[go: up one dir, main page]

JP3711471B1 - Sorter using flowing water class and settling velocity - Google Patents

Sorter using flowing water class and settling velocity Download PDF

Info

Publication number
JP3711471B1
JP3711471B1 JP2004351955A JP2004351955A JP3711471B1 JP 3711471 B1 JP3711471 B1 JP 3711471B1 JP 2004351955 A JP2004351955 A JP 2004351955A JP 2004351955 A JP2004351955 A JP 2004351955A JP 3711471 B1 JP3711471 B1 JP 3711471B1
Authority
JP
Japan
Prior art keywords
sorting
air
pulsation
sorter
sorting tank
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.)
Expired - Fee Related
Application number
JP2004351955A
Other languages
Japanese (ja)
Other versions
JP2006130490A (en
Inventor
猛 大阪
道紀 菅原
Original Assignee
株式会社イーエムエス
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 株式会社イーエムエス filed Critical 株式会社イーエムエス
Priority to JP2004351955A priority Critical patent/JP3711471B1/en
Application granted granted Critical
Publication of JP3711471B1 publication Critical patent/JP3711471B1/en
Publication of JP2006130490A publication Critical patent/JP2006130490A/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Classifications

    • 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

Landscapes

  • Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)

Abstract

【課題】磁性体金属除去後の破砕業廃棄物の均質な有価物の提供をすると共に、破砕業廃棄物の混在比率を安定させ選別槽に過大な負荷をかけない搬送攪拌手段と、自動化制御によって処理能力を向上させるために好適な、流水分級と沈降速度を利用した選別機を提供する。
【解決手段】選別槽12にフロート1が上下動する脈動検知手段6を吊設し、前記選別槽12内の液体の脈動振幅及び脈動周期を前記脈動検知手段6の情報によって空気バルブ部13で空気量と流水調整バルブ部20で液体の供給量を制御し、破砕産業廃棄物を攪拌と搬送する搬送攪拌手段36で前記選別槽12に投入する破砕産業廃棄物の投入量を制御することを特徴とする。
【選択図】 図2
[PROBLEMS] To provide a uniform and valuable material for crushing waste after removing magnetic metal, to stabilize the mixing ratio of crushing waste and to prevent excessive load on the sorting tank, and to perform automated control. By the above, a sorter using a flowing water class and a sedimentation speed suitable for improving the processing capacity is provided.
SOLUTION: A pulsation detecting means 6 in which a float 1 moves up and down is suspended in a sorting tank 12, and the pulsation amplitude and pulsation period of the liquid in the sorting tank 12 are determined by an air valve unit 13 according to information of the pulsation detecting means 6. The amount of air and flowing water adjustment valve unit 20 controls the amount of liquid supplied, and the amount of crushing industrial waste introduced into the sorting tank 12 is controlled by the transport agitating means 36 for agitating and conveying the crushing industrial waste. Features.
[Selection] Figure 2

Description

本発明は、磁性体金属除去後の破砕産業廃棄物の流水分級と沈降速度を利用した空気動水選別機に係るものであって、均質な固体有価物を提供すると共に、自動化制御によって円滑経済的に可動させるために好適な、流水分級と沈降速度を利用した選別機に関するものである。  The present invention relates to an air dynamic water sorter that uses the flowing water class and settling speed of crushed industrial waste after magnetic metal removal, and provides homogeneous solid valuables and smooth economy through automation control. The present invention relates to a sorter that uses a flowing water class and a sedimentation speed, which is suitable for moving the water.

従より、分離処理技術において空気動水選別機は、選炭や選鉱するための比重選別の技術であった。近年、空気動水選別は、石炭や鉱石に代わって破砕産業廃棄物を処理対象とする環境化学技術の分野からも見直されている。環境負荷の少ない持続可能な経済社会の必須の課題として、液体を利用する破砕産業廃棄物の処理選別機は、低コスト低負荷の分離処理手段であり、資源の再利用及び環境問題にも寄与出来る技術である。  Therefore, in the separation treatment technology, the air / water sorter has been a specific gravity sorting technology for coal preparation and mineral processing. In recent years, air and water sorting has been reconsidered from the field of environmental chemical technology for treating crushed industrial waste instead of coal and ore. As an indispensable issue for a sustainable economic society with low environmental impact, crushing industrial waste processing and sorting machine using liquid is a low-cost and low-load separation processing means, contributing to resource reuse and environmental problems. It is a technology that can be done.

しかしながら、石炭や鉱石と違い、破砕産業廃棄物は、廃車両の磁性体金属を除去した固体破砕産業廃棄物でも、様々な物品や素材が混在する複合廃物である。これら複合廃物を有効なリサイクル原料に水選別するにあたっては、「硬質浮遊物」「軟質浮遊物」「中間浮遊物」「網下落下物」が混在し、選別素材としては、ポリウレタン(以下「ウレタン」と称する)、ポリプロピレン(以下「PP」と称する)、ポリエチレン(以下「PE」と称する)、ポリスチレン(以下「PS」と称する)、アクリルニトリルブタジエンスチレン樹脂(以下「ABS」と称する)、ポリ塩化ビニール(以下「塩ビ」と称する)、「木材」「ゴム類」「石」「ガラス」「基板屑」「塗装膜」「繊維屑」「銅線屑」「ステンレス」「アルミニウム」等さまざまな素材が混在している。これら複合廃物の混在比率は不定であり逐次変化するものである。  However, unlike coal and ore, crushing industrial waste is a solid waste that is a mixture of various articles and materials, even a solid crushing industrial waste from which the magnetic metal of a scrap vehicle has been removed. When sorting these composite wastes into effective recycled materials, there are a mixture of “hard floats”, “soft floats”, “intermediate floats” and “falling nets”. ), Polypropylene (hereinafter referred to as “PP”), polyethylene (hereinafter referred to as “PE”), polystyrene (hereinafter referred to as “PS”), acrylonitrile butadiene styrene resin (hereinafter referred to as “ABS”), poly Various types such as vinyl chloride (hereinafter referred to as “PVC”), “wood”, “rubbers”, “stone”, “glass”, “substrate waste”, “painted film”, “fiber waste”, “copper wire waste”, “stainless steel”, “aluminum”, etc. The material is mixed. The mixing ratio of these composite wastes is indefinite and changes sequentially.

不定で逐次変化する様々な素材の複合廃物の水選別では、目的とする素材までさらに選別槽で選別を繰り返す必要があり、選別槽の大きさや、形状、処理能力が異なる選別槽も必要となる。加えて、処理能力を効率良くするためには、複合廃物の投入量、選別槽水への処理溶液の流水量及び気室の空気入排気量を各選別槽に逐次調整する必要があるため、選炭や選鉱の分離処理技術を使っても実現できなかった。  In the water sorting of complex wastes of various materials that change indefinitely and sequentially, it is necessary to repeat sorting in the sorting tank up to the target material, and sorting tanks with different sizes, shapes, and processing capabilities are also required. . In addition, in order to improve the processing capacity efficiently, it is necessary to sequentially adjust the input amount of composite waste, the flow amount of the treatment solution to the sorting tank water, and the air intake and exhaust amount of the air chamber to each sorting tank. It could not be realized by using separation and separation technologies for coal preparation and mineral processing.

実全昭63−039440号公報では、ダイヤフラム式のジグ選鉱機でダイヤフラムの衝動数をインバータにより調節可能とし、補給水バルブと精鉱排出バルブを電気的に連動したものが開示されているが、選別の脈動の検知手段には言及していない。
実全昭63−098735号公報では、固定網を斜設したダイヤフラムジグ槽の固定網式ジグ選別機で、フロートを垂設した比重変化面検出装置を設置し掻出羽根の回転速度を制御するもだが、給水や鉱石の投入を可動制御するものではない。
特開平01−164456号公報においては、鉱物、家庭用品あるいは自動車等の各種破砕物を脈動比重選別する方法が開示されているが、具体的な制御手段については、触れられていないため、特に家庭用品自動車等各種破砕物の脈動比重選別は難しい。
特開2003−38981号公報では、排出物の組成を検知する検知手段が開示され、排出物を撮像の色画像抽出装置によって、排出手段を駆動制御するものが掲載されているが、選別槽についての脈動を制御するものではない。
特開2004−58032号公報では、シュレッダーダストからプラスチック類、金属類を分類するため湿式による比重選別機で、気泡を間欠的に排出させる脈動バブリング槽による分別が開示されているが、制御については説明がされていない。
In Japanese Utility Model Publication No. 63-039440, a diaphragm-type jig beneficiation machine is disclosed in which the number of impulses of the diaphragm can be adjusted by an inverter, and a makeup water valve and a concentrate discharge valve are electrically linked. No reference is made to means for detecting the pulsation of sorting.
In Japanese Utility Model Publication No. 63-098735, a fixed net type jig sorter for a diaphragm jig tank in which a fixed net is obliquely installed, a specific gravity change surface detection device in which a float is suspended is installed to control the rotation speed of the scraping blade. However, it does not control the water supply or the input of ore.
Japanese Patent Application Laid-Open No. 01-164456 discloses a method for selecting pulsation specific gravity of various crushed materials such as minerals, household goods, and automobiles, but since specific control means are not mentioned, it is particularly useful for households. It is difficult to select pulsation specific gravity of various crushed materials such as automobiles.
Japanese Patent Laid-Open No. 2003-38981 discloses detection means for detecting the composition of the discharged matter, and discloses a means for driving and controlling the discharging means by a color image extraction device for imaging the discharged matter. It does not control pulsation.
JP 2004-58032 A discloses a pulsating bubbling tank in which bubbles are intermittently discharged by a specific gravity sorter using a wet method for classifying plastics and metals from shredder dust. There is no explanation.

以上のことから、破砕産業廃棄物である複合廃物の逐次変化混在する投入に対し、選別槽の大きさや、形状、処理能力がそれぞれ異なる個別の選別槽内の脈動を即応可能な検知手段で、気室の空気入排気量の制御と処理溶液流水量の制御、複合廃物の投入量の制御による流水分級と沈降速度を利用した選別機については、その実現は極めて困難であった。  From the above, it is a detection means that can immediately respond to pulsations in individual sorting tanks with different sizes, shapes, and processing capacities for sorting tanks, with respect to the mixed changes of mixed waste that is crushing industrial waste, It has been extremely difficult to realize a sorter that uses the flowing water class and settling velocity by controlling the air intake / exhaust volume of the air chamber, the flow rate of the treatment solution flow, and the input volume of the composite waste.

実用新案文献1Utility model document 1

実全昭63−039440号公報  Japanese Utility Model Publication No. 63-039440

実用新案文献2Utility model document 2

実全昭63−098735号公報 特開平01−164456号公報 特開2003−38981号公報 Japanese Utility Model Publication No. 63-098735 Japanese Patent Laid-Open No. 01-164456 JP 2003-38981 A

本発明は、前述の従来技術の問題点を解決し、磁性体金属除去後の破砕業廃棄物の均質な固体有価物を提供すると共に、さまざまな素材が混在する複合廃物の破砕産業廃棄物の混在比率を安定させ、選別槽に過大な負荷をかけない搬送攪拌手段を可能とし、自動化制御によって処理能力を経済的に可動させるために好適な、流水分級と沈降速度を利用した選別機を提供することを課題とする。  The present invention solves the above-mentioned problems of the prior art, provides a homogenous solid valuable material of crushing waste after removal of magnetic metal, and also provides a composite waste crushing industrial waste mixed with various materials. Providing a sorter that uses flowing water class and settling velocity, which is suitable for stabilizing the mixing ratio, making it possible to transport and agitate the sorting tank without overloading, and making the processing capacity economically movable through automated control. The task is to do.

本発明に係る流水分級と沈降速度を利用した選別機の特徴は、磁性体金属除去後の破砕産業廃棄物を比重分離・選別する空気動水選別機において、気室を有する選別槽にフロートが上下動する脈動検知手段を吊設し、前記選別槽内には上下で仕切るスクリーン部を設け、前記気室に空気入排気量を調整する空気バルブ部を設け、前記選別槽内の液体の脈動振幅及び脈動周期を前記脈動検知手段からの情報によって前記気室の空気量を空気バルブ部で制御することができる点である。  The characteristics of the sorting machine using the flowing water class and settling velocity according to the present invention is that the float is placed in the sorting tank having an air chamber in the air dynamic water sorter that separates and sorts the crushed industrial waste after the magnetic metal removal. A pulsation detecting means that moves up and down is suspended, a screen part that is divided into upper and lower parts is provided in the sorting tank, an air valve part that adjusts an air intake / exhaust amount is provided in the air chamber, and a pulsation of liquid in the sorting tank is provided. The air valve unit can control the air amount of the air chamber based on the information from the pulsation detecting means for the amplitude and the pulsation cycle.

また、本発明において、前記選別槽に液体を供給するための液体供給口を設け、前記液体供給口に流水調整バルブ部を設け、前記脈動検知手段からの情報によって液体の供給量を流水調整バルブ部で制御することができる点である。  Further, in the present invention, a liquid supply port for supplying a liquid to the sorting tank is provided, a water flow adjustment valve unit is provided in the liquid supply port, and a liquid supply amount is controlled according to information from the pulsation detecting means. It is a point which can be controlled by the unit.

あるいは、本発明において、前記脈動検知手段は、複数の前記選別槽内に個別に設けられ、前記気室の空気量及び液体の供給量を個別に制御することができる点である。  Alternatively, in the present invention, the pulsation detecting means is individually provided in the plurality of sorting tanks, and can individually control the air amount and the liquid supply amount of the air chamber.

さらに、本発明において、前記選別槽に前記破砕産業廃棄物を投入する前工程において、前記破砕産業廃棄物を攪拌と搬送する回転筒を前記選別槽に隣設させ、前記回転筒には前記破砕産業廃棄物の出口と入口を設け、前記回転筒に搬送攪拌翼と回転モーターを設け、前記回転モーターで前記回転筒を回転させ、前記破砕産業廃棄物を前記選別槽に投入する搬送攪拌手段によって、投入量を制御することができる点である。  Further, in the present invention, in a pre-process for introducing the crushed industrial waste into the sorting tank, a rotating cylinder for stirring and conveying the crushed industrial waste is provided adjacent to the sorting tank, An industrial waste outlet and an inlet are provided, the rotary cylinder is provided with a carrier stirring blade and a rotary motor, the rotary cylinder is rotated by the rotary motor, and a carrier agitating means for feeding the crushed industrial waste into the sorting tank That is, the input amount can be controlled.

本発明の流水分級と沈降速度を利用した選別機は、複数槽の選別槽内の液体の脈動している動きを直接検知するものであり、稼動を自動化することで、全体の比重分離・選別工程を円滑経済的に効率良くできるものである。さらに、さまざまな素材が混在する複合廃物の破砕産業廃棄物を選別する前工程で、混在比率の不定な複合廃物を搬送攪拌手段によって安定させ、選別槽に過大な負荷をかけないで、処理選別するものであるため、低コスト低負荷で均質な固体有価物を提供すると共に、資源の再利用及び環境問題にも寄与するため産業上著しい効果を奏する。  The sorter using the flowing water class and settling velocity of the present invention directly detects the pulsating movement of the liquid in the multiple tanks. By automating the operation, the specific gravity separation and sorting of the whole is performed. The process can be carried out smoothly and efficiently. Furthermore, in the pre-process for sorting industrial waste that is a mixture of various materials, it is stabilized by conveying and agitating means, and processing sorting without overloading the sorting tank. Therefore, the present invention provides a solid solid value with low cost and low load, and contributes to the reuse of resources and environmental problems, and thus has a significant industrial effect.

以下、本発明の最良の形態について図面を用いて説明する。
図1は、本発明の脈動検知手段(6)を示す側面図であり、図2は、本発明の実施形態を示す脈動検知手段(6)と一槽空気動水選別機(22)の模式図である。3図は、本発明の実施形態を示すフローチャートである。図4は、本発明の実施形態を示す二槽空気動水選別機(23)の模式図である。図5は、本発明の搬送攪拌手段(35)を示す模式図である。図6は、本発明の実施形態を示す四槽空気動水選別機(24)の模式図である。図7は、本発明の全工程の実施形態を示すフローチャートである。
Hereinafter, the best mode of the present invention will be described with reference to the drawings.
FIG. 1 is a side view showing the pulsation detecting means (6) of the present invention, and FIG. 2 is a schematic view of the pulsation detecting means (6) and the one tank air / water sorter (22) showing the embodiment of the present invention. FIG. FIG. 3 is a flowchart showing an embodiment of the present invention. FIG. 4 is a schematic diagram of a two-tank air dynamic water sorter (23) showing an embodiment of the present invention. FIG. 5 is a schematic diagram showing the conveyance stirring means (35) of the present invention. FIG. 6 is a schematic diagram of a four tank air dynamic water sorter (24) showing an embodiment of the present invention. FIG. 7 is a flowchart showing an embodiment of all the steps of the present invention.

図1を参照しつつ、脈動検知手段(6)について説明する。前記脈動検知手段(6)は、選別槽(12)内の液体の脈動振幅及び脈動周期を直接検知するため、液体と同じ比重のフロート(1)を前記選別槽(12)内の液体内に配置する。前記フロート(1)には上部に伸びるフロート用ロッド(2)と発磁体(3)を設ける。前記フロート(1)より連動する前記発磁体(3)の上下動を変位センサーロッド(4)で振幅周期を測定し磁歪センサー(5)より波形化した情報を得る構成である。  The pulsation detecting means (6) will be described with reference to FIG. Since the pulsation detecting means (6) directly detects the pulsation amplitude and pulsation cycle of the liquid in the sorting tank (12), the float (1) having the same specific gravity as the liquid is placed in the liquid in the sorting tank (12). Deploy. The float (1) is provided with a float rod (2) and a magnetism generator (3) extending upward. The configuration is such that the vertical movement of the magnetomotive body (3) interlocked with the float (1) is measured by the displacement sensor rod (4) and the amplitude period is obtained and the waveform is obtained from the magnetostrictive sensor (5).

図2は、本発明の実施形態と可動状態を説明する。気室(11)を有する選別槽(12)に脈動検知手段(6)を吊設し、流水調整バルブ部(20)にて制御された液体が液体供給口(19)より前記選別槽(12)に流入する。前記選別槽(12)内には、上下に仕切るスクリーン部(21)が設けられ、下方には給排気口(17)を有する前記気室(11)設けられ、前記給排気口(17)より空気バルブ部(13)にて脈動が開始される。処理する磁性体金属除去後の破砕産業廃棄物は、前記選別槽(12)の投入口(14)より投入し、流水分級と沈降速度を利用した選別により比重分離・選別処理される。処理後は、回収口(15)のロータリフィーダ(18)によって排出口(16)へ液体と共に処理物が排出される。  FIG. 2 illustrates an embodiment of the present invention and a movable state. A pulsation detecting means (6) is suspended from a sorting tank (12) having an air chamber (11), and the liquid controlled by the flowing water adjusting valve section (20) is transferred from the liquid supply port (19) to the sorting tank (12). ). In the sorting tank (12), there is provided a screen portion (21) for partitioning vertically, and the air chamber (11) having an air supply / exhaust port (17) is provided below, from the air supply / exhaust port (17). Pulsation is started at the air valve section (13). The crushed industrial waste after the removal of the magnetic metal to be processed is fed from the inlet (14) of the sorting tank (12), and is subjected to specific gravity separation and sorting by sorting using the flowing water class and the settling speed. After the treatment, the processed material is discharged together with the liquid to the discharge port (16) by the rotary feeder (18) of the recovery port (15).

図3では、脈動検知手段(6)の情報経路を示しており、選別槽(12)内の液体の脈動振幅及び脈動周期を直接検知する脈動検知手段(6)の情報で、作動変換情報に変え、搬送攪拌手段(36)の破砕産業廃棄物の投入量、空気バルブ部(13)の気室(11)の空気量、流水調整バルブ部(20)による液体の供給量を制御するものである。  FIG. 3 shows the information path of the pulsation detecting means (6), and the information of the pulsation detecting means (6) for directly detecting the pulsation amplitude and pulsation period of the liquid in the sorting tank (12) is converted into the operation conversion information. In other words, it controls the amount of crushed industrial waste charged by the conveying and stirring means (36), the amount of air in the air chamber (11) of the air valve (13), and the amount of liquid supplied by the flowing water adjusting valve (20). is there.

図4は、複数の選別槽(12)に複数の脈動検知手段(6)を吊設した二槽空気動水選別機(23)の構成を示しているもので、複数の前記選別槽(12)が連接されている。前選別槽(12)で処理できない処理物を、連接されている後選別槽(12)へ流入させ、処理を繰り返すものである。よって、一槽空気動水選別機(22)と同様に、気室(11)を有する前記選別槽(12)に脈動検知手段(6)を吊設し、流水調整バルブ部(20)にて制御された液体が液体供給口(19)より前記選別槽(12)に流入し、前記選別槽(12)内には、上下に仕切るスクリーン部(21)が設けられ、下方には給排気口(17)を有する前記気室(11)設けられ、前記給排気口(17)より空気バルブ部(13)にて脈動が開始されものであり、処理する磁性体金属除去後の破砕産業廃棄物は、前記前選別槽(12)の投入口(14)より投入し、流水分級と沈降速度を利用した選別により処理され、処理できない処理物を、連接されている前記後選別槽(12)へ流入させ、適所の回収口(15)のロータリフィーダ(18)によって排出口(16)へ排出される。  FIG. 4 shows the structure of a two-tank air dynamic water sorter (23) in which a plurality of pulsation detecting means (6) are suspended from a plurality of sorting tanks (12). ) Are connected. The processing object which cannot be processed in a pre-sorting tank (12) is made to flow into the post-sorting tank (12) connected, and processing is repeated. Therefore, like the one tank air dynamic water sorter (22), the pulsation detecting means (6) is suspended from the sorting tank (12) having the air chamber (11), and the flowing water adjusting valve section (20) is used. The controlled liquid flows into the sorting tank (12) from the liquid supply port (19), and the sorting tank (12) is provided with a screen portion (21) that is divided into upper and lower portions, and an air supply / exhaust port below. The air chamber (11) having (17) is provided, pulsation is started from the air supply / exhaust port (17) by the air valve part (13), and the crushed industrial waste after removal of magnetic metal to be processed Is fed from the inlet (14) of the pre-sorting tank (12), processed by sorting using the flowing water class and settling velocity, and processed materials that cannot be treated are connected to the connected post-sorting tank (12). In the rotary feeder (18) of the recovery port (15) at the right place. And it is discharged to the discharge port (16) Te.

図5の搬送攪拌手段(36)は、選別槽(12)に破砕産業廃棄物を投入する前工程において、前記破砕産業廃棄物を攪拌と搬送する回転筒(31)を前記選別槽(12)に隣設させ、前記回転筒(31)に入口(32)と出口(33)を設け、搬送攪拌翼(34)を有する前記回転筒(31)に回転モーター(35)を設けるものであり、回転する速度によって、前記破砕産業廃棄物を前記分離槽(12)に投入する投入量を制御するものである。  The transport agitating means (36) of FIG. 5 is configured so that the rotating cylinder (31) for agitating and transporting the crushed industrial waste is placed in the sorting tank (12) in the previous step of putting the crushed industrial waste into the sorting tank (12). The rotary cylinder (31) is provided with an inlet (32) and an outlet (33), and the rotary cylinder (31) having a conveying stirring blade (34) is provided with a rotary motor (35). The amount of input of the crushed industrial waste into the separation tank (12) is controlled by the rotating speed.

図6は、さらに複数の選別槽(12)に複数の脈動検知手段(6)を吊設した四槽空気動水選別機(23)の構成を示しているもので、複数の前記選別槽(12)が連接されている。複数の前記選別槽(12)を連接すると、処理できない処理物の搬送が容易であると共に、設備自体を縮小できる利点がある。最前の選別槽(12)には、流水調整バルブ部(20)にて制御された液体が液体供給口(19)より最前の前記選別槽(12)に流入し、処理する磁性体金属除去後の破砕産業廃棄物は、前記前選別槽(12)の投入口(14)より投入させる。各選別槽(12)には脈動検知手段(6)を吊設し、前記選別槽(12)内には、上下に仕切るスクリーン部(21)が設けられ、下方には給排気口(17)を有する前記気室(11)設けられ、前記給排気口(17)より空気バルブ部(13)にて脈動が開始されものであり、流水分級と沈降速度を利用した選別により処理され、処理できない処理物を、連接されている前記後選別槽(12)へ流入させ、適所の回収口(15)のロータリフィーダ(18)によって排出口(16)へ排出される。  FIG. 6 shows a configuration of a four-tank air dynamic water sorter (23) in which a plurality of pulsation detecting means (6) are suspended from a plurality of sorting tanks (12). 12) are connected. When the plurality of sorting tanks (12) are connected, there is an advantage that it is easy to transport a processed material that cannot be processed and the facility itself can be reduced. In the foremost sorting tank (12), the liquid controlled by the flowing water adjusting valve part (20) flows into the foremost sorting tank (12) from the liquid supply port (19), and after the magnetic metal to be processed is removed. The crushing industrial waste is fed from the inlet (14) of the pre-sorting tank (12). A pulsation detecting means (6) is suspended in each sorting tank (12), and a screen portion (21) for partitioning vertically is provided in the sorting tank (12), and a supply / exhaust port (17) is provided below. The air chamber (11) is provided, and pulsation is started from the air supply / exhaust port (17) at the air valve part (13). The processed material is introduced into the connected post-sorting tank (12) and discharged to the discharge port (16) by the rotary feeder (18) of the recovery port (15) at an appropriate place.

図7を参照しつつ、本発明の全工程の実施形態を示すフローチャートに沿って最良の形態について説明する。本発明は、ELV(End of Life Vehicle)(以下「適正処理解体」と称する)、後の車両を適正選別処理を可能とするもので、ASR(シュレッダーダスト)(以下「破砕産業廃棄物」と称する)処理と並列したブラントも容易に考えられる。  With reference to FIG. 7, the best mode will be described along a flowchart showing an embodiment of all the steps of the present invention. The present invention is an ELV (End of Life Vehicle) (hereinafter referred to as “appropriate treatment dismantling”), which enables a subsequent vehicle to be properly selected and processed by ASR (shredder dust) (hereinafter referred to as “crushing industrial waste”). A blunt in parallel with the processing is also conceivable.

初めにステップS−1は、適正処理解体された固体物である車両を破砕機により破砕する工程である。この工程では、さまざまな素材が混在している複合廃物を0.1mm〜40mm程度に破砕する。複合廃物には、磁性体金属と非磁性体金属が混在しているが、破砕工程より破砕された複合廃物から磁性体金属を磁選機での除くことが容易に可能である。磁性体金属除去後の破砕産業廃棄物には、「ウレタン」「PP」「PE」「PS」「ABS」「塩ビ」「木材」「ゴム類」「石」「ガラス」「基板屑」「塗装膜亅「繊維屑」「銅線屑」「ステンレス」「アルミニウム」等さまざまな素材が混在している。これら複合廃物の混在比率は不定であり逐次変化するものである。  First, step S-1 is a step of crushing a vehicle, which is a solid object dismantled properly, with a crusher. In this process, composite waste containing various materials is crushed to about 0.1 mm to 40 mm. In the composite waste, magnetic metal and non-magnetic metal are mixed, but it is possible to easily remove the magnetic metal from the composite waste crushed by the crushing step with a magnetic separator. For crushing industrial waste after removing magnetic metal, "urethane" "PP" "PE" "PS" "ABS" "PVC" "wood" "rubber" "stone" "glass" "substrate scrap" "painting" There are various materials such as membrane fiber “fiber waste” “copper wire waste” “stainless steel” “aluminum”. The mixing ratio of these composite wastes is indefinite and changes sequentially.

そこで、ステップS−1では、破砕と磁性体金属除去に加え、選別槽(12)に搬送するだけでなく、搬送攪拌手段(36)を加えている。図5でも示しているが、磁性体金属除去後破砕産業廃棄物である複合廃物を、回転筒(31)内でストックしながら混在比率の不定な複合廃物を安定させつつ攪拌と搬送を同時に行うものである。破砕産業廃棄物が前記回転筒(31)の入口(32)に投入されると、回転モーター(35)により前記回転筒(31)を回転させ、搬送攪拌翼(34)によって攪拌しながら出口(33)へ誘導される。前記回転モーター(35)の回転する速度によって、前記破砕産業廃棄物を前記分離槽(12)に投入する投入量を制御するものである。  Therefore, in step S-1, in addition to crushing and removal of the magnetic metal, in addition to transporting to the sorting tank (12), a transport stirring means (36) is added. As shown in FIG. 5, the composite waste, which is the crushed industrial waste after removing the magnetic metal, is stocked in the rotating cylinder (31), and the composite waste with an indefinite mixture ratio is stabilized and simultaneously stirred and conveyed. Is. When the crushed industrial waste is introduced into the inlet (32) of the rotary cylinder (31), the rotary cylinder (31) is rotated by the rotary motor (35), and the outlet ( 33). The amount of input of the crushed industrial waste into the separation tank (12) is controlled by the rotation speed of the rotary motor (35).

次に、ステップS−2は、磁性体金属除去後の非磁性体廃材の選別工程であり、図6に示している複数の選別槽(12)に複数の脈動検知手段(6)を吊設した四槽空気動水選別機(23)によって比重分離・選別する。ステップS−2では、「硬質浮遊物」「軟質浮遊物」「中間浮遊物」「網下落下物」に比重分離・選別する。「軟質浮遊物」及び「硬質浮遊物」は、浮遊物吸引口(25)より吸引する。「硬質浮遊物」「軟質浮遊物」「網下落下物」は再度破砕機によって0.1mm〜12mm程度に破砕し、次工程での比重選分離・別処理効率を高める。  Next, step S-2 is a non-magnetic waste sorting process after removing the magnetic metal, and a plurality of pulsation detecting means (6) are suspended from the plurality of sorting tanks (12) shown in FIG. The specific gravity is separated and sorted by the four tank air dynamic water sorter (23). In step S-2, the specific gravity is separated and sorted into “hard floating material”, “soft floating material”, “intermediate floating material”, and “falling material under the net”. “Soft floating matter” and “hard floating matter” are sucked from the floating matter suction port (25). “Hard suspended matter”, “soft suspended matter” and “falling material under the net” are again crushed to about 0.1 mm to 12 mm by a crusher, and the specific gravity separation / separation processing efficiency in the next process is increased.

ステップS−2以降の比重分離・選別では、すべての前記選別槽(12)内の液体を前記脈動検知手段(6)で脈動振幅及び脈動周期を直接確認できるため、最適な処理状況で可動させることができる。例えば、前記選別槽(12)の処理能力を向上させるには、空気バルブ部(13)で空気量と流水調整バルブ部(20)で液体の供給量を増加させ、場合によっては搬送攪拌手段(36)で前記選別槽(12)に投入する破砕産業廃棄物の投入量を加減する。または、前記選別槽(12)処理能力を下げる必要がある場合、空気バルブ部(13)で空気量と流水調整バルブ部(20)で液体の供給量を減らし、場合によっては搬送攪拌手段(36)で前記選別槽(12)に投入する破砕産業廃棄物の投入量を加減する。尚、本発明の比重分離・選別する各工程で選別槽(12)のすべてに脈動検知手段(6)を吊設して実施するため、全体の処理能力を集中して制御することも可能となる。  In the specific gravity separation / sorting after step S-2, the liquid in all the sorting tanks (12) can be directly checked in the pulsation detecting means (6) for the pulsation amplitude and pulsation period, so that it can be moved in an optimum processing state. be able to. For example, in order to improve the processing capacity of the sorting tank (12), the air amount is increased by the air valve portion (13) and the liquid supply amount by the flowing water adjustment valve portion (20). In 36), the input amount of the crushed industrial waste charged into the sorting tank (12) is adjusted. Alternatively, when it is necessary to reduce the processing capacity of the sorting tank (12), the air valve unit (13) reduces the air amount and the flowing water adjustment valve unit (20), and the liquid stirring amount (36) may be reduced. ) To adjust the input amount of the crushed industrial waste to be input to the sorting tank (12). In addition, since the pulsation detecting means (6) is suspended in all the sorting tanks (12) in each step of separating and sorting specific gravity according to the present invention, it is possible to centrally control the entire processing capacity. Become.

ステップS−3では、「軟質浮遊物」をさらに図4に示した複数の選別槽(12)に複数の脈動検知手段(6)を吊設した二槽空気動水選別機(23)によって、「PE」を比重分離・選別される。「ウレタン」「PP」「木材」類は、脱水処理後に圧縮成型機で成型され、高カロリーな固形燃料(Refuse Paper and Plastic Fuel)(以下「RPF」と称する)に加工することが可能である。  In step S-3, the “soft suspended matter” is further separated by a two-tank air / water sorter (23) in which a plurality of pulsation detecting means (6) are suspended from a plurality of sorting tanks (12) shown in FIG. “PE” is separated and sorted by specific gravity. “Urethane”, “PP”, and “wood” are molded by a compression molding machine after dehydration and can be processed into a high-calorie solid fuel (Refuse Paper and Plastic Fuel) (hereinafter referred to as “RPF”). .

ステップS−4では、「硬質浮遊物」を図4に示した複数の選別槽(12)に複数の脈動検知手段(6)を吊設した二槽空気動水選別機(23)によって、「塩ビ」と「ゴム類」に比重分離・選別される。さらに、「再硬質浮遊物」が発生する。  In step S-4, the “hard floating matter” is separated by a two-tank air / water sorter (23) in which a plurality of pulsation detecting means (6) are suspended from a plurality of sorting tanks (12) shown in FIG. Specific gravity is separated and sorted into PVC and rubber. Furthermore, “re-hard floating matter” is generated.

ステップS−5では、「再硬質浮遊物」を図4に示した複数の選別槽(12)に複数の脈動検知手段(6)を吊設した二槽空気動水選別機(23)によって、「ABS」と「PS」に選別される。  In step S-5, the “re-hard floating substance” is divided into a plurality of sorting tanks (12) shown in FIG. 4 by a two-tank air dynamic water sorter (23) in which a plurality of pulsation detecting means (6) are suspended. Sorted into “ABS” and “PS”.

ステップS−6は、「網下落下物」を図4に示した複数の選別槽(12)に複数の脈動検知手段(6)を吊設した二槽空気動水選別機(23)によって、「ガラス」「基板材」「塗装膜」「繊維屑」に比重分離・選別される。  Step S-6 is a two tank air dynamic water sorter (23) in which a plurality of pulsation detecting means (6) are suspended from a plurality of sorting tanks (12) shown in FIG. Specific gravity is separated and sorted into “glass”, “substrate material”, “painted film” and “fiber waste”.

ステップS−7は、「中間浮遊物」を図4に示した複数の選別槽(12)に複数の脈動検知手段(6)を吊設した二槽空気動水選別機(23)によって、「石」「ガラス」「基板屑」に比重分離・選別される。  In step S-7, “intermediate suspended matter” is separated by a two-tank air dynamic water sorter (23) in which a plurality of pulsation detecting means (6) are suspended from a plurality of sorting tanks (12) shown in FIG. Specific gravity separation and sorting into stone, glass, and substrate waste.

ステップS−8は、「中間浮遊物」 図2に示した選別槽(12)に脈動検知手段(6)を吊設した一槽空気動水選別機(22)によって、「ステンレス」「アルミニウム」に比重分離・選別される。  Step S-8 is "intermediate suspended matter" "Stainless steel" "Aluminum" by the one tank air dynamic water sorter (22) which suspended the pulsation detection means (6) in the sorting tank (12) shown in FIG. Specific gravity separation and sorting.

以上のように、本発明の実施形態の流水分級と沈降速度を利用した選別機によれば、比重や形状の異なるさまざまな素材が混在している磁性体金属除去後の破砕産業廃棄物を比重分離・選別することができる。
尚、本発明の実施形態は限定されるものではなく、分離槽の大きさや、形状、処理能力がそれぞれ異なる個別の分離槽の構成等、破砕産業廃棄物である複合廃物の変化に応じ、適時変更することができる。
As described above, according to the sorting machine using the flowing water class and the settling velocity of the embodiment of the present invention, the specific gravity of the crushed industrial waste after removal of the magnetic metal from which various materials having different specific gravity and shape are mixed. Can be separated and sorted.
The embodiment of the present invention is not limited, and it is timely according to changes in composite waste that is crushing industrial waste, such as the size, shape, and configuration of individual separation tanks with different separation tanks. Can be changed.

本発明の脈動検知手段を示す側面図である。It is a side view which shows the pulsation detection means of this invention. 本発明の実施形態を示す脈動検知手段と一槽空気動水選別機の模式図である。It is a schematic diagram of the pulsation detection means and one tank air dynamic water sorter which show the embodiment of the present invention. 本発明の実施形態を示すフローチャートである。It is a flowchart which shows embodiment of this invention. 本発明の実施形態を示す二槽空気動水選別機の模式図である。It is a mimetic diagram of a two tank air dynamics water sorter showing an embodiment of the present invention. 本発明の搬送攪拌手段を示す模式図である。It is a schematic diagram which shows the conveyance stirring means of this invention. 本発明の実施形態を示す四槽空気動水選別機の模式図である。It is a mimetic diagram of a four tank air dynamic water sorter showing an embodiment of the present invention. 本発明の全工程の実施形態を示すフローチャートである。It is a flowchart which shows embodiment of all the processes of this invention.

符号の説明Explanation of symbols

1 フロート(1)
2 フロート用ロッド(2)
3 発磁体(3)
4 変位センサーロッド(4)
5 磁歪センサー(5)
6 脈動検知手段(6)
11 気室(11)
12 選別槽(12)
13 空気バルブ部(13)
14 投入口(14)
15 回収口(15)
16 排出口(16)
17 給排気口(17)
18 ロータリフィーダ(18)
19 液体供給口(19)
20 流水調整バルブ部(20)
21 スクリーン部(21)
22 一槽空気動水選別機(22)
23 二槽空気動水選別機(23)
24 四槽空気動水選別機(24)
25 浮遊物吸引口(25)
31 回転筒(31)
32 入口(32)
33 出口(33)
34 搬送攪拌翼(34)
35 回転モーター(35)
36 搬送攪拌手段(36)
1 Float (1)
2 Rod for float (2)
3 Magnetism body (3)
4 Displacement sensor rod (4)
5 Magnetostrictive sensor (5)
6 Pulsation detection means (6)
11 Air chamber (11)
12 sorting tank (12)
13 Air valve (13)
14 slot (14)
15 Collection port (15)
16 outlet (16)
17 Supply / exhaust port (17)
18 Rotary feeder (18)
19 Liquid supply port (19)
20 Flowing water adjustment valve (20)
21 Screen (21)
22 One tank air dynamic water sorter (22)
23 Two tank air dynamic water sorter (23)
24 four tank air dynamic water sorter (24)
25 Floating object suction port (25)
31 Rotating cylinder (31)
32 entrance (32)
33 Exit (33)
34 Conveying stirring blade (34)
35 Rotating motor (35)
36 Conveying and stirring means (36)

Claims (4)

磁性体金属除去後の破砕産業廃棄物を比重分離・選別する空気動水選別機において、気室を有する選別槽にフロートが上下動する脈動検知手段を吊設し、前記選別槽内には上下に仕切るスクリーン部を設け、前記気室に空気入排気量を調整する空気バルブ部を設け、前記選別槽内の液体の脈動振幅及び脈動周期を前記脈動検知手段からの情報によって、前記気室の空気量を前記空気バルブ部で制御することを特徴とする流水分級と沈降速度を利用した選別機。  In an air dynamic water sorter that separates and sorts crushed industrial waste after removing magnetic metal, a pulsation detecting means that floats up and down is suspended in a sorting tank having an air chamber, A screen portion for partitioning the air chamber, and an air valve portion for adjusting an air intake / exhaust amount in the air chamber, and a pulsation amplitude and a pulsation period of the liquid in the sorting tank according to information from the pulsation detecting means. A sorter using a flowing water class and a settling velocity, wherein the air amount is controlled by the air valve unit. 前記選別槽に液体を供給するための液体供給口を設け、前記液体供給口に流水調整バルブ部を設け、前記脈動検知手段からの情報によって液体の供給量を流水調整バルブ部で制御することを特徴とする請求項1に記載の流水分級と沈降速度を利用した選別機。  A liquid supply port for supplying a liquid to the sorting tank is provided, a water flow adjustment valve unit is provided in the liquid supply port, and a liquid supply amount is controlled by the flow water adjustment valve unit according to information from the pulsation detecting means. The sorter using the flowing water class and settling velocity according to claim 1. 前記脈動検知手段は、複数の前記選別槽内に個別に設けられ、前記気室の空気量及び液体の供給量を個別制御することを特徴とする請求項1〜請求項2に記載の流水分級と沈降速度を利用した選別機。  3. The flowing water class according to claim 1, wherein the pulsation detecting unit is individually provided in the plurality of sorting tanks, and individually controls the air amount and the liquid supply amount of the air chamber. And sorter using sedimentation speed. 前記選別槽に前記破砕産業廃棄物を投入する前工程において、前記破砕産業廃棄物を攪拌と搬送する回転筒を前記選別槽に隣設させ、前記回転筒には前記破砕産業廃棄物の出口と入口を設け、前記回転筒に搬送攪拌翼と回転モーターを設け、前記回転モーターで前記回転筒を回転させ、前記破砕産業廃棄物を前記選別槽に投入する搬送攪拌手段によって投入量を制御することを特徴とする請求項1〜請求項3に記載の流水分級と沈降速度を利用した選別機。  In a pre-process for charging the crushed industrial waste into the sorting tank, a rotating cylinder for stirring and conveying the crushed industrial waste is provided next to the sorting tank, and the rotating cylinder has an outlet for the crushed industrial waste. An inlet is provided, a conveying stirring blade and a rotating motor are provided in the rotating cylinder, the rotating cylinder is rotated by the rotating motor, and the input amount is controlled by a conveying stirring means that inputs the crushed industrial waste into the sorting tank. The sorter using the flowing water class and settling velocity according to claim 1.
JP2004351955A 2004-11-05 2004-11-05 Sorter using flowing water class and settling velocity Expired - Fee Related JP3711471B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2004351955A JP3711471B1 (en) 2004-11-05 2004-11-05 Sorter using flowing water class and settling velocity

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2004351955A JP3711471B1 (en) 2004-11-05 2004-11-05 Sorter using flowing water class and settling velocity

Publications (2)

Publication Number Publication Date
JP3711471B1 true JP3711471B1 (en) 2005-11-02
JP2006130490A JP2006130490A (en) 2006-05-25

Family

ID=35445613

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2004351955A Expired - Fee Related JP3711471B1 (en) 2004-11-05 2004-11-05 Sorter using flowing water class and settling velocity

Country Status (1)

Country Link
JP (1) JP3711471B1 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008132484A (en) * 2006-10-31 2008-06-12 Jig Engineering Co Ltd Recovery control device for reticulated air chamber type wet specific gravity sorter using magnetostrictive float sensor
JP5845658B2 (en) * 2011-06-28 2016-01-20 株式会社大林組 Purification method and system for contaminated soil

Also Published As

Publication number Publication date
JP2006130490A (en) 2006-05-25

Similar Documents

Publication Publication Date Title
KR102762574B1 (en) Systems and methods for separating materials using stirring, layering and vertical motions
US20250229275A1 (en) Apparatus and method for separating materials using stratification
KR101260026B1 (en) Recycling device of scrap iron waste by using comminution and selection
US20230294106A1 (en) Systems for separating copper from shredder residue
EP0469903A2 (en) Process and apparatus for separating a mixture of plastic material into fractions
JP3711471B1 (en) Sorter using flowing water class and settling velocity
CN104114290B (en) Dry type separation method and dry type segregation apparatuss
US12059687B2 (en) Methods and systems for high throughput separation of materials using stratification and rotational motion
CN113573815A (en) System and method for processing a combination of liquid and particulate matter
JP3711472B1 (en) Sorting method of crushing industrial waste using flowing water class and settling velocity
KR102880337B1 (en) Methods and facilities for hyperpure recycling kind recycled plastics by type using waste home appliances plastics
US12097508B2 (en) Metal filament recovery system
KR102892110B1 (en) Facilities and Methods for electrostatic separating kind recycled plastics using waste home appliances plastics
CN114917682B (en) Blast furnace dust removal ash separation system
JP2025039421A (en) Sorting system, sorting method, and control program
JP2025039420A (en) Sorting system, sorting method, and control program
JP2025039422A (en) Sorting system, sorting method, and control program
JP2025039419A (en) Sorting system, sorting method, and control program
Dodbiba et al. Separation of Plastics for Recycling
KR20240082101A (en) Methods and facilities for specific gravity separation of recycled plastics by type using waste home appliances plastic
JP2000024543A (en) Sorting apparatus utilizing ascending water flow
RU1801574C (en) Gravity concentration method
JP2025039423A (en) Floating/sinking sorting device, sorting system, and control program
CN119747073A (en) A mineral screening system and method
KR20040021929A (en) Floating Matters and Soil Separating Device from Construction Refuse

Legal Events

Date Code Title Description
TRDD Decision of grant or rejection written
A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20050802

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

LAPS Cancellation because of no payment of annual fees