JP3024745B2 - Solid fuel conversion system for combustible waste including garbage - Google Patents
Solid fuel conversion system for combustible waste including garbageInfo
- Publication number
- JP3024745B2 JP3024745B2 JP35889196A JP35889196A JP3024745B2 JP 3024745 B2 JP3024745 B2 JP 3024745B2 JP 35889196 A JP35889196 A JP 35889196A JP 35889196 A JP35889196 A JP 35889196A JP 3024745 B2 JP3024745 B2 JP 3024745B2
- Authority
- JP
- Japan
- Prior art keywords
- combustible waste
- combustible
- solid fuel
- combustibles
- waste
- 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
Links
- 239000010849 combustible waste Substances 0.000 title claims description 47
- 239000010813 municipal solid waste Substances 0.000 title claims description 21
- 239000004449 solid propellant Substances 0.000 title claims description 21
- 238000006243 chemical reaction Methods 0.000 title description 4
- 238000000465 moulding Methods 0.000 claims description 18
- 239000006148 magnetic separator Substances 0.000 claims description 12
- 239000000126 substance Substances 0.000 claims description 10
- 239000000654 additive Substances 0.000 claims description 9
- 230000000996 additive effect Effects 0.000 claims description 9
- 238000001035 drying Methods 0.000 claims description 9
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 claims description 8
- 229910001861 calcium hydroxide Inorganic materials 0.000 claims description 8
- 235000011116 calcium hydroxide Nutrition 0.000 claims description 8
- 239000000920 calcium hydroxide Substances 0.000 claims description 8
- 239000002699 waste material Substances 0.000 claims description 7
- 239000000463 material Substances 0.000 description 29
- 239000000428 dust Substances 0.000 description 9
- 239000002184 metal Substances 0.000 description 8
- 229910052751 metal Inorganic materials 0.000 description 8
- 238000011038 discontinuous diafiltration by volume reduction Methods 0.000 description 7
- 239000007789 gas Substances 0.000 description 7
- 239000000696 magnetic material Substances 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 238000005192 partition Methods 0.000 description 4
- 239000000460 chlorine Substances 0.000 description 3
- 238000002485 combustion reaction Methods 0.000 description 3
- 230000001877 deodorizing effect Effects 0.000 description 3
- 239000004576 sand Substances 0.000 description 3
- 101150076749 C10L gene Proteins 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 229910052801 chlorine Inorganic materials 0.000 description 2
- 239000010806 kitchen waste Substances 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000013049 sediment Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 230000002195 synergetic effect Effects 0.000 description 2
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 2
- 229920002554 vinyl polymer Polymers 0.000 description 2
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000010791 domestic waste Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 239000002828 fuel tank Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000010348 incorporation Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 235000019645 odor Nutrition 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Classifications
-
- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
-
- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
-
- 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
- Y02W30/20—Waste processing or separation
Landscapes
- Processing Of Solid Wastes (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
Description
【0001】[0001]
【発明の属する技術分野】この発明は、主として家庭な
どから排出される生ごみを含む可燃性ごみの固形燃料化
装置に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for converting combustible waste, including garbage discharged mainly from homes, into solid fuel.
【0002】[0002]
【従来の技術】この種固形燃料化装置として、特開平7
−150158号を挙げることができる。これはごみや
汚泥などの廃棄物から固形燃料を製造する際の可燃物選
別成形装置において、廃棄物の収容袋の破袋機と、廃棄
物から磁性体金属を除去する磁選機と、磁性体金属を除
去された廃棄物を一次破砕する一次破砕機と、一次破砕
機を経由した廃棄物を乾燥する乾燥機と、乾燥機からで
た廃棄物から風力により可燃物と不燃物とに選別する風
力選別機と、風力選別された可燃物を二次破砕する二次
破砕機と、二次破砕後の可燃物を成形して固形燃料化す
る成形機と、からなる可燃物選別成形装置であり、これ
により、一般家庭から排出される生活ごみから、可燃物
と、磁性体、非磁性体に関係なくほとんどの金属類を不
燃物を外部に悪臭を発生することなく確実に選別すると
ともに、短時間かつ効率よく固形燃料を製造することが
できる、と記載されている。そして、(前記乾燥機とし
て特殊ロータリ式乾燥機を用いるとともに、)風力選別
機として内部循環型風力選別機を用いることが開示され
ている。2. Description of the Related Art Japanese Patent Application Laid-Open No.
No. -150158. This is a combustible material sorting and molding device for producing solid fuel from waste such as garbage and sludge.It is a machine that breaks bags containing waste, a magnetic separator that removes magnetic metal from waste, and a magnetic separator. A primary crusher for primary crushing waste from which metals have been removed, a dryer for drying waste that has passed through the primary crusher, and sorting of combustibles and non-combustibles by wind from the waste from the dryer It is a combustible material sorting and molding device comprising a wind separator, a secondary crusher for secondary crushing the combustible material subjected to the wind crushing, and a molding machine for molding the combustible material after the secondary crushing into a solid fuel. This ensures that most metals, regardless of whether they are combustibles, magnetic or non-magnetic materials, are separated from household waste discharged from ordinary households without any inconvenient odors. Solid fuel can be manufactured in a timely and efficient manner , It has been described as. It is disclosed that an internal circulation type wind separator is used as a wind separator (as well as a special rotary dryer is used as the dryer).
【0003】[0003]
【発明が解決しようとする課題】しかしながら、家庭な
どから排出される生ごみを含む可燃性ごみの中に廃棄さ
れる植木や観用植物に付着した土砂および庭掃除したご
みのなかにも土砂が多く含まれている。このようなごみ
を内部循環型風力選別機で可燃物と不燃物とに選別する
と、不燃物である土砂は細かくて軽量であることから、
風力によって可燃物側に選別されることとなり、可燃物
の純度が低下してしまうという問題がある。However, sediment attached to plant and ornamental plants discarded in combustible waste including garbage discharged from homes and the like, and sediment also adhered to garbage cleaned in the garden. Many are included. When such garbage is separated into combustibles and incombustibles by an internal circulation type wind separator, the non-combustible earth and sand is fine and lightweight,
There is a problem that the flammable material is sorted by the wind force and the purity of the flammable material is reduced.
【0004】この発明は、前記問題を改良するためにな
したものであり、可燃物から不燃物を確実に除去し、可
燃物の純度を大幅に向上することができる可燃性ごみの
固形燃料化装置を提供することを目的とするものであ
る。SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned problem, and it has been proposed to convert combustible waste into solid fuel which can surely remove incombustibles from combustibles and greatly improve the purity of combustibles. It is intended to provide a device.
【0005】[0005]
【課題を解決するための手段】上記の課題を解決するた
めに、この発明の生ごみを含む可燃性ごみの固形燃料化
装置は、可燃性ごみを破袋する破袋機と、破袋された可
燃性ごみを破砕する破砕機と、破砕された可燃性ごみを
乾燥する乾燥機と、乾燥された可燃性ごみ中の磁性物を
除去する磁選機と、磁性物が除去された可燃性ごみを風
力により浮上する可燃物と篩下物の不燃物と篩上物の不
燃物とに選別する風力併用型振動篩機と、可燃物を捕集
する捕集機と、可燃物を減容成形して固形燃料とする減
容成形機と、消石灰を前記減容成形機に供給する添加剤
供給機と、からなることである。In order to solve the above-mentioned problems, a solid fuel converting apparatus for combustible waste including garbage according to the present invention is provided with a bag-breaking machine for breaking the combustible waste and a bag-breaking machine. Crusher for crushing combustible waste, dryer for drying crushed combustible waste, magnetic separator for removing magnetic substances in dried combustible waste, and combustible waste from which magnetic substances have been removed The wind
Combustibles and non-combustible materials that float due to force
Combined wind-type vibrating sieve for separating into combustibles, collector for collecting combustibles, volume-reducing molding machine for reducing the volume of combustibles into solid fuel, and the volume-reducing molding machine for slaked lime And an additive supply device for supplying the additive.
【0006】[0006]
【発明の実施の形態】この発明は、可燃性ごみを破袋す
る破袋機と、破袋された可燃性ごみを破砕する破砕機
と、破砕された可燃性ごみを乾燥する乾燥機と、乾燥さ
れた可燃性ごみ中の磁性物を除去する磁選機と、磁性物
が除去された可燃性ごみを風力により浮上する可燃物と
篩下物の不燃物と篩上物の不燃物とに選別する風力併用
型振動篩機と、可燃物を捕集する捕集機と、可燃物を減
容成形して固形燃料とする減容成形機と、消石灰を前記
減容成形機に供給する添加剤供給機と、から構成され
る。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a bag breaking machine for breaking combustible waste, a crusher for breaking bag-burned combustible waste, and a dryer for drying crushed combustible waste. A magnetic separator that removes magnetic substances from dried combustible waste, and a combustible substance that floats combustible waste from which magnetic substances have been removed by wind power
Combined wind-type vibrating sieve that separates non-combustible material and non-combustible material on the sieve , collector for combustible material, volume reduction of combustible material, volume reduction to solid fuel by molding It comprises a molding machine and an additive supply machine for supplying slaked lime to the volume reducing molding machine.
【0007】そして、袋詰めされた水分を含んだ厨芥
(生ごみ)などの可燃性ごみは破袋機で破袋され、破袋
された可燃性ごみは破砕機で破砕され、破砕された可燃
性ごみは乾燥機で所定水分まで乾燥され、乾燥された可
燃性ごみ中の磁性物は磁選機により除去され、磁性物が
除去された可燃性ごみは風力併用型振動篩機に供給さ
れ、可燃物と不純物とに選別される。すなわち、不燃物
は振動篩機の多孔板から落下する篩下物と落下しない篩
上物として回収され、可燃物は前記多孔板の下方から吹
き上げる空気により浮上し、捕集機に吸引捕集される。
前記捕集された可燃物は、添加剤供給装置からの消石灰
とともに減容成形機に供給され、該減容成形機において
圧縮減容され、この過程で混在する樹脂の軟化溶融によ
るバインダーとなって棒状などに成形されて固形燃料と
なる。固形燃料に消石灰を予め添加しておくことによっ
て、該固形燃料の燃焼時に発生する塩素などの有害ガス
を反応により中和させ無害化することができる。[0007] The combustible waste such as kitchen garbage (garbage) containing water packed in a bag is broken by a bag breaker, and the combustible waste thus broken is crushed by a crusher, and the crushed combustible waste is crushed. The garbage is dried to a predetermined moisture level by a dryer, and the magnetic material in the dried flammable garbage is removed by a magnetic separator, and the flammable garbage from which the magnetic material has been removed is supplied to a vibrating sieve combined with a wind power for flammability. And impurities. In other words, incombustibles are collected as sifters falling from the perforated plate of the vibrating sieve and unsieved uppers not falling, and combustibles are lifted by air blown from below the perforated plate, and are suction-collected by the collector. You.
The collected combustibles are supplied to a volume reduction molding machine together with slaked lime from an additive supply device, and are compressed and reduced in the volume reduction molding machine, and become a binder due to softening and melting of mixed resin in this process. It is shaped into a rod or the like and becomes a solid fuel. By adding slaked lime to the solid fuel in advance, harmful gases such as chlorine generated during combustion of the solid fuel can be neutralized by the reaction and made harmless.
【0008】また、前記乾燥機と前記磁選機との間に乾
燥された可燃性ごみを解砕する解砕機を設ける。そし
て、水分を多量に含む可燃性ごみの場合、乾燥機での乾
燥過程で可燃性ごみの一部が塊(だんご)状のまま排出
されるが、このような塊(だんご)状の可燃性ごみを解
砕機で解砕(解き解し)することにより、その後の磁性
物の回収や、可燃物と不燃物との選別が容易となる。Further, a crusher for crushing the dried combustible waste is provided between the dryer and the magnetic separator. In the case of combustible waste containing a large amount of water, a part of the combustible waste is discharged as lump (dango) during the drying process in the dryer. By crushing (disintegrating) the refuse with a crusher, it is easy to collect the magnetic material thereafter and to separate the combustible material from the non-combustible material.
【0009】[0009]
【実施例】本発明の実施例について図面を参照して説明
する。図1〜3において、2は厨芥を含む可燃性ごみの
受入れホッパ1を有する搬送コンベヤ、3は破袋機、4
は搬送コンベヤ、5は金属検知器、6は破砕機で、例え
ば剪断式一軸破砕機や衝撃式破砕機、7は搬送コンベ
ヤ、8は乾燥機で、例えばロータリドライヤー、9は搬
送コンベヤ、10は解砕機で、例えばチェンミル、11
は搬送コンベヤ、12は磁力選別機、13は風力併用型
振動篩機で、14は可燃物捕集機で、例えばサイクロン
およびバグフィルタ(サイクロン付集塵機)、15は搬
送コンベヤ、16は消石灰などの添加剤供給機、17は
容成形機で、例えば二軸式減容押出成形機および18は
搬送コンベヤである。磁力選別機12は図示例のドラム
形の他ベルト形でもよい。Embodiments of the present invention will be described with reference to the drawings. 1 to 3, reference numeral 2 denotes a conveyor having a hopper 1 for receiving combustible waste including kitchen waste, 3 denotes a bag breaker,
Is a conveyor, 5 is a metal detector, 6 is a crusher, for example, a shear type single-shaft crusher or impact crusher, 7 is a conveyor, 8 is a dryer, for example, a rotary dryer, 9 is a conveyor, 10 is a conveyor. In a crusher, for example, a chain mill, 11
Is a conveyor, 12 is a magnetic separator, 13 is a vibrating sieve combined with wind, 14 is a combustible collector, for example, a cyclone and a bag filter (a dust collector with a cyclone), 15 is a conveyor, and 16 is a slaked lime etc. An additive feeder 17 is a volume forming machine, for example, a twin-screw volume reducing extruder and 18 is a conveyor. The magnetic separator 12 may be a belt type in addition to the drum type shown in the drawing.
【0010】乾燥機8は、例えばロータリドライヤー本
体20、熱風発生炉21、燃料タンク22、燃焼ブロア
23、導管24、サイクロン25、循環ブロア26、分
岐導管27、ガスクーラ28および排風機29により構
成される。The dryer 8 comprises, for example, a rotary dryer body 20, a hot air generator 21, a fuel tank 22, a combustion blower 23, a conduit 24, a cyclone 25, a circulation blower 26, a branch conduit 27, a gas cooler 28, and a blower 29. You.
【0011】風力併用型振動篩機13は次のような構成
からなる。一端上部に供給口31と他端下部に排出口3
2を有するほぼ水平で横長な箱形本体30内に、上部室
33と下部室34とに二分するように多孔板35を設
け、箱型本体30をばね36を介して載置した機台37
上に、これら両間に斜めに設けた揺動レバー38とスプ
リング39により支持し、かつ、振動手段40により斜
め(図示の矢印)方向に振動するようになっている。こ
の振動手段40はモータ41、プーリ42および振動発
振機43からなるものである。44は下部室34を前部
室45と後部室46とに区画する仕切壁である。多孔板
35は前部室45に対応する供給口31直下の無孔部3
5aと、その下流側に形成した多数の小篩孔35bと、
後部室46に対応して形成した多数の大篩孔35cとか
らなっている。そして、小篩孔35bの孔径を7〜10
mm、大篩孔35cの孔径を15〜20mmとする。The vibrating sieve 13 combined with wind power has the following configuration. Supply port 31 at one upper end and discharge port 3 at the lower end
A perforated plate 35 is provided in a substantially horizontal and horizontally long box-shaped main body 30 having an upper chamber 33 and a lower chamber 34, and a machine base 37 on which the box-shaped main body 30 is mounted via a spring 36.
Above, it is supported by a swing lever 38 and a spring 39 which are provided diagonally between the two, and vibrates in a diagonal (arrow in the drawing) direction by vibrating means 40. The vibration means 40 comprises a motor 41, a pulley 42 and a vibration oscillator 43. A partition wall 44 partitions the lower chamber 34 into a front chamber 45 and a rear chamber 46. The perforated plate 35 is a non-porous portion 3 immediately below the supply port 31 corresponding to the front chamber 45.
5a, a large number of small sieve holes 35b formed on the downstream side thereof,
It comprises a number of large sieve holes 35c formed corresponding to the rear chamber 46. And, the pore size of the small sieve hole 35b is 7 to 10
mm and the diameter of the large sieve hole 35c is 15 to 20 mm.
【0012】47,48はそれぞれ前部室45および後
部室46の篩下物を排出する排出口である。49は送風
機で、配管50,51により前部室45,後部室46の
側面に形成した空気供給口52,53に接続される。5
4,55は空気調節用のバルブである。小篩孔35bを
通る空気の通過速度を大略10m/s、大篩孔35cを
通る空気の通過速度を大略20m/sに設定する。56
は箱型本体31の開口57を経て上部室33内にそれぞ
れに突出させた吸引口58を有する吸引フードで、図示
の場合4個であるが多孔板35の長さによって変更でき
る。吸引口58はスリツト状で多孔板35のほぼ全幅に
わたる長さである。また、吸引フード56は架台59の
スリーブ60に摺動自在に嵌装され、ボルト61によ
り、所定の位置で上下方向に動かないように固定され
る。したがって、吸引口58の位置は多孔板35の上方
で多孔板35との高さが調節されるようになっている。
62はフレキシブルチューブである。Reference numerals 47 and 48 denote outlets for discharging the sieves in the front chamber 45 and the rear chamber 46, respectively. A blower 49 is connected to air supply ports 52 and 53 formed on the side surfaces of the front chamber 45 and the rear chamber 46 by pipes 50 and 51. 5
Reference numerals 4 and 55 denote valves for adjusting air. The passing speed of the air passing through the small sieve hole 35b is set to approximately 10 m / s, and the passing speed of the air passing through the large sieve hole 35c is set to approximately 20 m / s. 56
Is a suction hood having suction ports 58 respectively protruding into the upper chamber 33 through the opening 57 of the box-shaped main body 31. In the illustrated case, the number of the suction hoods is four. The suction port 58 has a slit-like length and extends over almost the entire width of the perforated plate 35. Further, the suction hood 56 is slidably fitted to the sleeve 60 of the gantry 59 and is fixed by a bolt 61 so as not to move in a vertical direction at a predetermined position. Accordingly, the position of the suction port 58 is adjusted above the perforated plate 35 above the perforated plate 35.
62 is a flexible tube.
【0013】各フード56は導管63を経て捕集機14
に接続される。捕集機14は、前部側のサイクロン部6
4と後部側の集塵部65とが一体のサイクロン付集塵機
で、サイクロン部64に導管63が接続され、集塵部6
5に導管66を経て排風機67および導管68を経て脱
臭装置69が接続される。なお、捕集機14は前記のよ
うに一体型のものとすることによりコンパクトとなる
が、独立したサイクロンと集塵機であってもよい。Each hood 56 is connected to a collector 14 via a conduit 63.
Connected to. The trap 14 is a cyclone unit 6 on the front side.
4 and a dust collector 65 on the rear side are an integrated dust collector with a cyclone. A conduit 63 is connected to the cyclone 64 and a dust collector 6 is provided.
5 is connected to an exhaust fan 67 via a conduit 66 and a deodorizing device 69 via a conduit 68. The collector 14 is made compact by being integrated as described above, but may be an independent cyclone and a dust collector.
【0014】前記実施例において、ビニール等に袋詰め
された厨芥を含む可燃性ごみを受入れホッパ1に投入
し、搬送コンベヤ2により、破袋機3に供給して破袋す
る。破袋された可燃性ごみを搬送コンベヤ4の搬送途中
で、金属検知器5により鉄類や非鉄金属の存在を検知し
て、これを人手により取り除く。金属が除かれた可燃性
ごみは搬送コンベヤ4を経て、破砕機6に供給され破砕
される。破砕された可燃性ごみは搬送コンベヤ7を経
て、乾燥機8に供給され、所定水分(20%程度)にな
るまで乾燥される。すなわち、破砕された可燃性ごみ
は、熱風発生炉21を経てをロータリドライヤー本体2
0内に供給される熱風(400〜500℃)により水分
を蒸発させて乾燥される。蒸発水分はガスとともに、循
環ブロア26により導管24、サイクロン25を経て、
熱風発生炉21に環流され再び加熱される。このように
熱風は高温度かつ高湿度であることから、可燃性ごみは
直接乾燥であっても燃えることなく乾燥される。なお、
前記乾燥により発生する蒸発水分を含むガスの一部は、
排風機29により分岐導管27を経て、ガスクーラ28
で冷却され、脱臭装置75により脱臭され排出される。In the above embodiment, combustible waste containing kitchen waste packed in a bag such as vinyl is put into a receiving hopper 1 and supplied to a bag breaker 3 by a conveyor 2 to break the bag. In the course of transporting the opened combustible waste by the transport conveyor 4, the presence of iron or non-ferrous metal is detected by the metal detector 5 and removed by hand. The combustible waste from which the metal has been removed is supplied to a crusher 6 via a conveyor 4 and crushed. The crushed combustible waste is supplied to the dryer 8 via the conveyor 7 and is dried until it reaches a predetermined moisture level (about 20%). That is, the crushed combustible waste passes through the hot-air generating furnace 21 and passes through the rotary dryer main body 2.
The water is evaporated by hot air (400 to 500 ° C.) supplied to the inside and dried. Evaporated moisture is passed through the conduit 24 and the cyclone 25 by the circulation blower 26 together with the gas.
It is returned to the hot-air generating furnace 21 and is heated again. Since the hot air has a high temperature and a high humidity, the combustible waste is dried without burning even if it is directly dried. In addition,
Part of the gas containing evaporated water generated by the drying,
The gas cooler 28 passes through a branch conduit 27 by an exhaust fan 29.
And is deodorized and discharged by the deodorizing device 75.
【0015】乾燥された可燃性ごみは搬送コンベヤ9を
経て、解砕機10に供給され解砕される。解砕機10は
水分を多量に含む生ごみ主体の可燃性ごみを乾燥する場
合に有効である。すなわち乾燥機8としてロータリドラ
イヤーを使用すると、回転乾燥過程で可燃性ごみの一部
が塊(だんご)状となって排出されることがある。この
ような可燃性ごみを解砕(解き解し)することによっ
て、その後の磁性物の回収や、可燃物と不燃物との選別
を容易にする利点があるが、生ごみ多く含まない可燃性
ごみであれば省略することができる。解砕された可燃性
ごみを搬送コンベヤ11を経て風力併用型振動篩機13
への搬送途中で、前記搬送コンベヤ4上で取り切れなか
った残余の磁性物を磁力選別機12により除去する。The dried combustible waste is supplied to a crusher 10 via a conveyor 9 and crushed. The crusher 10 is effective when drying combustible waste mainly composed of garbage containing a large amount of water. That is, when a rotary drier is used as the dryer 8, a part of the combustible waste may be discharged as a lump (dango) in the rotation drying process. Disintegrating (disintegrating) such combustible waste has the advantage of facilitating the subsequent recovery of magnetic materials and the separation of combustibles and non-combustibles. If it is garbage, it can be omitted. The crushed combustible waste is passed through a conveyor 11 and combined with a wind-driven vibrating sieve 13
In the course of the transfer to the conveyor, the remaining magnetic substances that cannot be removed on the transfer conveyor 4 are removed by a magnetic separator 12.
【0016】磁性物が除去された可燃性ごみを風力併用
型振動篩機13に投入し、ここで可燃物と不燃物とに選
別する。すなわち、前記磁性物が除去された可燃性ごみ
は風力併用型振動篩機13の供給口31から投入され、
投入された該可燃性ごみは多孔板35の無孔部35aに
乗り、振動手段40による振動作用によって、多孔板3
5上を篩幅方向に広がり層を均一にして、排出口32側
へ移動する。一方、各空気供給口52,53から前後部
室45,46に供給される空気は多孔板35の各篩孔3
5b,35cを通って、上方へ吹き上がる。可燃性ごみ
のうち比較的重い土砂などの小粒不燃物は小篩孔35b
を通過する空気流に抗して小篩孔35bを通過して前部
室45内に落下し、排出口47から回収される。次い
で、小篩孔35bを通過しないものは大篩孔35cへ移
動し、ここで比較的重い中粒不燃物は大篩孔35cを通
過する空気流に抗して大篩孔35cを通過して後部室4
6内に落下し、排出口48から回収される。さらに、大
篩孔35cを通過しなかった粗片は排出口32を経て回
収される。The combustible waste from which the magnetic substances have been removed is put into a vibrating sieve 13 combined with wind power, where it is separated into combustibles and non-combustibles. That is, the combustible waste from which the magnetic material has been removed is introduced from the supply port 31 of the vibrating sieve 13 combined with wind power,
The injected combustible waste rides on the non-porous portion 35a of the perforated plate 35 and is vibrated by the vibrating means 40 so that the perforated plate 3
5 is spread in the width direction of the sieve to make the layer uniform, and is moved to the outlet 32 side. On the other hand, the air supplied from the air supply ports 52, 53 to the front and rear chambers 45, 46 is supplied to the respective sieve holes 3 of the perforated plate 35.
It blows upward through 5b and 35c. Small incombustible materials such as relatively heavy earth and sand among combustible waste are small sieve holes 35b.
, Falls into the front chamber 45 through the small sieve hole 35 b against the airflow passing through, and is collected from the outlet 47. Then, those that do not pass through the small sieve hole 35b move to the large sieve hole 35c, where the relatively heavy medium-sized incombustible material passes through the large sieve hole 35c against the airflow passing through the large sieve hole 35c. Rear room 4
6 and is collected from the outlet 48. Further, the coarse pieces that have not passed through the large sieve hole 35c are recovered through the outlet 32.
【0017】上記の過程で、ビニールなどの軽量な可燃
物は、各篩孔35b、35cから上方に吹き出す空気流
により浮上し、吸引フード56の吸引口58から吸引さ
れ、導管63を経て捕集機14(サイクロン付集塵機)
に捕集・回収される。前記のように多孔板35の振動と
各篩孔35b、35cから吹き上げる空気流との相乗作
用によって、不燃物を、小粒片の砂状物、中粒片の小石
状物及び多孔板35上の大粒片に確実に篩分けることが
できるとともに、軽い可燃物を確実に浮上選別すること
ができる。したがって、可燃物の選別を極めて高い精度
に維持することができる。In the above process, lightweight combustibles such as vinyl float by the airflow blown upward from the sieve holes 35b and 35c, are sucked through the suction port 58 of the suction hood 56, and collected through the conduit 63. Machine 14 (dust collector with cyclone)
Collected and collected at As described above, the non-combustible material is removed by the synergistic action of the vibration of the perforated plate 35 and the air flow blown up from each sieve hole 35b, 35c, the small-grained sand, the medium-grained pebble and the perforated plate 35. In addition to being able to sift into large pieces reliably, it is also possible to reliably float and sort light combustibles. Therefore, the selection of combustibles can be maintained with extremely high accuracy.
【0018】捕集機14(サイクロン付集塵機)に捕集
・回収された可燃物は、気密的に排出されて、搬送コン
ベヤ15により搬送され、減容成形機17に投入される
とともに、消石灰が添加剤供給機16により減容成形機
17に投入される。可燃物は、減容成形機15で減容さ
れて棒状で押出され一定の長さに切断されて成形品とな
り、搬送コンベヤ18を経てコンテナバック等に収納さ
れる。固形燃料に消石灰を予め添加しておくことによっ
て、該固形燃料の燃焼時に発生する塩素などの有害ガス
を反応により中和させ無害化することができる。The combustibles collected and collected by the collector 14 (a dust collector with a cyclone) are discharged in an airtight manner, conveyed by a conveyor 15 and fed into a volume reduction molding machine 17 while slaked lime is removed. The additive is supplied to the volume reducing molding machine 17 by the additive supplying machine 16. The combustible material is reduced in volume by a volume reducing molding machine 15, extruded in a rod shape, cut into a predetermined length to be formed into a molded product, and stored in a container bag or the like via a conveyor 18. By adding slaked lime to the solid fuel in advance, harmful gases such as chlorine generated during combustion of the solid fuel can be neutralized by the reaction and made harmless.
【0019】また、多孔板35の篩孔の開口率を20〜
25%にして空気の通過抵抗、すなわち圧力損失を発生
させることにより、下部室34の前部室45と後部室4
6内の供給空気が篩孔35b、35cを通って吹き上が
る際に、該供給空気は部分的な吹き抜けを起こすことが
なく、多孔板35の篩孔35b、35cの全面から均一
に吹き上がり、これによって多孔板35の不燃物は多孔
板の全面から均等にな吹上げ力を受け、この中で粉塵お
よび可燃物のみが確実に浮上することとなる。The aperture ratio of the sieve holes of the perforated plate 35 is 20 to
By making the air passage resistance, that is, the pressure loss, 25%, the front chamber 45 and the rear chamber 4 of the lower chamber 34 are formed.
When the supply air in 6 is blown up through the sieve holes 35b, 35c, the supply air does not cause partial blow-through, but uniformly blows up from the entire surface of the sieve holes 35b, 35c of the perforated plate 35, As a result, the non-combustible material of the perforated plate 35 receives a uniform blowing force from the entire surface of the perforated plate 35, and only the dust and the combustible material are surely levitated therein.
【0020】また、空気調整用バルブ54,55によ
り、多孔板35からの吹き出し風速を調節して可燃物の
多孔板35からの浮上の程度を調節し、吸引空気量調整
用バルブ35により、吸引口58での吸引速度を調節す
るとともに吸引口58の取付高さ(多孔板35との間
隔)を調節することにより、軽量物のみを確実に吸引す
ることができる。また、多孔板35の小篩孔35bの板
厚tを孔径dと同じか、より大とすることにより、棒状
の木片が、篩孔35bから落ちる確率が減少する。した
がって、小篩孔35bの板厚tは10mm程度が好まし
く、また、大篩孔35cの場合は小篩孔35bと同一に
するか少し厚い程度とし、製作上の点などから最大でも
15mmまでとする。さらに、前記実施例において、多孔
板35を大小2種類の篩孔35b,35cにするととも
に下部室34を2室45,46としたが、大篩孔35c
を省略して小篩孔35bのみとすることができる。この
場合、仕切壁44および排出口47は省略される。The air velocity of the combustibles floating from the perforated plate 35 is adjusted by adjusting the velocity of air blown from the perforated plate 35 by the air adjusting valves 54 and 55, and the suction amount of air is adjusted by the suction air amount adjusting valve 35. By adjusting the suction speed at the port 58 and adjusting the mounting height of the suction port 58 (the distance from the perforated plate 35), it is possible to reliably suction only a lightweight object. Further, by setting the thickness t of the small sieve holes 35b of the perforated plate 35 to be equal to or larger than the hole diameter d, the probability that the bar-shaped wood pieces fall from the sieve holes 35b is reduced. Therefore, the plate thickness t of the small sieve hole 35b is preferably about 10 mm, and in the case of the large sieve hole 35c, it is the same as or slightly thicker than the small sieve hole 35b. I do. Further, in the above-described embodiment, the perforated plate 35 has two types of large and small sieve holes 35b and 35c and the lower chamber 34 has two chambers 45 and 46.
Can be omitted and only the small sieve hole 35b can be provided. In this case, the partition wall 44 and the discharge port 47 are omitted.
【0021】[0021]
【発明の効果】この発明は、以上説明したような形態で
実施されるので、以下に記載されるような効果を奏す
る。請求項1の発明によれば、風力併用型振動篩機の多
孔板の振動と各篩孔から流入する空気流との相乗作用に
よって、可燃物を不燃物である小粒片の砂状物、中粒片
の小石状物及び多孔板上の大粒片から確実に篩分けるこ
とができるとともに、可燃物を確実に浮上選別すること
ができる。このため、可燃物は不燃物をほとんど含まな
いものとなり、極めて純度の高い固形燃料を製造するこ
とができる。また、可燃物の純度が極めて高いことか
ら、不燃物の混入に伴う減容成形機のさらに、不燃物も
その純度が高いことから、不燃物の混入に伴う、減容成
形機の摩耗が大幅に減少し、長期の使用に耐えることが
できる。さらに不燃物もその純度が純度が高いことか
ら、安定型埋立処分ができるとともに路床材や土地造成
材などの埋め戻し用として有効利用することができる。The present invention is embodied in the form described above, and has the following effects. According to the invention of claim 1, due to the synergistic action of vibration of the perforated plate of the vibrating sieve combined with wind power and the air flow flowing from each sieve hole, the combustible material is a non-combustible small-grained sandy material. It is possible to reliably sieve from the pebble-like material of the particle pieces and the large particle pieces on the perforated plate, and it is possible to reliably float and sort combustible materials. For this reason, the combustibles contain almost no incombustibles, and it is possible to produce a solid fuel with extremely high purity. In addition, since the purity of combustible materials is extremely high, the volume reduction molding machine associated with the incorporation of incombustibles is also highly pure. And can withstand long-term use. Furthermore, since non-combustible materials have high purity, they can be stably landfilled and can be effectively used for backfilling of roadbed materials and land preparation materials.
【0022】請求項2の発明によれば、乾燥機での乾燥
後における可燃性ごみを解砕機で解き解しすることによ
り、その後の磁性物の回収や可燃物と不燃物との選別が
極めて容易となる。According to the second aspect of the present invention, the combustible waste after the drying in the dryer is crushed and broken by the crusher, so that the subsequent collection of the magnetic material and the separation of the combustible material from the incombustible material are extremely possible. It will be easier.
【図1】この発明の実施の形態に係る生ごみを含む可燃
性ごみの固形燃料化装置を示す説明図である。FIG. 1 is an explanatory diagram showing a solid fuel conversion device for combustible waste including garbage according to an embodiment of the present invention.
【図2】同上の生ごみを含む可燃性ごみの固形燃料化装
置の風力併用型振動篩機を示す縦断面図である。FIG. 2 is a longitudinal sectional view showing a vibrating sieve combined with wind power of the solid fuel converting apparatus for combustible waste including garbage as described above.
【図3】同上の生ごみを含む可燃性ごみの固形燃料化装
置の他の実施の形態を示す説明図である。FIG. 3 is an explanatory view showing another embodiment of the solid fuel converting apparatus for combustible waste including garbage as described above.
1 受入れホッパ 2 搬送コンベヤ 3 破袋機 4 搬送コンベヤ 5 金属検知器 6 破砕機 7 搬送コンベヤ 8 乾燥機 9 搬送コンベヤ 10 解砕機 11 搬送コンベヤ 12 磁力選別機 13 風力併用型振動篩機 14 捕集機 15 搬送コンベヤ 16 添加剤供給機 17 減容成形機 18 搬送コンベヤ 28 ガスクーラ 30 箱形本体 33 上部室 34 下部室 35 多孔板 44 仕切壁 45 前部室 46 後部室 47 排出口 48 排出口 56 吸引フード 64 サイクロン部 65 集塵部 69 脱臭装置 DESCRIPTION OF SYMBOLS 1 Receiving hopper 2 Conveyor 3 Breaker 4 Conveyor 5 Metal detector 6 Crusher 7 Conveyor 8 Dryer 9 Conveyor 10 Crusher 11 Conveyor 12 Magnetic separator 13 Wind vibrating sieve 14 Collector DESCRIPTION OF SYMBOLS 15 Conveyor 16 Additive feeder 17 Volume reduction molding machine 18 Conveyor 28 Gas cooler 30 Box-shaped main body 33 Upper chamber 34 Lower chamber 35 Perforated plate 44 Partition wall 45 Front chamber 46 Rear chamber 47 Discharge port 48 Discharge port 56 Suction hood 64 Cyclone section 65 Dust collection section 69 Deodorizing device
───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平7−150158(JP,A) 特開 平8−85797(JP,A) (58)調査した分野(Int.Cl.7,DB名) C10L 5/46 B09B 3/00 B09B 5/00 C10L 5/48 WPI/L(QUESTEL)────────────────────────────────────────────────── ─── Continuation of the front page (56) References JP-A-7-150158 (JP, A) JP-A 8-85797 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) C10L 5/46 B09B 3/00 B09B 5/00 C10L 5/48 WPI / L (QUESTEL)
Claims (2)
れた可燃性ごみを破砕する破砕機と、破砕された可燃性
ごみを乾燥する乾燥機と、乾燥された可燃性ごみ中の磁
性物を除去する磁選機と、磁性物が除去された可燃性ご
みを風力により浮上する可燃物と篩下物の不燃物と篩上
物の不燃物とに選別する風力併用型振動篩機と、可燃物
を捕集する捕集機と、可燃物を減容成形して固形燃料と
する減容成形機と、消石灰を前記減容成形機に供給する
添加剤供給機と、からなることを特徴とする生ごみを含
む可燃性ごみの固形燃料化装置。Claims: 1. A bag breaking machine for breaking combustible waste, a crusher for crushing broken bag combustible waste, a dryer for drying crushed combustible waste, and a dried combustible waste. A magnetic separator that removes magnetic substances inside, and a combustible substance that floats combustible waste from which magnetic substances have been removed by wind power
Combined wind-type vibrating sieve that sorts into non- combustibles, collectors that collect combustibles, volume-reducing molding machines that reduce the volume of combustibles to solid fuel, and reduce the volume of slaked lime An apparatus for converting combustible waste including garbage into solid fuel, comprising: an additive feeder for feeding to a molding machine.
乾燥された可燃性ごみを解砕する解砕機と、からなるこ
とを特徴とする請求項1記載の生ごみを含む可燃性ごみ
の固形燃料化装置。2. The flammable garbage containing garbage according to claim 1, further comprising a crusher provided between the dryer and the magnetic separator for crushing the dried flammable waste. Garbage solid fuel converter.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP35889196A JP3024745B2 (en) | 1996-12-27 | 1996-12-27 | Solid fuel conversion system for combustible waste including garbage |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP35889196A JP3024745B2 (en) | 1996-12-27 | 1996-12-27 | Solid fuel conversion system for combustible waste including garbage |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH10195466A JPH10195466A (en) | 1998-07-28 |
JP3024745B2 true JP3024745B2 (en) | 2000-03-21 |
Family
ID=18461640
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP35889196A Expired - Fee Related JP3024745B2 (en) | 1996-12-27 | 1996-12-27 | Solid fuel conversion system for combustible waste including garbage |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3024745B2 (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20040018022A (en) * | 2002-08-24 | 2004-03-02 | 백두환경기술 주식회사 | Apparatus and Method for manufacturing building materials using waste |
ITRM20040297A1 (en) * | 2004-06-17 | 2004-09-17 | Sorain Cecchini Ambiente Sca Spa | METHOD FOR THE REALIZATION OF INTEGRAL RECYCLING WITH LOW ENVIRONMENTAL IMPACT OF SOLID URBAN WASTE AND IMPLEMENTATION DEVICES. |
CN101982532B (en) * | 2010-11-11 | 2013-06-12 | 沈阳航空航天大学 | System for preparing refuse derived fuel from high-calorific-value components of house refuse |
CN102041127A (en) * | 2011-01-18 | 2011-05-04 | 杨健 | Preparation method for preparing derived fuel by utilizing combustible materials in garbage |
-
1996
- 1996-12-27 JP JP35889196A patent/JP3024745B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH10195466A (en) | 1998-07-28 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
KR101785217B1 (en) | Screening methods and screening systems for municipal waste into fuel and combustible waste landfill | |
US4044695A (en) | Multi-stage pneumatic municipal solid waste separation and recovery of a plurality of classifications | |
US3951081A (en) | Method and apparatus for incinerating of refuse | |
US3925198A (en) | Apparatus and method of air classifying municipal solid wastes | |
WO2010013202A1 (en) | Method for processing a mixture of cellulose/plastic waste particles to form a fuel | |
RU2374009C2 (en) | Method and device for treating municipal solid wastes and biomass material produced from said wastes | |
JP2010241082A (en) | Separation and regeneration plant for agricultural plastic | |
KR101814123B1 (en) | Method and apparatus for muiti recycling of waste | |
JP3512291B2 (en) | Method and apparatus for producing solid fuel from waste | |
KR101533288B1 (en) | Method for separating landfilled waste or domestic waste for manufacturing Solid Refuse Fuel | |
JP3024745B2 (en) | Solid fuel conversion system for combustible waste including garbage | |
US5231936A (en) | Apparatus for drying and burning high-hydrous combustible solids | |
JP3029018B2 (en) | Combustible waste solid fuel conversion system | |
JP6059022B2 (en) | Solid fuel production system and solid fuel production method | |
JP3029017B2 (en) | Solid fuel conversion system for combustible waste including garbage | |
KR20020024264A (en) | sorting equipment of constructional wastes | |
CN205887453U (en) | Waste sorting device that vibration screening and wind -force were used simultaneously | |
JP2865541B2 (en) | Method and apparatus for sorting and molding combustibles in waste | |
JP3434569B2 (en) | How to sort construction waste | |
JP3729723B2 (en) | Waste pretreatment equipment | |
JPH0427476A (en) | Apparatus for separating plastics | |
EP0417288A1 (en) | Drying and combustion apparatus of high moisture content solid inflammable matters | |
GB2414427A (en) | Reducing contaminants in biomass material using air density separators | |
JP2001219126A (en) | Air current sorting/drying and refuse solidified fuel manufacturing installation using this device | |
JPH08166115A (en) | Current selection/drier |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
LAPS | Cancellation because of no payment of annual fees |