Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JP3609738B2 - Garbage drying equipment - Google Patents
[go: Go Back, main page]

JP3609738B2 - Garbage drying equipment - Google Patents

Garbage drying equipment Download PDF

Info

Publication number
JP3609738B2
JP3609738B2 JP2001088237A JP2001088237A JP3609738B2 JP 3609738 B2 JP3609738 B2 JP 3609738B2 JP 2001088237 A JP2001088237 A JP 2001088237A JP 2001088237 A JP2001088237 A JP 2001088237A JP 3609738 B2 JP3609738 B2 JP 3609738B2
Authority
JP
Japan
Prior art keywords
garbage
drying
space
screw
heating
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
JP2001088237A
Other languages
Japanese (ja)
Other versions
JP2002286365A (en
Inventor
功之輔 片野
Original Assignee
有限会社三功
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 有限会社三功 filed Critical 有限会社三功
Priority to JP2001088237A priority Critical patent/JP3609738B2/en
Publication of JP2002286365A publication Critical patent/JP2002286365A/en
Application granted granted Critical
Publication of JP3609738B2 publication Critical patent/JP3609738B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Drying Of Solid Materials (AREA)
  • Processing Of Solid Wastes (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、生ゴミの乾燥装置に関する。
【0002】
【従来の技術】
生ゴミは放置すると短期間のうちに腐敗する傾向があり、悪臭の発生、河川の水質汚濁等環境汚染の発生原因になったり、ハエ、蚊等害虫の発生原因になったりするおそれがある。とりわけ生ゴミとして毎日多量の加工残さが発生する食品加工工場、食べ残しが出る飲食店・レストラン、さらには売れ残りの食品廃棄物が生じる食料品店・スーパーマーケット等においては、放置することのできない深刻な問題である。このようないわゆる事業系生ゴミは自治体による回収が制限されることもあるため、個々のあるいは複数の事業所毎に、自ら又は専門業者に委託して堆肥化処理、飼料化処理等を行う事例が増加しつつある。なお、ここでいう生ゴミには、廃棄物の処理及び清掃に関する法律にいう動植物性食物残さ(食べ残しや調理屑)の他、動植物性食物廃棄物(賞味期限切れ・消費期限切れ等のため廃棄される食品・食材)及び有機質性不用物等も含むものとする。
【0003】
ところで、生ゴミの堆肥化処理、飼料化処理等をスムーズに行うために、予め含水率を低減させておく場合がある。このようなときに用いられる乾燥装置の一例として、実公平6−42722号公報、実公平6−46560号公報等に示される縦型内部循環式の乾燥装置がある。これらの乾燥装置では、筒状の乾燥室内に上下方向に配置されたらせんスクリューで生ゴミを上昇させた後自重で落下させる形で循環流動させながら、乾燥室を構成する内外壁面間に蒸気等の熱源流体を流通させ、内壁面を伝熱面として加熱した生ゴミから水分を蒸発させて含水率を低減させている。
【0004】
【発明が解決しようとする課題】
このような乾燥装置において、乾燥時間(生ゴミの含水率を所定割合低減させるに要する時間)の短縮化を図るには、伝熱面積を広くするため筒状の乾燥室を長く(高く)する必要がある。しかしながら、乾燥室が細長くなると乾燥室の底部に生ゴミの重量が集中してかかるため、底部を押す押圧力が大きくなり、らせんスクリューの下端部(始端部)での生ゴミの取り込みに支障(詰まり)を生じやすくなる。また、乾燥室が細長くなると、乾燥室の倒れや傾きを防止するために頑丈な支持構造を要し、装置の大型化を招くことにもなる。
【0005】
そこで、本発明の課題は、装置全長を長くしなくても伝熱面積を広くとることができるとともに、らせんスクリュー始端部での生ゴミの取り込みに詰まりを生じにくくして、乾燥効率と稼動率の向上により乾燥時間の短縮化を図ることができる生ゴミの乾燥装置を提供することにある。
【0006】
【課題を解決するための手段】
上記課題を解決するため、本発明に係る生ゴミの含水率を低減する乾燥装置は、
上下に延びる外筒部と、
その外筒部の内側に設けられて、外筒部内を中心側の生ゴミの上昇空間と外側の生ゴミの下降空間とに区画する内筒部と、
前記内筒部の内側の前記上昇空間内で上下に延びるように配置されたスクリュー軸及びこれに形成されたらせん状の羽根部を有するスクリューと、
そのスクリューを回転させるスクリュー駆動装置と、
前記下降空間と上昇空間とを上側で連通させる上部連通部の上方に設けられた生ゴミの供給部と、
前記下降空間と上昇空間とを下側で連通させるとともに前記生ゴミの荷重を受ける底部と、
前記外筒部の内部及び前記内筒部の内部に加熱蒸気を流通させる熱源流通部として設けられた加熱部と、
前記スクリュー軸の内部に形成され、前記加熱蒸気と共通の加熱源により加熱された加熱乾燥流体が供給管路を介して上端部から供給されるとともに、少なくとも下端部に前記加熱乾燥流体の吹出口が設けられた乾燥熱源流通部とを備え、
前記供給部から供給された生ゴミが前記下降空間内を自重で下降する一方、前記底部に移行した生ゴミが前記スクリューの回転により前記上昇空間を上昇し、さらに前記上部連通部から前記下降空間に戻る循環移動中に前記加熱部に前記加熱蒸気を流通させ前記外筒部及び内筒部との接触に基づく乾燥と、前記乾燥熱源流通部を通りその下端部の吹出口から吹き出す加熱乾燥流体による乾燥とが、同時進行する形で行われて生ゴミが加熱され、水分の蒸発によりその生ゴミの含水率が低減されることを特徴とする。
【0007】
すなわち、本発明においては、外筒部と内筒部とにより乾燥空間を生ゴミの下降空間と上昇空間とに区画し、外筒部と内筒部との少なくとも一方の内部に加熱部を設けることにより、装置全長を長くしなくても伝熱面積を広くとることができる。また、装置を細長くしなくてすむため底部を押す押圧力は相対的に小さくなり、スクリュー始端部での生ゴミの取り込みに詰まりを生じにくくなる。したがって、乾燥効率と稼動率の向上により乾燥時間の短縮化を図ることができる。なお、装置の倒れや傾きを防止するために頑丈な支持構造を要せず、装置の大型化を防止することにもなる。
【0008】
そして、底部がテーパ状に傾斜した傾斜内壁を有し、その傾斜内壁に近接してスクリューと同軸で一体的に回転する撹拌部材を設けると、その傾斜内壁及び撹拌部材により生ゴミが撹拌されつつ下降空間から上昇空間側へ案内される。したがって、生ゴミは傾斜内壁に沿うようにしてスムーズにスクリューの始端部に取り込まれ、この部分での詰まりが生じにくくなる。
【0009】
さらに、外筒部の内部及び/又は内筒部の内部に熱源流体を流通させ、これら外筒部及び/又は内筒部との接触に基づく加熱による乾燥のみならず、スクリュー軸の内部を通り、その下端部の吹出口から加熱乾燥流体(乾燥加熱空気など)が吹き出すことによって、生ゴミの乾燥を一層促進させることができる。
【0010】
【発明の実施の形態】
次に、本発明の実施の形態を、図面に示す実施例を参照して説明する。図1は本発明の一実施例である乾燥装置の縦断面図である。この乾燥装置1は、縦型内部循環式の乾燥室50を有し、生ゴミGを上部の供給部40から乾燥室50内に投入して、その含水率を例えば初期の80%から50%程度にまで低減させた後、下端部の開閉取出し部60から取り出せるようにしたもので、堆肥化処理又は飼料化処理の前工程等に使用される。
【0011】
この乾燥装置1は、上下方向に延びる外筒部10と、その内側に設けられる内筒部20と、これら外筒部10及び内筒部20の上下端の開口をそれぞれ塞ぐ形で取り付けられる頂部39と底部30とを有している。そして、外筒部10の内側に設けられた内筒部20によって、外筒部10(乾燥室50)内は、内筒部20の中心側に位置する生ゴミGの柱状の上昇空間53と、その外側に位置する生ゴミGの環状の下降空間51とに区画されている。
【0012】
このうち上昇空間53内には、スクリュー軸23及びこの外周に形成されたらせん状の羽根部23aを有するスクリュー24が、上下に延びるように配置されている。スクリュー24の羽根部23aの先端は、内筒内壁21に近接する形で回転し、上昇空間53内での生ゴミGの上昇移動を可能にしている。さらに、下降空間51と上昇空間53とは、上側において上部連通部54で、また下側において下部連通部52で各々連通される。その結果、外筒部10(乾燥室50)の内部空間には、下降空間51→下部連通部52→上昇空間53→上部連通部54→下降空間51で示される生ゴミGの循環径路が形成される。なお、下降空間51では生ゴミGは自重により落下する。
【0013】
生ゴミの供給部40は、その入口開口41がスクリュー24(羽根部23a)先端の接線方向を向くようにほぼ水平状に設けられている(図2参照)。言い換えれば、入口開口41と連通し外筒内壁11の上部に開口する投入口42は、内筒部20及び外筒部10の半径方向に対し、前記スクリュー24の回転方向に沿うように所定角度傾斜して、上部連通部54の上方に設けられている。供給部40(投入口42)から投入された生ゴミGは、外筒内壁11に沿うように環状の下降空間51の上方に放出され、自重により落下して上記循環径路に合流する。
【0014】
底部30の内側において、下降空間51と上昇空間53とが連通され、生ゴミGが下降側(下降空間51)から上昇側(上昇空間53)へと方向転換する下部連通部52が形成される。そして、底部30の底部内壁31は乾燥室50内の生ゴミGの荷重を受け止めている。
【0015】
外筒部10、内筒部20及び底部30の内部には加熱部90が設けられている。具体的には、図6にも示すとおり、加熱部90は、外筒内壁11と外筒外壁12との間に熱源流体としての水蒸気を流通させる外筒側熱源流通部91(熱源流通部)を有している。加熱源80の貫流ボイラ等よりなる熱蒸気発生装置81からの加熱蒸気(水蒸気;熱源流体)が、周方向に所定間隔で複数(例えば2〜4個)設けられた外筒側熱源入口91a(図2も参照)から供給され、周方向に所定間隔で複数(例えば2〜4個)設けられた外筒側熱源出口91bから流出して熱蒸気発生装置81に戻る。
【0016】
また、加熱部90は、内筒内壁21と内筒外壁22との間に水蒸気を流通させる内筒側熱源流通部92(熱源流通部)を有している。水蒸気が周方向に所定間隔で複数(例えば2〜4個)設けられた内筒側熱源入口92aから供給され、周方向に所定間隔で複数(例えば2〜4個)設けられた内筒側熱源出口92b(図3も参照)から流出する。さらに、加熱部90は、底部内壁31と底部外壁32との間に水蒸気を流通させる底部側熱源流通部93(熱源流通部)を有しており、水蒸気が底部側熱源入口93aから供給され、底部側熱源出口93bから流出する。
【0017】
このように、外筒部10、内筒部20及び底部30の内部に加熱部90を設けることで、装置全長を長くしなくても伝熱面積を広くとれる。なお、内筒側熱源入口92a及び内筒側熱源出口92bを構成する管路には、内筒部20を外筒部10に支持固定する支持ステーとしての機能を兼用させてあり、これによって構造の簡素化を図っている。なお、図6において外筒側熱源流通部91、内筒側熱源流通部92及び底部側熱源流通部93は各々別個の熱源流通ループを形成しているが、例えば、熱蒸気発生装置81→外筒側熱源流通部91→内筒側熱源流通部92→底部側熱源流通部93→熱蒸気発生装置81のような連続した1本のループを形成するようにしてもよく、かかる場合には配管の長さを短くできる。
【0018】
以上とは別に、熱蒸気発生装置81で発生する水蒸気の一部は加熱空気発生装置82に供給され、加熱空気発生装置82内の熱交換器等によって例えば70〜150℃、中でも100〜120℃に加熱された加熱乾燥空気が、ブロワ83と供給管路84を介してスクリュー軸23の上端部に供給される。スクリュー軸23の内部は、水蒸気と共通の加熱源により加熱された加熱乾燥空気を流通させるスクリュー軸側熱源流通部94(乾燥熱源流通部)とされており、加熱乾燥空気がスクリュー軸23上端のスクリュー軸側熱源入口94aから供給され、スクリュー軸23下端のスクリュー軸側熱源出口94b(吹出口)から噴出する。
【0019】
このように、乾燥室50内においては、外筒側熱源流通部91及び内筒側熱源流通部92に水蒸気を流通させ、これら外筒部10あるいは内筒部20との接触に基づく加熱による乾燥と、スクリュー軸側熱源流通部94を通り、その下端部のスクリュー軸側熱源出口94bから吹き出す加熱乾燥空気による乾燥とが、同時進行する形で行われている。したがって、生ゴミGの乾燥を一層促進させることができる。
【0020】
供給管路84とスクリュー軸側熱源入口94aとはロータリジョイント94cにより相対回転可能に連結されており、これによって、加熱乾燥空気のスクリュー軸側熱源流通部94への供給とスクリュー24の回転による生ゴミGの搬送とがスクリュー軸23の内側と外側とで支障なく行える。スクリュー軸側熱源出口94bから噴出する加熱乾燥空気は、下降空間51の終端部(下端部)、下部連通部52あるいは上昇空間53の始端部(下端部)を移動する生ゴミに対しても加熱乾燥作用を及ぼすことができ、生ゴミの乾燥効率を高めることができる。また、加熱乾燥空気は水蒸気と共通の加熱源(熱蒸気発生装置81)により加熱されるので、熱配管系の簡素化を図ることができる。
【0021】
また、スクリュー軸23の内部を流通する加熱乾燥空気は、上昇空間53を上昇移動中の生ゴミGに対して、その中心側からも加熱して水分の蒸発を促すことができ、一層乾燥効率を高め、乾燥時間の短縮化を図ることができる。なお、スクリュー軸23の周面に径方向の噴出口を設けて、それらから加熱乾燥空気を吹き出させることにより、生ゴミGからの水分の蒸発をさらに促進してもよい。
【0022】
上部連通部54の近傍には、生ゴミGからの蒸発水分を排気するダクト70が設けられている。上昇空間53から下降空間51への方向転換位置である上部連通部54では、生ゴミG同士の隙間が広がりバラけることによって、水分が蒸発しやすくなるので、この蒸発水分の排気がスムーズに滞りなくなされる。
【0023】
図1において、100はスクリュー駆動装置を示し、スクリュー軸23を駆動するための減速機付き電動モータ、チェーン等の伝動部材等を有している。また、110は乾燥室50を外部から覆って断熱するための断熱材、111は乾燥室50を外部から支持する支持フレーム、112は頂部39の上面に設ける点検口蓋、113は外筒部10の外周面に設ける点検口蓋である。
【0024】
次に、図4に示す拡大図により、スクリュー軸23の下端部と底部30の構造について説明する。図4(a)に示すように、底部30は、ほぼ等しい傾斜(例えば30〜60°)を有するテーパ状に傾斜した傾斜内壁31及び傾斜外壁32を有し、その傾斜内壁31に近接してスクリュー軸23と一体的に回転する撹拌棒25(撹拌部材)が、軸直交断面において先端が乾燥時回転方向側に折れ曲がる形で、1本又は周方向に所定間隔をおいて複数(図では3本;図4(b)参照)設けられている。傾斜内壁31及び撹拌棒25により生ゴミGが撹拌されつつ下部連通部52を介して下降空間51から上昇空間53側へ掻き込み案内される。したがって、生ゴミGは傾斜内壁31に沿うようにしてスムーズにスクリュー24の始端部に取り込まれ、比較的粒径の大きい生ゴミGの場合でも撹拌棒25が流れを阻害せず、詰まりが生じにくくなる。
【0025】
また、撹拌棒25の上端はスクリュー24の始端(下端)及び傾斜内壁31の上端よりも上に位置している。このような位置関係の設定によって、撹拌棒25による下部連通部52での生ゴミGの取り込みが滑らかに行われる。
【0026】
さらに、スクリュー24の始端(下端)は傾斜内壁31の上端よりも下方に位置しているので、上昇空間53の始端部における生ゴミGの詰まりを防止できる。
【0027】
なお、図4(b)において、26は撹拌棒25のスクリュー軸23への固定を兼ねた補強材である。
【0028】
図5に撹拌部材の変形例を示す。傾斜内壁31に近接してスクリュー軸23と一体的に回転する撹拌羽根25a(撹拌部材)が設けられ、傾斜内壁31及び撹拌羽根25aにより生ゴミGが撹拌されつつ下部連通部52を介して下降空間51から上昇空間53側へ案内される。したがって、撹拌羽根25aによっても生ゴミGは、傾斜内壁31に沿うようにしてスムーズにスクリュー24の始端部に取り込まれるようになる。
【0029】
再び図4(a)に戻り、底部30には、乾燥後の生ゴミG’の取り出しのための開閉取出し部60が設けられている。底部30の中央開口30aを塞ぐ底蓋61は、運転時(乾燥時)にはエアシリンダ62により(エアの閉じ込み等)ロックされている。乾燥後の生ゴミG’を取り出すときは、エアシリンダ62を介して(エア解放等)底蓋61の上端面を底部30の下端面よりも下位に位置させる。次いで、軸方向の支持軸63を中心に支持アーム64を大きく(望ましくは90〜180°)回動して中央開口30aを開放する。中央開口30aから落下する乾燥後の生ゴミG’をコンテナボックスCB等で受け、あるいはベルトコンベア、スクリューコンベア、エア搬送等で搬送したりして、堆肥化処理工程等、適宜の次工程に移行する。なお、乾燥後の生ゴミG’の取出しの際、スクリュー24を乾燥時とは逆方向に回転させれば、乾燥後の生ゴミG’の取出しが容易となる場合がある。
【図面の簡単な説明】
【図1】本発明の一実施例である乾燥装置の縦断面図。
【図2】図1の平面図。
【図3】図1のX−X断面図。
【図4】図1の一部拡大縦断面図及びそのY−Y断面図。
【図5】撹拌部材の変形例を示す一部拡大縦断面図。
【図6】熱源流体の流れを示す説明図。
【符号の説明】
1 乾燥装置
10 外筒部
20 内筒部
23 スクリュー軸
23a 羽根部
24 スクリュー
25 撹拌棒(撹拌部材)
30 底部
31 傾斜内壁
40 供給部
50 乾燥室
51 下降空間
52 下部連通部
53 上昇空間
54 上部連通部
60 開閉取出し部
70 ダクト
80 加熱源
90 加熱部(熱源流通部)
94 スクリュー軸側熱源流通部(乾燥熱源流通部)
94b スクリュー軸側熱源出口(吹出口)
100 スクリュー駆動装置
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a garbage drying apparatus.
[0002]
[Prior art]
If garbage is left untreated, it tends to rot in a short period of time, which may cause foul odors, cause environmental pollution such as water pollution in rivers, and cause pests such as flies and mosquitoes. Especially in food processing factories where a large amount of processing residue is generated as raw garbage every day, restaurants and restaurants where leftovers are left over, and grocery stores and supermarkets where unsold food waste is generated. It is a problem. Such so-called business-related garbage may be restricted from being collected by local governments, so each individual or multiple business establishments outsources composting or fodder processing to itself or a specialist. Is increasing. In addition, in addition to the food and animal food residue (leftover food and cooking waste) referred to in the Waste Disposal and Cleaning Act, the food waste here is discarded due to animal and vegetable food waste (expiration of expiration date, expiry date, etc.). Food and ingredients) and organic wastes.
[0003]
By the way, in order to smoothly perform the composting process of raw garbage, a feed process, etc., a moisture content may be reduced beforehand. As an example of the drying apparatus used in such a case, there are vertical internal circulation type drying apparatuses disclosed in Japanese Utility Model Publication Nos. 6-42722 and 6-46560. In these drying devices, steam or the like is formed between the inner and outer wall surfaces constituting the drying chamber while circulating and flowing the garbage in a cylindrical drying chamber in the vertical direction after being lifted by a helical screw and dropped by its own weight. The moisture content is reduced by evaporating moisture from the heated garbage with the inner wall surface as the heat transfer surface.
[0004]
[Problems to be solved by the invention]
In such a drying apparatus, in order to shorten the drying time (the time required for reducing the moisture content of raw garbage), the cylindrical drying chamber is lengthened (increased) to widen the heat transfer area. There is a need. However, when the drying chamber is elongated, the weight of garbage is concentrated on the bottom of the drying chamber, which increases the pressing force that pushes the bottom, which hinders the collection of garbage at the lower end (starting end) of the helical screw ( Clogging) is likely to occur. In addition, if the drying chamber is elongated, a sturdy support structure is required to prevent the drying chamber from falling or tilting, which leads to an increase in the size of the apparatus.
[0005]
Therefore, the problem of the present invention is that the heat transfer area can be widened without increasing the overall length of the apparatus, and it is difficult for clogging to take up garbage at the beginning of the helical screw. It is an object of the present invention to provide a garbage drying apparatus capable of shortening the drying time by improving the above.
[0006]
[Means for Solving the Problems]
In order to solve the above problems, a drying apparatus for reducing the moisture content of garbage according to the present invention is as follows:
An outer cylinder extending vertically,
An inner cylinder part that is provided inside the outer cylinder part and divides the inside of the outer cylinder part into a rising space for garbage on the center side and a falling space for garbage on the outside;
A screw shaft disposed so as to extend vertically in the rising space inside the inner cylinder portion and a screw having a spiral blade portion formed on the screw shaft;
A screw drive for rotating the screw;
A garbage supply unit provided above an upper communication part for communicating the descending space and the ascending space on the upper side,
A bottom part for communicating the descending space and the ascending space on the lower side and receiving a load of the garbage;
A heating part provided as a heat source circulation part for circulating heating steam inside the outer cylinder part and inside the inner cylinder part ;
A heating and drying fluid formed inside the screw shaft and heated by a heating source common to the heating steam is supplied from the upper end portion through a supply pipe, and at least the lower end portion has a blowout opening for the heating and drying fluid. And a drying heat source distribution section provided with
While the garbage supplied from the supply unit descends by its own weight in the descending space, the garbage transferred to the bottom part rises in the ascending space by the rotation of the screw, and further, the descending space from the upper communication part. in the circulation moving back to, heated and dried to blow the the heating unit is flowing through the heating steam and drying based on contact with the outer cylindrical portion and the inner cylindrical portion, the dry heat source circulating unit through the outlet at the lower end portion Drying with a fluid is performed in the form of simultaneous progress, the garbage is heated, and the moisture content of the garbage is reduced by evaporation of moisture.
[0007]
That is, in the present invention, the drying space is divided into the falling space and the rising space of the garbage by the outer tube portion and the inner tube portion, and the heating portion is provided in at least one of the outer tube portion and the inner tube portion. Thus, the heat transfer area can be widened without increasing the overall length of the apparatus. In addition, since the apparatus does not have to be elongated, the pressing force pushing the bottom becomes relatively small, and clogging is less likely to occur when taking up garbage at the screw start end. Therefore, the drying time can be shortened by improving the drying efficiency and the operation rate. In addition, in order to prevent the apparatus from falling or tilting, a sturdy support structure is not required, and the apparatus can be prevented from being enlarged.
[0008]
And if the bottom part has the inclined inner wall which inclined in the taper shape and the stirring member which rotates coaxially integrally with the screw in the vicinity of the inclined inner wall is provided, the garbage is stirred by the inclined inner wall and the stirring member. Guided from the descending space to the ascending space. Accordingly, the garbage is smoothly taken into the starting end portion of the screw along the inclined inner wall, and clogging at this portion is less likely to occur.
[0009]
Furthermore, the heat source fluid is circulated through the inside of the outer cylinder part and / or the inside of the inner cylinder part, and not only drying by heating based on contact with the outer cylinder part and / or the inner cylinder part but also the inside of the screw shaft. Further, the drying of the garbage can be further promoted by blowing out the heating and drying fluid (dry heating air or the like) from the outlet at the lower end.
[0010]
DETAILED DESCRIPTION OF THE INVENTION
Next, embodiments of the present invention will be described with reference to examples shown in the drawings. FIG. 1 is a longitudinal sectional view of a drying apparatus according to an embodiment of the present invention. This drying apparatus 1 has a vertical internal circulation type drying chamber 50. The garbage G is introduced into the drying chamber 50 from the upper supply unit 40, and the moisture content thereof is, for example, 80% to 50% from the initial 80%. After being reduced to the extent, it can be taken out from the opening / closing take-out part 60 at the lower end, and is used in a pre-process of composting treatment or feed conversion treatment.
[0011]
The drying apparatus 1 includes an outer cylinder portion 10 that extends in the vertical direction, an inner cylinder portion 20 provided inside the outer cylinder portion 10, and a top portion that is attached in such a manner as to close the openings at the upper and lower ends of the outer cylinder portion 10 and the inner cylinder portion 20. 39 and the bottom 30. And by the inner cylinder part 20 provided inside the outer cylinder part 10, the inside of the outer cylinder part 10 (drying chamber 50) and the column-shaped rising space 53 of the garbage G located in the center side of the inner cylinder part 20 and And an annular descending space 51 of the garbage G located outside thereof.
[0012]
Among these, in the ascending space 53, the screw 24 having a screw shaft 23 and a spiral blade portion 23a formed on the outer periphery thereof is arranged so as to extend vertically. The tip of the blade portion 23 a of the screw 24 rotates so as to be close to the inner cylinder inner wall 21, and allows the garbage G to move up in the rising space 53. Further, the descending space 51 and the ascending space 53 communicate with each other through the upper communication portion 54 on the upper side and the lower communication portion 52 on the lower side. As a result, in the internal space of the outer cylinder portion 10 (drying chamber 50), a circulation path of the garbage G shown by the descending space 51 → the lower communicating portion 52 → the ascending space 53 → the upper communicating portion 54 → the descending space 51 is formed. Is done. In the descending space 51, the garbage G falls by its own weight.
[0013]
The garbage supply unit 40 is provided substantially horizontally so that the inlet opening 41 faces the tangential direction of the tip of the screw 24 (blade 23a) (see FIG. 2). In other words, the insertion port 42 that communicates with the inlet opening 41 and opens at the top of the inner cylinder inner wall 11 has a predetermined angle with respect to the radial direction of the inner cylinder part 20 and the outer cylinder part 10 along the rotational direction of the screw 24. Inclined and provided above the upper communication portion 54. Garbage G introduced from the supply unit 40 (input port 42) is discharged above the annular descending space 51 along the inner wall 11 of the outer cylinder, falls by its own weight, and joins the circulation path.
[0014]
Inside the bottom portion 30, the descending space 51 and the ascending space 53 are communicated, and a lower communicating portion 52 is formed in which the garbage G changes its direction from the descending side (the descending space 51) to the ascending side (the ascending space 53). . The bottom inner wall 31 of the bottom 30 receives the load of the garbage G in the drying chamber 50.
[0015]
A heating part 90 is provided inside the outer cylinder part 10, the inner cylinder part 20 and the bottom part 30. Specifically, as shown in FIG. 6, the heating unit 90 includes an outer cylinder side heat source circulation unit 91 (heat source circulation unit) that circulates water vapor as a heat source fluid between the outer cylinder inner wall 11 and the outer cylinder outer wall 12. have. Outer cylinder side heat source inlet 91a (a plurality of (for example, 2 to 4)) heating steam (water vapor; heat source fluid) from a heat steam generator 81 including a once-through boiler of the heating source 80 is provided at a predetermined interval in the circumferential direction. 2) and flows out from a plurality of (for example, 2 to 4) outer cylinder side heat source outlets 91b provided at a predetermined interval in the circumferential direction and returns to the thermal steam generator 81.
[0016]
The heating unit 90 includes an inner cylinder side heat source circulation section 92 (heat source circulation section) that circulates water vapor between the inner cylinder inner wall 21 and the inner cylinder outer wall 22. A plurality of (for example, 2 to 4) steam is supplied from the inner cylinder side heat source inlet 92a provided at a predetermined interval in the circumferential direction, and a plurality of (for example, 2 to 4) inner cylinder side heat sources provided at a predetermined interval in the circumferential direction. It flows out from the outlet 92b (see also FIG. 3). Furthermore, the heating unit 90 has a bottom side heat source circulation part 93 (heat source circulation part) for circulating water vapor between the bottom inner wall 31 and the bottom outer wall 32, and the water vapor is supplied from the bottom side heat source inlet 93a. It flows out from the bottom side heat source outlet 93b.
[0017]
Thus, by providing the heating part 90 inside the outer cylinder part 10, the inner cylinder part 20, and the bottom part 30, the heat transfer area can be increased without increasing the overall length of the apparatus. The pipes constituting the inner cylinder side heat source inlet 92a and the inner cylinder side heat source outlet 92b also have a function as a support stay for supporting and fixing the inner cylinder part 20 to the outer cylinder part 10, thereby providing a structure. Simplification. In FIG. 6, the outer cylinder side heat source circulation section 91, the inner cylinder side heat source circulation section 92, and the bottom side heat source circulation section 93 each form a separate heat source circulation loop. For example, the heat steam generator 81 → outside A continuous loop such as the cylinder side heat source circulation part 91 → the inner cylinder side heat source circulation part 92 → the bottom side heat source circulation part 93 → the thermal steam generator 81 may be formed. Can be shortened.
[0018]
Apart from the above, a part of the water vapor generated in the hot steam generator 81 is supplied to the heated air generator 82 and is, for example, 70 to 150 ° C., particularly 100 to 120 ° C. by a heat exchanger or the like in the heated air generator 82. The heated and dried air heated to is supplied to the upper end portion of the screw shaft 23 via the blower 83 and the supply pipe 84. The inside of the screw shaft 23 is a screw shaft side heat source circulation section 94 (drying heat source circulation section) that circulates heated and dried air heated by a common heat source with water vapor, and the heated and dried air is at the upper end of the screw shaft 23. Supplied from the screw shaft side heat source inlet 94a and ejected from a screw shaft side heat source outlet 94b (blower) at the lower end of the screw shaft 23.
[0019]
Thus, in the drying chamber 50, water vapor is circulated through the outer cylinder side heat source circulation part 91 and the inner cylinder side heat source circulation part 92, and drying is performed by heating based on contact with the outer cylinder part 10 or the inner cylinder part 20. And the drying by the heating dry air which blows off from the screw shaft side heat source exit 94b of the lower end part through the screw shaft side heat source circulation part 94 is performed in the form which advances simultaneously. Therefore, drying of the garbage G can be further promoted.
[0020]
The supply pipe 84 and the screw shaft side heat source inlet 94a are coupled to each other by a rotary joint 94c so as to be relatively rotatable. As a result, the supply of heated and dried air to the screw shaft side heat source circulation section 94 and the rotation of the screw 24 generate the product. The transfer of the waste G can be performed without any trouble between the inside and the outside of the screw shaft 23. The heated and dried air ejected from the screw shaft side heat source outlet 94 b also heats the garbage moving through the terminal end (lower end) of the descending space 51, the lower communication portion 52, or the starting end (lower end) of the ascending space 53. A drying effect can be exerted, and the drying efficiency of garbage can be increased. In addition, since the heated and dried air is heated by a common heat source (thermal steam generator 81) with water vapor, it is possible to simplify the heat piping system.
[0021]
Further, the heated and dried air that circulates inside the screw shaft 23 can also heat the raw garbage G that is moving up the ascending space 53 from its center side to promote the evaporation of moisture, thereby further improving the drying efficiency. And the drying time can be shortened. The evaporation of moisture from the garbage G may be further promoted by providing a radial outlet on the peripheral surface of the screw shaft 23 and blowing heated dry air therefrom.
[0022]
In the vicinity of the upper communication portion 54, a duct 70 for exhausting evaporated water from the garbage G is provided. In the upper communication portion 54 which is a position changing direction from the ascending space 53 to the descending space 51, the gap between the garbages G spreads and varies, so that the moisture easily evaporates. Will be lost.
[0023]
In FIG. 1, reference numeral 100 denotes a screw drive device, which includes an electric motor with a speed reducer for driving the screw shaft 23, a transmission member such as a chain, and the like. In addition, 110 is a heat insulating material for covering and drying the drying chamber 50 from the outside, 111 is a support frame for supporting the drying chamber 50 from the outside, 112 is an inspection lid provided on the upper surface of the top 39, and 113 is the outer cylinder portion 10. This is an inspection cover provided on the outer peripheral surface.
[0024]
Next, the structure of the lower end portion and the bottom portion 30 of the screw shaft 23 will be described with reference to an enlarged view shown in FIG. As shown in FIG. 4 (a), the bottom portion 30 has a tapered inner wall 31 and an outer wall 32 inclined in a tapered shape having substantially the same inclination (for example, 30 to 60 °), and is close to the inclined inner wall 31. A plurality of stirring rods 25 (stirring members) that rotate integrally with the screw shaft 23 are bent at one end or a predetermined interval in the circumferential direction so that the tip of the stirring rod 25 is bent in the direction orthogonal to the axis when drying. Book; see FIG. 4B). The garbage G is stirred by the inclined inner wall 31 and the stirring rod 25, and is scraped and guided from the descending space 51 to the ascending space 53 through the lower communication portion 52. Accordingly, the garbage G is smoothly taken into the start end portion of the screw 24 along the inclined inner wall 31, and even when the garbage G has a relatively large particle size, the stirring rod 25 does not impede the flow and clogging occurs. It becomes difficult.
[0025]
Further, the upper end of the stirring rod 25 is located above the starting end (lower end) of the screw 24 and the upper end of the inclined inner wall 31 . By setting the positional relationship as described above, the garbage G is smoothly taken in by the lower communicating portion 52 by the stirring rod 25.
[0026]
Furthermore, since the starting end (lower end) of the screw 24 is located below the upper end of the inclined inner wall 31, clogging of the garbage G at the starting end portion of the rising space 53 can be prevented.
[0027]
In FIG. 4B, reference numeral 26 denotes a reinforcing material that also serves to fix the stirring rod 25 to the screw shaft 23.
[0028]
FIG. 5 shows a modification of the stirring member. A stirring blade 25a (stirring member) that rotates integrally with the screw shaft 23 is provided close to the inclined inner wall 31, and the garbage G is lowered by the inclined inner wall 31 and the stirring blade 25a through the lower communication portion 52 while being stirred. Guided from the space 51 to the rising space 53 side. Therefore, the garbage G is smoothly taken into the starting end portion of the screw 24 along the inclined inner wall 31 also by the stirring blade 25a.
[0029]
Returning to FIG. 4A again, the bottom portion 30 is provided with an open / close extraction portion 60 for taking out the garbage G ′ after drying. The bottom lid 61 that closes the central opening 30a of the bottom portion 30 is locked by an air cylinder 62 (such as air closing) during operation (during drying). When taking out the garbage G ′ after drying, the upper end surface of the bottom lid 61 is positioned lower than the lower end surface of the bottom portion 30 via the air cylinder 62 (air release or the like). Next, the support arm 64 is rotated largely (preferably 90 to 180 °) around the support shaft 63 in the axial direction to open the central opening 30a. The dried garbage G ′ falling from the central opening 30a is received by a container box CB or the like, or conveyed by a belt conveyor, screw conveyor, air conveyance, etc., and transferred to an appropriate next process such as a composting process. To do. In addition, when taking out the garbage G ′ after drying, if the screw 24 is rotated in the direction opposite to that at the time of drying, the garbage G ′ after drying may be easily taken out.
[Brief description of the drawings]
FIG. 1 is a longitudinal sectional view of a drying apparatus according to an embodiment of the present invention.
FIG. 2 is a plan view of FIG.
3 is a sectional view taken along line XX in FIG.
4 is a partially enlarged longitudinal sectional view of FIG. 1 and a YY sectional view thereof.
FIG. 5 is a partially enlarged longitudinal sectional view showing a modification of the stirring member.
FIG. 6 is an explanatory diagram showing the flow of a heat source fluid.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Drying apparatus 10 Outer cylinder part 20 Inner cylinder part 23 Screw shaft 23a Blade | wing part 24 Screw 25 Stirring rod (stirring member)
30 Bottom 31 Inclined inner wall 40 Supply unit 50 Drying chamber 51 Lowering space 52 Lower communication part 53 Ascending space 54 Upper communication part 60 Opening and closing extraction part 70 Duct 80 Heating source 90 Heating part (heat source circulation part)
94 Screw shaft side heat source circulation section (dry heat source circulation section)
94b Screw shaft side heat source outlet (air outlet)
100 Screw drive

Claims (4)

生ゴミの含水率を低減する乾燥装置において、
上下に延びる外筒部と、
その外筒部の内側に設けられて、外筒部内を中心側の生ゴミの上昇空間と外側の生ゴミの下降空間とに区画する内筒部と、
前記内筒部の内側の前記上昇空間内で上下に延びるように配置されたスクリュー軸及びこれに形成されたらせん状の羽根部を有するスクリューと、
そのスクリューを回転させるスクリュー駆動装置と、
前記下降空間と上昇空間とを上側で連通させる上部連通部の上方に設けられた生ゴミの供給部と、
前記下降空間と上昇空間とを下側で連通させるとともに前記生ゴミの荷重を受ける底部と、
前記外筒部の内部及び前記内筒部の内部に加熱蒸気を流通させる熱源流通部として設けられた加熱部と、
前記スクリュー軸の内部に形成され、前記加熱蒸気と共通の加熱源により加熱された加熱乾燥流体が供給管路を介して上端部から供給されるとともに、少なくとも下端部に前記加熱乾燥流体の吹出口が設けられた乾燥熱源流通部とを備え、
前記供給部から供給された生ゴミが前記下降空間内を自重で下降する一方、前記底部に移行した生ゴミが前記スクリューの回転により前記上昇空間を上昇し、さらに前記上部連通部から前記下降空間に戻る循環移動中に前記加熱部に前記加熱蒸気を流通させ前記外筒部及び内筒部との接触に基づく乾燥と、前記乾燥熱源流通部を通りその下端部の吹出口から吹き出す加熱乾燥流体による乾燥とが、同時進行する形で行われて生ゴミが加熱され、水分の蒸発によりその生ゴミの含水率が低減されることを特徴とする生ゴミの乾燥装置。
In a drying device that reduces the moisture content of raw garbage,
An outer cylinder extending vertically,
An inner cylinder part that is provided inside the outer cylinder part and divides the inside of the outer cylinder part into a rising space for garbage on the center side and a falling space for garbage on the outside;
A screw shaft disposed so as to extend vertically in the rising space inside the inner cylinder portion, and a screw having a spiral blade portion formed on the screw shaft;
A screw drive for rotating the screw;
A garbage supply unit provided above an upper communication part for communicating the descending space and the ascending space on the upper side,
A bottom portion for communicating the descending space and the ascending space on the lower side and receiving a load of the garbage;
A heating part provided as a heat source circulation part for circulating heating steam inside the outer cylinder part and the inner cylinder part ;
A heating and drying fluid formed inside the screw shaft and heated by a heating source common to the heating steam is supplied from an upper end portion via a supply pipe, and at least a lower end portion of the heating and drying fluid outlet And a drying heat source distribution section provided with
While the garbage supplied from the supply unit descends by its own weight in the descending space, the garbage that has moved to the bottom part ascends the ascending space by the rotation of the screw, and further from the upper communication part to the descending space. in the circulation moving back to, heated and dried to blow the the heating unit is flowing through the heating steam and drying based on contact with the outer cylindrical portion and the inner cylindrical portion, the dry heat source circulating unit through the outlet at the lower end portion A drying apparatus for garbage which is characterized in that drying with a fluid is performed in the form of simultaneous progress, the garbage is heated, and the moisture content of the garbage is reduced by evaporation of moisture.
前記底部には、前記生ゴミの取り出しのための開閉取出し部が設けられ、
前記開閉取出し部を開放し前記スクリューを乾燥時とは逆方向に回転させて前記生ゴミが取り出される請求項1に記載の生ゴミの乾燥装置。
The bottom is provided with an open / close take-out part for taking out the garbage,
Garbage drying apparatus according to claim 1, wherein the garbage is rotated in the reverse direction is Eject that during drying the screw opening the closing extraction unit.
前記生ゴミの供給部は、その入口開口が前記上部連通部の上方にて前記スクリュー先端の接線方向を向くようにほぼ水平状に設けられるとともに、
前記上部連通部の近傍には、前記生ゴミからの蒸発水分を排気するダクトが設けられている請求項1又は2に記載の生ゴミの乾燥装置。
The raw garbage supply unit is provided substantially horizontally so that its inlet opening faces the tangential direction of the screw tip above the upper communication part,
Wherein in the vicinity of the upper communication portion, garbage drying apparatus according to claim 1 or 2 duct for evacuating the evaporation water from the garbage is provided.
前記底部はテーパ状に傾斜した傾斜内壁を有し、その傾斜内壁に近接して前記スクリューと同軸で一体的に回転する撹拌部材がその上端を前記傾斜内壁の上端よりも上に位置する形態で設けられ、その傾斜内壁及び撹拌部材により前記生ゴミが撹拌されつつ前記下降空間から上昇空間側へ案内される請求項1ないし3のいずれか1項に記載の生ゴミの乾燥装置。The bottom portion has an inclined inner wall that is inclined in a tapered shape, and a stirring member that rotates integrally coaxially with the screw in the vicinity of the inclined inner wall has its upper end positioned above the upper end of the inclined inner wall. The garbage drying apparatus according to any one of claims 1 to 3, wherein the garbage garbage is provided and guided from the descending space to the ascending space side while being stirred by the inclined inner wall and the stirring member .
JP2001088237A 2001-03-26 2001-03-26 Garbage drying equipment Expired - Fee Related JP3609738B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001088237A JP3609738B2 (en) 2001-03-26 2001-03-26 Garbage drying equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001088237A JP3609738B2 (en) 2001-03-26 2001-03-26 Garbage drying equipment

Publications (2)

Publication Number Publication Date
JP2002286365A JP2002286365A (en) 2002-10-03
JP3609738B2 true JP3609738B2 (en) 2005-01-12

Family

ID=18943363

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001088237A Expired - Fee Related JP3609738B2 (en) 2001-03-26 2001-03-26 Garbage drying equipment

Country Status (1)

Country Link
JP (1) JP3609738B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4679336B2 (en) * 2005-11-01 2011-04-27 新明和工業株式会社 Kitchen garbage dryer
GB2507949B (en) * 2012-09-16 2017-03-29 Lawrence Timothy Richard Hall Philip Apparatus and method for processing municipal waste into bio-ethanol
KR200484766Y1 (en) * 2015-06-18 2017-10-23 권용성 Food waste disposal container

Also Published As

Publication number Publication date
JP2002286365A (en) 2002-10-03

Similar Documents

Publication Publication Date Title
US5440823A (en) Process and apparatus for efficiently drying wet-milled corn germ and for processing other materials
CN106574819B (en) Apparatus for cooking and drying organic materials
US4038021A (en) Continuous grain drier and method
JP3659397B2 (en) Drying apparatus and drying method thereof
HUT67647A (en) Method and device for drying wet materials
JP2008267738A (en) Low-speed moving stirring heat transfer-type drying method and its device
KR101610602B1 (en) Hotplate conveyor drying chamber type food waste unit
JP2001324269A (en) Heat transfer type vertical dryer
JP3609738B2 (en) Garbage drying equipment
KR100282014B1 (en) Mixed drying apparatus for composting and feed using organic wastes and concentrated by-products.
US4643108A (en) Apparatus for dehydrating metal hydroxide sludge
JP3808315B2 (en) Vertical dryer and drying device
JP2000176399A (en) Organic waste treatment equipment
JP2006007025A (en) Dryer
AU766575B2 (en) Batch sludge dehydrator
JP2003065675A (en) Organic continuous dryer
JP2002162165A (en) Heating mixer
US3481049A (en) Fish meal rotary dryer
EP0015357A1 (en) Apparatus for drying manure and similar residual products
JP3138388U (en) High speed dryer
JP3544646B2 (en) Garbage recycling system
JP3008122U (en) Dryer and dryer
JPH076683U (en) Crushing type heating dryer
JP3560923B2 (en) Garbage disposal method and apparatus
JP2006007026A (en) Dryer

Legal Events

Date Code Title Description
A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20040611

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20040810

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20040929

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20041014

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