JP2004222589A - Apparatus and method for deliquoring and drying cooked product or the like of edible plant - Google Patents

Apparatus and method for deliquoring and drying cooked product or the like of edible plant Download PDF

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JP2004222589A
JP2004222589A JP2003014233A JP2003014233A JP2004222589A JP 2004222589 A JP2004222589 A JP 2004222589A JP 2003014233 A JP2003014233 A JP 2003014233A JP 2003014233 A JP2003014233 A JP 2003014233A JP 2004222589 A JP2004222589 A JP 2004222589A
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Prior art keywords
housing
juice
drying
injection pipe
dewatering
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JP2003014233A
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JP3687965B2 (en
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Hiromichi Yoshida
吉田博道 株式会社京浜プランテック内
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Keihin Plantech Co Ltd
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Keihin Plantech Co Ltd
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  • Filtration Of Liquid (AREA)
  • Drying Of Solid Materials (AREA)
  • Apparatuses For Bulk Treatment Of Fruits And Vegetables And Apparatuses For Preparing Feeds (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To obtain a juice while pressurizing and stirring an edible plant, a cooked product or the like after being sliced to small chips by a long screw, and to reuse the dried residue as a food material, a fodder or a fertilizer. <P>SOLUTION: A slicer into which a material such as the edible plant such as a fruit and a vegetable, and a cooked product is put and in which the material is crushed small is installed in a top wall of a hopper-shaped housing. A large amount of the granular materials is deliquored by being dropped in the housing by deadweight, and being compressed and pressurized by a pair of parallel long screws installed in the lower part of the housing and rotatably driven while changing the rotation directions within each prescribed time to provide a vegetable juice or a fruit juice taken out from a filtering plate at the lower side, and a large amount of the dried residue reusable as the food material, the fodder or the fertilizer. <P>COPYRIGHT: (C)2004,JPO&NCIPI

Description

【0001】
【発明が属する技術分野】
本発明は、廃棄される新鮮な食用植物や料理品などの素材を脱液して乾燥する装置及びその方法に関し、特に多量の素材を微粒粉にスライスしたのち、押圧縮してジュース類を絞り出すと共に残渣は乾燥して食品、飼料、肥料として再利用するための装置及びその方法に関するものである。
【0002】
【従来の技術】
近時、農地で採集した果実野菜類の傷物や形状不良品、集荷市場での傷物や売れ残り物、ホテル、レストランなどでの賞味期限時の食べ残り品は巨大な量である。これを産業廃棄物として焼却したり、廃棄場の埋め立てをしても、多量の含有水分のため処理の困難性があり、且つ、腐敗による悪臭で近隣に支障をきたし、更に捨て場が見当たらない現状である。
【0003】
現在廃棄用の新鮮な食用植物中でリンゴ、トマト、などの果実やキャベツ、にんじんなどの野菜からジュース類を専門に製造している。これ等の業者は500〜600kg程度の素材量をスライスして遠心分離器に投入しジュース類を絞り出したのち、絞りかすとしての僅かな量の残渣は再利用するには事業として成立しないので、高額な費用を支払って処理業者に廃棄させているものである。
【0004】
【発明が解決しようとする課題】
この種従来の装置は通常遠心分離器でジュース類を製造することに主たる目的機能を有するのでスライサや乾燥器は別個に配設する必要がある。従って、処理素材の種類が限定され、1バッチ当たりの処理量が少ない。そして多量のジュースを絞り出すには長時間を要するだけでなく、ジュースの生産効率が悪い。更に残渣の生産量が少ないために別に設けた乾燥機で乾燥処理するよりも廃棄費用を支払って投棄埋設したほうが低廉であり、しかも、粉砕用スライサと脱液装置と乾燥器への移送処理上の作業性が非効率であるなどの問題点があった。
【0005】
本発明は果実野菜は勿論、コーヒー、茶香辛料の出しがら、おから、売れ残りの家畜肉を含む調理品、弁当など廃棄食材食品の広範な種類を処理可能とし、脱液乾燥共用の装置上側に設けたスライサーで微粒紛にした素材は自重による落下で筐体に投入される。そして撹拌圧縮により脱液されながら、乾燥工程に移行することを目的とし、更に筐体内で最終的に乾燥した残渣が処理前の素材重量の平均約20分の1の量となり、筐体容積に顧慮することなく素材を短時間に順次投入して処理することが可能である。しかも、1日当たり13tから16t程度処理可能であるなど素材処理量は極めて巨大な量を処理可能とし、残渣の再利用を充分になし得て、食材、食品投棄の大部分がなくなり、環境破壊の防止を目的とするものである。
【0006】
【課題を解決するための手段】
上記の目的を達成するために、本発明の脱液乾燥装置は機枠に固設された筐体が頂壁と下部が内側へ傾斜した両側壁と両端壁からホツパー状に形成され、両端壁の下部間には一対のスクリユが平行して配設貫通し、一方の端壁外のスクリユの軸端は支持枠を介して駆動部を設け、他軸端側は支持枠に回転自在に支持され、そして両スクリユの羽根の外端の回転軌跡の下部に近接して配設されている多孔濾過板は両壁下端縁に取付けたものである。更には両端壁の中央部間に設けた一対の管材にはノズル孔を介して90℃から120℃程度の飽和蒸気と加熱気体が下向きに噴射され殺菌脱液乾燥をする構成とされる。
【0007】
上記機枠を設置する際に素材より脱液されたジュース原液のおりを除去する濾過槽その他の附属機器を床面に設けるときは台枠上に搭載するが、床面を掘り込んで設けるときは台枠は必要ではない。
【0008】
集荷された食用植物、調理品などの素材は予め滅菌水で洗浄して水切りしたのち、重量を測定して、少ない量の素材を所定の時間間隔を有して上部のスライサの開口より投入される。
【0009】
スライサは駆動される斜軸に数個の回転刃と該刃間に介挿される固定刃で素材は平均5mm〜10mm程度の径に切削されて自重により下方へ移動し、該筐体内の一対のスクリユへ落下する。筐体は下方が狭小となったホッパー形状となして素材の自重によりスムースに下降する。
【0010】
前記一対のスクリユの夫々は時間隔をおいて両者が右廻りしたり、左廻りしたり、また一方が右廻りすると他方は左廻りさせ、さらに一方が左廻りすると他方が右廻りするように電気的自動的に作動させる。これにより、投入上部素材はその一側部が側壁側に片寄ることにより他側壁側の素材はスクリユ部分に下降する。その逆の場合も発生したり、上部素材は楕円形状に回動して、素材が筐体中に片寄って投入されても全体を平滑になるよう作用をする。従って、装置の筐体中に時間的に順次投入されても均一に一対のスクリユにより撹拌圧縮脱水されるものである。
【0011】
スクリユで押圧され絞られるようにして移動する素材は上部素材からの圧力も加わって、脱液され、新鮮なジュースとして濾過されて再利用される一方、急速に脱液されて、略20分の1程度まで重量及び嵩張りが縮小した乾燥残渣は新鮮な食品増量材、機能材、家畜、養殖魚の飼料や肥料として保管しながら必要に応じて直ちに利用することが可能である。
【0012】
筐体の両端壁の中央部間には透孔を有する噴射管が配設され、これに接続されたボイラより供給される飽和蒸気が噴射され、常時脱液されている素材は40℃以上に加温されることにより柔らかくなり、スクリユの回転が良好となり、使用電力が省力化され、急速に脱液される。さらに、素材は加温されることにより殺菌されて、食料や飼料として安全に用いられる。
【0013】
前記蒸気噴射管の噴射で脱液工程が終了すると、該噴射管の上側に配設されている加熱気体の噴射管から加熱気体が噴出されて、乾燥工程に移行する。この加熱気体は既に加温されている筐体内の気体を強制的に取出して前述したボイラの飽和蒸気で熱交換されたのち加熱気体噴射管の透孔より80℃〜120℃程度の加熱気体が噴射されるので、含有液体の水分が50〜60%程度に加温されて脱水されたものを10〜15%の含水量に急速に乾燥してゆく。この残渣の乾燥状態で20日〜30日間程度は変化や腐敗することなく保存可能であり、必要なときその目的に応じて使用する。
【0014】
筐体内の前記蒸気と過熱気体の低温化したものは筐体頂壁上に吸引管を介して設けたブロアで強制的に吸引し、それから素材自体やジュースの臭気を公知の消臭機で吸収除去したのち、煙突から排気する。その際、素材自体は新鮮であって腐敗臭や悪臭はないが、素材自体の臭気はあるので近隣や環境に影響しないように配慮するものである。
【0015】
素材は極めて多種である。一般に果実、野菜は含有液分が92%から96%程度あり、特にトマトは97%に達し、白菜は脱水が促進するにつれて粘性がなくなるのでスクリユーの駆動エネルギーが低減され乾燥工程時間が短くなる。また、脱水乾燥の時間は含液量、新鮮度、粘性、等により差異があって、電気制御回路の自動化により効率良く処理しようとしても困難性がある。
【0016】
素材中の茶がら、コーヒー紅茶かす(搾)などは含有液(水分)分は90%以下のものが多く、微紛状にしてスライスすれば粘性もないので乾燥処理は短時間で完了し、ダイエット食に混合すると好ましい。更に、おからは元来豆乳液分を絞り出していて、粘性もなく、微細にスライスすれば脱液乾燥は短時間且つ、迅速に処理が可能である、従って多くの食材、飼料、肥料に用いられる。
【0017】
素材中の調理品、弁当などの料理品は肉類や粘性のある飯米などが混在し、含有液量も少ない乾燥おからと混合する。しかし脱液操作は注意深く行うことにより海中養魚場の飼料とすることが多い。
【0018】
【発明の実施の形態】
発明の実施の形態を実施例にもとづき図面を参照して説明する。
図1の装置1で処理する素材を新鮮な白菜屑で説明すれば、前処理として人畜に無害とされる程度次亜塩素酸ソーダを混入して200PPMの殺菌剤からなる水槽に浸漬して洗浄する。そのとき、鉄製包丁、はさみなどは側壁の永久磁石に吸着し、ステンレス鋼材や軽金属器具は底壁の溝部に自重で沈下させ、処理を終了した乾燥残渣は食品、飼料として再利用する際に人畜の食用として不足の危険が発生しないようにする。このように滅菌浄化した白菜屑は多孔台板に移載して水切りする。水切りした白菜屑は最大で1度に1t程度を10分〜13分間毎に積込槽に投入し、その底部はスクリユコンベアで移送する。
【0019】
水切り移送された白菜屑を脱液乾燥する装置1は角形鋼管や溝形鋼材で直方体形状に機枠2を形成する。この機枠2にはステンレス鋼板製筺体8をホッパー形状に形成する。筺体の両側壁3及び4の下部は約30度内側方へ折曲させた傾斜部3a、4aを設ける。両側壁の下端縁には駆動側端壁5と残渣排出側端壁6を設ける一方、上側機枠を介して頂壁7を設けて筺体を形成したものである。
【0020】
両端壁5、6の下部には一対の平行で水平な軸10a,10bにつる巻状の羽根11a,11bを有するスクリユ12a,12bを設け、その両端軸部が回動自在に貫通し、機枠に取付けた支持枠13の溝形鋼材14と保持版15の軸受16で支持される。他端側軸部は支持枠17内の溝形鋼材18に軸受19を介して回動自在に保持される。
【0021】
機枠2の下枠延長部上には一対の調節台20a,20b付き支持台21を設け、両調節台には駆動モータ21a,21bを備えた減速器22a,22bを配設し、減速器の回転軸に設けた駆動歯車23a,23bには前記保持版14より突出した軸端の従動歯車24a,24bを夫々噛合させている。これによりスクリユ12a,12bは素材の種類、新鮮度、水分含有量によるが1分間あたり12〜18回転させて素材を脱水する。
【0022】
前記両スクリユー12a、12bの羽根11a,11bの外端縁の回転軌跡の下半周部に近接して脱液ジュースを透過する直径3mm程度の多数の透孔25a、25bを穿ったステンレス鋼板からなる断面W形状の濾過板26a,26b番が配置され、両側壁下縁と両端壁に取付けられる。そして、濾過板26a,26bの中央部の切欠部には両濾過板内端縁部を両側部で覆うようにした濾過板27が取外し可能に配置され、両側壁下縁部にねじ止めされている。これは筐体内を水の噴射で洗浄したときの塵介排出部である。
【0023】
図4は図2のA‐A線に沿う端面図であって、端壁6の下方延長部6aに設けたスクリユの羽根の対応部には開口28を設ける。そして、この開口を覆う多数の透孔25cを穿った蓋29が軸10a、10bを介装して配置される。この蓋29の複数の受部材には端壁6aに回動可能に設けた錠30が施錠され、蓋29が開閉可能に設けられる。
【0024】
上記蓋29にスクリユで圧縮移動してきた粒子素材はジュースを透孔25cより飛散するように吐出するので、軸10a,10bの支持枠17側に介装した止板32で飛散ジュースを受止めて、下方の誘導溝33bに落下させ、濾過槽34に導く。一方、端壁6aに近接する軸10a,10b部には撹拌杆34aを半径方に設けて粒子素材を横方向へ移送し、蓋29への過大な押圧負荷を軽減することにより不慮の損傷を防止する。
【0025】
図5で示す駆動側端壁5下部の羽根11a,11b対応部分には多数の透孔25dを設ける。この透孔25dより外方へ飛散するジュースを下方の誘導溝33aへ落下して流下させるため、端壁5の外側方には図1、図2に示す如く止板35を軸10a、10bに介装させながら、その上端を端壁5に取着する。端壁5内面に近接した軸10a、10b部分には撹拌杆34bを半径方向に設けて、端壁5に圧縮される粒子素材を横方に移動させることにより、端壁5への過負荷を抑制して損傷することを防止する。
【0026】
筐体頂壁7の一側部にはスライサ36を設ける。このスライサ36は傾斜した円筒筐体37の先端下部が頂壁7に開口し、後端壁の後方には駆動モータ38と減速器の駆動軸に接続する。回転軸39が円筒筐体37の両端壁を貫通して配設され、回転軸39には半径方向直行方向に4個の切刃40が所望間隔を有して複数筐所に設けられる。切刃40間には円筒筐体内上下部に配設した補助切刃41が介装されている。そして、円筒筐体37の後端上部に設けた投入開口42には前述した水切り素材がスクリューコンベアによって計量した所望量ごとに順次投入され、略直径5〜10mm程度の不規則な形状に破砕されながら、自重により流れ下り、筐体内に落下してゆく。そして、スライサは素材を投入しない不使用時にはダンパーなどで閉鎖することが好ましい。
【0027】
筐体8下部に落下した素材を圧縮脱液する一対のスクリュー12a、12bは効率良く且つ低電力で作動させるため素材を蒸気加温することが好ましい。そのため、図6に示すボイラ44で90℃〜120℃の飽和蒸気を供給管45に吐出させ、電磁弁46、手動弁47を閉鎖し、分岐した撓曲管48の電磁弁49、手動弁50を開にして端壁5より筐体内に配設した噴射管51に導内する。蒸気噴射管51は下部の中央部に1個と両側部に2個の透孔52を20cm間隔に穿設する。そして管部の透孔52は3mmの径とするが、終端側になるに従って径を5mm程度に増大してゆく。これにより、噴射管の全域より蒸気が均一に下方へ噴射され、粒子素材は40℃〜50℃の温度に加温されて軟化する。軟化した素材はスクリュの省力化された電力エネルギーにより効率良く圧縮されて脱液されると共に摩擦力で素材は更に微粒化する。そしてこの加熱により殺菌される。
【0028】
素材の脱液処理により、含有液の水分含有率が白菜屑の場合は50〜60%に達したとき、蒸気噴射よりなる脱液処理工程を停止して乾燥処理工程に切換える。乾燥処理工程は図6に示す如く、先ず、撓曲管48に設けた電磁弁49、手動弁50を閉とし、供給管45の電磁弁46と手動弁47を開とする。一方、筐体頂壁7に接続して内部気体をブロア55で強制吸引するための撓曲管56の可変ダンパ57を開として該内部気体を熱交換器54に供給する。内部気体が熱交換器54で90℃〜120℃程度に加熱された後、熱交換器54に接続された撓曲管58の先端は端壁5に一端が設けられた加熱気体の噴射管59に接続される。噴射管59は基部から先端側になるに従って、周壁下部に径3mmで3個の透孔が20cmおきに穿設され、噴射気体により加熱された微粒素材は40℃〜60℃程度に加熱されて乾燥してゆくものである。そして、6時間から8時間に亘り乾燥処理がなされると、含有水分が10から15%程度となる。この乾燥程度で取り出して保存しても2〜3週間程度は腐敗することはない。しかし、含有水分を10パーセント以下まで脱水するには、別に設けた真空乾燥器で処理することが本装置の稼働効率を良好とする。
【0029】
濾過板26a,26b及び両端壁5及び6の透孔及び蓋29の透孔より濾過されたジュースは誘導溝33a,33bに落下して濾過槽34に流入する。濾過槽34は順次、メッシュ径を小径とした数個の金網板を配設して、おりを濾過沈殿させてジュース原液を作成する。一方乾燥工程を終了して、残渣を筐体から取り出すときは、前以て、誘導溝33bを引き抜いた後、蓋29を開放移動し、スクリュ12a,12bを作動することにより残渣が排出されて、図1に示すベルトコンベア53で所望の包装処理場へ移送される。
【0030】
本装置の筐体頂壁7上の所望位置には原動機付ブロア60が筐体内の蒸気を含む気体の吸引管61を介して配設される。ブロア60はこれに接続した撓曲管を介して公知の各種臭気を消臭して煙突より排気される。筐体8内は飽和蒸気を噴射しながら脱液処理をなしたのちに加熱気体を供給しながら更に乾燥をなす。この水蒸気は本来処理素材が新鮮であるので、腐敗臭や悪臭はないが、素材本来の臭気は発生する。この臭気は工場団地に装置を設置しても迷惑を及ぼすので、ブロア60より公知の各種消臭機で臭気分を吸収消去するか除去した後煙突より外部に排出する。
【0031】
装置の筐体8内で熱風により脱液乾燥する工程において、一対のスクリュの回転により素材の動きを制御盤31のスイッチ、タイマ、正逆変換機の各々の自動切換えにしたがって具体的に説明する。駆動側より見た両クスリュ12a,12bを右回転させると、両スクリュ部の素材は駆動側の端壁5に圧縮され絞り込まれて移動し、脱液されながら上昇する。そして、上部の全素材は側壁3側に移動し、側壁4側の上部素材は下降してスクリュ12b部に下降する。その作動時間は素材の種類にもよるが、白菜屑の場合は5〜10分間程度である。次にスクリュ12bが逆回転すると、その部分の素材は端壁6側へ移動し、その上部の素材は両側壁側に移動するので、中央上部素材は下降する。それと共にスクリュ12b上部の素材は端壁6側へ移動するが、スクリュ12a上部の素材は端壁5へ移動する傾向にあるので全体的に右回りの楕円形状に回動する。これは10〜20分間程度で終了させる。次にスクリュ12aを左回転させると共に12bを右回転させると、12a部の素材は端壁6側に圧縮移動し、12b部の素材は端壁5側に移動する。そして、上部素材は筐体の中心軸側に寄せられる傾向にあり、両側部の素材は12a,12bに降下する。しかも上部素材は全体として筐体内を楕円状に左回転する。これも5〜10分間程度作動させる。次に12aも12bも左回転させると両スクリュ−部の素材は端壁6側へ圧縮移動し、上部素材は側壁4側に移動し、しかも側壁3側の素材はスクリュ12a部に降下する。この作動時間は5〜10分間程度である。このように素材は移動するので素材が順次投入されても、その全体は均一に脱液乾燥される。
【0032】
【発明の効果】
本発明は、以上説明したように構成されているので、以下に記載されるような効果を奏する。
【0033】
装置筐体の底部に配設した一対の回転するスクリュ−は微粒子化した素材を圧縮して脱液する工程で多量の食用ジュースを発生しながら同一構成のもので乾燥処理もなしているもので、極めて効率的処理をすることができる。
【0034】
筐体中に投入する切削粒子状素材はスクリュで圧縮されるので、時間的間隔をおいて順次計量のうえ投入すれば筐体容積を考慮することなく急速に脱液して素材の重量も急滅する。従って、短時間に多量の脱液処理が可能となり、最終的に乾燥残渣が筐体容積の1/2となることを予測しているだけで一日あたり14tから16tの素材を処理可能である。
【0035】
さらに、装置筐体の頂壁上に設けたスライサの開口に水切り素材を投入すれば、切削破砕されながら筐体下部のスクリュ部に落下し、スクリュの回転により脱液して発生するジュースは自重で下部の多孔濾過板から濾過されて流下し、生鮮飲料とされる。このように自重による流下式で自動的多量の素材を低コストで効率的に処理することが可能となったものである。
【0036】
素材を脱液して含水量10〜15%程度に乾燥すると、粉体状残渣として保管しておき必要に応じて、各種食品及び食品の機能材、増量材、飼料、肥料として従来は大部分を生ごみとして廃棄していたものを再利用可能とすることが可能となったものである。このようにして、従来、売れ残り、食べ残しなどの新鮮な生ごみは集荷ネットワークが整備されるにつれ、その大部分が再利用され環境を破壊することは無くなるという大きな効果を奏する。
【図面の簡単な説明】
【図1】脱液乾燥装置の一部切欠全体斜視図である。
【図2】脱液乾燥装置の一部切欠全体正面図である。
【図3】脱液乾燥装置の一部切欠全体平面図である。
【図4】図2のA〜A線断面に沿う端面図である。
【図5】図2のB〜B線断面に沿う端面図である。
【図6】装置筐体内に蒸気と加熱気体を噴射する経路図である。
【符号の説明】
1 脱液乾燥装置
2 機枠
3 3a4,4a 側壁
5、6.6a 端壁
7 頂壁
8 筐体
10a.10b 軸
12 スクリユ
13.17 支持枠
15 保持板
21a.21b 駆動モータ
22a,22b 減速機
23a,23b 24a,24b 歯車
25a,25b 25c,25b 透孔
26a,26b 濾過板
29 蓋
33a,33b 誘導溝
34a,34b 撹拌杆
36 スライサ
40 切刃
41 補助切刃
48.56.58 撓曲管
51 蒸気噴射管
59 加熱気体噴射管
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to an apparatus and a method for dewatering and drying materials such as fresh edible plants and foods to be discarded, and in particular, after slicing a large amount of materials into fine powder, pressing and compressing to squeeze juices. Also, the present invention relates to an apparatus and a method for drying and reusing the residue as food, feed, or fertilizer.
[0002]
[Prior art]
In recent years, the amount of wounds and defective products of fruit and vegetables collected on farmland, wounds and unsold goods at collection markets, and leftover foods at the expiration date in hotels and restaurants are huge. Even if it is incinerated as industrial waste or landfilled at a landfill, there is a large amount of water in it, making it difficult to dispose of it. It is the current situation.
[0003]
At present, the company specializes in producing juices from fruits such as apples and tomatoes and vegetables such as cabbage and carrots in fresh edible plants for disposal. These companies slice about 500-600 kg of raw material, put it in a centrifuge, and squeeze out juices.Since a small amount of residue as marc is not feasible as a business to reuse, They pay a high cost and dispose of them at a processing company.
[0004]
[Problems to be solved by the invention]
Such a conventional apparatus usually has a main purpose function of producing juices by a centrifugal separator, so that a slicer and a dryer need to be provided separately. Therefore, the types of processing materials are limited, and the processing amount per batch is small. In addition, it takes a long time to squeeze out a large amount of juice, and the production efficiency of juice is poor. Furthermore, since the amount of residue produced is small, it is more inexpensive to pay disposal costs and dump and bury the waste than to dry it with a separate dryer. However, there is a problem that the work efficiency is inefficient.
[0005]
The present invention makes it possible to process a wide variety of waste foodstuffs, such as fruit and vegetables, coffee, tea spices, okara, unsalted cooked foods including livestock meat, and bento boxes, and is installed on the upper side of a common dewatering and drying device. The material that has been made into fine powder by the provided slicer is dropped into the housing by its own weight. The purpose is to shift to the drying process while being dewatered by stirring and compression, and the residue finally dried in the casing becomes an average of about 1/20 of the weight of the raw material before treatment, and the It is possible to feed and process materials sequentially in a short time without consideration. In addition, the material processing amount can be extremely large, for example, 13 to 16 tons can be processed per day, the residue can be sufficiently reused, food and food dumping can be largely eliminated, and environmental destruction can be prevented. It is intended for prevention.
[0006]
[Means for Solving the Problems]
In order to achieve the above object, in the dewatering and drying apparatus of the present invention, a casing fixed to a machine frame is formed in a hopper shape from a top wall, both side walls having a lower portion inclined inward, and both end walls. A pair of screws are arranged and penetrated in parallel between the lower parts of the screws, and the screw end of the screw outside one end wall is provided with a drive unit via a support frame, and the other shaft end side is rotatably supported by the support frame. The perforated filter plate is disposed near the lower part of the rotation trajectory of the outer ends of the screw blades of both screws, and is attached to the lower edge of both walls. Further, a saturated steam of about 90 ° C. to 120 ° C. and a heated gas are jetted downward through a nozzle hole to a pair of pipes provided between the center portions of both end walls, so that sterilization, drainage, and drying are performed.
[0007]
When installing a filter tank and other attached equipment on the floor surface to remove the cage of the juice undiluted from the material when installing the above machine frame, it is mounted on the underframe, but when digging the floor surface No underframe is required.
[0008]
Collected edible plants, cooked materials, etc. are washed in advance with sterilized water and drained, then weighed, and a small amount of material is injected from the upper slicer opening at predetermined time intervals. You.
[0009]
The slicer has several rotating blades on the driven oblique shaft and a fixed blade inserted between the blades, and the material is cut to a diameter of about 5 mm to 10 mm on average and moves downward by its own weight, and a pair of blades in the housing Fall to Skrill. The casing has a hopper shape with a narrow bottom, and descends smoothly due to the weight of the material.
[0010]
Each of the pair of screeds is turned so as to turn clockwise or counterclockwise at an interval, and when one turns clockwise, the other turns counterclockwise, and when one turns counterclockwise, the other turns clockwise. Activate automatically. As a result, one side of the input upper material is offset toward the side wall, and the material on the other side is lowered to the screw portion. The reverse case also occurs, or the upper material rotates in an elliptical shape, and acts so that the entire material becomes smooth even if the material is thrown into the housing in one direction. Therefore, even if they are sequentially introduced into the housing of the apparatus in time sequence, they are uniformly stirred and dewatered by a pair of screws.
[0011]
The material that moves as it is pressed and squeezed by the screw is subjected to the pressure from the upper material, and is drained, filtered and reused as fresh juice. The dried residue whose weight and bulk have been reduced to about 1 can be immediately used as needed while storing it as a fresh food extender, functional material, livestock, farmed fish feed or fertilizer.
[0012]
An injection pipe having a through hole is disposed between the center portions of both end walls of the housing, and saturated steam supplied from a boiler connected to the injection pipe is injected, and the material which is constantly dewatered is heated to 40 ° C or more. Heating makes the screw softer, the rotation of the screw becomes better, power consumption is reduced, and liquid is rapidly drained. Further, the material is sterilized by heating, and is safely used as food or feed.
[0013]
When the liquid removing step is completed by the injection of the steam injection pipe, the heating gas is ejected from the injection pipe of the heating gas disposed above the injection pipe, and the process proceeds to the drying step. The heated gas is forcibly taken out of the already heated gas in the housing and heat-exchanged with the above-described saturated steam of the boiler. Since the liquid is sprayed, the water content of the liquid is heated to about 50 to 60%, and the dehydrated liquid is rapidly dried to a water content of 10 to 15%. The residue can be stored in a dry state for about 20 to 30 days without any change or decay, and used according to the purpose when necessary.
[0014]
The low-temperature vapor and superheated gas in the casing are forcibly sucked by a blower provided on the top wall of the casing via a suction pipe, and then the odor of the material itself or juice is absorbed by a known deodorizer. After removal, exhaust from the chimney. At this time, the raw material itself is fresh and has no putrid odor or bad odor, but since the raw material itself has an odor, consideration should be given not to affect the neighborhood and the environment.
[0015]
The materials are extremely diverse. In general, fruits and vegetables have a liquid content of about 92% to 96%, especially tomatoes reach 97%, and Chinese cabbage loses viscosity as dehydration is accelerated, so that the driving energy of the screw is reduced and the drying process time is shortened. In addition, the time for dehydration and drying varies depending on the liquid content, freshness, viscosity, and the like, and there is a difficulty in efficiently processing by automation of an electric control circuit.
[0016]
Most of the ingredients, such as tea flakes and coffee black tea (squeezed), contain less than 90% of the liquid (water) content. It is preferable to mix it with food. In addition, soybean milk is originally squeezed out of soy milk, it is not sticky, and if it is sliced finely, it can be quickly and quickly processed by deliquoring and drying. Therefore, it is used for many foodstuffs, feeds, and fertilizers. Can be
[0017]
Cooked foods such as lunches, etc. in the ingredients are mixed with meat and viscous cooked rice, and are mixed with dried okara, which contains a small amount of liquid. However, careful deliquescence is often used as feed for underwater fish farms.
[0018]
BEST MODE FOR CARRYING OUT THE INVENTION
Embodiments of the present invention will be described based on examples with reference to the drawings.
If the raw material to be processed by the apparatus 1 in FIG. 1 is described as fresh cabbage waste, as a pretreatment, sodium hypochlorite is mixed to the extent that it is harmless to humans and animals, and it is immersed in a water tank made of a 200 PPM disinfectant and washed. I do. At this time, iron knives, scissors, etc. are attracted to the permanent magnets on the side walls, stainless steel materials and light metal appliances are settled by their own weight in the grooves on the bottom wall, and the dried residue that has been treated is used as human food when it is reused as food or feed. Avoid the danger of shortage as food. The cabbage waste sterilized and purified in this way is transferred to a perforated base plate and drained. The drained Chinese cabbage is put into a loading tank at a time of about 1 t at a time every 10 to 13 minutes, and the bottom thereof is transferred by a screw conveyor.
[0019]
The apparatus 1 for removing and drying the drained and transferred Chinese cabbage waste forms a machine frame 2 in the shape of a rectangular parallelepiped with a square steel pipe or a grooved steel material. A casing 8 made of a stainless steel plate is formed in the machine frame 2 in a hopper shape. The lower portions of both side walls 3 and 4 of the housing are provided with inclined portions 3a and 4a which are bent inward by about 30 degrees. A drive-side end wall 5 and a residue discharge-side end wall 6 are provided at lower end edges of both side walls, and a top wall 7 is provided via an upper machine frame to form a housing.
[0020]
Screws 12a, 12b having a pair of parallel horizontal shafts 10a, 10b and wound blades 11a, 11b are provided at the lower portions of both end walls 5, 6, and the shafts at both ends are rotatably penetrated. It is supported by the channel steel member 14 of the support frame 13 attached to the frame and the bearing 16 of the holding plate 15. The other end side shaft portion is rotatably held by a channel steel material 18 in a support frame 17 via a bearing 19.
[0021]
On the lower frame extension of the machine frame 2, there is provided a support base 21 with a pair of adjustment stands 20a, 20b, and on both adjustment stands, reduction gears 22a, 22b provided with drive motors 21a, 21b are provided. Driven gears 23a and 23b provided on the rotating shaft are engaged with driven gears 24a and 24b at the shaft end protruding from the holding plate 14, respectively. Thus, the screws 12a and 12b rotate the material 12 to 18 times per minute to dehydrate the material, depending on the type, freshness, and moisture content of the material.
[0022]
It is made of a stainless steel plate having a large number of through holes 25a and 25b having a diameter of about 3 mm, which are close to the lower half of the rotation trajectory of the outer edges of the blades 11a and 11b of the two screws 12a and 12b. Filter plates 26a and 26b having a W-shaped cross section are arranged, and attached to the lower edges of both side walls and both end walls. A filter plate 27 having both sides covering the inner edges of both filter plates is removably disposed in the notch at the center of the filter plates 26a and 26b, and is screwed to the lower edges of both side walls. I have. This is a dust discharge unit when the inside of the housing is washed by spraying water.
[0023]
FIG. 4 is an end view taken along the line AA in FIG. 2, and an opening 28 is provided in a corresponding portion of the screw blade provided on the lower extension 6 a of the end wall 6. Then, a lid 29 having a large number of through holes 25c covering the opening is disposed with the shafts 10a and 10b interposed. Locks 30 rotatably provided on the end wall 6a are locked to a plurality of receiving members of the lid 29, and the lid 29 is provided to be openable and closable.
[0024]
Since the particle material compressed and moved to the lid 29 by the screw is discharged so that the juice is scattered from the through hole 25c, the scattered juice is received by the stop plate 32 interposed on the support frame 17 side of the shafts 10a and 10b. , And falls into the lower guiding groove 33 b and is guided to the filtration tank 34. On the other hand, stirring rods 34a are provided radially on the shafts 10a and 10b adjacent to the end wall 6a to transfer the particle material in the lateral direction and reduce an excessive pressing load on the lid 29 to prevent accidental damage. To prevent.
[0025]
A large number of through holes 25d are provided in a portion corresponding to the blades 11a and 11b below the driving side end wall 5 shown in FIG. In order to cause the juice scattered outward from the through-hole 25d to fall into the lower guide groove 33a and flow down, a stop plate 35 is attached to the shafts 10a and 10b outside the end wall 5 as shown in FIGS. The upper end is attached to the end wall 5 while being interposed. Stirring rods 34b are provided in the radial direction on the shafts 10a and 10b close to the inner surface of the end wall 5, and the particle material compressed on the end wall 5 is moved laterally, so that the overload on the end wall 5 is reduced. Suppress to prevent damage.
[0026]
A slicer 36 is provided on one side of the housing top wall 7. In the slicer 36, the lower end of the inclined cylindrical housing 37 is opened at the top wall 7, and behind the rear end wall, a drive motor 38 and a drive shaft of a speed reducer are connected. The rotating shaft 39 is provided through both end walls of the cylindrical housing 37, and the rotating shaft 39 is provided with four cutting blades 40 in a plurality of housings at desired intervals in a direction perpendicular to the radial direction. Between the cutting blades 40, auxiliary cutting blades 41 disposed at upper and lower portions in the cylindrical housing are interposed. Then, the above-described draining material is sequentially injected into the input opening 42 provided at the upper end of the rear end of the cylindrical housing 37 for each desired amount measured by a screw conveyor, and crushed into an irregular shape having a diameter of about 5 to 10 mm. Meanwhile, it flows down by its own weight and falls into the housing. It is preferable that the slicer be closed with a damper or the like when not using a material.
[0027]
It is preferable that the pair of screws 12a and 12b for compressing and dewatering the material dropped to the lower part of the housing 8 heat the material by steam in order to operate efficiently and with low power. Therefore, saturated steam of 90 ° C. to 120 ° C. is discharged to the supply pipe 45 by the boiler 44 shown in FIG. 6, the solenoid valve 46 and the manual valve 47 are closed, and the solenoid valve 49 and the manual valve 50 of the branched bent pipe 48 are closed. Is opened and guided from the end wall 5 to the injection pipe 51 disposed in the housing. The steam injection pipe 51 has one through hole 52 at the center and two through holes at 20 cm intervals on both sides. The diameter of the through-hole 52 of the tube is 3 mm, and the diameter increases to about 5 mm toward the end. As a result, steam is uniformly injected downward from the entire area of the injection pipe, and the particle material is heated to a temperature of 40 ° C to 50 ° C and softened. The softened material is efficiently compressed and drained by the energy-saving power energy of the screw, and the material is further atomized by frictional force. And it is sterilized by this heating.
[0028]
When the water content of the liquid contained in the cabbage waste reaches 50 to 60% as a result of the material dewatering process, the dewatering process consisting of steam injection is stopped and switched to the drying process. In the drying process, as shown in FIG. 6, first, the solenoid valve 49 and the manual valve 50 provided on the bending pipe 48 are closed, and the solenoid valve 46 and the manual valve 47 of the supply pipe 45 are opened. On the other hand, the variable damper 57 of the flexible tube 56 connected to the housing top wall 7 and forcibly sucking the internal gas by the blower 55 is opened, and the internal gas is supplied to the heat exchanger 54. After the internal gas is heated to about 90 ° C. to 120 ° C. in the heat exchanger 54, the distal end of the flexible pipe 58 connected to the heat exchanger 54 is connected to the heated gas injection pipe 59 having one end provided on the end wall 5. Connected to. As the injection pipe 59 is moved from the base to the tip side, three through holes with a diameter of 3 mm are drilled at intervals of 20 cm in the lower part of the peripheral wall, and the fine material heated by the injection gas is heated to about 40 ° C. to 60 ° C. It dries out. When the drying process is performed for 6 hours to 8 hours, the water content becomes about 10 to 15%. Even if it is taken out and stored with this degree of drying, it does not rot for about 2 to 3 weeks. However, in order to dehydrate the water content to 10% or less, the operation efficiency of the present apparatus is improved by treating with a vacuum dryer provided separately.
[0029]
The juice filtered from the through holes of the filter plates 26a, 26b and the end walls 5 and 6 and the through hole of the lid 29 falls into the guide grooves 33a, 33b and flows into the filtration tank. In the filtration tank 34, several wire mesh plates having a smaller mesh diameter are sequentially arranged, and the cage is filtered and settled to produce a juice stock solution. On the other hand, when removing the residue from the housing after finishing the drying step, the guide 29 is pulled out beforehand, the lid 29 is opened and the screws 12a and 12b are operated to discharge the residue. Then, it is transferred to a desired packaging processing site by a belt conveyor 53 shown in FIG.
[0030]
At a desired position on the top wall 7 of the housing of the present apparatus, a blower with a motor 60 is disposed via a suction pipe 61 for gas containing steam in the housing. The blower 60 deodorizes various known odors through a flexible tube connected to the blower 60 and is exhausted from the chimney. The inside of the housing 8 is subjected to a liquid removal process while injecting saturated steam, and then further dried while supplying a heated gas. Since this steam is originally a raw material to be treated, there is no rotten odor or bad odor, but the odor inherent to the material is generated. This odor causes annoyance even if the apparatus is installed in a factory complex. Therefore, the odor is absorbed or eliminated by various known deodorizers from the blower 60 and then discharged from the chimney.
[0031]
In the step of dewatering and drying with hot air in the housing 8 of the apparatus, the movement of the material by the rotation of the pair of screws will be specifically described according to the automatic switching of the switch, timer, and forward / reverse converter of the control panel 31. . When the two screws 12a and 12b viewed from the driving side are rotated clockwise, the material of the two screw parts is compressed and narrowed by the driving end wall 5, moves, and rises while being drained. Then, all the material on the upper side moves to the side wall 3 side, and the upper material on the side wall 4 side descends and descends to the screw 12b. The operating time depends on the type of material, but is about 5 to 10 minutes for Chinese cabbage. Next, when the screw 12b rotates in the reverse direction, the material at that portion moves toward the end wall 6, and the material above the material moves toward both side walls, so that the central upper material descends. At the same time, the material above the screw 12b moves toward the end wall 6, but the material above the screw 12a tends to move toward the end wall 5, so that the whole rotates in a clockwise elliptical shape. This is completed in about 10 to 20 minutes. Next, when the screw 12a is rotated to the left and the screw 12b is rotated to the right, the material in the portion 12a is compressed and moved toward the end wall 6, and the material in the portion 12b is moved toward the end wall 5. The upper material tends to be moved toward the central axis of the housing, and the materials on both sides descend to 12a and 12b. Moreover, the upper material rotates leftward in an elliptical shape as a whole in the housing. This is also activated for about 5 to 10 minutes. Next, when both 12a and 12b are rotated counterclockwise, the material of both screw parts is compressed and moved toward the end wall 6, the upper material is moved to the side wall 4, and the material on the side wall 3 is lowered to the screw 12a. This operation time is about 5 to 10 minutes. Since the material moves in this way, even if the material is sequentially charged, the entire material is uniformly drained and dried.
[0032]
【The invention's effect】
The present invention is configured as described above, and has the following effects.
[0033]
A pair of rotating screws disposed at the bottom of the device casing have the same configuration and have been subjected to a drying process while generating a large amount of edible juice in the step of compressing and draining the finely divided material. , Extremely efficient processing can be performed.
[0034]
Since the cut particulate material to be put into the case is compressed by a screw, if it is weighed and put in sequence at intervals of time, it will quickly drain without regard to the case volume, and the weight of the material will also steep. Perish. Accordingly, a large amount of liquid can be removed in a short period of time, and a material of 14 to 16 tons per day can be processed only by predicting that the dry residue eventually becomes 1/2 of the housing volume. .
[0035]
In addition, if a draining material is put into the opening of the slicer provided on the top wall of the device housing, it will fall into the screw part at the bottom of the housing while being cut and crushed, and the juice generated by draining the liquid by the rotation of the screw will have its own weight. The water is filtered from the lower porous filter plate and flows down to produce a fresh beverage. In this way, a large amount of material can be automatically and efficiently processed at low cost by a flow-down method using its own weight.
[0036]
When the material is drained and dried to a water content of about 10 to 15%, it is stored as a powdery residue, and if necessary, it is used as a functional material for various foods and foods, a bulking material, a feed, and a fertilizer. It is now possible to reuse what was discarded as garbage. In this way, fresh garbage, such as unsold and uneaten garbage, has a great effect that, as the collection network is established, most of the garbage is reused and the environment is not destroyed.
[Brief description of the drawings]
FIG. 1 is a partially cutaway overall perspective view of a liquid removing and drying apparatus.
FIG. 2 is a partially cutaway front view of the liquid drying apparatus.
FIG. 3 is a partially cutaway overall plan view of the liquid removing and drying apparatus.
FIG. 4 is an end view along a cross section taken along line AA of FIG. 2;
FIG. 5 is an end view along a cross section taken along line BB of FIG. 2;
FIG. 6 is a path diagram for injecting steam and heated gas into an apparatus housing.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Dewatering and drying apparatus 2 Machine frame 3 3a4, 4a Side wall 5, 6.6a End wall 7 Top wall 8 Case 10a. 10b Shaft 12 Screw 13.17 Support frame 15 Holding plate 21a. 21b Drive motors 22a, 22b Reduction gears 23a, 23b 24a, 24b Gears 25a, 25b 25c, 25b Through holes 26a, 26b Filter plate 29 Lids 33a, 33b Guide grooves 34a, 34b Stirring rod 36 Slicer 40 Cutting blade 41 Auxiliary cutting blade 48 .56.58 Flexible tube 51 Steam injection tube 59 Heated gas injection tube

Claims (6)

機枠に設けたホッパ形状の筺体の両端壁下部を一対の平行なスクリユの両端壁軸部が貫通して両端壁外側の支持枠に回動自在に配設され、両軸部の一端側に設けた従動歯車は、駆動機構と接続した減速器軸の駆動歯車と噛合し、これにより粒子状素材を撹拌圧縮して絞り出す両スクリユは夫々電気的制御盤のタイマと電圧の正逆変換器を介して所望の時間的設定値で回転方向を自動的に制御して作動し、両スクリユの羽根外端の回転軌跡の下側半周に近接した多孔濾過板は筐体下端壁部に固設され、両端壁間には筐体内の素材を50℃〜60℃に上昇させて乾燥する加熱気体噴射管を設け、筐体頂壁の一側には駆動機付傾斜スライサの先端側を配設し、且つ、頂壁の適所には筐体内の気体や臭気を吸引するブロアより臭気吸収除去機を介して廃棄する煙突を設けていることを特徴とする食用植物料理品等の脱液乾燥装置。A pair of parallel screw screws penetrate the lower portions of both end walls of the hopper-shaped housing provided on the machine frame, and are rotatably disposed on the support frame outside the both end walls. The provided driven gear meshes with the drive gear of the reducer shaft connected to the drive mechanism, and thereby the agitating and compressing and squeezing the particulate material, the two screws respectively use the timer of the electrical control panel and the forward / reverse converter of voltage. The rotation direction is automatically controlled and operated at a desired time setting value through the operation, and a perforated filtration plate close to the lower half of the rotation trajectory of the outer ends of the blades of both screws is fixed to the bottom wall of the housing. A heated gas injection pipe is provided between both end walls to raise and dry the material in the housing to 50 ° C. to 60 ° C., and a tip side of an inclined slicer with a driving device is provided on one side of the top wall of the housing. And a blower for sucking gas and odor in the housing at an appropriate position on the top wall through an odor absorbing and removing machine. Drainer drying apparatus edible plant food be rinsed, characterized in that it provided a stack of disposal. 前記筐体の両端壁間には間隔を有して下向きに複数個の透孔を設けた蒸気の噴射管を設ける一方、筐体外に設けたボイラに発生する90℃から110℃程度の飽和蒸気は撓曲管により蒸気噴射管に接続し、筐体の素材を少くとも40℃から50℃に加温して脱液処理を良好にすることを特徴とする請求項1記載の食用植物料理品などの脱液乾燥装置。A steam injection pipe provided with a plurality of downwardly extending through holes with a space between both end walls of the casing is provided, and a saturated steam of about 90 ° C. to 110 ° C. generated in a boiler provided outside the casing is provided. 2. The edible vegetable food product according to claim 1, wherein the hood is connected to the steam injection pipe by a flexible pipe, and the material of the housing is heated at least from 40 ° C. to 50 ° C. to improve the dewatering process. Dewatering and drying equipment. 前記蒸気噴射管の上側の両端壁間には下向きに複数個の透孔を間隔を有して穿設した加熱気体噴射管を設ける一方前記ボイラの飽和蒸気は供給管を介して熱交換器へ導入され、該熱交換器には筐体頂壁に接続した撓曲管で筐体内の気体を吸引するブロアが接続され、該ブロアに接続された熱交換により加熱された気体は撓曲管を介して導入される前記加熱気体噴射管に接続されて素材を乾燥することを特徴とする請求項1記載の食用植物料理品等の脱液乾燥装置。A heated gas injection pipe having a plurality of through-holes formed in a downward direction at intervals between upper end walls of the steam injection pipe is provided, while saturated steam of the boiler is supplied to a heat exchanger through a supply pipe. The heat exchanger is connected to a blower that sucks gas in the housing by a flexible tube connected to a top wall of the housing, and the gas heated by heat exchange connected to the blower passes through the flexible tube. 2. The dehydrating / drying apparatus for edible vegetable dishes according to claim 1, wherein the apparatus is connected to the heated gas injection pipe introduced through the apparatus and dries the material. 筐体の駆動側端壁下部のスクリユ軸部域には素材が圧縮脱液されてジュースが吐出されるための多数の透孔を有する濾過部を設け、濾過部の外側にはジュースの飛散を防止する止板を設けると共に、下側にはジュースの誘導溝を設けたことを特徴とする請求項1記載の食用植物料理品などの脱液乾燥装置。A filtering part having a large number of through holes for compressing and draining the material and discharging the juice is provided in the screw shaft area at the lower part of the drive side end wall of the housing, and the scattering of the juice is provided outside the filtering part. 2. The dewatering and drying apparatus for edible vegetable dishes according to claim 1, wherein a stop plate for preventing the edible food is provided and a guide groove for juice is provided on a lower side. 筐体の残渣吐出側端壁下部域の吐出開口にはジュースを吐出する多数の透孔を有する開閉蓋を錠で開放可能に設ける一方、素材の脱液乾燥を終了したときは開閉蓋を開放すると共に前記誘導溝の取り外し可能部分を引抜いて、筐体内の残渣を下側のベルトコンベアに落下移送する構成としたことを特徴とする請求項1記載の食用植物料理品等の脱液乾燥装置。An opening / closing lid with a large number of through holes for discharging juice is provided in the discharge opening in the lower region of the end wall on the residue discharge side of the housing so that it can be opened with a lock, while the opening / closing lid is opened when the material is drained and dried. 2. A dewatering and drying apparatus for edible vegetable dishes according to claim 1, wherein the removable portion of the guide groove is pulled out, and the residue in the housing is dropped and transferred to a lower belt conveyor. . 新鮮であるが変形屑状の果実野菜料理品などの素材は分別して集荷し、少量の滅菌剤を混入した水槽水で洗浄し、次に金属などを除去したのち水切りし、所定重量の素材を順次装置上のスライサ開口に投入してゆく、スライサで直径5〜10mm程度に切削された素材は自重で順次装置の筐体内に落下し、その後一対の水平で平行なスクリユが時間的に回転方向の変更を繰返すことにより切削された素材は撹拌されながら圧縮されて脱液される、脱液工程では効率良く処理するために飽和蒸気を噴射して素材を40℃から50℃に加温し、ジュースの吐出量が少なくなったことを視認すると蒸気噴射を停止したのち、加熱気体を噴射して乾燥工程に移行する。ジュース吐出量がなくなると筐体下部の蓋を開放して乾燥残渣を取出して再利用のための処理をなす、一方筐体頂壁からは筐体内の含有水分及び臭気を吸引して臭気を吸収後に煙突から排気することを特徴とする食用植物料理品などの脱液乾燥方法。Materials such as fresh but deformed debris-like fruit and vegetable dishes are separated and collected, washed with aquarium water mixed with a small amount of sterilant, then metal is removed, then drained, and the specified weight of material is removed. The material cut into the slicer opening on the device in order is cut into a diameter of about 5 to 10 mm by the slicer, and falls by its own weight sequentially into the housing of the device, and then a pair of horizontal and parallel screws are rotated in the time direction. The material cut by repeating the change of the above is compressed and dewatered while being stirred.In the dewatering step, the material is heated from 40 ° C to 50 ° C by injecting saturated steam to process it efficiently. When it is visually confirmed that the amount of juice discharged has decreased, the steam injection is stopped, and then the heating gas is injected to shift to the drying step. When the amount of juice discharged is exhausted, the lid at the bottom of the housing is opened to take out the dried residue and perform processing for reuse, while the moisture and odor contained in the housing are sucked from the top wall of the housing to absorb the odor A method for draining and drying edible vegetable dishes, which is later exhausted from the chimney.
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