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JP4191442B2 - Sludge freeze / thaw tank - Google Patents
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JP4191442B2 - Sludge freeze / thaw tank - Google Patents

Sludge freeze / thaw tank Download PDF

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Publication number
JP4191442B2
JP4191442B2 JP2002208704A JP2002208704A JP4191442B2 JP 4191442 B2 JP4191442 B2 JP 4191442B2 JP 2002208704 A JP2002208704 A JP 2002208704A JP 2002208704 A JP2002208704 A JP 2002208704A JP 4191442 B2 JP4191442 B2 JP 4191442B2
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Japan
Prior art keywords
sludge
freezing
tank
heat transfer
thawing
Prior art date
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Expired - Fee Related
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JP2002208704A
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JP2004049993A (en
Inventor
知彦 平尾
隆裕 吉井
定和 山田
憲彦 杉本
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Takuma Co Ltd
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Takuma Co Ltd
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  • Treatment Of Sludge (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)

Description

【0001】
【発明の属する技術分野】
最近、浄水場排泥、下水汚泥、浄化槽汚泥、し尿、あるいは産業排水や埋立地排水の処理において排出される汚泥に対し、ろ過・脱水する前に施す凍結・融解の効果が注目されるようになった。本発明は、前記汚泥の凍結・融解処理に使用する汚泥の凍結・融解槽に関する。
【0002】
【従来の技術】
前記の汚泥類は、通常、多量の水の中に固体成分が含まれているので、沈降、ろ過、脱水などの幾つかの固液分離方法を適宜に選択して組み合わせ、固体成分から大量の水を順次に除去して濃縮し脱水して、最終的に得られた固体分をコンポスト化し、あるいは埋立、焼却などの最終処分を行っている。多くの場合、濃縮された汚泥は加圧ろ過器などを用い、ろ過・脱水処理されている。ところが、これらの汚泥はろ過・脱水性が極めて悪く、ろ過・脱水処理に長い時間を要していた。
【0003】
前記の問題を解決する1つの手段として、事前に汚泥を凍結し融解してからろ過、脱水する凍結・融解処理法が提案され、その効果が認められるようになってきた。ろ過・脱水しようとする汚泥は、凍結・融解処理を施されることにより、汚泥粒子が凝集して粒子が粗大化し、かつ汚泥内部に保留されている水が脱水されて、その後のろ過・脱水操作が容易になる。凍結・融解処理には、通常、凍結・融解槽を用い、処理を迅速に実施するため凍結・融解槽内に伝熱管を設け、槽内に導入した汚泥を冷却ならびに加熱するための熱媒体として、例えば塩化カルシウム、塩化ナトリウム、エチレングリコール等の水溶液をブラインと称して用いる。汚泥を凍結する際、冷凍機で冷却されたブラインを冷ブラインと称して槽内の伝熱管内に流す。反対に凍結したブラインを解凍する際には温水で加熱されたブラインを温ブラインと称して槽内の伝熱管内に交互に流して槽内の汚泥を凍結、融解させ、バッチ処理している。
【0004】
凍結・融解処理を利用した汚泥の脱水システムの基本的な一例を図3にフローシートで示した。本例示によると、汚泥を含む原水31を沈殿池32に導いて汚泥を沈降分離し、ついで沈降した汚泥を濃縮槽33に送入し分離・濃縮する。濃縮された汚泥を凍結・融解槽34に導いて槽内の伝熱管36に冷ブラインを流して凍結させ、ついで温ブラインに切り替えて融解し、上澄水37を分離して濃縮し、脱水性を向上させた汚泥を加圧ろ過器35に送り加圧、脱水する。
【0005】
【発明が解決しようとする課題】
汚泥のろ過・脱水操作における凍結・融解処理効果は大きいが、汚泥の凍結・融解処理に要する時間が長いので、設備費用、運転費用がかさむという問題が生じる。汚泥の凍結を短時間で終了するには伝熱管のピッチを狭くし伝熱管の本数を増やす必要がある。その結果、設備コスト、ブラインの使用量、熱損失や循環のための所要動力が増大する。本発明は、凍結・融解処理を効果的に実行するために、操作が短時間で終了し、かつ設備コスト及び運転コストを低減する手段を課題に鋭意研究した結果、完成されたものである。
【0006】
【課題を解決するための手段】
前記の課題を解決する手段として本発明は、汚泥のろ過・脱水に先だって施され る凍結・融解処理のために使用する凍結・融解槽であって、中心軸を通る一平面内 において曲げられた蛇管又はU字管と、前記平面内に取り付けたフィンとによって 構成されたフィン付伝熱管が、槽内において平行又は同一の平面内に配列されてい る、汚泥の凍結・融解槽を用いる。
【0007】
【発明の実施の形態】
本発明について図面を参照しながら具体的に説明する。図1は、本発明に係る汚泥の凍結・融解槽内伝熱管の形状及び配列の実施形態の一例を示す横方向断面図であり、図2はその縦方向断面図である。
【0008】
本発明において凍結・融解して脱水しようとする汚泥は、有機質でも無機質でもよく、濃縮処理されていない生の汚泥、あるいは前記の方法などにより濃縮されている汚泥であってもよい。凍結・融解槽の上部形状は円筒状であっても角筒状であってもよいが、凍結・融解槽汚泥を排出しやすいように底部は谷状又はコーン状にする。汚泥の排出、伝熱管の配置、製作コストを考慮すれば、上部が角筒、底部を谷状にするとよい。槽内には汚泥を凍結し融解するために冷ブラインや温ブラインを流すフィン2付きの伝熱管1を取り付ける。凍結汚泥の性状や含有成分にもよるが、通常、槽本体の構成には炭素鋼を用い表面に腐食防止ならびに保冷断熱、汚泥が凍結する際の体積膨張による槽の破損防止のクッション材として独立気泡のスポンジゴムなどを槽内面に貼り付ける。伝熱管1は、凍結による汚泥の体積膨張によって大きな外圧が加わるので円管が望ましく、ステンレス鋼管や溶融アルミメッキ管などを用いる。
【0009】
伝熱管1は、効率的に槽内に収納し、かつ管内流速を高くして熱伝達率を大きくするためにジグザグに曲げた蛇管又はU字管(ヘリボーン型熱交換器)を用いる。汚泥の排出を容易にするため、伝熱管は直管部を縦方向に、フィン2はシンプルな形状の平板とし、伝熱管1の直径方向の両側を軸方向に沿って、他の伝熱管のフィン2と相互に平行又は同一平面上になるように取り付ける。
【0010】
凍結・融解される汚泥には粘着性があるので、僅かの水平突起物が原因になり汚泥排出時にブリッジが形成されて汚泥を完全に排出できなくなり、あるいは汚泥を投入する際に空気が混入したり槽内に均一に汚泥が充填されないなどの問題を生じる恐れがある。従って、伝熱管1が蛇管又はU字管の場合、伝熱管1は、その曲げ方向に同一又は相互に平行な方向Aに配列し、フィン2もまた、当該(取り付けられる)伝熱管1の中心を通り曲げ方向と同じ平面A内に取付けることが望まれる。1本の蛇管で構成される伝熱管を上記に準じて平行な複数列にわたり配列してもよい。フィンと伝熱管軸方向とが交叉する方向や、フィンを含む平面が相互に交叉する方向には取り付けない方がよい。汚泥の付着を防止し、送入、排出や清掃を容易にする観点から好ましくない。
【0011】
冷却時のブライン温度は一般に−10〜−20℃、ブライン温度にもよるがフィン表面を含む冷却表面積は、汚泥1トンあたり40〜50mが好ましい。
【0012】
【実施例】
本発明を具体的に理解するため、従来の凍結・融解槽を、本発明に係る凍結・融解槽に改造した実施例をあげながら具体的に説明するが、本実施例は本発明の範囲を限定するものではない。
【0013】
従来例及び実施例
従来の凍結・融解槽は、内辺の長さが約120cm、内部高さが約150cm、底がV字形の炭素鋼製角槽内に、外径が27.6mmのSUS304TP管を用い、端部をU字形にしてピッチ約5.5cmで同一平面内にジグザグに15回曲げて16本の蛇管状伝熱管とし、この16本を約4.7cm間隔で平行に取り付けていた。伝熱面積は約26mであった。
【0014】
上記の従来の凍結・融解槽の伝熱管を、図1及び図2に例示したのと同様な形状のフィン付伝熱管を製作して交換、取り付け、本発明に係る凍結・融解槽とした。具体的に説明すると、伝熱管には外径が27.6mmのSUS304TP管を用い、端部をU字形にしてピッチ約11cmで同一平面内にジグザグに7回曲げ、これに厚さ0.6cm、幅3.6cmのSUS304板をフィンとして、伝熱管の直管部中心線上の両側、曲げ方向と同じ方向に溶接した。この伝熱管18本を約4.7cm間隔で平行に並べた。フィンの表面を含む伝熱面積は約30mであった。
【0015】
前記の2形式の凍結・融解槽にともに0.6トンの汚泥を供給し、−15℃のブラインで凍結させた。この結果、従来の凍結・融解槽に較べて所要ブライン量は約1/2、ブラインの循環動力も約1/2となり、同一条件での凍結に要する時間は前記従来槽に較べて約10%短縮され、また、汚泥の投入、排出および清掃が容易になり、作業効率が向上した。
【0016】
【発明の効果】
本発明を利用して伝熱管にフィンを効果的に取り付けるすることにより、従来の汚泥の凍結・融解槽に較べて伝熱管の本数が約1/2に削減され、これにともなって使用するブライン量も減少し、逆に槽内に充填できる処理汚泥の供給量を約5容量%増加することができる。伝熱管の所要総延長を短縮することができるので管内のブライン流速を早くして熱伝達率を向上させ、さらに凍結・溶解操作の所要時間を短縮できる。また、Uベントの曲率を大きくすることができるので製作上の制限が緩和される。また、フィンに平板を用い取付を一方向に、伝熱管がU字管又は蛇管の場合には曲げ方向に合わせて取り付けることにより、汚泥の充填・排出や清掃を容易にすることができる。
【図面の簡単な説明】
【図1】本発明に係る汚泥の凍結・融解槽内伝熱管の形状及び配列の実施形態の一例を示す横方向断面図
【図2】同上縦方向断面図
【図3】凍結・融解処理法を利用した従来の汚泥処理を例示する概略フローシート
【符号の説明】
1:伝熱管 2:フィン
A:伝熱管の中心を通り曲げ方向と同じ平面
31:汚泥を含む原水 32:沈殿池
33:濃縮槽 34:凍結・融解槽
35:ろ過・脱水器(加圧ろ過器) 36:伝熱管
37:上澄水
[0001]
BACKGROUND OF THE INVENTION
Recently, attention has been paid to the effect of freezing and thawing before filtering and dewatering wastewater sludge, sewage sludge, septic tank sludge, human waste, or sludge discharged in the treatment of industrial and landfill wastewater. became. The present invention relates to a sludge freezing / thawing tank used for the sludge freezing / thawing treatment.
[0002]
[Prior art]
Since the sludge usually contains a solid component in a large amount of water, several solid-liquid separation methods such as sedimentation, filtration, and dehydration are appropriately selected and combined, and a large amount of solid component is obtained. Water is removed sequentially, concentrated and dehydrated, and the final solids are composted or finally disposed of, such as landfill and incineration. In many cases, the concentrated sludge is filtered and dehydrated using a pressure filter or the like. However, these sludges have extremely poor filtration / dehydration properties, and a long time is required for the filtration / dehydration treatment.
[0003]
As one means for solving the above-mentioned problems, a freezing / thawing treatment method in which sludge is frozen and thawed in advance, followed by filtration and dehydration has been proposed, and its effect has been recognized. Sludge to be filtered and dewatered is subjected to freezing and thawing treatment, causing sludge particles to aggregate and coarsen, and water retained in the sludge to be dehydrated, followed by filtration and dewatering. Easy to operate. Freezing and thawing treatment is usually performed using a freezing and thawing tank, and a heat transfer tube is provided in the freezing and thawing tank for rapid processing, and as a heat medium for cooling and heating the sludge introduced into the tank. For example, an aqueous solution of calcium chloride, sodium chloride, ethylene glycol or the like is used as brine. When the sludge is frozen, the brine cooled by the refrigerator is called cold brine and flows into the heat transfer tube in the tank. On the other hand, when the frozen brine is thawed, the brine heated with warm water is called warm brine and is alternately flown into the heat transfer tube in the tank to freeze and thaw the sludge in the tank, and batch processing is performed.
[0004]
A basic example of a sludge dewatering system using freezing and thawing treatment is shown in the flow sheet of FIG. According to this example, the raw water 31 containing sludge is guided to the settling basin 32 and the sludge is settled and separated, and then the settled sludge is fed into the concentration tank 33 and separated and concentrated. The concentrated sludge is guided to the freezing / thawing tank 34, and cold brine is allowed to flow through the heat transfer tube 36 in the tank for freezing. Then, the sludge is switched to warm brine for thawing, and the supernatant water 37 is separated and concentrated. The improved sludge is sent to the pressure filter 35 and pressurized and dehydrated.
[0005]
[Problems to be solved by the invention]
The effect of freezing and thawing treatment in sludge filtration and dehydration operations is great, but the time required for the sludge freezing and thawing treatment is long, resulting in a problem of increased equipment and operating costs. To finish the sludge freezing in a short time, it is necessary to reduce the pitch of the heat transfer tubes and increase the number of heat transfer tubes. As a result, the equipment cost, the amount of brine used, the heat loss and the required power for circulation increase. The present invention has been completed as a result of earnestly researching the means for reducing the equipment cost and the operating cost while the operation is completed in a short time in order to effectively execute the freezing / thawing process.
[0006]
[Means for Solving the Problems]
As a means for solving the above-mentioned problems, the present invention is a freezing / thawing tank used for freezing / thawing treatment performed prior to sludge filtration / dehydration, and is bent in a plane passing through the central axis . A sludge freezing / thawing tank is used, in which finned heat transfer tubes formed of a serpentine tube or U-shaped tube and fins mounted in the plane are arranged in parallel or in the same plane.
[0007]
DETAILED DESCRIPTION OF THE INVENTION
The present invention will be specifically described with reference to the drawings. FIG. 1 is a transverse sectional view showing an example of the shape and arrangement of heat transfer tubes in a sludge freezing / thawing tank according to the present invention, and FIG. 2 is a longitudinal sectional view thereof.
[0008]
In the present invention, the sludge to be dehydrated by freezing and thawing may be organic or inorganic, and may be raw sludge that has not been concentrated, or sludge that has been concentrated by the method described above. The upper shape of the freezing / thawing tank may be cylindrical or rectangular, but the bottom is valley-shaped or cone-shaped so that the freezing / thawing tank sludge can be easily discharged. Considering sludge discharge, heat transfer tube arrangement, and manufacturing costs, the upper part should be a square tube and the bottom part should be a valley. A heat transfer tube 1 with fins 2 for flowing cold brine or warm brine is attached in the tank to freeze and thaw sludge. Depending on the nature and components of the frozen sludge, the tank body is usually made of carbon steel to prevent corrosion on the surface, as well as for insulation and cooling, and as a cushioning material to prevent damage to the tank due to volume expansion when the sludge freezes. Adhere foam sponge rubber etc. on the inner surface of the tank. The heat transfer tube 1 is preferably a circular tube because a large external pressure is applied by volume expansion of sludge due to freezing, and a stainless steel tube, a molten aluminum plated tube, or the like is used.
[0009]
The heat transfer tube 1 uses a serpentine tube or a U-shaped tube (helibone type heat exchanger) bent in a zigzag shape in order to efficiently store in the tank and increase the flow rate in the tube to increase the heat transfer coefficient. In order to facilitate the discharge of sludge, the heat transfer tube has a straight pipe portion in the vertical direction, the fin 2 is a simple flat plate, and both diametrical sides of the heat transfer tube 1 along the axial direction, The fins 2 are attached so as to be parallel to or flush with each other.
[0010]
The sludge that is frozen and thawed is sticky, so a few horizontal protrusions can cause a bridge to form when sludge is discharged, preventing sludge from being completely discharged, or air being mixed when sludge is thrown in. There is a risk that the sludge will not be uniformly filled in the tank. Therefore, when the heat transfer tube 1 is a serpentine tube or a U-shaped tube, the heat transfer tubes 1 are arranged in a direction A that is the same or parallel to the bending direction, and the fin 2 is also the center of the (attached) heat transfer tube 1. It is desired to be mounted in the same plane A as the bending direction. You may arrange | position the heat exchanger tube comprised by one snake tube over several parallel rows according to the above. It is better not to attach in the direction where the fin and the heat transfer tube axis direction intersect, or in the direction where planes including the fin intersect each other. It is not preferable from the viewpoint of preventing sludge from adhering and facilitating feeding, discharging and cleaning.
[0011]
The brine temperature during cooling is generally −10 to −20 ° C., and depending on the brine temperature, the cooling surface area including the fin surface is preferably 40 to 50 m 2 per ton of sludge.
[0012]
【Example】
In order to understand the present invention in detail, the conventional freezing / thawing tank will be described in detail with reference to an example in which the freezing / thawing tank according to the present invention is modified. It is not limited.
[0013]
Conventional Example and Example A conventional freezing and thawing tank is a SUS304TP having an inner diameter of about 120 cm, an inner height of about 150 cm, and a V-shaped carbon steel square tank with an outer diameter of 27.6 mm. Using tubes, the ends are U-shaped and bent in a zigzag manner 15 times in the same plane at a pitch of about 5.5 cm to form 16 serpentine tubular heat transfer tubes, which are attached in parallel at intervals of about 4.7 cm. It was. The heat transfer area was about 26 m 2 .
[0014]
The conventional heat transfer tube of the freezing / thawing tank was manufactured by replacing and attaching a finned heat transfer tube having the same shape as illustrated in FIGS. 1 and 2 to obtain the freezing / thawing tank according to the present invention. More specifically, a SUS304TP tube having an outer diameter of 27.6 mm is used as the heat transfer tube, and the end is U-shaped and bent in a zigzag manner seven times in the same plane at a pitch of about 11 cm. The SUS304 plate having a width of 3.6 cm was used as a fin and welded in the same direction as the bending direction on both sides of the center line of the straight tube portion of the heat transfer tube. The 18 heat transfer tubes were arranged in parallel at intervals of about 4.7 cm. The heat transfer area including the surface of the fin was about 30 m 2 .
[0015]
Both of the two types of freeze / thaw tanks were fed with 0.6 tons of sludge and frozen in -15 ° C brine. As a result, the required brine amount is about ½ and the circulation power of the brine is about ½ compared to the conventional freezing / thawing tank, and the time required for freezing under the same conditions is about 10% compared to the conventional tank. It has been shortened, and sludge can be easily charged, discharged and cleaned, improving work efficiency.
[0016]
【The invention's effect】
By effectively attaching fins to the heat transfer tube using the present invention, the number of heat transfer tubes is reduced to about 1/2 compared with the conventional sludge freezing and thawing tank, and the brine to be used accordingly. On the contrary, the amount of treated sludge that can be filled in the tank can be increased by about 5% by volume. Since the total required length of the heat transfer tube can be shortened, the brine flow rate in the tube can be increased to improve the heat transfer rate, and further the time required for the freezing / thawing operation can be shortened. In addition, since the curvature of the U vent can be increased, manufacturing restrictions are eased. In addition, when a flat plate is used for the fin and attachment is performed in one direction, and the heat transfer tube is a U-shaped tube or a serpentine tube, the sludge can be easily filled / discharged and cleaned by being attached in accordance with the bending direction.
[Brief description of the drawings]
FIG. 1 is a transverse sectional view showing an example of the shape and arrangement of heat transfer tubes in a sludge freezing / thawing tank according to the present invention. FIG. 2 is a longitudinal sectional view of the same. FIG. 3 is a freezing / thawing treatment method. Schematic flow sheet exemplifying conventional sludge treatment using slag
1: Heat transfer tube 2: Fin A: The same plane as the bending direction through the center of the heat transfer tube 31: Raw water containing sludge 32: Sedimentation basin 33: Concentration tank 34: Freezing / thawing tank 35: Filtration / dehydrator (pressure filtration 36) Heat transfer tube 37: Supernate water

Claims (1)

汚泥のろ過・脱水に先だって施される凍結・融解処理のために使用する凍結・融 解槽であって、中心軸を通る一平面内において曲げられた蛇管又はU字管と、前記 平面内に取り付けたフィンとによって構成されたフィン付伝熱管が、槽内において 平行又は同一の平面内に配列されていることを特徴とする汚泥の凍結・融解槽。Freezing and thawing tank used for freezing and thawing treatment prior to sludge filtration and dewatering, and a serpentine tube or U-shaped tube bent in a plane passing through the central axis, and the plane A sludge freezing and thawing tank, characterized in that finned heat transfer tubes configured with attached fins are arranged in parallel or in the same plane in the tank.
JP2002208704A 2002-07-17 2002-07-17 Sludge freeze / thaw tank Expired - Fee Related JP4191442B2 (en)

Priority Applications (1)

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