bonded together, and then crushes it. It is characterized by pulverizing each material to a different average particle size by stirring with a high-speed stirrer, and then classifying it.
本発明方法において、廃棄物はその各材料の硬さが互い
に異なる必要があり、ウレタン付着P■Cのように硬さ
の差が大きいほど良好に分離回収できるが、通常複合材
の廃棄物は互いに硬さの異なる材料でできているから、
本発明方法は殆どの廃棄物に対して適用できる。なお゜
゜複数の材料が接着した複合材゜゜というのは、その各
材料が相互に溶融したり、均一に分散したりしていない
材料、例えば各材料が積層した又は組み合わさった材料
を意味する。複合材の構成材料としては熱可塑性樹脂、
熱硬化性樹脂、軟質及び硬質ゴム等が挙げられる。In the method of the present invention, each material of the waste must have a different hardness, and the greater the difference in hardness, such as urethane-adhered P■C, the better the separation and recovery can be made. Because they are made of materials with different hardnesses,
The method of the invention can be applied to most wastes. Note that a composite material in which multiple materials are adhered refers to a material in which the materials are not mutually fused or uniformly dispersed, for example, a material in which each material is laminated or combined. The constituent materials of the composite material are thermoplastic resin,
Examples include thermosetting resins, soft and hard rubbers, and the like.
本発明方法はいわば、廃棄物を粗粉砕する第l工程、高
速撹拌機で粉砕する第2工程及び粉砕集合物を分級ずる
第3工程からなっている。以下各工程ごとに説明する。The method of the present invention, so to speak, consists of a first step in which the waste is coarsely pulverized, a second step in which the waste is pulverized with a high-speed stirrer, and a third step in which the pulverized material is classified. Each step will be explained below.
第1工程での粗粉砕は、工場等から発生する廃棄物がト
リミング屑のように細長いものであるから、第2工程で
の作業性を向上させるために行なうものである。よって
粗粉砕といえどもなるべく細かくした方がよいが、細か
くするほど粉砕コス1・がアップし、再生利用のメリッ
トが無くなる。The coarse pulverization in the first step is carried out to improve workability in the second step, since the waste generated from factories and the like is elongated like trimming waste. Therefore, even though it is coarsely ground, it is better to make it as fine as possible, but the finer the grinding, the higher the grinding cost 1.0 and the benefit of recycling is lost.
方、大きく粗粉砕するほど次工程での作業性が悪化する
。そのため第1工程の粗粉砕工程では適当な破砕機もし
くは切断機等を用いて、外寸約20mm〜50mm程度
の塊状物に粗粉砕するのが好ましい。On the other hand, the larger the grinding, the worse the workability in the next process. Therefore, in the first step of coarse pulverization, it is preferable to use a suitable crusher or cutter to coarsely crush the material into lumps having an outer size of approximately 20 mm to 50 mm.
第2工程はいわば高速撹拌機による廃棄物の粉砕工程で
ある。従来のカッターミルによる粉砕は複合材の各材料
とも同程度に粉砕しているのに対して、本発明において
は材料毎に異なる平均粒度に即ち各材料が互いに離れた
粒度分布を持つこととなるように粉砕する。The second step is, so to speak, a step of crushing the waste using a high-speed agitator. In conventional pulverization using a cutter mill, each material of a composite material is pulverized to the same degree, whereas in the present invention, each material has a different average particle size, that is, each material has a particle size distribution that is separated from each other. Shatter it like this.
従来、撹拌機は2種以上の材料を均一に混合するのに利
用されていたのに対して、本発明では2種以上の材料を
分離するのに利用するため、従来とは全く正反対の作用
を働かせることにな−る。またその効果として上記の選
択的粉砕が可能となる。Conventionally, a stirrer was used to uniformly mix two or more types of materials, but in the present invention, it is used to separate two or more types of materials, so it has a completely opposite effect to the conventional one. It will make you work. Moreover, as an effect, the above-mentioned selective pulverization becomes possible.
高速撹拌機の回転数、回転羽根形状、撹拌時間、温度等
の条件は処理する複合材廃棄物の各材料が異なる粒度で
粉砕されるように選択すればよい。Conditions such as the rotational speed of the high-speed stirrer, the shape of the rotary blades, the stirring time, and the temperature may be selected so that each material of the composite waste to be treated is pulverized to a different particle size.
第3工程では、第2工程で得られた粉砕集合体を適当に
分級ずるが、粒度差を利用してフルイ分けずるのが簡便
であり、傾斜式、振動式、回転式等のフルイ分け機で十
分である。もし各材料にかなりの比重差がある場合には
従来通り比重を利用して分離するこどもできる。In the third step, the pulverized aggregate obtained in the second step is appropriately classified, and it is convenient to use a sieve sorter using the particle size difference. is sufficient. If there is a considerable difference in specific gravity between the materials, they can be separated using the specific gravity as usual.
くイ乍用〉
硬さの異なる材料が接着した複合材の廃棄物を高速撹拌
機で撹拌すると、廃棄物は高速で回転する撹拌羽根から
剪断力を受ける。それに対ずる応力は硬さの異なる材料
毎に異なることから、一材料のみが粉砕されるか又は各
材料が離れた粒度分布を持つように粉砕される。粉砕集
合体を粒度の揃ったいくつかの級別に分けると各材料の
単離されたものが得られる。When a high-speed agitator is used to agitate composite waste consisting of materials of different hardness bonded together, the waste receives shearing force from the agitation blades rotating at high speed. Since the corresponding stress differs for materials of different hardness, either only one material is pulverized or each material is pulverized so that it has a separate particle size distribution. By dividing the crushed aggregate into several classes with uniform particle sizes, isolated materials of each material can be obtained.
〈実施例〉
自動車用インストルメントパネルパッド(内層材:軟質
ウレタンフォーム、表皮材:PVC)の製造工程で生じ
るトリミング屑(約140X 50cmの枠形、周囲肉
部の幅10〜15cm、同厚さ10〜l5mm)を入手
し、外寸30mm程度の大きさに粗粉砕した。この粉砕
は通常の一軸式のカッターミルを利用し、φ30のカッ
タースクリーンを通過した粗粉砕物を集め、それを次ぎ
のように高速撹拌処理した。<Example> Trimming waste generated in the manufacturing process of an automobile instrument panel pad (inner layer material: soft urethane foam, outer layer material: PVC) (frame shape of approximately 140 x 50 cm, width of surrounding flesh part 10 to 15 cm, same thickness) 10 to 15 mm) was obtained and coarsely ground to an outer size of about 30 mm. This pulverization was carried out using an ordinary single-shaft cutter mill, and the coarsely pulverized material that had passed through a φ30 cutter screen was collected and subjected to high-speed agitation treatment as follows.
ここで使用する高速撹拌機は、三井三池化工機■製の三
井ヘンシェルミキサーFMl50Jであり、図に示すよ
うな構造をしている。混合槽1の容量は150℃であり
、幣度調節できるジャケット2を備えている。排出弁3
の開閉はエアシリンダ4で行なわれる。上羽根5及び下
羽根6は三相誘導電動機7により回転する。図中の8は
ベル1〜が掛け渡された各Vプーりを表わしている。The high-speed stirrer used here is a Mitsui Henschel mixer FM150J manufactured by Mitsui Miike Kakoki ■, and has a structure as shown in the figure. The mixing tank 1 has a capacity of 150° C. and is equipped with a jacket 2 that allows temperature adjustment. Discharge valve 3
Opening and closing is performed by an air cylinder 4. The upper blade 5 and the lower blade 6 are rotated by a three-phase induction motor 7. 8 in the figure represents each V-pulley around which bells 1 to 1 are stretched.
エアー抜き9及びデフレクタioが取り付けられている
蓋l1を開け、ウレタン付着Pvc廃棄物の粗粉砕物を
投入し蓋l1を閉めてから高速撹拌機を作動させると、
混合槽1内の処理物は下羽根6によって上方向の回転力
を与えられ流動し、上羽根5によって強力な剪断カを受
ける。この剪断カによって極めて短時間でウレタンがP
Vcから剥脱されると共に微粉砕される。PVCはほぼ
粗粉砕時の寸法のままである。Open the lid l1 to which the air vent 9 and deflector io are attached, put in the coarsely ground urethane-adhered PVC waste, close the lid l1, and then operate the high-speed agitator.
The material to be treated in the mixing tank 1 is given an upward rotational force by the lower blade 6 and flows, and is subjected to a strong shearing force by the upper blade 5. This shearing force converts urethane into P in an extremely short time.
It is exfoliated from Vc and pulverized. PVC remains approximately at the same size as when it was coarsely ground.
この処理では室温常圧下、上記高速撹拌機を7000r
pmで5分間回転させた。取り出した処理物を次いで8
メッシュのフルイによって粒径1〜2mmの粉末状ウレ
タンと外寸30mm程度のシート片状PVCを分離した
。こうして回収されたPVCは理論回収率の約95%で
あった。In this treatment, the high-speed stirrer was heated at 7000 rpm at room temperature and normal pressure.
pm for 5 minutes. The processed material taken out is then
Powdered urethane with a particle size of 1 to 2 mm and sheet piece PVC with an outer dimension of about 30 mm were separated using a mesh sieve. The PVC thus recovered had a theoretical recovery rate of about 95%.
上記の様に分離回収されたPVCを2本ロール機にて1
5分間練ることによって試験片を作り、比重、硬さ、引
張強さ、伸び、及び引裂強さについて調べた。なお比重
はJIS−K−7112試験法6.2水中置換法によっ
て測定し、硬さはJIS−K−6031試験法:スプリ
ング硬度(20℃)法で測定した。また引張強さ、伸び
及び引裂強さはいづれもJIS−K6301試験法に基
づいて測定した。The PVC separated and recovered as described above is processed into 1 roll using a 2-roll machine.
Test specimens were prepared by kneading for 5 minutes and examined for specific gravity, hardness, tensile strength, elongation, and tear strength. The specific gravity was measured by JIS-K-7112 test method 6.2 submersion method, and the hardness was measured by JIS-K-6031 test method: Spring hardness (20° C.) method. Moreover, tensile strength, elongation, and tear strength were all measured based on the JIS-K6301 test method.
得られた試験結果を下記表に示す。対照試験として従来
方法により分離回収されたpvc,新品のPVC及び未
処理の廃棄物について行なわれた試験の結果も示す。The test results obtained are shown in the table below. As a control test, the results of tests conducted on PVC separated and recovered by conventional methods, new PVC, and untreated waste are also shown.
この結果から従来方法よりも本発明方法で分離回収され
たPVcの方が再生利用に適する物性を備えていること
が分かる。This result shows that the PVc separated and recovered by the method of the present invention has physical properties more suitable for recycling than the conventional method.
上記のように回収されたPVcは単体でPVcシー!〜
として利用したり、炭酸カルシウム等を加えて防振シー
1・等として利用できる。また回収されたウレタンは微
粉化しているため高付加価値製品として幅広く利用でき
る。その利用先としては、サンバイザー基材、クッショ
ン材等がある。The PVc collected as described above can be used alone as PVc Sea! ~
It can be used as a vibration-proof sheet 1, etc. by adding calcium carbonate, etc. In addition, since the recovered urethane is pulverized, it can be widely used as a high value-added product. Its uses include sun visor base materials, cushion materials, etc.
9
{ 0
この実施例では2層構造の廃棄物を用いたが、3層以上
の廃棄物でも本実施例と同様にあるいは高速撹拌とフル
イ分けを繰り返して材料の分離回収を行なえることは今
までの説明から容易に理解されよう。9 { 0 In this example, waste with a two-layer structure was used, but it is now known that waste with three or more layers can be separated and recovered in the same way as in this example, or by repeating high-speed stirring and sieving. This will be easily understood from the explanation given above.
〈発明の効果〉
本発明の複合材廃棄物の分離回収方法は以下のような効
果を奏する。<Effects of the Invention> The method for separating and recovering composite material waste of the present invention has the following effects.
まず高速撹拌機の回転羽根により複合材廃棄物に剪断力
を与えて各材料をほぼ完全に分離できるので回収率が一
段と向上し、省資源に寄与できる。First, the rotating blades of the high-speed stirrer apply shearing force to the composite waste, allowing almost complete separation of each material, further improving the recovery rate and contributing to resource conservation.
また上記のほぼ完全な分離によって、回収された材料の
純度が高まる。このことは物性的に新品材料に尚更近い
ものが得られることを意味しており、再利用範囲の拡大
を図ることができる。The nearly complete separation also increases the purity of the recovered material. This means that it is possible to obtain materials that are even closer to new materials in terms of physical properties, and the range of reuse can be expanded.
そのうえ各材料を互いに粒度の異なる粉砕物として回収
できるため、分級方法が容易であり、フルイでも十分分
級できる。したがって分離回収費の低コスト化を実現で
きる。Furthermore, since each material can be recovered as pulverized products with different particle sizes, the classification method is easy, and even a sieve can be used for sufficient classification. Therefore, it is possible to reduce the cost of separation and recovery.
図は本発明方法の一実施例で使用された高速撹拌機を示
す概要図である。The figure is a schematic diagram showing a high-speed stirrer used in one embodiment of the method of the present invention.
Claims (1)
粉砕し、次いでそれを高速撹拌機で撹拌することにより
各材料毎に異なる平均粒度に粉砕した後、分級すること
を特徴とする複合材廃棄物の分離回収方法。It is characterized by coarsely pulverizing composite waste made up of multiple materials of different hardness bonded together, and then stirring it with a high-speed stirrer to crush each material to a different average particle size, and then classifying it. Separation and recovery method for composite waste.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15851489A JP2649419B2 (en) | 1989-06-21 | 1989-06-21 | Separation and recovery method of composite waste |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15851489A JP2649419B2 (en) | 1989-06-21 | 1989-06-21 | Separation and recovery method of composite waste |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0323909A true JPH0323909A (en) | 1991-01-31 |
JP2649419B2 JP2649419B2 (en) | 1997-09-03 |
Family
ID=15673402
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP15851489A Expired - Fee Related JP2649419B2 (en) | 1989-06-21 | 1989-06-21 | Separation and recovery method of composite waste |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2649419B2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE4216638C1 (en) * | 1992-05-20 | 1993-09-16 | Daimler-Benz Aktiengesellschaft, 70567 Stuttgart, De | |
JP2011110452A (en) * | 2009-11-24 | 2011-06-09 | Calsonic Kansei Corp | Apparatus for pulverizing/separating laminated resin |
-
1989
- 1989-06-21 JP JP15851489A patent/JP2649419B2/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE4216638C1 (en) * | 1992-05-20 | 1993-09-16 | Daimler-Benz Aktiengesellschaft, 70567 Stuttgart, De | |
FR2691381A1 (en) * | 1992-05-20 | 1993-11-26 | Daimler Benz Ag | Method for dissociating and separating into categories the different plastics of composite parts to be recycled. |
US5297741A (en) * | 1992-05-20 | 1994-03-29 | Daimler-Benz Ag | Process for disintegration and pure-sorted separation of recyclable different plastics of composite structural parts |
JP2011110452A (en) * | 2009-11-24 | 2011-06-09 | Calsonic Kansei Corp | Apparatus for pulverizing/separating laminated resin |
Also Published As
Publication number | Publication date |
---|---|
JP2649419B2 (en) | 1997-09-03 |
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