JP3850985B2 - Vegetation base material, vegetation base and method of manufacturing vegetation base material - Google Patents

Vegetation base material, vegetation base and method of manufacturing vegetation base material Download PDF

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JP3850985B2
JP3850985B2 JP18344598A JP18344598A JP3850985B2 JP 3850985 B2 JP3850985 B2 JP 3850985B2 JP 18344598 A JP18344598 A JP 18344598A JP 18344598 A JP18344598 A JP 18344598A JP 3850985 B2 JP3850985 B2 JP 3850985B2
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dehydrated cake
vegetation base
mixer
base material
mixed
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JP2000014239A (en
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邦裕 富田
六男 松田
孝 岡
政弘 庄田
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Kumagai Gumi Co Ltd
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Kumagai Gumi Co Ltd
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
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Description

【0001】
【発明の属する技術分野】
本発明は、骨材の洗浄水等により発生する濁水を脱水処理して形成された脱水ケーキの有効活用を図るものに関する。
【0002】
【従来の技術】
ダム等の建設現場では、コンクリート打設時の骨材(砂利,砂)生産、バッチャプラントの運転及び基礎処理、原石山の降雨等に伴い、粒度の細かい粘土を含む濁水が発生する。これらの濁水は、それぞれ濁水処理設備に送られ薬品等で処理されるが、その方法としては、濁水処理されたスラッジを予め掘削した沈殿池にポンプ等で貯留して自然乾燥させる沈澱池方式と、上記スラッジをフィルタープレス等の脱水装置で脱水して脱水ケーキを生成し、この脱水ケーキをダンプトラック等で運搬し、指定された建設発生土受け入れ地等に盛土する機械式脱水ケーキ方式とがある。上記沈澱池方式を採用する場合には、ダム工事で発生する大量のスラッジを処理するための広大な沈殿池用地を確保する必要があるため、上記沈澱池用地の確保が難しい場合には、機械式脱水ケーキ方式による濁水処理が行われている。
【0003】
【発明が解決しようとする課題】
しかしながら、脱水ケーキを受け入れ地に盛土する方式では、受け入れ地となるべき広い面積の用地(盛土容量を確保できる分)をあらかじめ確保しなければならないので、コスト面及び管理面で不利となる。また、上記脱水ケーキは土の強度を示す指数であるコーン指数で表わすと0.2MPa以下のいわゆる泥土の状態であるため、このままの状態では運搬時に流動性を呈して運搬に不便なだけでなく、その上を人が歩けない状態であるため、上記脱水ケーキを受け入れ地に盛土する場合にも順次積み重ねて盛土施工できるだけの強度がなかった。また、ダンプ等による運搬時には道路に落とさないようにする等取扱いに注意が必要であった。したがって、脱水ケーキを連続して上記受け入れ地に盛土処分するためには、脱水ケーキの強度を盛土材に適した状態に改良し、盛土施工性の向上を図るとともに、盛土での長期の滑り出しに対する安全性を確保する必要があった。このようなことから、脱水ケーキを受け入れ地に盛土する方式の採用は、コスト面、運搬面、取扱い面、処理量の点である程度の限界を有していた。
【0004】
本発明は、従来の問題点に鑑みてなされたもので、脱水ケーキを植生基盤材及び植生基盤として用いるようにして、盛土の用地を確保する必要がなく、また運搬を容易に行え、しかも取扱い処理量に限界を与えないようにするとともに、植生基盤材の製造方法を提供して、植生基盤材の効率的な製造を可能とする。
【0005】
【課題を解決するための手段】
本発明の請求項1の植生基盤材は、脱水ケーキとセメントなどの固化材とを、複数の平板状の切断板をその回転軸に取付けて成るロータを具備した混合機に投入し、上記脱水ケーキを上記切断板で細断して細分化しながら上記固化材と混合して細粒化処理し、この固化材と混合しながら細粒化した脱水ケーキの粒状体、すなわち、上記混合機を用いて細粒化した脱水ケーキの粒状体を所定時間養生した後に再度細粒化処理して得られた粒状体に、肥料を混合したものである。
【0006】
請求項2の発明の植生基盤は、脱水ケーキとセメントなどの固化材とを、複数の平板状の切断板をその回転軸に取付けて成るロータを具備した混合機に投入し、上記脱水ケーキを上記切断板で細断して細分化しながら上記固化材と混合して細粒化処理し、この上記混合機で固化材と混合しながら細粒化した脱水ケーキの粒状体を所定時間養生した後に再度細粒化処理して得られた粒状体肥料を混合し、植生部位に圧送吹付けして形成したものである。
【0007】
請求項3の発明は、植物の育成が可能な植生基盤材を製造する方法であって、脱水ケーキを粒状化しながらセメントなどの固化材とを、複数の平板状の切断板をその回転軸に取付けて成るロータを具備した混合機に投入し、上記脱水ケーキを上記切断板で細断して細分化しながら上記固化材と混合して細粒化処理し、この上記混合機で固化材と混合しながら細粒化した脱水ケーキの粒状体を所定時間養生した後に再度細粒化処理して得られた粒状体に肥料を混合して、植物の育成が可能な植生基盤材を製造するようにしたものである。
【0009】
請求項の発明は、請求項3記載の植生基盤材の製造方法において、上記再度の細粒化処理は、上記細粒化された脱水ケーキの粒状体上記混合機に再度投入して行うことを特徴とするものである
【0010】
請求項の発明は、請求項3記載の植生基盤材の製造方法において、上記再度の細粒化処理は、上記細粒化された脱水ケーキの粒状体をパドルミキサーに通過させて整粒化することにより行うことを特徴とするものである
【0011】
【発明の実施の形態】
実施の形態1.
以下、本発明の実施の形態について、図面に基づき説明する。
図1は、植生基盤材と植生基盤及び植生基盤材の製造方法を説明するための構成図であり、同図において、1は脱水ケーキと固化材とを混合しながら細粒化を行う装置である混合機、2は脱水ケーキ供給装置、3は固化材供給装置、4は脱水ケーキの処理装置である。
5は図外の濁水処理設備から送られてきたスラッジを脱水して脱水ケーキを生成するためのフィルタープレス、6は上記生成された脱水ケーキを貯蔵するストックヤード、7Aは固化材A(例えばセメント)を貯蔵するサイロ、7Bは固化材B(例えば石灰)を貯蔵するサイロ、8は上記混合機1で固化処理された脱水ケーキを貯蔵するとともに運搬用トラックに上記固化処理された脱水ケーキを供給するための積込みホッパーである。10は細粒化された脱水ケーキを再度細粒化するための搬送ラインを示す。
なお、上記混合機1には、混合機1に備えられたローターの回転数を制御することにより脱水ケーキの処理速度を制御する処理速度制御手段Clが備えられ、上記固化材供給装置3には、上記固化材Aと上記固化材Bとの混合比と固化材の供給量とを制御する固化材供給量制御手段C3が設けられている。
【0012】
次に、上記構成の脱水ケーキの処理システムについて説明する。ダム等の建設現場において、コンクリート打設時の骨材(砂利、砂)生産,バッチャプラントの運転及び基礎処理、原石山の洪水等に伴って発生した濁水は、それそれ濁水処理設備に送られ薬品等で処理された後、フィルタープレス5に送られ脱水処理され、脱水ケーキが生成される。上記脱水ケーキは、脱水ケーキストックヤード6に一時貯蔵された後、所定の処理量だけベルトコンベヤ等の搬送機で脱水ケーキの処理装置4の脱水ケーキ供給装置2に送られ、図外の含水率測定器及び粒度分布測定器により含水率及び粒度を計測された後、脱水ケーキ供給装置2の混合機1に所定の投入速度で投入される。一方、サイロ7Aに貯蔵された固化材A(例えば、セメント)とサイロBに貯蔵された固化材B(例えば、石灰)とは、予め設定された所定量だけ脱水ケーキ供給装置2の固化材供給装置3に送られ、上記計測された脱水ケーキの含水率及び粒度に基づいた比率で混合された後、混合機1に所定の投入速度で投入される。
混合機1には、後述するように、投入された上記脱水ケーキを細断し細粒化するローター1A,1B,1Cが備えられており、この細粒化された上記脱水ケーキは上記固化材と均一に混合した状態で混合機1からホッパー8に排出される。上記固化処理された脱水ケーキの強度は、固化材A(例えば、セメント)と固化材B(例えば、石灰)との混合比や混合機1の処理速度等の混合条件によって多少異なるが、コーン指数で表わすと約0.4MPa以上となり、処理前の脱水ケーキに比べて強度が著しく向上する。
細粒化処理された上記脱水ケーキは、所定量ベルトコンベヤ等の搬送機で積込ホッパー8に送られた後、このホッパー8で所定時間(例えば24時間)養生されてから、搬送ライン10(例えば、ベルトコンベヤ)を経て脱水ケーキ供給装置2から再度混合機1に供給されて細粒化される。この場合、脱水ケーキストックヤード6からの細粒化前の脱水ケーキの供給は停止され、また固化材供給装置3からの固化材の投入は停止された状態で、再度の細粒化が行われる。
【0013】
ここで、上記混合機1の構成及び動作の詳細について説明する。混合機1は、多軸式垂直混合機と呼ばれるもので、図2(a)に示すように、側面のそれぞれ異なる角度の位置に複数の羽根部1bを備えた円筒状の回転軸1aから成る複数のローター1A,1B,1Cを備え、混合機1の上部の材料投入口より投入された脱水ケーキを上記羽根1bで細断し細粒化するとともに、上記材料投入口より投入された固化材と上記細粒化された脱水ケーキとを撹拌混合し、脱水ケーキを固化処理するものである。このように細断による脱水ケーキの粒状化の処理を、本例では細粒化という。上記羽根部1bは、図2(a)に示すように、平板状の脱水ケーキ切断板1cを棒状の支持部材1dを介して上記回転軸1aに取付けたもので、図外のモータにより上記回転軸1aを駆動し上記複数の羽根1bを回転させることにより、図2(b)に示すように、塊状の脱水ケーキ9を細断し細粒化するものである。また、図1に示すように、上記ローター1A,1Bは上記混合機1の上部に対向するように配置され、その回転方向は上記ローター1A,1Bの隙間に投入された脱水ケーキを取込むように互いの回転方向を逆に設定してある。そして、上記ローター1A,1Bの下方に設置されたローター1Cにより、上記ローター1A,1Bで細断され細粒化され固化材と混合された脱水ケーキを更に細断し細粒化して上記固化材と混合することにより、上記脱水ケーキと固化材とを均一に混合することができ、また、処理速度が速いので大量の脱水ケーキの細粒化処理を行うことができる。
【0014】
以上述べたように、一旦混合機1で固化材と混合しながら細粒化した脱水ケーキをホッパー8から搬送ライン10を経由して再度混合機1に投入して、ここで再度の細粒化処理を行う。このように再度細粒化処理することにより、後述するように、比較的小さい粒状体が得られ、これを肥料混合機11に供給して、肥料と混合することにより肥料混合機11より植生すべき植物の育成に最も適した植生基盤材12が得られる。次に肥料と混合された脱水ケーキから成る植生基盤材12は、そのままトラックなどで運搬して造園敷地などに敷いて、これにより得られる造園内の植生基盤に植物を植生してもよい。又この植生基盤材12を図3に示す圧送吹付け装置13に供給してこの圧送吹付け装置13から植生部位14に吹付けることにより植生基盤15を形成してもよい。上記圧送吹付け装置13は空気吸入口16からの空気と、導入管17から導入される上記植生基盤材12と、導入管18から導入される疎水剤19とを、吹出し口20から比較的高速で吹出して植生部位14の表面に吹付けるようにした装置であり、上記疎水剤19は吹出口20から吹き出される植生基盤材を団粒化するための機能を果たす。上記導入管17に導入される粒状化された脱水ケーキと肥料との混合体から成る植生基盤材12は、適当な水が加えられて泥状材として導入管17に供給されて、空気とともに吹出される。
また、再度の細粒化処理を行った脱水ケーキを、図示しない通常の吹付プラント装置を用いて圧送吹付けし、植生部位14に植生基盤15を形成しても良い。
【0015】
このような圧送吹付け装置13を用いて植生部位14の表面にほぼ均一な厚みを有して吹付けることに基づき、植生基盤15を形成することができ、この植生基盤15に所定の植物を植えることができる。
上記植生部位14としては、例えば崩壊地斜面開発工事等により発生する切土及び盛土の傾斜面、乾燥の甚だしい砂丘の地表面、あるいは岩盤とか土壌の少ない軟岩や粘性土壌などが考えられるが、その他、ビルなどの構造物の傾斜部分等人工のものであってもよく、要は緑化すべき部位であればどの様な所でもよい。図4は、図1に示す細粒化の装置で粒状化されることにより得られる粒状体をふるいにかけた場合を示す特性図であり、図4において特性曲線21は脱水ケーキと固化材とを混合機1に投入して細粒化しながら混合する細粒化処理を一回だけ行った場合(初回)の特性を示すもので、特性曲線22は搬送ライン10を用いて初回に細粒化された脱水ケーキを再度混合機1によって細粒化処理した場合の特性を示すものである。この特性曲線21,22において、圧送吹付け装置13に使用し得る脱水ケーキの粒状体のふるい呼び寸法20mm程度以下のメッシュを通過できる程度に小さいものが好ましいのであるが、この程度の粒径の小さい粒状体は、特性曲線21(細粒化1回のみ)では最大50パーセント程度しか得られないが、特性曲線22(細粒化2回)ではふるい呼び寸法20mm程度で90パーセント以上のものがふるいを通ることが理解できるので、このことから、2回細粒化処理を行うことにより圧送吹付け装置13に使用し得る小さな粒形の粒状体を含む植生基盤材12を得ることができることがわかる。
【0016】
実施の形態2.
図5は、本発明による実施の形態2の植生基盤材と植生基盤及び植生基盤材の製造方法を示す構成図であり、図1と同じものは同一符号を用いている。この実施の形態2ではホッパー8に貯えられた脱水ケーキを、例えば1日養生した後、搬送ライン23を介してパドルミキサー24に供給し、このパドルミキサー24のパドル25の回転に基づいて脱水ケーキを一定方向に送りながら、しかも下から上に持ち上げるようにして、解すようにして脱水ケーキを再度粒状化処理するものである。このパドルミキサー24による細粒化を本例では整粒化という。
図6(a),(b)は、パドルミキサー24の概略を示す図で、パドル25は、パドルミキサー24の樋部26の長手方向に設けられた互いに2本の平行なシャフト27,28の外周から、一定の間隔をおいて互いに円周方向に90度ずつずれて突出する複数の腕部29に所定の角度(例えば、45度)に取り付けられている。上記シャフト27,28の回転に伴って、上記複数のパドル25が回転し、パドルミキサー24の樋部26に投入される脱水ケーキを下流に送りながら解すことにより脱水ケーキを細かく整粒化する。なお、上記平行なシャフト27,28は、投入された脱水ケーキが上記シャフト27,28間に運ばれるように、互いに反対方向に回転している。
このようにして再度、パドルミキサー24で整粒化処理した植生基盤材12は図3において説明した圧送吹付け装置13に供給されて植生部位14に吹付けられることにより、植生基盤15を形成する。この場合には、この再度粒状化された脱水ケーキをふるいにかけると、図4の特性曲線23が選られた。この特性曲線23から理解できるように、ふるいの呼び寸法が20mm程度でほぼ90パーセント以上のものがふるいを通るので、これを圧送吹付け装置13に適応し得ることになる。
【0017】
実施の形態3.
図7は実施の形態3の一例を示す図であり、図1と同じものは同一符号を用いている。この場合は、混合機1と同じローター1A,1B,1Cを備えた細粒化処理を行う装置30を別途設けており、この装置30の中に、ホッパー8に投入された混合機1側からの脱水ケーキを一旦養生してから再度投入して細粒化するものである。即ち、図1と異なる点は、細粒化する装置30を別途設けて脱水ケーキを細断により再度細粒化するものである。このように別な装置30を用いて2回細粒化しても、図1の場合と同様な好ましい結果が得られる。
【0018】
なお、本発明においては圧送吹付け装置13に対して最も好ましいふるい呼び寸法の大きさは最大20mmであるとして説明したが、この最大値は圧送吹付け装置13の処理速度及び吹出し口20の径の大きさなどにより変化することはもちろんである。
【0019】
又、肥料の混合は肥料混合機11を別途設けて脱水ケーキと混合するとして説明したが、肥料を混合機1に投入するようにして混合機1を用いて肥料を脱水ケーキに混合するようにしても、あるいは圧送吹付け装置13に肥料を含む液体を供給するようにして、圧送吹付け装置13によって脱水ケーキと混合するようにしても良い。
【0020】
又、脱水ケーキは2回細粒化又は、整粒化などの粒状化処理を行うとして説明したが、3回以上の粒状化処理を行うようにしても良い。
又、細粒化あるいは整粒化などの粒状化処理は、混合機あるいはパドルミキサーなどを用いて処理するものに限定されず、他の装置を用いて粒状化してもよいことはもちろんである。
【0021】
又、初回の粒状化処理の後で行う再度の粒状化処理は、初回の粒状化処理を行った脱水ケーキを一旦ある程度の時間養生してから行うのが好ましいことが判明している。この養生の時間は粒状化して得られる植生基盤材に含まれる粒状体の大きさを考慮して設定される。
【0022】
又、脱水ケーキに混合する肥料は例えばバーク堆肥などが考えられるが、植生すべき植物の種類に応じて種々の肥料が考えられ、またその混合割合においても植生による育成の結果を判断して、最適な値に設定すれば良い。
この場合、バーク堆肥に換えてピートモスを用いても良く、その置き換えの量については植生基盤材12中の有機物濃度を検出することにより算定される。
又、混合機1に脱水ケーキと共に供給するセメントなどの固化材の量及び水の量などについては、吹付けられて形成された植生基盤15自体の土壌硬度の大きさ及び支持力強度を算出することにより設定されることはもちろんである。
又、植生基盤材12は脱水ケーキと固化材以外に例えば土砂などの成分を混合しても良いことはもちろんである。
【0023】
又、脱水ケーキに加える固化材としてのセメントと石灰は重量比で1対1を解砕混合することが考えられるが、上記重量比についても植生すべき植物あるいは、植生基盤の硬度などを考慮して種々の値に設定される。
又、初回の粒状化処理は、混合機1で行うとして説明したが、この処理をパドルミキサー24で行ってもよい。
【0024】
【発明の効果】
請求項1の発明によれば、脱水ケーキと固化材とを、複数の平板状の切断板をその回転軸に取付けて成るロータを具備した混合機に投入し、上記脱水ケーキを上記切断板で細断して細分化しながら上記固化材と混合して細粒化処理し、この上記混合機で固化材と混合しながら細粒化した脱水ケーキの粒状体を所定時間養生した後に再度細粒化処理して得られた粒状体に、肥料を混合して植生基盤材を形成したので、この植生基盤材を造園を行う場所とか、或いは岩盤などの種々の植生部位に層状に堆積することにより、ここに植物を植えて育成することが可能となり、従来のように脱水ケーキの盛土の用地を確保する必要がなく、コスト的にも有利で、しかも植生基盤材は粒状体となっているので運搬及び取扱いの点でも有利となる。
【0025】
請求項2の発明によれば、脱水ケーキとセメント等の固化材とを、複数の平板状の切断板をその回転軸に取付けて成るロータを具備した混合機に投入し、上記脱水ケーキを上記切断板で細断して細分化しながら上記固化材と混合して細粒化処理し、この上記混合機で固化材と混合しながら細粒化した脱水ケーキの粒状体を所定時間養生した後に再度細粒化処理して得られた粒状体肥料を混合し、これを植生部位に圧送吹付けすることにより植生基盤を形成するようにしたので、上記吹付けにより岩盤などの傾斜した部分に植生基盤を容易に形成することが可能となる。
【0026】
請求項3の発明によれば、脱水ケーキを固化材とを、複数の平板状の切断板をその回転軸に取付けて成るロータを具備した混合機に投入し、上記脱水ケーキを上記切断板で細断して細分化しながら上記固化材と混合して細粒化処理し、この上記混合機で固化材と混合しながら細粒化した脱水ケーキの粒状体を所定時間養生した後に再度細粒化処理して得られた粒状体に肥料を混合して、植物の育成が可能な植生基盤材を製造するようにしたので、運搬及び取扱いが容易で、かつ、圧送吹付け装置に使用し得る植生基盤材を得ることができる。
【0028】
請求項の発明によれば、上記再度の細粒化処理は、上記細粒化された脱水ケーキの粒状体上記混合機に再度投入して行うので簡単な設備により細粒化の処理を行うことができる。
【0029】
請求項の発明によれば、上記再度の細粒化処理は、上記細粒化された脱水ケーキの粒状体をパドルミキサーに通過させて行うようにしたので、より粒径の小さい粒状体を含む植生基盤材を得る事ができる。
【図面の簡単な説明】
【図1】 この発明の1実施の形態を示す簡略構成図である。
【図2】 この発明の1実施の形態の要部を示す簡略構成図である。
【図3】 この発明の1実施の形態に用いる圧送吹付け装置の一例を示す図である。
【図4】 この発明の1実施の形態及び他の実施の形態の植生基盤材に含まれる粒状体の大きさを説明するための特性図である。
【図5】 この発明の他の実施の形態を示す簡略構成図ある。
【図6】 この発明の他の実施の形態に用いるパドルミキサーの概略を示す図である。
【図7】 この発明の他の実施の形態を示す図である。
【符号の説明】
1 混合機、2 脱水ケーキ供給装置、3 固化材供給装置、8 ホッパー、10,23 搬送ライン、11 肥料混合機、12 植生基盤材、13 圧送吹付け装置、14 植生部位、15 植生基盤、24 パドルミキサー。
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to an effective utilization of a dehydrated cake formed by dehydrating muddy water generated by washing water for aggregates or the like.
[0002]
[Prior art]
At construction sites such as dams, turbid water containing fine-grained clay is generated due to aggregate production (gravel, sand) at the time of concrete placement, operation and basic treatment of the batcher plant, rainfall on the rough rocks, etc. These muddy waters are respectively sent to muddy water treatment facilities and treated with chemicals, etc., as a method for this, a sludge treated with muddy water is stored in a settling pond that has been excavated in advance with a pump or the like and is naturally dried. The sludge is dehydrated with a dehydrator such as a filter press to produce a dehydrated cake, and the dehydrated cake is transported with a dump truck, etc. is there. When the above sedimentation basin method is adopted, it is necessary to secure a large sedimentation basin site for treating a large amount of sludge generated during dam construction. The muddy water treatment by the dehydrated cake method is performed.
[0003]
[Problems to be solved by the invention]
However, the method of embedding the dehydrated cake on the receiving site is disadvantageous in terms of cost and management because a large area of land (to be able to secure the embankment capacity) has to be secured in advance. In addition, the dehydrated cake is in a so-called mud state of 0.2 MPa or less in terms of the cone index, which is an index indicating the strength of the soil. Since it is in a state in which no one can walk on it, even when the dehydrated cake is embanked on the receiving ground, it has not been strong enough to be piled up one after another. In addition, it was necessary to be careful in handling such as not to drop it on the road during transportation by dump. Therefore, in order to continuously dispose of the dewatered cake on the above receiving land, the strength of the dewatered cake is improved to a state suitable for the embankment material, and the workability of the embankment is improved, and the long-term sliding on the embankment is prevented. It was necessary to ensure safety. For this reason, the adoption of the method of embedding the dehydrated cake on the receiving site has some limitations in terms of cost, transportation, handling, and throughput.
[0004]
The present invention has been made in view of the conventional problems, and it is not necessary to secure a land for embankment by using a dehydrated cake as a vegetation base material and a vegetation base, and it can be easily transported and handled. The processing amount is not limited and a method for manufacturing a vegetation base material is provided to enable efficient manufacture of the vegetation base material.
[0005]
[Means for Solving the Problems]
The vegetation base material according to claim 1 of the present invention is charged with a dehydrating cake and a solidified material such as cement into a mixer equipped with a rotor having a plurality of flat cutting plates attached to a rotating shaft thereof. The cake is shredded with the cutting plate and mixed with the solidification material while being subdivided, and then granulated , and the dehydrated cake granulated while mixing with the solidification material , that is, using the mixer Then , fertilizer is mixed with the granulate obtained by curing the granulated dehydrated cake for a predetermined time and then repulverizing it again.
[0006]
The vegetation base of the invention of claim 2 is a method in which a dehydrated cake and a solidified material such as cement are put into a mixer equipped with a rotor having a plurality of flat cut plates attached to a rotating shaft thereof, after while subdivided chopped by the cutting plate then mixed with the solidifying material treated comminuted, granular material of fine phased dehydrated cake while mixing with solidifying material in the above mixer and cured a predetermined time It is formed by mixing granular fertilizers obtained by re-fine graining again and pressurizing and spraying onto the vegetation site.
[0007]
The invention of claim 3 is a method for producing a vegetation base material capable of growing a plant, wherein a solidified material such as cement is granulated into a dehydrated cake, and a plurality of flat plate-shaped cutting plates are used as rotation axes thereof. The dehydrated cake is mixed with the solidified material while being shredded by the cutting plate and mixed with the solidified material, and then granulated, and mixed with the solidified material by the mixer. a mixture of fertilizer granules of fine phased dewatered cake granules obtained by re-fining process after a predetermined time curing with, so as to produce the vegetation base material capable of plant growth It is a thing.
[0009]
The invention of claim 4 is a method of manufacturing a vegetation base material according to claim 3, wherein, grain refining process in again, the particulate material of the grain refining has been dehydrated cake was re-introduced into the mixer It is characterized by doing.
[0010]
The invention of claim 5 is a method of manufacturing a vegetation base material according to claim 3, wherein, grain refining process in again, in the granules of the grain refining has been dehydrated cake is passed through a paddle mixer sizing It is characterized by being performed.
[0011]
DETAILED DESCRIPTION OF THE INVENTION
Embodiment 1 FIG.
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
FIG. 1 is a configuration diagram for explaining a vegetation base material, a vegetation base, and a method for manufacturing the vegetation base material. In FIG. 1, reference numeral 1 denotes an apparatus that performs fine granulation while mixing a dehydrated cake and a solidified material. A mixing machine, 2 is a dehydrated cake supply device, 3 is a solidifying material supply device, and 4 is a dewatered cake processing device.
5 is a filter press for dewatering sludge sent from a muddy water treatment facility (not shown) to produce a dehydrated cake, 6 is a stock yard for storing the produced dehydrated cake, and 7A is a solidified material A (for example, cement). 7B is a silo for storing solidified material B (for example, lime), 8 is for storing the dehydrated cake solidified by the mixer 1, and supplying the solidified dehydrated cake to the transport truck. It is a loading hopper. Reference numeral 10 denotes a conveyance line for re-sizing the refined dehydrated cake.
The mixer 1 is provided with processing speed control means Cl for controlling the processing speed of the dehydrated cake by controlling the rotational speed of the rotor provided in the mixer 1, and the solidifying material supply device 3 includes Solidification material supply amount control means C3 for controlling the mixing ratio of the solidification material A and the solidification material B and the supply amount of the solidification material is provided.
[0012]
Next, the dewatering cake processing system having the above-described configuration will be described. At the construction site such as a dam, muddy water generated by the production of aggregates (gravel, sand) at the time of concrete placement, operation and basic treatment of the batcher plant, flooding of the rough rocks, etc. is sent to the muddy water treatment facility. After being treated with chemicals or the like, it is sent to the filter press 5 and dehydrated to produce a dehydrated cake. The dehydrated cake is temporarily stored in the dehydrated cake stock yard 6 and then sent to the dehydrated cake supply device 2 of the dehydrated cake processing device 4 by a conveyor such as a belt conveyor by a predetermined processing amount. After the moisture content and particle size are measured by the measuring device and the particle size distribution measuring device, the water content and the particle size are measured and then charged into the mixer 1 of the dehydrated cake supply device 2 at a predetermined charging speed. On the other hand, the solidified material A (for example, cement) stored in the silo 7A and the solidified material B (for example, lime) stored in the silo B are supplied to the dehydrated cake supply device 2 by a predetermined amount. After being sent to the apparatus 3 and mixed at a ratio based on the measured moisture content and particle size of the dehydrated cake, it is charged into the mixer 1 at a predetermined charging speed.
As will be described later, the mixer 1 is provided with rotors 1A, 1B, and 1C for chopping and finely pulverizing the charged dehydrated cake, and the finely divided dehydrated cake is the solidified material. And is uniformly mixed and discharged from the mixer 1 to the hopper 8. The strength of the solidified dehydrated cake varies somewhat depending on the mixing conditions such as the mixing ratio of the solidifying material A (for example, cement) and the solidifying material B (for example, lime) and the processing speed of the mixer 1, but the cone index. Is about 0.4 MPa or more, and the strength is remarkably improved as compared with the dehydrated cake before the treatment.
The dehydrated cake that has been subjected to the fine granulation process is sent to the loading hopper 8 by a predetermined amount of conveyor such as a belt conveyor, and then cured by the hopper 8 for a predetermined time (for example, 24 hours). For example, the mixture is supplied again from the dehydrated cake supply device 2 via the belt conveyor) to the mixer 1 and is finely divided. In this case, the supply of the dehydrated cake before the fine granulation from the dehydrated cake stock yard 6 is stopped, and the addition of the solidified material from the solidified material supply device 3 is stopped, and the fine granulation is performed again. .
[0013]
Here, the configuration and operation of the mixer 1 will be described in detail. The mixer 1 is called a multi-axis vertical mixer, and as shown in FIG. 2 (a), comprises a cylindrical rotary shaft 1a having a plurality of blade portions 1b at different angular positions on the side surfaces. A plurality of rotors 1A, 1B, and 1C are provided, and the dehydrated cake fed from the material inlet at the top of the mixer 1 is shredded and pulverized by the blade 1b, and the solidified material fed from the material inlet And the finely divided dehydrated cake are stirred and mixed to solidify the dehydrated cake. In this example, the process of granulating the dehydrated cake by chopping is called fine graining. As shown in FIG. 2 (a), the blade portion 1b is obtained by attaching a flat plate-shaped dewatered cake cutting plate 1c to the rotary shaft 1a via a rod-like support member 1d. By driving the shaft 1a and rotating the plurality of blades 1b, as shown in FIG. 2 (b), the massive dehydrated cake 9 is shredded and made fine. Further, as shown in FIG. 1, the rotors 1A and 1B are arranged so as to face the upper part of the mixer 1, and the rotation direction of the rotors 1A and 1B is to take in the dehydrated cake put into the gap between the rotors 1A and 1B. The rotation directions of each other are set in reverse. Then, by the rotor 1C installed below the rotors 1A and 1B, the dehydrated cake shredded by the rotors 1A and 1B and then finely divided and mixed with the solidified material is further shredded and finely divided to obtain the solidified material. The dehydrated cake and the solidified material can be uniformly mixed, and the processing speed is fast, so that a large amount of dehydrated cake can be refined.
[0014]
As described above, the dehydrated cake once refined while being mixed with the solidified material in the mixer 1 is charged again into the mixer 1 from the hopper 8 via the conveying line 10 and is then refined again. Process. As described later, a relatively small granule is obtained by performing the refining process again in this manner, and this is supplied to the fertilizer mixer 11 and mixed with the fertilizer to vegetate from the fertilizer mixer 11. A vegetation base material 12 most suitable for growing a plant to be obtained is obtained. Next, the vegetation base material 12 made of a dehydrated cake mixed with fertilizer may be transported as it is by a truck or the like and spread on a landscaping site or the like, and plants may be vegetated on the vegetation base in the landscaping obtained as a result. Alternatively, the vegetation base 15 may be formed by supplying the vegetation base 12 to the pressure blowing device 13 shown in FIG. The pressure blowing device 13 is configured to remove air from the air inlet 16, the vegetation base material 12 introduced from the introduction pipe 17, and the hydrophobic agent 19 introduced from the introduction pipe 18 from the outlet 20 at a relatively high speed. The hydrophobic agent 19 fulfills the function of aggregating the vegetation base material blown from the blower outlet 20. The vegetation base material 12 made of a mixture of granulated dehydrated cake and fertilizer introduced into the introduction pipe 17 is supplied to the introduction pipe 17 as a muddy material by adding appropriate water and blown out together with air. Is done.
Alternatively, the dehydrated cake that has been subjected to the refining treatment again may be pressure-fed and sprayed using a normal spray plant device (not shown) to form the vegetation base 15 in the vegetation site 14.
[0015]
A vegetation base 15 can be formed based on spraying the surface of the vegetation site 14 with a substantially uniform thickness using such a pressure-feeding spraying device 13, and a predetermined plant is applied to the vegetation base 15. Can be planted.
Examples of the vegetation site 14 include cuts and embankment slopes generated by collapsing slope development, etc., dry sand dunes, or soft rocks and clayey soils with little rock or soil. An artificial part such as an inclined part of a structure such as a building may be used. In short, any part may be used as long as it is a part to be greened. FIG. 4 is a characteristic diagram showing the case where the granulated material obtained by granulating with the atomization apparatus shown in FIG. 1 is sieved. In FIG. 4, the characteristic curve 21 shows the dehydrated cake and the solidified material. The characteristic curve 22 shows the characteristic when the fine granulation process is performed only once (the first time) while mixing into the mixer 1 while finely pulverizing, and the characteristic curve 22 is first refined using the transport line 10. This shows the characteristics when the dehydrated cake is again refined by the mixer 1. In these characteristic curves 21 and 22, it is preferable that the particle size of the dehydrated cake that can be used for the pressure spraying device 13 is small enough to pass through a mesh having a nominal size of about 20 mm or less. A small granular material can be obtained only about 50% at maximum in the characteristic curve 21 (only once finely pulverized), but the characteristic curve 22 (2 times finely divided) has a sieve nominal size of about 20 mm and more than 90%. Since it can be understood that it passes through a sieve, it is possible to obtain a vegetation base material 12 containing small granular particles that can be used in the pressure spraying device 13 by performing the granulation process twice. Recognize.
[0016]
Embodiment 2. FIG.
FIG. 5 is a configuration diagram showing a vegetation base material, a vegetation base, and a method for manufacturing the vegetation base material according to the second embodiment of the present invention, and the same components as those in FIG. In the second embodiment, the dehydrated cake stored in the hopper 8 is cured for one day, for example, and then supplied to the paddle mixer 24 via the transport line 23, and the dehydrated cake is rotated based on the rotation of the paddle 25 of the paddle mixer 24. The dehydrated cake is granulated again by lifting it up from below and lifting it up in a certain direction. In the present example, the fine graining by the paddle mixer 24 is referred to as granulating.
FIGS. 6A and 6B are diagrams schematically showing the paddle mixer 24. The paddle 25 is composed of two parallel shafts 27 and 28 provided in the longitudinal direction of the flange portion 26 of the paddle mixer 24. FIG. A plurality of arm portions 29 projecting from the outer periphery by 90 degrees in the circumferential direction with a certain interval are attached to the arms 29 at a predetermined angle (for example, 45 degrees). As the shafts 27 and 28 rotate, the plurality of paddles 25 rotate, and the dehydrated cake is finely sized by unraveling while feeding the dehydrated cake put into the flange portion 26 of the paddle mixer 24 downstream. The parallel shafts 27 and 28 rotate in directions opposite to each other so that the dewatered cake that has been introduced is carried between the shafts 27 and 28.
In this way, the vegetation base material 12 that has been subjected to the particle size regulation by the paddle mixer 24 is supplied to the pressure spraying device 13 described in FIG. 3 and sprayed onto the vegetation site 14 to form the vegetation base 15. . In this case, when this de-granulated dehydrated cake was sieved, the characteristic curve 23 of FIG. 4 was selected. As can be understood from the characteristic curve 23, since a sieve having a nominal size of about 20 mm and approximately 90% or more passes through the sieve, it can be applied to the pressure blowing device 13.
[0017]
Embodiment 3 FIG.
FIG. 7 is a diagram showing an example of the third embodiment, and the same components as those in FIG. In this case, a device 30 for carrying out the fine graining process, which is provided with the same rotor 1A, 1B, 1C as that of the mixer 1, is provided separately from the side of the mixer 1 charged into the hopper 8. The dehydrated cake is cured once and then charged again to make it fine. That is, the point different from FIG. 1 is that a device 30 for finely pulverizing is separately provided and the dehydrated cake is pulverized again by chopping. Thus, even if it refines twice using another apparatus 30, the same preferable result as the case of FIG. 1 is obtained.
[0018]
In the present invention, it has been described that the most preferable size of the sieve size for the pressure blowing device 13 is 20 mm at maximum, but this maximum value is the processing speed of the pressure blowing device 13 and the diameter of the outlet 20. Of course, it varies depending on the size of the.
[0019]
In addition, it has been described that the fertilizer is mixed with the dehydrated cake by separately providing the fertilizer mixer 11, but the fertilizer is added to the mixer 1 so that the fertilizer is mixed with the dehydrated cake. Alternatively, a liquid containing fertilizer may be supplied to the pressure spraying device 13 and mixed with the dehydrated cake by the pressure spraying device 13.
[0020]
Further, the dehydrated cake has been described as being subjected to a granulation process such as two times of granulation or sizing, but the granulation process may be performed three or more times.
Further, the granulation treatment such as fine granulation or sizing is not limited to the treatment using a mixer or a paddle mixer, and it goes without saying that the granulation may be carried out using another apparatus.
[0021]
Further, it has been found that the re-granulation process performed after the first granulation process is preferably performed after the dehydrated cake subjected to the first granulation process is once cured for a certain period of time. This curing time is set in consideration of the size of the granular material contained in the vegetation base material obtained by granulation.
[0022]
In addition, the fertilizer to be mixed with the dehydrated cake can be, for example, bark compost, etc., but various fertilizers can be considered according to the type of plant to be vegetated, and also determine the result of growth by vegetation in the mixing ratio, What is necessary is just to set to the optimal value.
In this case, peat moss may be used instead of bark compost, and the amount of replacement is calculated by detecting the organic matter concentration in the vegetation base material 12.
Moreover, about the quantity of solidification materials, such as cement supplied to the mixer 1 with a dewatering cake, and the quantity of water, the magnitude | size of soil hardness and the bearing strength intensity of the vegetation base 15 itself formed by spraying are calculated. Of course, it is set by
Of course, the vegetation base material 12 may be mixed with components such as earth and sand in addition to the dehydrated cake and the solidified material.
[0023]
Cement and lime as a solidifying material to be added to the dehydrated cake may be crushed and mixed one to one by weight, but the weight ratio also takes into account the plant to be vegetated or the hardness of the vegetation base. Are set to various values.
Further, although the first granulation process is described as being performed by the mixer 1, this process may be performed by the paddle mixer 24.
[0024]
【The invention's effect】
According to the first aspect of the present invention, the dewatered cake and the solidified material are put into a mixer having a rotor formed by attaching a plurality of flat plate-shaped cutting plates to the rotating shaft thereof, and the dewatered cake is fed by the cutting plate. while subdividing chopped and mixed with the solidifying material treated comminuted again fining after the granules of fine phased dehydrated cake while mixing with solidifying material in the above mixer was cured a predetermined time Since the vegetation base material was formed by mixing the fertilizer with the granular material obtained by processing, by depositing this vegetation base material in a layered manner on various vegetation sites such as a place to landscaping, It is possible to plant and grow plants here, and it is not necessary to secure a land for embedding dehydrated cake as before, which is advantageous in terms of cost, and the vegetation base material is granular, so it is transported And it is also advantageous in terms of handling.
[0025]
According to the invention of claim 2, the dehydrated cake and the solidified material such as cement are put into a mixer having a rotor in which a plurality of flat cut plates are attached to the rotating shaft, and the dehydrated cake is added to the above-mentioned dehydrated cake. while finely divided by chopping the cutting plate treated comminuted and mixed with the solidifying material, again granulate of granules phased dehydrated cake while mixing with solidifying material in the above mixer after a predetermined time curing Since the vegetation base was formed by mixing the granular fertilizer obtained by the fine graining treatment and pressurizing and spraying this to the vegetation site, the vegetation base was formed on the inclined part of the bedrock by the above spraying Can be easily formed.
[0026]
According to the invention of claim 3, the dehydrated cake is put into a solidifying material, and the dehydrated cake is put into the mixer with a rotor formed by attaching a plurality of flat plate-shaped cutting plates to the rotating shaft. while subdividing chopped and mixed with the solidifying material treated comminuted again fining after the granules of fine phased dehydrated cake while mixing with solidifying material in the above mixer was cured a predetermined time Since the fertilizer is mixed with the granular material obtained by the treatment to produce a vegetation base material capable of growing plants, vegetation that is easy to transport and handle and that can be used in a pressure spraying device A base material can be obtained.
[0028]
According to the invention of claim 4, grain refining process in again, the process of grain refinement by simple equipment since the granules of the grain refining has been dehydrated cake was re-introduced into the mixer It can be performed.
[0029]
According to the invention of claim 5, grain refining process in again, so was to perform granules of the grain refining has been dehydrated cake was passed through a paddle mixer, more small particle diameter granules Can be obtained vegetation base material containing.
[Brief description of the drawings]
FIG. 1 is a simplified configuration diagram showing an embodiment of the present invention.
FIG. 2 is a simplified configuration diagram showing a main part of one embodiment of the present invention.
FIG. 3 is a view showing an example of a pressure blowing apparatus used in one embodiment of the present invention.
FIG. 4 is a characteristic diagram for explaining the size of a granular material contained in a vegetation base material according to one embodiment and another embodiment of the present invention.
FIG. 5 is a simplified configuration diagram showing another embodiment of the present invention.
FIG. 6 is a diagram showing an outline of a paddle mixer used in another embodiment of the present invention.
FIG. 7 is a diagram showing another embodiment of the present invention.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Mixer, 2 Dehydrated cake supply apparatus, 3 Solidification material supply apparatus, 8 Hoppers, 10, 23 Conveyance line, 11 Fertilizer mixing machine, 12 Vegetation base material, 13 Pressure feeding apparatus, 14 Vegetation site, 15 Vegetation base, 24 Paddle mixer.

Claims (5)

骨材の洗浄水等により発生する濁水を脱水処理して形成された脱水ケーキと固化材とを、複数の平板状の切断板をその回転軸に取付けて成るロータを具備した混合機に投入し、上記脱水ケーキを上記切断板で細断して細分化しながら上記固化材と混合して細粒化処理し、この上記混合機で固化材と混合しながら細粒化した脱水ケーキの粒状体を所定時間養生した後に再度細粒化処理して得られた粒状体に、肥料を混合して成ることを特徴とする植生基盤材。The dehydrated cake formed by dehydrating the turbid water generated by the washing water of the aggregate and the solidified material are put into a mixer equipped with a rotor having a plurality of plate-shaped cutting plates attached to its rotating shaft. , the dehydrated cake was mixed with the solidifying material with finely divided by chopping in the cutting plate treated comminuted, granular material of fine phased dehydrated cake while mixing with solidifying material in the above mixer A vegetation base material obtained by mixing a fertilizer with a granule obtained by curing for a predetermined time and then re-sizing. 骨材の洗浄水等により発生する濁水を脱水処理して形成された脱水ケーキと固化材とを、複数の平板状の切断板をその回転軸に取付けて成るロータを具備した混合機に投入し、上記脱水ケーキを上記切断板で細断して細分化しながら上記固化材と混合して細粒化処理し、この上記混合機で固化材と混合しながら細粒化した脱水ケーキの粒状体を所定時間養生した後に再度細粒化処理して得られた粒状体肥料を混合し、植生部位に圧送吹付けして形成したことを特徴とする植生基盤。The dehydrated cake formed by dehydrating the turbid water generated by the washing water of the aggregate and the solidified material are put into a mixer equipped with a rotor having a plurality of plate-shaped cutting plates attached to its rotating shaft. , the dehydrated cake was mixed with the solidifying material with finely divided by chopping in the cutting plate treated comminuted, granular material of fine phased dehydrated cake while mixing with solidifying material in the above mixer A vegetation base characterized by being formed by mixing granular fertilizers obtained by refining after a predetermined period of curing and pressure-spraying the vegetation site. 骨材の洗浄水等により発生する濁水を脱水処理して形成された脱水ケーキと固化材とを、複数の平板状の切断板をその回転軸に取付けて成るロータを具備した混合機に投入し、上記脱水ケーキを上記切断板で細断して細分化しながら上記固化材と混合して細粒化処理し、この上記混合機で固化材と混合しながら細粒化した脱水ケーキの粒状体を所定時間養生した後に再度細粒化処理して得られた粒状体に肥料を混合して、植物の育成が可能な植生基盤材を製造するようにしたことを特徴とする植生基盤材の製造方法。The dehydrated cake formed by dehydrating the turbid water generated by the washing water of the aggregate and the solidified material are put into a mixer equipped with a rotor having a plurality of plate-shaped cutting plates attached to its rotating shaft. , the dehydrated cake was mixed with the solidifying material with finely divided by chopping in the cutting plate treated comminuted, granular material of fine phased dehydrated cake while mixing with solidifying material in the above mixer A method for producing a vegetation base material, characterized in that fertilizer is mixed with granules obtained by refining again after curing for a predetermined time to produce a vegetation base material capable of growing plants. . 上記再度の細粒化処理は、上記細粒化された脱水ケーキの粒状体を上記混合機に再度投入して行うことを特徴とする請求項3記載の植生基盤材の製造方法。  4. The method for producing a vegetation base material according to claim 3, wherein the refining treatment is performed again by feeding the finely divided dehydrated cake granules into the mixer. 上記再度の細粒化処理は、上記細粒化された脱水ケーキの粒状体をパドルミキサーに通過させて整粒化することにより行うことを特徴とする請求項3記載の植生基盤材の製造方法。  4. The method for producing a vegetation base material according to claim 3, wherein the re-granulation treatment is performed by passing the granulated particles of the dehydrated cake through a paddle mixer for size regulation. .
JP18344598A 1998-06-30 1998-06-30 Vegetation base material, vegetation base and method of manufacturing vegetation base material Expired - Lifetime JP3850985B2 (en)

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