JPH03181379A - Treatment of waste and resource recovering method - Google Patents

Treatment of waste and resource recovering method

Info

Publication number
JPH03181379A
JPH03181379A JP1319725A JP31972589A JPH03181379A JP H03181379 A JPH03181379 A JP H03181379A JP 1319725 A JP1319725 A JP 1319725A JP 31972589 A JP31972589 A JP 31972589A JP H03181379 A JPH03181379 A JP H03181379A
Authority
JP
Japan
Prior art keywords
gas
waste
pyrolysis
furnace
metals
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.)
Pending
Application number
JP1319725A
Other languages
Japanese (ja)
Inventor
Shunei Arita
有田 俊英
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
JIYOUKAN SOGYO KK
Original Assignee
JIYOUKAN SOGYO KK
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 JIYOUKAN SOGYO KK filed Critical JIYOUKAN SOGYO KK
Priority to JP1319725A priority Critical patent/JPH03181379A/en
Publication of JPH03181379A publication Critical patent/JPH03181379A/en
Pending legal-status Critical Current

Links

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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel
    • 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
    • Y02W30/82Recycling of waste of electrical or electronic equipment [WEEE]

Landscapes

  • Processing Of Solid Wastes (AREA)

Abstract

PURPOSE:To reduce the cost of treatments by providing a pyrolysis reaction furnace and a non-utility power generator in treating equipment, decomposing and gasifying waste plastics and using the gas as fuel. CONSTITUTION:The plastic balls screened and discharged from a high-polymer screening machine is supplied to the pyrolysis reaction furnace 36. The plastic balls are then thermally decomposed to a gaseous state in a pyrolysis furnace 42 below a hopper 41. A heating furnace 50 with a burner 45 is installed below the pyrolysis furnace 42 and the pyrolysis reaction is effected by heating the pyrolysis furnace 42 from the outside. The cracked gas is sent to a condenser 47 where the gas acts as a metal catalyst and is cooled by the effect of circulating water. The low boiling gas is thus separated. The gas is introduced through a gas holder 56 into a gas tank 57 and is used as the fuel of the burner 45. Thus, the installation conditions of the equipment are drastically relieved.

Description

【発明の詳細な説明】 〈産業上の利用分野〉 この発明は自動車や家電製品その他、主としてプラスチ
ック、金属を含む廃棄物の処理及びこれらに含まれる資
源を回収する方法に関する。
DETAILED DESCRIPTION OF THE INVENTION <Industrial Application Field> The present invention relates to the treatment of automobiles, home appliances, and other wastes mainly containing plastics and metals, and to a method for recovering the resources contained therein.

〈従来の技術〉 従来例えば自動車の廃棄処理に際しては、金属と非金属
に分別処理され、金属は鉄、非鉄等に更に細分別されて
資源として回収されるが、非金属廃棄物は自動車で約3
0%を占めるにもかかわらず埋立て又は焼却処理してい
た。
<Conventional technology> Conventionally, for example, when disposing of automobiles, they are separated into metals and non-metals, and the metals are further subdivided into ferrous, non-ferrous, etc. and then recovered as resources. 3
Despite accounting for 0% of total waste, they were disposed of in landfills or incinerated.

また家電製品やOA機器については資源として回収すべ
き有価物量が少ない(金属約40%、非金属約60%)
ために一部は分別処理される事があるものの大半は粗大
ゴミとして埋立又は焼却処理されていた。
Furthermore, the amount of valuable materials that should be recovered as resources for home appliances and OA equipment is small (approximately 40% metals and approximately 60% non-metals).
Therefore, although some of the waste was separated, the majority was disposed of in landfills or incinerated as bulky waste.

そしてこれらの分別処理では廃棄製品を解体して材質群
毎に分別し、さらに粉砕、磁気選別、比重(風力)選別
等の工程を経て非金属は上述のように埋立・焼却処理さ
れていた。
In these sorting processes, waste products are dismantled and separated by material group, and then undergo processes such as crushing, magnetic sorting, and specific gravity (air force) sorting, and non-metals are then landfilled or incinerated as described above.

〈発明が解決しようとする課題〉 しかし従来のようにプラスチック等を埋立処理するには
広大な埋立地を必要とし、特に都市部では用地確保が困
難な上に運送等の処理コストも高くなるという問題があ
った。また焼却処理も独自の焼却設備を必要とするほか
、これも環境問題等を生じて用地確保が困難である上に
、コスト高を免れない。
<Problems to be solved by the invention> However, the conventional landfill disposal of plastics and other materials requires a vast amount of land, making it difficult to secure land, especially in urban areas, and increasing transportation and other processing costs. There was a problem. In addition, incineration requires its own incineration equipment, which also causes environmental problems, makes it difficult to secure land, and is inevitably costly.

殊にこれらの廃棄物処理設備等はいずれも環境問題に直
結するために、処理場所、設備設置場所等も各方面から
厳しく規制され、地域や建築物の規格等の面で民間企業
等では設置が容易に行えないという問題がある。
In particular, since all of these waste treatment facilities are directly connected to environmental problems, the treatment locations and equipment installation locations are strictly regulated from all directions, and private companies are prohibited from installing them due to regional and building standards. The problem is that it cannot be done easily.

〈課題を解決するための手段〉 」二記問題点を改善するための本発明の方法は、固体廃
棄物を一連の処理設備と工程により金属と非金属に分別
処理し、さらに該工程中で非金属中よりプラスチックを
分離して処理するとともに処理された結果物を有価資源
として回収する方法において、上記処理設備中に、熱分
解反応炉と燃焼機関で作動する自家発電装置を設け、廃
棄物中のプラスチックを熱分解反応炉で分解してガス化
又は液化してこれらの分解ガス又は分解液を前記燃焼機
関の燃料として自家発電を行わせ、該自家発電により処
理設備の電力を調達することを特徴としている。
<Means for Solving the Problems> The method of the present invention for improving the problem described in item 2 separates solid waste into metals and non-metals using a series of processing equipment and processes, and further, during the process, In a method of separating and processing plastics from non-metals and recovering the processed products as valuable resources, a private power generation device operated by a pyrolysis reactor and a combustion engine is installed in the processing equipment, and the waste is The plastic inside is decomposed in a pyrolysis reactor to gasify or liquefy, and the decomposed gas or decomposed liquid is used as fuel for the combustion engine to generate private power, and the private power generation is used to procure electricity for the processing equipment. It is characterized by

〈作用〉 本発明の方法においては自動車、家電製品等の粗大廃棄
物や一般不燃廃棄物から金属とプラスチックを中心とす
る有価資源を一連の処理設備を作動させて一連の工程で
処理することによって有効に回収するとともに、プラス
チック廃棄物は、さらに同設備内の熱分解反応炉36で
熱分解されて液化又はガス化され、これらのガス又は液
化樹脂によって同−設備内の燃焼機関を作動させて発電
機を駆動し、上記分解ガス又は分解液をエネルギー源と
して処理設備の電力を供給するものである。
<Operation> In the method of the present invention, valuable resources, mainly metals and plastics, are processed in a series of steps by operating a series of processing equipment from bulky waste such as automobiles and home appliances, and general non-combustible waste. In addition to being effectively collected, the plastic waste is further thermally decomposed and liquefied or gasified in a pyrolysis reactor 36 within the same facility, and these gases or liquefied resins are used to operate a combustion engine within the facility. A generator is driven to supply power to the processing equipment using the decomposed gas or decomposed liquid as an energy source.

〈実施例〉 以下図面に即して本発明の実施例につき詳述すると第1
図は本発明の廃棄物処理及び資源回収システムのフロシ
ートを示し、システムは1〜■からなっており、システ
ムIは自動車、家電製品、OA機器等比較的粗大な廃棄
物の処理システムである。システム■は比較的小物の袋
詰された不燃ゴミの処理を行うシステム、システム■は
上記システムI、■等で分別処理されたプラスチック類
の最終処理を行いさらにエネルギー利用するシステムで
本発明方法独自のものである。
<Example> The following is a detailed description of an example of the present invention based on the drawings.
The figure shows a flow sheet of the waste treatment and resource recovery system of the present invention, and the system consists of 1 to 3. System I is a system for treating relatively coarse waste such as automobiles, home appliances, and OA equipment. System ■ is a system that processes non-combustible garbage packed in relatively small bags, and system ■ is a system that performs final processing of plastics that have been separated and processed in systems I, ■, etc. above, and further utilizes energy, and is unique to the method of the present invention. belongs to.

システム■では予め解体された粗大物が搬入ステージ1
に搬入され、ここでは再利用資源としての価値が異なる
材質を可能な限り同−材質毎に人手により分類選別する
。このシステムで処理される対象物として分類例は次の
通りである。
In system ■, bulky items that have been dismantled in advance are transported to Stage 1.
Here, materials with different values as recyclable resources are manually sorted and sorted by the same material as much as possible. Examples of classification of objects processed by this system are as follows.

・自動車・事務機具(机、椅子、ロッカー、書棚等)・
オートバイ・自転車・家庭用器具(ガス台、流し台、等
) ・トタン類 ・家電製品(冷蔵庫、洗潅機、テレビ、電子レンジ、各
種オーディオ、掃除機等) ・OA機器 ・建設廃材(木屑、コンクリートの破片、煉瓦、等は除
く) ・その他(応接セット、ベント、カーペット、布団、冷
凍ケース、陳列棚、陳列ケース) 上記のように分類分別された粗大物は分類品目毎に次の
グランドシャー2に投入され、搬送コンベア3を介して
次のグリッパ−(造粒機)4の投入口の大きさに合わせ
て30〜50cmの大きさに順次切断する。グランドシ
ャー2は周知のギロチン式の切断機で油圧又はクランク
軸駆動式等いずれでも良い。
・Automobiles・Office equipment (desks, chairs, lockers, bookshelves, etc.)・
Motorcycles, bicycles, household appliances (gas stoves, sinks, etc.), corrugated iron, home appliances (refrigerators, washing machines, TVs, microwave ovens, various audio systems, vacuum cleaners, etc.), OA equipment, construction waste (wood chips, concrete, etc.)・Others (reception sets, vents, carpets, futons, freezer cases, display shelves, display cases) Bulky items that have been classified and separated as above will be placed in the following Grand Shear 2 for each classification item. The pellets are fed into a conveyor 3 and sequentially cut into pieces of 30 to 50 cm in size to match the size of the inlet of the next gripper (granulator) 4. The ground shear 2 is a well-known guillotine type cutting machine, and may be hydraulically driven or crankshaft driven.

上記のように切断された切断物は搬送コンベア3にてグ
リッパ−4に送られ、グリッパ−4は中間処理設備にお
いては粗破砕の工程に当たり、この実施例では一般に使
用されている回転式ハンマーで、その原理的な構造は第
2図に示される。
The cut pieces cut as described above are sent to the gripper 4 on the conveyor 3, and the gripper 4 is used for the rough crushing process in the intermediate processing equipment, and in this embodiment, it is a commonly used rotary hammer. , its basic structure is shown in FIG.

第2図に示す造粒機4は上部が投入口5として開口し、
下部に小経の排出口6を有する筒状のケーシング7内の
中心に回転シャフト8か軸支され、該回転シャフト8の
上下端にはブラケット9.10が突設されるとともに、
該ブラケット9.IO間には軸まわりに放射状に突出し
たハンマーアーム11に軸支されたハンマー軸12が上
下方向に支持されている。
The granulator 4 shown in FIG. 2 has an opening at the top as an input port 5,
A rotary shaft 8 is rotatably supported at the center of a cylindrical casing 7 having a small diameter outlet 6 at the bottom, and brackets 9 and 10 are protruded from the upper and lower ends of the rotary shaft 8.
The bracket9. A hammer shaft 12 supported vertically by a hammer arm 11 projecting radially around the shaft is supported between the IOs.

上記ハンマー軸12は回転シャフト8とともにそれ自体
が回転し、さらにハンマー軸12には上記ハンマーアー
ム11の先端上面に沿って基端部が軸支される回転ハン
マー15が取り付けられているため、回転シャフト8の
回転とともに、遠心力によって回転ハンマー15つか開
き出すように回転し、投入口5により投入された切断物
は、回転ハンマー15に衝突破砕され、その衝撃と摩擦
熱によりプラスチック類を分離して下方に落下する。こ
の落下過程で高速回転中の下部の回転ハンマー15によ
って投入物はさらに打撃され且つケーシング7の内面に
接衝して回転するため、5〜l0cmの丸いボール状に
造粒され排出口6より放出され、排出コンベア14及び
磁選コンベア16(第3図)を介して次工程の磁選機1
7に送られる。
The hammer shaft 12 itself rotates together with the rotary shaft 8, and a rotary hammer 15 whose base end is pivotally supported along the top surface of the distal end of the hammer arm 11 is attached to the hammer shaft 12, so that the hammer shaft 12 rotates. As the shaft 8 rotates, the rotary hammer 15 rotates to open due to centrifugal force, and the cut material inputted through the input port 5 collides with the rotary hammer 15 and is crushed, and the plastics are separated by the impact and frictional heat. and fall downward. During this falling process, the input material is further hit by the rotating hammer 15 at the bottom rotating at high speed and rotates while contacting the inner surface of the casing 7, so that it is granulated into a round ball shape of 5 to 10 cm and discharged from the discharge port 6. The magnetic separator 1 is then sent to the magnetic separator 1 for the next process via the discharge conveyor 14 and the magnetic separator 16 (Fig. 3).
Sent to 7.

第3図は上記磁選機17の原理的構造を示し、磁選コン
ベア16上に横断方向に設けられた樹脂製の回転ベルト
18は、回転ローラ19.19.19に巻装されており
、上記回転ベルト18のループ内の底辺上には強力なマ
グネット20が近接して設置されている。
FIG. 3 shows the basic structure of the magnetic separator 17, in which a resin rotating belt 18 provided transversely on the magnetic separator 16 is wound around rotating rollers 19, 19, 19. A strong magnet 20 is placed close to the bottom of the loop of the belt 18.

モして磁選コンベア16上のボール21のうち磁性材(
鉄系)のものだけが回転ベル目8の底面に吸着され、ベ
ルト回転に従って磁選コンベア16外に搬送落下され、
磁選コンベア16上に残された非磁性材(非鉄)のボー
ル2Iは、第4図に示す高分子分別機22に送り込まれ
る。
Among the balls 21 on the magnetic separation conveyor 16, the magnetic material (
Only those (iron-based) are attracted to the bottom of the rotating bell eye 8, and transported and dropped outside the magnetic separation conveyor 16 as the belt rotates.
The balls 2I of non-magnetic material (non-ferrous) remaining on the magnetic separation conveyor 16 are sent to a polymer separator 22 shown in FIG. 4.

磁選機17によって分別された鉄屑は切替コンベア23
上に落下し、例えば軟鉄、鋼材、鋼鉄等のように材質別
に人手によって分類されて資源として回収される。
The iron scraps separated by the magnetic separator 17 are transferred to the switching conveyor 23
They fall to the top and are manually sorted by material, such as soft iron, steel, steel, etc., and then collected as resources.

高分子分別機22は、横軸方向に回転自在に支持された
前後端が開口した選別筒24と該選別筒24の後方端側
を覆うように横設された排出フード26とからなり、選
別筒24の前半部内周にはその回転に伴って投入口27
から投入された非鉄ボールを強力な送風と共働して後方
に送り出す間欠らせん状の送り羽根28が付設されてい
る。
The polymer separator 22 consists of a sorting tube 24 that is rotatably supported in the horizontal axis direction and has open front and rear ends, and a discharge hood 26 installed horizontally so as to cover the rear end side of the sorting tube 24. An inlet 27 is formed on the inner periphery of the front half of the cylinder 24 as it rotates.
An intermittent spiral sending blade 28 is attached which sends out the non-ferrous balls thrown in backwards in cooperation with a powerful air blower.

選別筒24の後半部周壁には、送風によって送り出され
る非鉄ボール21の比重の高いもの(金属ボール)を局
外に排出するための選別孔28が多数穿設されており、
比重の低いプラスチック等の非金属ボールは風圧によっ
て排出フード26より後方に送り出され、プラスチック
と金属が分別される。
A large number of sorting holes 28 are bored in the peripheral wall of the rear half of the sorting tube 24 for discharging non-ferrous balls 21 having a high specific gravity (metal balls) sent out by air blowing.
Non-metallic balls such as plastic having a low specific gravity are sent rearward from the discharge hood 26 by wind pressure, and plastic and metal are separated.

29は選別筒24より排出された金属ボールを非鉄金属
ンユート・定量供給装置31に送り込むコンベアである
。図示した高分子選別機は一般にトロンメルと称される
ものであるか、この他磁界を用いたノニア式又は振動に
よるふるい分は若しくはこれらを粘合して用いる場合も
ある。
29 is a conveyor that sends the metal balls discharged from the sorting cylinder 24 to the non-ferrous metal unit/quantity supply device 31. The illustrated polymer separator is generally called a trommel, or may use a nonier type using a magnetic field, a sieve using vibration, or a combination of these.

上記非鉄金属シュート・定量供給装置31に供給された
金属ポールは、選別コンベア32上に定量的に供給され
、選別コンベア32は搬送される金属ボールか人手によ
って選別が可能なように任意に起動停止できる構成とな
っており、ここではアルミウニュウム、銅、真鍮、ステ
ンレス鋼その他の残渣に分別され、利用価値の乏しい無
機物等の少量の残渣は埋立処分される。その他の分別回
収物は材質毎の貯留桝(図示しない)に収容されて資源
として回収される。
The metal poles supplied to the non-ferrous metal chute/quantitative supply device 31 are quantitatively supplied onto a sorting conveyor 32, and the sorting conveyor 32 is started and stopped at will so that the metal balls being conveyed can be sorted manually. Here, residues such as aluminum, copper, brass, stainless steel, and others are separated, and small amounts of residues, such as inorganic substances with little utility, are disposed of in a landfill. Other separated and collected materials are stored in storage basins (not shown) for each material and collected as resources.

一方高分子遭別機22よりノ!別排出されたプラスチッ
クホールは、かさ比重を大きくする必要がある場合はコ
ンベア29よりプラスチック減容器33に投入されて減
容される。このプラスチック減容器33はプラスチック
ボールを投入して溶解減容する機構又は二軸スクリュ一
方式により加圧搬送する過程でその摩擦熱によって溶解
状態にして麺状にして押出す機構のもの等が使用され、
搬送コンベア34を介して貯留槽・定量供給装置35に
送られる。
Meanwhile, from Polymer Encounter Machine 22! If it is necessary to increase the bulk specific gravity, the separately discharged plastic holes are put into a plastic reducing container 33 from the conveyor 29 and reduced in volume. This plastic reduction container 33 has a mechanism that melts and reduces the volume by inserting plastic balls, or a mechanism that uses frictional heat to melt the plastic balls and extrude them into a noodle shape during pressurized conveyance using one type of twin screw screw. is,
It is sent to a storage tank/quantitative supply device 35 via a conveyor 34.

上記プラスチック減容器33は次工程のプラスチック材
の性質又は次工程の熱分解反応炉36の処理能力との関
係で必ずしも必要ない場合もある。
The plastic reduction container 33 may not necessarily be necessary depending on the properties of the plastic material in the next step or the processing capacity of the pyrolysis reactor 36 in the next step.

上記貯留槽・定量供給装置35では搬送コンベア35が
送られたプラスチック材を貯留するとともに、第5図に
示す熱分解反応炉36に、その処理能力に応じて定量的
に貯留プラスチックを供給する。熱分解(接触)反応炉
36はプラスチック類を加熱してガス状に熱分解する公
知の装置で、システムI(又はシステム■)で処理され
たプラスチックが、脱水機付の粉砕機43に導入されて
小粒子に粉砕され、粉砕機43下方の熱風発生機で発生
した熱風とともに送風機46によってホッパー41に投
入され、ブラスチック粉砕粒子はホッパー41の下方の
熱分解炉42でガス状に熱分解される。上記熱風供給は
熱分解炉42内の温度降下を防止するためのものである
The storage tank/quantitative supply device 35 stores the plastic material sent by the conveyor 35, and supplies the stored plastic quantitatively to the pyrolysis reactor 36 shown in FIG. 5 according to its processing capacity. The pyrolysis (contact) reactor 36 is a known device that heats plastics to pyrolyze them into a gaseous state, and the plastics treated in System I (or System ■) are introduced into a crusher 43 equipped with a dehydrator. The crushed plastic particles are pulverized into small particles by a blower 46 together with hot air generated by a hot air generator below the pulverizer 43, and then put into a hopper 41 by a blower 46. Ru. The above-mentioned hot air supply is for preventing the temperature inside the pyrolysis furnace 42 from dropping.

また熱分解炉42の下方にはバーナー45付の加熱炉5
0が付設され、熱分解炉42を外部から加熱する事によ
り熱分解反応を行わせる機構となっている。
Further, below the pyrolysis furnace 42 is a heating furnace 5 equipped with a burner 45.
0 is attached, and the pyrolysis furnace 42 is heated from the outside to perform a pyrolysis reaction.

そして熱分解炉42内で分解されない少量の貴金属、無
機質等は有価物含有残渣として熱分解炉42の底部より
取出されて資源として回収される。
A small amount of precious metals, inorganic substances, etc. that are not decomposed in the pyrolysis furnace 42 are taken out from the bottom of the pyrolysis furnace 42 as a residue containing valuables and recovered as resources.

熱分解炉42で分解されたガスは、内部に金属触媒を内
蔵し冷却装置を兼ねたコンデンサー47に送られて金属
触媒と作用するとともに循環水の作用で冷却され、沸点
の低い揮発性のガス、例えばガソリン系のガス等のガス
が分離されて吸収塔48に導かれ、ここで固体微粒子等
の異物を分離し、水を貯留した中和槽49に導かれて中
和処理される。
The gas decomposed in the thermal decomposition furnace 42 is sent to the condenser 47, which has a built-in metal catalyst and also serves as a cooling device, where it interacts with the metal catalyst and is cooled by the action of circulating water, producing volatile gas with a low boiling point. A gas such as gasoline-based gas is separated and guided to an absorption tower 48, where foreign substances such as solid particles are separated, and then led to a neutralization tank 49 storing water for neutralization treatment.

またコンデンサー47より分離排出された液体は油水分
離槽51にて油性分と水に分離され、油性分(灯油状の
油)はポンプ′52により地下の貯油タンク53に送ら
れて貯留される。他方油水分離槽51で分離された塩素
を含む水分は中和装置54を経て中和槽49に導かれる
。油水分離槽51で分離された一部少量のガスは加水微
爆燃焼装置55に送られて焼却処理される。
The liquid separated and discharged from the condenser 47 is separated into an oily component and water in an oil-water separation tank 51, and the oily component (kerosene-like oil) is sent to an underground oil storage tank 53 by a pump '52 and stored therein. On the other hand, the water containing chlorine separated in the oil-water separation tank 51 is led to the neutralization tank 49 via the neutralization device 54. A small amount of the gas separated in the oil-water separation tank 51 is sent to the hydrating micro-explosive combustion device 55 and incinerated.

前記中和槽49て中和されたガソリン系等のガスはガス
ホルダー56を経てガスタンク57に導かれ貯留され、
バーナー45の燃料として利用される。
Gas such as gasoline neutralized in the neutralization tank 49 is led to a gas tank 57 via a gas holder 56 and stored therein.
It is used as fuel for the burner 45.

一般に材質が一定で大量に発生する廃プラスチックは再
生利用が可能であり且つ加熱分解によらない処理もでき
るが、廃棄物中に含まれる廃プラスチックは多種類のプ
ラスチックの混合物であるため、上記の加熱分解で油化
又はガス化してエネルギー源として利用する事が最も有
効であり且つ減量効果及び環境に与える影響も少なくて
すむ。
In general, waste plastics of a certain material that are generated in large quantities can be recycled and treated without thermal decomposition, but since the waste plastics contained in waste are a mixture of many types of plastics, the above-mentioned It is most effective to turn it into oil or gas through thermal decomposition and use it as an energy source, and it also has a reduced weight loss effect and less impact on the environment.

貯留タンク53に貯留された油性分は燃料タンク59に
導かれて本発明の方法の実施に用いるディーゼル自家発
電装置6Iにおいて燃料として利用され、発生電力は分
電設@62を介して本発明の諸装置の駆動用設備電源と
して利用され、設備全体の電力を調達するものである。
The oil content stored in the storage tank 53 is led to the fuel tank 59 and used as fuel in the diesel private power generation device 6I used for implementing the method of the present invention, and the generated power is sent to the various methods of the present invention via the distribution facility @62. It is used as the equipment power source for driving the equipment and procures power for the entire equipment.

また設備用電源燃料として利用した残りの剰余油あ燃料
として資源回収され、他の用途に利用できる。
In addition, the remaining oil used as power source fuel for equipment can be recovered as a resource and used for other purposes.

次に一般不燃ゴミを処理するシステムHについて説明す
ると、通常地方の中核都市及びその近郊の平均的不燃ゴ
ミの組成は概ね次表の通りである。
Next, System H for processing general non-combustible garbage will be explained. The composition of average non-combustible garbage in the core cities of the regions and their suburbs is generally as shown in the following table.

第1表 このうちプラスチック類と残渣を除いては従来から選別
分類されて再資源化されているが、本実施例ではシステ
ム■をシステム■に結合する事によりプラスチック類を
資源化して再利用するものである。
Table 1 Of these, except for plastics and residue, conventionally they are sorted and classified and recycled, but in this example, by combining system ■ with system ■, plastics will be recycled and recycled. It is something.

不燃ゴミ搬入ステージ71に搬入された梱包又は袋詰め
された不燃ゴミは、第6図に示す投入ホッパー72に投
入され、これと直結したエプロンコンベア73によって
次の破袋コンベア74に送られる。
The packaged or bagged noncombustible garbage carried into the noncombustible garbage carry-in stage 71 is put into the input hopper 72 shown in FIG. 6, and sent to the next bag-breaking conveyor 74 by an apron conveyor 73 directly connected thereto.

またガラス瓶(生ピン)、ダンボール以外の紙等のよう
にそのまま利用又は回収できるものは通常別個に持ち込
まれるのでそのまま資源として回収される。
Additionally, items that can be used or collected as they are, such as glass bottles (raw pins) and paper other than cardboard, are usually brought in separately and are collected as resources.

破袋コンベア74ではコンベア両側に配置された作業員
により、梱包2袋詰めを破袋解体し、各作業員がプラス
チック類、ダンボール及び紙屑類を分類して拾い出し、
ダンボールは古紙プレス機75にかけて輸送及び保管コ
ストを低減すべく圧縮梱包する。
On the bag-breaking conveyor 74, workers placed on both sides of the conveyor break and disassemble the two packages, and each worker sorts and picks out plastics, cardboard, and paper waste.
The cardboard is compressed and packaged by a waste paper press 75 to reduce transportation and storage costs.

上記工程で分類された混合プラスチックは二軸式剪断機
76によって繰り返し切断され、熱分解に適した約5c
x位の大きさに形成された後、システム■において説明
した貯留槽・定量供給装置35に送られ、さらに熱分解
反応炉36において既に述べた方法により油化又はガス
化されて再利用される。
The mixed plastic classified in the above process is repeatedly cut by a twin-screw shearing machine 76, and the mixed plastic is cut into approximately 5cm pieces suitable for pyrolysis.
After it is formed into a size of x, it is sent to the storage tank/quantity supply device 35 described in system (2), and then converted into oil or gas by the method already described in the pyrolysis reactor 36 and reused. .

剪断機は回転式ハンマーでも良い。The shearing machine may be a rotary hammer.

破袋コンベア74で分別された紙類及びプラスチック類
以外のもののうち、回収可能なものはそのまま分類回収
するが、それ以外のものはシステムIで説明した磁選機
17と同様な磁選機77によって鉄系の廃棄物と非鉄系
の廃棄物に選別し、鉄系のものは鉄屑貯留例78に貯留
して資源回収する。
Among the items other than paper and plastics that are separated by the bag-breaking conveyor 74, those that can be collected are sorted and collected as is, but other items are separated by a magnetic separator 77 similar to the magnetic separator 17 described in System I. They are sorted into iron-based waste and non-ferrous waste, and ferrous waste is stored in iron scrap storage example 78 for resource recovery.

磁選機77に選別された残りの廃棄物は近傍に作業員を
配した選別コンベア79に送られ、アルミニウムその他
の非鉄金属、白(透明)、茶、混合色のカレット(ガラ
ス)等に人手により分別し、ガラス類はそれぞれの貯留
例81に貯留され資源として回収される。また比較的量
の多いアルミニウムはアルミプレス機82で圧縮固化さ
れて資源として回収される。上記以外の残渣は選別コン
ベア79上から残渣貯留例83に貯留され埋立処分され
る。
The remaining waste sorted by the magnetic separator 77 is sent to a sorting conveyor 79 with workers nearby, where it is manually sorted into aluminum and other nonferrous metals, white (transparent), brown, mixed-color cullet (glass), etc. The glasses are separated and stored in respective storage examples 81 and recovered as resources. Further, a relatively large amount of aluminum is compressed and solidified by an aluminum press machine 82 and recovered as a resource. Residues other than those mentioned above are stored in a residue storage example 83 from the sorting conveyor 79 and disposed of in a landfill.

なお、上記実施例なおけるディーゼル自家発電装置の代
わりにプラスチック分解より生じたガスや油を燃料とす
るボイラー等によって発電機を作動させ、自家発電を行
わせることも可能である。
Note that instead of the diesel private power generation device in the above embodiment, it is also possible to operate the generator using a boiler or the like that uses gas or oil generated from plastic decomposition as fuel to perform private power generation.

〈発明の効果〉 以上の如く構成される本発明の方法によれば、産業廃棄
物か、生活廃棄物かを問わず、金属やプラスチックを含
む多くの廃棄物の処理に当たり、従来のように広大な埋
立地や埋立のための運送費を必要とせず、大量の廃棄物
を焼却するための焼却設備やその用地が不要となるばか
りでなく、多量のプラスチックの焼却による大気汚染等
の環境問題等も発生しないという利点を生じ、さらに−
旦設備を備えればその運転は廃棄物をエネルギー源とし
た自家発電により電力調達が出来るので、処理のエネル
ギーコストが著しく軽減できる。
<Effects of the Invention> According to the method of the present invention configured as described above, it is possible to treat a large amount of waste, including metals and plastics, regardless of whether it is industrial waste or domestic waste. Not only does it eliminate the need for landfill sites and transportation costs for landfills, it also eliminates the need for incineration equipment and land for incinerating large amounts of waste, as well as environmental problems such as air pollution caused by incinerating large amounts of plastic. It also has the advantage that -
Once the equipment is installed, it can be operated using electricity generated by in-house power generation using waste as an energy source, which can significantly reduce energy costs for treatment.

特に本方法においては僅かな廃棄物残渣を除いてはその
殆どが有価物としての資源回収システムであるため、著
しい環境破壊を伴う大量の焼却や埋立を中心とするいわ
ゆる「廃棄物処理事業」とは見なされず、廃棄物処理設
備のような厳しい法的規制を受けることもなく、設備の
設置条件も大幅に緩和されるという利点を有するもので
ある。
In particular, in this method, except for a small amount of waste residue, most of it is a resource recovery system as valuable materials, so it is not a so-called "waste treatment business" that mainly involves incineration or landfilling of large amounts of waste, which causes significant environmental damage. It has the advantage that it is not subject to strict legal regulations like waste treatment facilities, and the conditions for installing the facility are significantly relaxed.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明の作業工程を示すフロシート、第2図は
処理設備の一部である造粒機の断面図、第3図は同じく
磁選機の原理図、第4図は高分子選別機の原理図、第5
図は同じく熱分解接触反応炉、第6図は投入ホッパーと
エプロンコンベアの平面図である。 粗大物処理システム 不燃ゴミ処理システム プラスチック処理システム 熱分解接触反応炉 ディーゼル自家発電装置 第 図 第 図 第 4 図 第 図 第 図 1
Figure 1 is a flow sheet showing the working process of the present invention, Figure 2 is a cross-sectional view of a granulator, which is part of the processing equipment, Figure 3 is a principle diagram of a magnetic separator, and Figure 4 is a polymer separator. Principle diagram, 5th
The same figure shows the pyrolysis contact reactor, and FIG. 6 is a plan view of the charging hopper and apron conveyor. Bulky material processing system Non-combustible garbage processing system Plastic processing system Pyrolysis contact reactor Diesel private power generator Fig. Fig. 4 Fig. Fig. 1

Claims (1)

【特許請求の範囲】[Claims] 固体廃棄物を一連の処理設備と工程により金属と非金属
に分別処理し、さらに該工程中で非金属中よりプラスチ
ックを分離して処理するとともに処理された結果物を有
価資源として回収する方法において、上記処理設備中に
、熱分解反応炉と燃焼機関で作動する自家発電装置を設
け、廃棄物中のプラスチックを熱分解反応炉で分解して
ガス化又は液化してこれらの分解ガス又は分解液を前記
燃焼機関の燃料として自家発電を行わせ、該自家発電に
より処理設備の電力を調達することを特徴とする廃棄物
の処理及び資源回収方法。
A method of separating solid waste into metals and non-metals using a series of processing equipment and processes, further separating and processing plastics from the non-metals during the process, and recovering the processed products as valuable resources. , A private power generation device operated by a pyrolysis reactor and a combustion engine is installed in the above processing equipment, and the plastics in the waste are decomposed in the pyrolysis reactor and gasified or liquefied to produce these decomposed gases or decomposed liquids. A method for processing waste and recovering resources, characterized in that the combustion engine is used as fuel to generate in-house power, and the in-house power generation supplies electricity for a treatment facility.
JP1319725A 1989-12-08 1989-12-08 Treatment of waste and resource recovering method Pending JPH03181379A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1319725A JPH03181379A (en) 1989-12-08 1989-12-08 Treatment of waste and resource recovering method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1319725A JPH03181379A (en) 1989-12-08 1989-12-08 Treatment of waste and resource recovering method

Publications (1)

Publication Number Publication Date
JPH03181379A true JPH03181379A (en) 1991-08-07

Family

ID=18113475

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1319725A Pending JPH03181379A (en) 1989-12-08 1989-12-08 Treatment of waste and resource recovering method

Country Status (1)

Country Link
JP (1) JPH03181379A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08267455A (en) * 1995-03-31 1996-10-15 Hitachi Ltd Waste treatment equipment
WO2001089730A3 (en) * 2000-05-22 2002-03-14 Metso Paper Inc Method for processing waste and waste processing plant
JP2008073634A (en) * 2006-09-22 2008-04-03 Sharp Corp Recycling method of waste microwave oven
CN109500052A (en) * 2018-10-19 2019-03-22 章琴 A kind of Biohazard Waste recycling and processing device

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5768522A (en) * 1980-10-15 1982-04-26 Tsukishima Kikai Co Ltd Electric power generating method in solid waste treatment

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5768522A (en) * 1980-10-15 1982-04-26 Tsukishima Kikai Co Ltd Electric power generating method in solid waste treatment

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08267455A (en) * 1995-03-31 1996-10-15 Hitachi Ltd Waste treatment equipment
WO2001089730A3 (en) * 2000-05-22 2002-03-14 Metso Paper Inc Method for processing waste and waste processing plant
JP2008073634A (en) * 2006-09-22 2008-04-03 Sharp Corp Recycling method of waste microwave oven
CN109500052A (en) * 2018-10-19 2019-03-22 章琴 A kind of Biohazard Waste recycling and processing device

Similar Documents

Publication Publication Date Title
CN101632994B (en) Totally-closed automatic crushing and sorting technical device of domestic garbage and resource-based product production
US20180015515A1 (en) A novel method and an apparatus in converting unsorted municipal solid waste into geo-polymer pellets/briquettes and geo-polymer bricks/paver blocks
KR101785217B1 (en) Screening methods and screening systems for municipal waste into fuel and combustible waste landfill
CN108273827B (en) An integrated domestic waste treatment system and method with high sorting accuracy
JP2019155319A (en) Metal separation from shredder dust and fuel formation of organic combustible residue, effective utilization method of inorganic residue and its treatment device
KR102218865B1 (en) Methods and systems for selection of compression cut-fracture for fueling combustible waste
GB2445465A (en) Municipal waste treatment
BR112014004919B1 (en) SYSTEM AND METHOD FOR PROCESSING MIXED SOLID WASTE
JP3476439B2 (en) Solid waste fuel conversion plant
KR100310406B1 (en) Process and system for recycling of household waste
US6152306A (en) Solid waste reduction
KR102495589B1 (en) Renewable and composting system for municipal solid waste
JP3580098B2 (en) Fuel production method from waste
CN111019675A (en) Domestic waste treatment system and method
CN102205342A (en) Device for comprehensively treating electronic garbage
CN101658855A (en) Integrated machine for sorting domestic garbage
JPH03181379A (en) Treatment of waste and resource recovering method
JP2892639B1 (en) Municipal garbage decontamination treatment plant
KR102344255B1 (en) Method for manufacturing powder regenerative fuels using petrochemical waste and combustible powder production apparatus thereof
JPH06226242A (en) Treating system and treating device for waste household electrical appliances and office automatic equipment
Fitzgerald et al. Technical and economic analysis of pre-shredding municipal solid wastes prior to disposal
KR100400191B1 (en) the method and equipment of sorting controls for construction waste Environment friendship
JPH1177013A (en) Pollution-free regeneration treatment plant for waste
JP2002220594A (en) Solid fuel conversion facility deodorization method and solid fuel conversion facility
JP2865541B2 (en) Method and apparatus for sorting and molding combustibles in waste