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JP4016898B2 - Freezing and thawing equipment - Google Patents
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JP4016898B2 - Freezing and thawing equipment - Google Patents

Freezing and thawing equipment Download PDF

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JP4016898B2
JP4016898B2 JP2003190029A JP2003190029A JP4016898B2 JP 4016898 B2 JP4016898 B2 JP 4016898B2 JP 2003190029 A JP2003190029 A JP 2003190029A JP 2003190029 A JP2003190029 A JP 2003190029A JP 4016898 B2 JP4016898 B2 JP 4016898B2
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sludge
freeze
thaw
tank
raw
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JP2005021802A (en
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幹昌 山口
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Fuji Electric Co Ltd
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Fuji Electric Systems Co Ltd
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Description

【0001】
【発明の属する技術分野】
本発明は浄水場の排水汚泥、産業排水汚泥の脱水処理において、凍結処理と融解処理とを用いて汚泥の脱水性を改善した、汚泥の脱水装置に関する。
【0002】
【従来の技術】
上下水処理場汚泥や産業排水汚泥の発生量は年々増加する傾向にあり、脱水汚泥の処分地不足が大きな問題となっている。また最近では、環境保全あるいは循環型社会の構築に向けて脱水汚泥の有効利用化が促進されている。この処分や有効利用に際しては、原汚泥に薬品を添加することなく効率よく濃縮して低含水状態に脱水することが重要である。
この汚泥脱水装置の一つとして凍結融解処理装置がある。凍結融解処理装置は無薬注方式であり、浄水汚泥などの難ろ過性の原汚泥を凍結融解処理により粗大粒子に改質し、高いろ過速度で低含水状態に脱水する際に使用される。
【0003】
凍結融解の原理は、霜柱の成長や凍み豆腐の製造に見られるように凍結により固体と液体との分離現象を脱水に応用したものであり、凍結融解の原理を説明するための汚泥の顕微鏡写真例を示す図を図5に示す。浄水場などの水処理設備で発生した原汚泥(浄水汚泥)は、図5(a)に示すように、アルミ系凝集剤より発生した綿状の水酸化アルミニウムと微細な土粒子、植物質、藻類など濁質の凝集フロックの沈降濃縮液である。凍結融解処理では、まずこの原汚泥を冷却凍結させると、凍結状態で汚泥は図5(b)に示すように、水分が氷の結晶となって針状に成長し、汚泥粒子は氷と氷の間に移動して圧縮され、強力に結合して粗大粒子が形成される。次にこの凍結汚泥を加温して融解すると、融解状態で汚泥は図5(c)に示すように、氷が溶けても汚泥粒子の結合が保たれているために、高密度の粗大粒子の固形物が沈降し、水は上澄水として分離する。
【0004】
この原理のために、遠心分離などの汚泥を加圧して脱水する装置では脱水が非常に困難であるが、凍結融解処理装置では容易に低含水状態に脱水できる多種類の汚泥に適用が可能である。特に適用効果が大きい汚泥としては、下記のようなものがある。
1)有機質を含む原水から発生した凝集沈殿汚泥、2)富栄養化したダム水、湖沼水など藻類を多く含む原水から発生した汚泥、3)渇水期、積雪時の河川の表流水やダム水などの抱く土が低い減水の凝集沈殿から発生する水酸化アルミニウムを多く含む汚泥、4)クリプトスポリジウム除去のため、原水にアルミ系凝集剤が多量に注入されて発生した凝集沈殿汚泥、5)井水(地下水)の酸化処理により発生した水酸化鉄や二酸化マンガンを多く含む汚泥、など。
【0005】
凍結融解処理を用いた汚泥処理の基本方式を図6に示す。この図において、水処理設備で発生した原汚泥(浄水汚泥)は、重力濃縮槽とろ過濃縮装置とで濃縮されて濃縮汚泥となり、凍結融解処理装置で上記の原理によって粗大粒子に改質され、脱水機で脱水汚泥と処理水に分離されて汚泥処理がなされる。
上記のろ過濃縮装置、凍結融解処理装置、脱水機を含む従来の凍結融解方式汚泥処理システムの例を図7に示す。この図において、まず原汚泥は、原汚泥槽5からサイホン式のろ過濃縮装置31に入り、ここでろ過濃縮装置31中のろ布31aと切換弁37bを開けて生じるサイホン作用や、ろ布31aとろ液排水用ポンプ36による吸引作用を利用して、ろ液が排出される。このろ液排出により濃縮された濃縮汚泥は、移送用ポンプ35aを使って濃縮汚泥貯槽32で貯留される。濃縮汚泥はその後に移送用ポンプ35bにより凍結融解処理槽33a、33bに送られ、ここでの凍結融解処理によって粗大粒子の凍結融解汚泥に改質される。この凍結融解汚泥は凍結融解処理槽33a、33bの下方に排出され、真空脱水などを使った脱水機34により脱水汚泥と処理水とに分離されて汚泥処理が完了する。
【0006】
ここで上記の凍結融解処理槽は、図7に示すように2基の槽33a、33bを一組とし、各槽の内部には蛇管形の熱交換器33hが設置され、原汚泥は冷却加熱装置22とこの熱交換器33hを使って、一方の槽(この図では33a)で凍結、他方の槽(この図で33b)で融解の処理が行われる。
冷却と加熱を行う冷却加熱装置22によって、凍結融解処理槽33a、33bの熱交換器(伝熱体)33hには冷ブラインと温ブラインが循環する系統がある。冷却側の系統は、冷ブライン槽11a、ブライン冷却用ポンプ12a、ブライン冷却用熱交換器13a、凍結融解処理槽33aの熱交換器等を循環する冷却回路が、加熱側の系統は、温ブライン槽11b、ブライン加熱用ポンプ12b、ブライン加熱用熱交換器13b、凍結融解処理槽33bの熱交換器等を循環する加熱回路が、それぞれ構成されている。また、凍結融解処理槽33a、33bの熱交換器の冷却と加熱とを切り換えるためには冷熱切換器38a、38bが設けられている。
【0007】
この構成で、一方の凍結融解処理槽33aの冷却は、冷凍機の冷熱で冷却された冷ブラインを熱交換器33hに供給して濃縮汚泥を冷却・凍結し、槽の凍結条件で定まる所定保持時間(例えば1.5時間)保持し、この後に凍結融解処理槽33aの加熱は冷熱切換器38a、38bを切換えて、冷凍機の排熱により加熱された温ブラインを熱交換器33hに供給して汚泥を加熱・融解し、槽の融解条件で定まる所定保持時間(例えば1.2時間)保持する。この汚泥の凍結保持時間と融解保持時間の差分の時間(ここでは0.3時間)内に粗大粒子に改質された脱水汚泥が、凍結融解処理槽33aの底部の図示しない排出ゲートを開いて脱水機34に排出され、次の濃縮汚泥が濃縮汚泥貯槽32から充填される。他方の凍結融解処理槽33bでは、上記の冷却と加熱処理が凍結融解処理槽33aとは半サイクル遅れて実行される。
【0008】
従来の凍結融解処理装置では、上記の装置の他に、過冷却が生じ難く均一な凍結を可能にして脱水効果を高めるために凍結融解処理槽に汚泥を振動させる振動手段を備えた装置(特許文献1参照)や、凍結融解処理装置で凍結融解された汚泥と未処理の原水とを混合する混合槽を設けてこの混合槽の汚泥を脱水する装置(特許文献2参照)などが提案されているが、何れも濃縮槽と凍結融解処理槽との間は配管で接続され、濃縮汚泥が移送されている。
【0009】
【特許文献1】
特開2001−334300
【特許文献2】
特開2002−205100
【0010】
【発明が解決しようとする課題】
これら無薬注で処理が可能で、通常の加圧脱水装置では脱水が難しい汚泥でも処理ができるという特徴のある従来の凍結融解処理装置では、汚泥中の水分の凍結に多くの消費電力量が必要であるという問題点がある。
消費電力量を少なくするために、従来は上記のように予め遠心分離機やろ過濃縮装置により原汚泥から水分を除去して汚泥の容積(重量)を減少した濃縮汚泥を凍結融解処理装置に供給する方式が利用されている。この方式では汚泥の容積が減るために凍結が必要な水分量が減少して消費電力量はかなり削減されるが、濃縮汚泥の濃度が高くなると流動性が低下して、濃縮汚泥の凍結融解処理槽への移送や凍結融解処理槽中の熱交換器間の空間に均一に充填するのが困難になる。このために実用上は流動性がまだ十分ある状態までしか汚泥を濃縮できないので消費電力の削減が十分できないことになる。また、融解処理後の汚泥は外部の脱水機に送って脱水する必要がある。
【0011】
そのために凍結融解処理装置では、凍結融解処理槽の他に、原汚泥の濃縮装置と融解処理汚泥の脱水機が必要で、凍結融解処理設備コストが高価になるという問題点が生じる。
本発明の目的は、 上記の問題点を解決し消費電力量が少なく、 設備コストが少ない実用性が高い凍結融解処理装置を提供することにある。
【0012】
【課題を解決するための手段】
上記の課題を解決するために、本発明では、浄水汚泥や産業排水汚泥の脱水処理を凍結融解の原理を用いて行う凍結融解処理装置において、原汚泥の供給手段と、供給された原汚泥を貯蔵する貯蔵手段と、貯蔵された原汚泥の冷却・加熱を行う伝熱手段と、貯蔵された原汚泥の水分をろ過する汚泥濃縮手段と、ろ過された処理水の排出手段と、ろ過後の脱水汚泥の排出手段とを凍結融解処理槽に設けることとする(請求項1)。従来の凍結融解処理装置では、濃縮手段と凍結融解処理手段と脱水手段とが別々の装置で構成され、汚泥をそれらの装置ごとに輸送することが必要であったが、この装置では、全て汚泥処理に必要な手段を凍結融解処理槽に一体化して構成したことに特徴がある。
【0013】
また、上記の凍結融解処理装置において、脱水汚泥の排出手段を、可動部を備えた排出手段として凍結融解処理槽の壁面の一部に構成し、この凍結融解処理槽の壁面側にはろ過体を、外側にはろ過処理水の排出口を設け、ろ過濃縮時にはこの排出口からろ水を排出し、脱水汚泥の排出時にはこの排出手段の可動部を移動することによって汚泥排出を行うこととする(請求項2)。
さらに、請求項1または2に記載の凍結融解処理装置において、凍結融解処理槽を密閉して加圧可能な容器とすると共に、原汚泥の供給手段に加圧用ポンプを設け、原汚泥の供給時とろ過濃縮時には原汚泥を加圧してろ液の排出を促進することとする(請求項3)。
【0014】
この他に、請求項1から3の何れかに記載の凍結融解処理装置において、凍結融解処理槽を密閉して加圧可能な容器とすると共に、原汚泥の濃縮促進用の圧縮空気槽と空気圧縮機とを設け、原汚泥のろ過濃縮時には圧縮空気により原汚泥を加圧してろ液の排出を促進することとする(請求項4)。
【0015】
【発明の実施の形態】
以下、本発明の2つの実施例について、図に基づき説明する。
〔実施例1〕
本発明の請求項1、2、3を含む凍結融解処理装置の実施例を図1に示す。この図から判るように、凍結融解処理装置は、原汚泥槽5、凍結融解処理槽21、冷却加熱装置22とで構成される。この中の凍結融解処理槽21は、原汚泥の供給および加圧手段(汚泥供給用ポンプ6と汚泥供給弁6a)と、処理を行うための原汚泥の貯蔵手段(汚泥処理槽1)と、冷却加熱装置22の冷・温ブラインを流して原汚泥との冷却・加熱の熱交換を行う伝熱手段(伝熱体2)と、原汚泥の水分をろ過する汚泥濃縮手段とろ過処理水の排出手段(ろ布3と排水ネット4とろ液排水管9a)と、可動部を備えた脱水汚泥の排出手段(脱水汚泥排水装置9)とを一体化して設けている。
【0016】
また、冷却加熱装置22は、従来装置と同じく、圧縮冷凍機10、冷(温)ブライン槽11a、11b、ブライン冷却(加熱)用ポンプ12a、12b、ブライン冷却(加熱)用熱交換器13a、13b、冷媒容器14、膨脹弁15、切換弁16a,16b、17a,17bで構成されている。
伝熱体(熱交換器)2とろ布3と排水ネット4との凍結融解処理槽21内での実際の配置例を示す断面図を図3に示す。図1では凍結融解処理槽21中の汚泥処理槽1、伝熱体2、ろ布3と排水ネット4を、説明を簡単にするためにそれぞれ図の中央、右側、左側に表示してあるが、原汚泥の水分除去と冷却・加熱の効果を上げるためには、原汚泥との接触面積を増やす必要があり、実際には、図3のように複数の蛇管や平型管を交互に配置する構造などが利用可能である。ただし、この配置については、種々の変形構造が可能であり、汚泥処理槽内に原汚泥の伝熱手段と濃縮手段とを設けたものであれば良く、この例に限定されるものでは無い。またその際の伝熱体2の材質としては、ステンレススチールや亜鉛メッキをした鉄などが、排水ネット4は金属やプラスチックの目の粗いネットなどが利用可能である。
【0017】
この装置での運転は、次の順序で進められる。1)原汚泥槽5内の原汚泥を汚泥供給用ポンプ6と汚泥供給弁6aを使って汚泥処理槽1に供給する。2)汚泥供給用ポンプ6の加圧などにより原汚泥に含まれる水はろ布3の目を通り金属製の排水ネット4の空隙を経由してろ液排出管9aより排出される。3)ステンレス容器などで作られた伝熱体2内に冷却加熱装置22の冷却側の切換弁16a、17aを開けて冷ブラインをブライン冷却用ポンプ12aにより供給し、原汚泥の水分を減らした濃縮汚泥を冷却する。4)濃縮汚泥を冷却して凍結が完了した後に冷ブラインの供給を停止する。5)冷却側の切換弁16a、17aを閉じて加熱側の切換弁16b、17bを開くことで冷ブラインから温ブラインに切換えて伝熱体2に温ブラインを供給し、凍結汚泥を加熱して融解状態にする。6)融解汚泥の水分はろ布3と排水ネット4の空隙を通りろ液排出管9aより排出される。7)脱水汚泥は脱水汚泥排出装置9の可動部(昇降装置)により蓋を下降して取り出す。
〔実施例2〕
上記の実施例1に本発明の請求項4を追加した凍結融解処理装置の実施例を図2に示す。この図と実施例1との差は、原汚泥の濃縮促進用の圧縮空気槽8と空気圧縮機7と加圧空気仕切弁7aとを、実施例1の凍結融解処理装置に追加したことである。
【0018】
この装置での運転は、実施例1の工程の一部を変更、追加したもので、この実施例2の運転順序を図4に示す。なお、この図において図2と同じ構成要件は同じ符号で示されている。すなわち、図4の工程で、1)原汚泥槽5内の原汚泥を汚泥供給用ポンプ6と汚泥供給弁6aを使って汚泥処理槽1に供給する。その際、実施例2では、汚泥供給用ポンプ6の加圧と共に、加圧空気仕切弁7a開けて圧縮空気槽8の空気加圧を追加することにより、原汚泥に含まれる水はろ布3の目を通り、金属製の排水ネット4の空隙を経由してろ液排出管9aより排出が促進される。2)ステンレス容器などで作られた伝熱体2内に冷ブライン供給し、原汚泥の水分を減らした濃縮汚泥を冷却する。濃縮汚泥を冷却して凍結が完了した後に、冷ブラインの供給を停止する。3)冷ブラインから温ブラインに切換えて伝熱体2に温ブラインを供給し、凍結汚泥を加熱して融解状態にする。4)融解汚泥の水分はろ布3と排水ネット4の空隙を通りろ液排出管9aより排出される。その際、実施例2では、加圧空気仕切弁7a開き、圧縮空気槽8の空気加圧を追加することにより、ろ液の排出を促進することができる。5)脱水汚泥は脱水汚泥排出装置9の可動部(昇降装置)により蓋を下降して取り出す。
【0019】
【発明の効果】
本発明では、凍結融解処理装置を原汚泥槽5、凍結融解処理槽21、冷却加熱装置22とで構成し、この中の凍結融解処理槽21を、原汚泥の供給および加圧が可能な汚泥供給用ポンプ6と、原汚泥の汚泥処理槽1と、原汚泥の冷却・加熱を行う伝熱体2と、原汚泥の水分をろ過して濃縮するろ布3と排水ネット4とろ液排水管9aと、可動部を持つ脱水汚泥排水装置9とを一体化して構成している。また原汚泥の濃縮促進用と融解汚泥の脱水用には圧縮空気槽8と空気圧縮機7を設けている。
【0020】
そのために、原汚泥の濃縮装置と凍結融解処理槽と脱水機と冷却加熱装置とが別々に構成されていた従来の凍結融解処理装置では、濃縮装置での汚泥濃度が高いと流動性が低下して汚泥の凍結融解処理槽への移送や凍結融解処理槽中の熱交換器間の空間に均一に充填するのが困難になり濃縮の度合いが制限されて消費電力量の低減が十分できないという問題点と、個別の装置を組み合わせて構成されるために凍結融解処理装置のコストが高価になるという問題点の2つが、本発明の凍結融解処理槽の一体化により一挙に解決できるという効果がある。
【図面の簡単な説明】
【図1】本発明の請求項1、2、3を含む凍結融解処理装置の実施例を示す図
【図2】実施例1に本発明の請求項4を追加した凍結融解処理装置の実施例を示す図
【図3】伝熱体とろ布と排水ネットとの汚泥処理槽での実際の配置例を示す断面図
【図4】実施例2の運転順序を示す図
【図5】凍結融解の原理を説明するための汚泥の顕微鏡写真例を示す図
【図6】凍結融解処理装置を用いた汚泥処理の基本方式を示す図
【図7】従来の凍結融解方式汚泥処理システムの例を示す図
【符号の説明】
1: 汚泥処理槽
2: 伝熱体(熱交換器)
3: ろ布
4: 排水ネット
5: 原汚泥槽
6: 汚泥供給用ポンプ
6a: 汚泥供給弁
7: 空気圧縮機
7a: 加圧空気仕切弁
8: 圧縮空気槽
9: 脱水汚泥排出装置
9a: ろ液排水管
10: 圧縮冷凍機
11a: 冷ブライン槽
11b: 温ブライン槽
12a: ブライン冷却用ポンプ
12b: ブライン加熱用ポンプ
13a: ブライン冷却用熱交換器
13b: ブライン加熱用熱交換器
14: 冷媒容器
15: 膨脹弁
16a,b: 切換弁
17a,b: 切換弁
21: 凍結融解処理槽
22: 冷却加熱装置
31: ろ過濃縮装置
31a: ろ布
32: 濃縮汚泥貯槽
33a,b: 凍結融解処理槽
33h: 熱交換器(伝熱体)
34: 脱水機
35a,b: 濃縮汚泥移送用ポンプ
36: ろ液排出用ポンプ
37a,b: 切換弁
38a,b: 冷熱切換器
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a sludge dewatering apparatus in which the dewaterability of sludge is improved by using freezing and thawing treatment in the dewatering treatment of wastewater sludge and industrial wastewater sludge in a water purification plant.
[0002]
[Prior art]
The amount of generated water and sewage treatment plant sludge and industrial wastewater sludge tends to increase year by year, and a shortage of dewatered sludge disposal sites is a major problem. Recently, effective utilization of dewatered sludge has been promoted for environmental conservation or the establishment of a recycling society. In this disposal and effective use, it is important to efficiently concentrate and dehydrate the raw sludge to a low water content without adding chemicals.
One of the sludge dewatering apparatuses is a freeze-thaw processing apparatus. The freeze-thaw treatment apparatus is a non-chemical injection method, and is used when dewatering raw sludge such as purified water sludge is modified into coarse particles by freeze-thaw treatment and dehydrated to a low water content state at a high filtration rate.
[0003]
The freezing and thawing principle is applied to the dehydration phenomenon of solid and liquid by freezing, as seen in the growth of frost pillars and the production of frozen tofu. Micrograph of sludge to explain the principle of freezing and thawing A diagram illustrating an example is shown in FIG. As shown in FIG. 5 (a), raw sludge generated in water treatment facilities such as water purification plants is composed of cotton-like aluminum hydroxide, fine soil particles, plant matter, It is a sedimentation concentrate of flocculated flocs such as algae. In the freezing and thawing process, when this raw sludge is first cooled and frozen, the sludge grows in the form of needles in the frozen state as shown in FIG. 5 (b), and the sludge particles are ice and ice. The particles are moved to be compressed and are strongly bonded to form coarse particles. Next, when this frozen sludge is heated and melted, as shown in FIG. 5 (c), the sludge in the melted state retains the sludge particles even when the ice melts. Solids settle and water separates as supernatant.
[0004]
Because of this principle, dehydration is very difficult with devices that pressurize and dewater sludge, such as centrifugal separation, but freeze-thaw treatment devices can be applied to many types of sludge that can be easily dehydrated to low water content. is there. Examples of sludge that are particularly effective in application include the following.
1) Coagulated sediment sludge generated from raw water containing organic matter, 2) Eutrophied dam water, sludge generated from raw water rich in algae such as lake water, 3) River surface water and dam water during drought and snowfall 4) Sludge containing a lot of aluminum hydroxide generated from coagulation sedimentation with low water content such as 4) Coagulation sedimentation sludge generated by injection of a large amount of aluminum coagulant into raw water to remove Cryptosporidium, 5) Well Sludge containing a lot of iron hydroxide and manganese dioxide generated by oxidation treatment of water (groundwater).
[0005]
FIG. 6 shows a basic method of sludge treatment using freeze-thaw treatment. In this figure, the raw sludge (purified water sludge) generated in the water treatment facility is concentrated in a gravity concentration tank and a filtration concentration device to become concentrated sludge, which is reformed into coarse particles by the above-mentioned principle in the freeze-thaw treatment device, It is separated into dewatered sludge and treated water by a dehydrator and sludge treatment is performed.
An example of a conventional freeze-thaw type sludge treatment system including the above-described filtration concentration apparatus, freeze-thaw treatment apparatus, and dehydrator is shown in FIG. In this figure, first, raw sludge enters a siphon type filtration and concentration device 31 from the raw sludge tank 5, where the siphon action produced by opening the filter cloth 31a and the switching valve 37b in the filtration concentration device 31 and the filter cloth 31a. The filtrate is discharged using the suction action of the filtrate drainage pump 36. The concentrated sludge concentrated by this filtrate discharge is stored in the concentrated sludge storage tank 32 using the transfer pump 35a. The concentrated sludge is then sent to the freeze / thaw treatment tanks 33a and 33b by the transfer pump 35b, and is reformed into freeze-thaw sludge of coarse particles by freeze-thaw treatment here. The freeze-thawed sludge is discharged below the freeze-thaw treatment tanks 33a and 33b, and separated into dehydrated sludge and treated water by a dehydrator 34 using vacuum dehydration or the like, and the sludge treatment is completed.
[0006]
Here, as shown in FIG. 7, the above-mentioned freeze-thaw treatment tank is a set of two tanks 33a and 33b. Inside each tank is a serpentine heat exchanger 33h, and the raw sludge is cooled and heated. The apparatus 22 and the heat exchanger 33h are used to perform freezing in one tank (33a in this figure) and thawing in the other tank (33b in this figure).
There is a system in which cold brine and warm brine circulate in the heat exchanger (heat transfer body) 33h of the freeze / thaw treatment tanks 33a and 33b by the cooling and heating device 22 that performs cooling and heating. The cooling side system is a cooling circuit that circulates through the cold brine tank 11a, the brine cooling pump 12a, the brine cooling heat exchanger 13a, the heat exchanger of the freeze / thaw processing tank 33a, etc. Heating circuits that circulate through the tank 11b, the brine heating pump 12b, the brine heating heat exchanger 13b, the heat exchanger of the freeze-thaw processing tank 33b, and the like are configured. Further, in order to switch between cooling and heating of the heat exchangers of the freeze / thaw treatment tanks 33a and 33b, cold / heat switchers 38a and 38b are provided.
[0007]
In this configuration, one of the freeze-thaw processing tanks 33a is cooled by supplying cold brine cooled by the cold heat of the refrigerator to the heat exchanger 33h to cool and freeze the concentrated sludge, and predetermined holding determined by the freezing conditions of the tanks Hold the time (for example, 1.5 hours), and then heat the freezing and thawing treatment tank 33a by switching the cold / hot switch 38a, 38b, and supply hot brine heated by the exhaust heat of the refrigerator to the heat exchanger 33h. The sludge is heated and melted and held for a predetermined holding time (for example, 1.2 hours) determined by the melting conditions of the tank. The dewatered sludge that has been modified into coarse particles within the difference between the freeze holding time and the melting hold time (here 0.3 hours) opens a discharge gate (not shown) at the bottom of the freeze thaw tank 33a. It is discharged to the dehydrator 34 and the next concentrated sludge is filled from the concentrated sludge storage tank 32. In the other freeze / thaw treatment tank 33b, the cooling and heating processes described above are executed with a half cycle delay from the freeze / thaw treatment tank 33a.
[0008]
In the conventional freeze-thaw treatment apparatus, in addition to the above-described apparatus, an apparatus provided with a vibration means that vibrates sludge in the freeze-thaw treatment tank in order to increase the dehydration effect by making uniform freezing difficult to cause overcooling (patent) Document 1), and a device (see Patent Document 2) that provides a mixing tank for mixing sludge frozen and thawed in a freeze-thaw treatment apparatus and untreated raw water to dewater the sludge in this mixing tank has been proposed. However, in both cases, the concentration tank and the freeze-thaw treatment tank are connected by piping, and the concentrated sludge is transferred.
[0009]
[Patent Document 1]
JP 2001-334300 A
[Patent Document 2]
JP 2002-205100 A
[0010]
[Problems to be solved by the invention]
In conventional freeze-thaw treatment equipment, which can be processed without these chemical injections and can treat even sludge that is difficult to dehydrate with ordinary pressure dehydration equipment, much power is consumed to freeze the water in the sludge. There is a problem that it is necessary.
Conventionally, in order to reduce power consumption, as previously mentioned, concentrated sludge with reduced sludge volume (weight) by removing water from the original sludge using a centrifuge or filtration concentrator is supplied to the freeze-thaw processor. This method is used. In this method, the amount of water that needs to be frozen is reduced because the volume of sludge is reduced, and the power consumption is considerably reduced.However, as the concentration of concentrated sludge increases, the fluidity decreases, and the sludge is frozen and thawed. It becomes difficult to uniformly fill the space between the heat exchangers in the tank and the freeze-thaw treatment tank. For this reason, since sludge can be concentrated only to a state where fluidity is still sufficient in practical use, power consumption cannot be sufficiently reduced. Moreover, it is necessary to send the sludge after the melting treatment to an external dehydrator for dehydration.
[0011]
Therefore, in the freeze-thaw treatment apparatus, in addition to the freeze-thaw treatment tank, a raw sludge concentrator and a melt-treated sludge dehydrator are necessary, and there is a problem that the cost of the freeze-thaw treatment equipment becomes expensive.
An object of the present invention is to provide a freeze-thaw treatment apparatus that solves the above-described problems, has low power consumption, and has low utility costs and high practicality.
[0012]
[Means for Solving the Problems]
In order to solve the above problems, in the present invention, in a freeze-thaw treatment apparatus that performs dewatering treatment of purified water sludge and industrial wastewater sludge using the principle of freeze-thaw, the raw sludge supply means and the supplied raw sludge Storage means for storing; heat transfer means for cooling and heating the stored raw sludge; sludge concentration means for filtering the moisture of the stored raw sludge; means for discharging the filtered treated water; The dewatering sludge discharging means is provided in the freeze-thaw treatment tank (Claim 1). In the conventional freeze-thaw treatment apparatus, the concentration means, the freeze-thaw treatment means, and the dewatering means are configured as separate devices, and it is necessary to transport sludge for each of these devices. It is characterized in that the means necessary for processing is integrated with the freeze-thaw processing tank.
[0013]
Further, in the above freeze-thaw treatment apparatus, the dewatering sludge discharging means is configured as a part of the wall surface of the freeze-thawing treatment tank as a discharging means having a movable portion, and a filter is provided on the wall surface side of the freeze-thawing treatment tank. In addition, an outlet for filtered water is provided on the outside, and filtered water is discharged from this outlet during filtration and concentration, and sludge is discharged by moving the moving part of this discharging means when discharging dewatered sludge. (Claim 2).
Furthermore, in the freeze-thaw treatment apparatus according to claim 1 or 2, the freeze-thaw treatment tank is hermetically sealed so as to be a pressurizable container, and a pressurizing pump is provided in the raw sludge supply means so that the raw sludge is supplied. During filtration and concentration, the raw sludge is pressurized to promote the discharge of the filtrate (claim 3).
[0014]
In addition to this, in the freeze-thaw treatment apparatus according to any one of claims 1 to 3, the freeze-thaw treatment tank is hermetically sealed to be a pressurizable container, and a compressed air tank and air for promoting concentration of raw sludge are used. A compressor is provided, and when the raw sludge is filtered and concentrated, the raw sludge is pressurized with compressed air to promote the discharge of the filtrate (claim 4).
[0015]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, two embodiments of the present invention will be described with reference to the drawings.
[Example 1]
An embodiment of a freeze-thaw processing apparatus including claims 1, 2, and 3 of the present invention is shown in FIG. As can be seen from this figure, the freeze / thaw treatment apparatus is composed of a raw sludge tank 5, a freeze / thaw treatment tank 21, and a cooling / heating apparatus 22. The freezing and thawing treatment tank 21 includes raw sludge supply and pressurization means (sludge supply pump 6 and sludge supply valve 6a), raw sludge storage means for treatment (sludge treatment tank 1), The heat transfer means (heat transfer body 2) that exchanges the cooling and heating heat with the raw sludge by flowing the cold and warm brine of the cooling and heating device 22, the sludge concentration means that filters the moisture of the raw sludge, and the filtered water The discharge means (filter cloth 3, drainage net 4, filtrate drain pipe 9a) and the dewatered sludge discharge means (dehydrated sludge drainage device 9) provided with a movable part are provided integrally.
[0016]
The cooling and heating device 22 is the same as the conventional device, the compression refrigerator 10, the cold (warm) brine tanks 11a and 11b, the brine cooling (heating) pumps 12a and 12b, the brine cooling (heating) heat exchanger 13a, 13b, the refrigerant container 14, the expansion valve 15, and the switching valves 16a, 16b, 17a, 17b.
FIG. 3 is a cross-sectional view showing an actual arrangement example of the heat transfer body (heat exchanger) 2, the filter cloth 3, and the drainage net 4 in the freeze / thaw treatment tank 21. In FIG. 1, the sludge treatment tank 1, the heat transfer body 2, the filter cloth 3, and the drainage net 4 in the freeze / thaw treatment tank 21 are shown at the center, right side, and left side, respectively, for the sake of simplicity. In order to improve the effect of water removal and cooling / heating of the raw sludge, it is necessary to increase the contact area with the raw sludge. Actually, multiple serpentine tubes and flat tubes are alternately arranged as shown in FIG. The structure to be used is available. However, this arrangement is not limited to this example as long as various deformation structures are possible and the heat transfer means and the concentration means for the raw sludge are provided in the sludge treatment tank. Further, as the material of the heat transfer body 2 at that time, stainless steel, galvanized iron or the like can be used, and the drainage net 4 can be a metal or plastic coarse net.
[0017]
The operation with this device proceeds in the following order. 1) The raw sludge in the raw sludge tank 5 is supplied to the sludge treatment tank 1 using the sludge supply pump 6 and the sludge supply valve 6a. 2) The water contained in the raw sludge is discharged from the filtrate discharge pipe 9a through the gap of the metal drainage net 4 through the filter cloth 3 by pressurization of the sludge supply pump 6 or the like. 3) In the heat transfer body 2 made of a stainless steel container or the like, the switching valves 16a and 17a on the cooling side of the cooling and heating device 22 are opened and cold brine is supplied by the brine cooling pump 12a to reduce the water content of the raw sludge. Cool the concentrated sludge. 4) After cooling the concentrated sludge and freezing is completed, the supply of cold brine is stopped. 5) Close the cooling side switching valves 16a, 17a and open the heating side switching valves 16b, 17b to switch from cold brine to warm brine to supply warm brine to the heat transfer body 2 and heat the frozen sludge. Thaw. 6) The water of the molten sludge passes through the gap between the filter cloth 3 and the drainage net 4 and is discharged from the filtrate discharge pipe 9a. 7) The dewatered sludge is taken out by lowering the lid by the movable part (elevating device) of the dewatered sludge discharge device 9.
[Example 2]
FIG. 2 shows an example of a freeze-thaw processing apparatus in which claim 4 of the present invention is added to Example 1 described above. The difference between this figure and Example 1 is that a compressed air tank 8, an air compressor 7 and a pressurized air gate valve 7a for concentrating raw sludge were added to the freeze / thaw treatment apparatus of Example 1. is there.
[0018]
The operation of this apparatus is obtained by changing and adding a part of the process of Example 1, and the operation sequence of Example 2 is shown in FIG. In this figure, the same constituent elements as those in FIG. 2 are denoted by the same reference numerals. That is, in the process of FIG. 4, 1) The raw sludge in the raw sludge tank 5 is supplied to the sludge treatment tank 1 using the sludge supply pump 6 and the sludge supply valve 6a. At that time, in Example 2, the water contained in the raw sludge is added to the filter cloth 3 by opening the pressurized air gate valve 7a and adding the air pressure of the compressed air tank 8 together with the pressure of the sludge supply pump 6. Through the eyes, the discharge is promoted from the filtrate discharge pipe 9a through the gap of the metal drainage net 4. 2) Cool brine is supplied into the heat transfer body 2 made of a stainless steel container or the like, and the concentrated sludge with reduced moisture in the raw sludge is cooled. After the concentrated sludge is cooled and freezing is completed, the supply of cold brine is stopped. 3) Switch from cold brine to warm brine, supply warm brine to heat transfer body 2, and heat frozen sludge to a molten state. 4) The water of the molten sludge passes through the gap between the filter cloth 3 and the drainage net 4 and is discharged from the filtrate discharge pipe 9a. In that case, in Example 2, the discharge of filtrate can be accelerated | stimulated by opening the pressurized air gate valve 7a and adding the air pressurization of the compressed air tank 8. FIG. 5) The dewatered sludge is taken out by lowering the lid by the movable part (elevating device) of the dewatered sludge discharge device 9.
[0019]
【The invention's effect】
In the present invention, the freeze / thaw treatment apparatus is composed of the raw sludge tank 5, the freeze / thaw treatment tank 21, and the cooling / heating apparatus 22, and the freeze / thaw treatment tank 21 is sludge capable of supplying and pressurizing the raw sludge. Pump 6 for supply, sludge treatment tank 1 of raw sludge, heat transfer body 2 that cools and heats raw sludge, filter cloth 3 that drains and concentrates water of raw sludge, drainage net 4 and filtrate drain pipe 9a and the dewatered sludge drainage device 9 having a movable part are integrated. A compressed air tank 8 and an air compressor 7 are provided for concentrating raw sludge and for dehydrating molten sludge.
[0020]
For this reason, in the conventional freeze-thaw treatment device in which the raw sludge concentrator, the freeze-thaw treatment tank, the dehydrator, and the cooling and heating device are configured separately, if the sludge concentration in the concentrator is high, the fluidity decreases. The problem is that it is difficult to transfer sludge to the freeze-thaw treatment tank and to uniformly fill the space between the heat exchangers in the freeze-thaw treatment tank, and the degree of concentration is limited, so the power consumption cannot be reduced sufficiently. There is an effect that two points of the problem that the cost of the freeze / thaw treatment apparatus becomes expensive due to the combination of the point and the individual apparatus can be solved at once by the integration of the freeze / thaw treatment tank of the present invention. .
[Brief description of the drawings]
FIG. 1 is a diagram showing an embodiment of a freeze-thaw processing apparatus including claims 1, 2, and 3 of the present invention. FIG. 2 is an embodiment of a freeze-thaw processing apparatus in which claim 4 of the present invention is added to the first embodiment. FIG. 3 is a cross-sectional view showing an actual arrangement example of a heat transfer body, a filter cloth, and a drainage net in a sludge treatment tank. FIG. 4 is a diagram showing an operation sequence of Example 2. FIG. Fig. 6 is a diagram showing an example of a micrograph of sludge for explaining the principle. Fig. 6 is a diagram showing a basic method of sludge treatment using a freeze-thaw treatment apparatus. Fig. 7 is a diagram showing an example of a conventional freeze-thaw type sludge treatment system. [Explanation of symbols]
1: Sludge treatment tank 2: Heat transfer body (heat exchanger)
3: Filter cloth 4: Drainage net 5: Raw sludge tank 6: Sludge supply pump 6a: Sludge supply valve 7: Air compressor 7a: Pressurized air gate valve 8: Compressed air tank 9: Dehydrated sludge discharge device 9a: Filter Liquid drain pipe 10: Compression refrigerator 11a: Cold brine tank 11b: Hot brine tank 12a: Brine cooling pump 12b: Brine heating pump 13a: Brine cooling heat exchanger 13b: Brine heating heat exchanger 14: Refrigerant container 15: expansion valves 16a, b: switching valves 17a, b: switching valves 21: freeze-thaw treatment tank 22: cooling and heating device 31: filtration and concentration device 31a: filter cloth 32: concentrated sludge storage tank 33a, b: freeze-thaw treatment tank 33h : Heat exchanger (heat transfer body)
34: Dehydrator 35a, b: Concentrated sludge transfer pump 36: Filtrate discharge pump 37a, b: Switching valve 38a, b: Cold / heat switching device

Claims (4)

浄水汚泥や産業排水汚泥の脱水処理を凍結融解の原理を用いて行う凍結融解処理装置において、原汚泥の供給手段と、供給された原汚泥を貯蔵する貯蔵手段と、貯蔵された原汚泥の冷却・加熱を行う伝熱手段と、貯蔵された原汚泥の水分をろ過する汚泥濃縮手段と、ろ過された処理水の排出手段と、ろ過後の脱水汚泥の排出手段とを凍結融解処理槽に設けることを特徴とする凍結融解処理装置。In freeze-thaw treatment equipment that performs dewatering treatment of purified water sludge and industrial wastewater sludge using the principle of freeze-thaw, raw sludge supply means, storage means for storing the supplied raw sludge, and cooling of the stored raw sludge・ Freezing and thawing treatment tank is provided with heat transfer means for heating, sludge concentration means for filtering the water of stored raw sludge, means for discharging filtered treated water, and means for discharging dewatered sludge after filtration. A freeze-thaw treatment apparatus characterized by the above. 請求項1に記載の凍結融解処理装置において、脱水汚泥の排出手段を、可動部を備えた排出手段として凍結融解処理槽の壁面の一部に構成し、この凍結融解処理槽の壁面側にはろ過体を、外側にはろ過処理水の排出口を設け、ろ過濃縮時にはこの排出口からろ水を排出し、脱水汚泥の排出時にはこの排出手段の可動部を移動することによって汚泥排出を行うことを特徴とする凍結融解処理装置。In the freeze thaw processing apparatus according to claim 1, the dewatering sludge discharging means is configured as a part of the wall surface of the freeze thaw processing tank as a discharging means having a movable part, The filter body is provided with an outlet for filtered water on the outside, and the filtered water is discharged from this outlet during filtration concentration, and the sludge is discharged by moving the moving part of this discharge means when discharging the dewatered sludge. A freeze-thaw treatment apparatus characterized by the above. 請求項1または2に記載の凍結融解処理装置において、凍結融解処理槽を密閉して加圧可能な容器とすると共に、原汚泥の供給手段に加圧用ポンプを設け、原汚泥の供給時とろ過濃縮時には原汚泥を加圧してろ液の排出を促進することを特徴とする凍結融解処理装置。3. The freeze / thaw treatment apparatus according to claim 1 or 2, wherein the freeze-thaw treatment tank is hermetically sealed to provide a pressurizable container, and a pressurizing pump is provided in the raw sludge supply means to supply and filter the raw sludge. A freezing and thawing device characterized in that the raw sludge is pressurized during concentration to promote the discharge of the filtrate. 請求項1から3の何れかに記載の凍結融解処理装置において、凍結融解処理槽を密閉して加圧可能な容器とすると共に、原汚泥の濃縮促進用の圧縮空気槽と空気圧縮機とを設け、原汚泥のろ過濃縮時には圧縮空気により原汚泥を加圧してろ液の排出を促進することを特徴とする凍結融解処理装置。The freeze / thaw treatment apparatus according to any one of claims 1 to 3, wherein the freeze-thaw treatment tank is hermetically sealed to be a pressurizable container, and a compressed air tank and an air compressor for promoting concentration of raw sludge are provided. A freezing and thawing treatment apparatus characterized in that when the raw sludge is filtered and concentrated, the raw sludge is pressurized with compressed air to accelerate the discharge of the filtrate.
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