JPS58164843A - Moving type dehydration car - Google Patents

Moving type dehydration car

Info

Publication number
JPS58164843A
JPS58164843A JP57049305A JP4930582A JPS58164843A JP S58164843 A JPS58164843 A JP S58164843A JP 57049305 A JP57049305 A JP 57049305A JP 4930582 A JP4930582 A JP 4930582A JP S58164843 A JPS58164843 A JP S58164843A
Authority
JP
Japan
Prior art keywords
dehydration
sludge
section
vehicle
dewatering
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP57049305A
Other languages
Japanese (ja)
Inventor
伏尾 正則
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hitachi Kiden Kogyo Ltd
Original Assignee
Hitachi Kiden Kogyo Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hitachi Kiden Kogyo Ltd filed Critical Hitachi Kiden Kogyo Ltd
Priority to JP57049305A priority Critical patent/JPS58164843A/en
Publication of JPS58164843A publication Critical patent/JPS58164843A/en
Pending legal-status Critical Current

Links

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 本発明は下水処理場特に多数の分散する小規模な下水処
理場等よp発生する汚泥を脱水処理するのに適した移動
型脱水単に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a mobile dewatering unit suitable for dewatering sludge generated in a sewage treatment plant, particularly a large number of dispersed small-scale sewage treatment plants.

従来我国の下水処理は大都市中心型で、処理水量が多く
、そのため発生する汚泥量も多いため各処理場に汚泥脱
水機を常設し、汚泥の脱水処理を行うが一般的である。
Traditionally, sewage treatment in Japan has been centered on large cities, where a large amount of water is processed, and therefore a large amount of sludge is generated, so it is common practice to permanently install a sludge dewatering machine at each treatment plant to dewater the sludge.

しかし最近大都市だけでなく地方の小都市、村落へと下
水道の普及される傾向がある。この小都市では発生する
処理水量も少なく従って汚泥の発生量も少くなる。一般
に200〜1000人位を対象とする小規模下水処理場
に於ける一日の発生汚泥量は0.1〜2がで、このよう
な小都市部での小規模下水処理場では1週間或いは2週
間に一回位で脱水処理すれば充分で大都市の処理場と同
様常設の脱水設備を設ける必要がない。小規模下水処理
場で脱水設備を設けるとその作業上から脱水機の予備機
、補修部品等を常備させる必要があり、また運転維持管
理においても作業員の常駐或いは巡回によるメンテナン
スを行う必要が生じ、コストアップとなシ、また嬢境保
全面からもこの脱水機部分が最も悪臭の発生するところ
なるため、この悪臭防止の設備をも必要とし、小規模処
理場では之等の諸設備を完備することは経済的に非常に
負担が大きいものとなる。
However, recently there has been a trend to spread sewerage systems not only in large cities but also in small cities and villages in rural areas. In this small city, the amount of treated water generated is small, and therefore the amount of sludge generated is also small. In general, the amount of sludge generated per day in a small-scale sewage treatment plant that serves 200 to 1,000 people is 0.1 to 2. It is sufficient to perform dehydration treatment once every two weeks, and there is no need to install permanent dehydration equipment like treatment plants in large cities. When installing dewatering equipment at a small-scale sewage treatment plant, it is necessary to always have spare equipment and repair parts for the dehydrator on hand, and in terms of operation and maintenance, it is necessary to have workers on site or on patrol. In addition to increasing costs, the dehydrator is the place where the most foul odors are generated, so equipment to prevent this foul odor is required, and small-scale treatment plants are equipped with such equipment. Doing so would be a huge financial burden.

従って斯る小規模の下水処理場が分散して設置される地
域では各処理場で発生する汚泥を#動型の汚泥脱水機で
各下水処理場を定期的に巡回して処理する方が経済的で
ある0 さらにこの方法で処理する際使用される凝集剤としては
使用蓋の少ない高分子凝集剤が虐し、また脱水性能、汚
泥の違いによる脱水機の調整等よシ考えればベルトプレ
ス型脱水機が有利であるがこの槙の脱水機は大きなスペ
ースを必要とし、且重量が大となる欠点が1りυ、この
ため処理量の少ない小型のテスト機を8トン車以上の大
型トラックの荷台に搭載して使用されているに過ぎず、
小規模処理場に於てもその処理能力が少なく処理時間が
長くかかるこのベルトプレス型脱水機にはP布の洗浄に
多量の洗浄水を使用するが小規模処理場では多量の洗浄
水を供給することは困離で、その不足分をトラックに積
載するため上述の如く重量大なものとなる・     
、、。
Therefore, in areas where such small-scale sewage treatment plants are installed in a dispersed manner, it is more economical to treat the sludge generated at each treatment plant by periodically visiting each sewage treatment plant using a #dynamic sludge dehydrator. In addition, the flocculant used when processing with this method is a polymer flocculant with a small amount of lids, and considering the dewatering performance and the adjustment of the dewatering machine depending on the difference in sludge, belt press type is recommended. Although a dehydrator is advantageous, Maki's dehydrator requires a large space and has the disadvantage of being heavy.For this reason, a small test machine with a small processing capacity was used for a large truck of 8 tons or more. It is only used by being mounted on a loading platform.
Even in small-scale treatment plants, this belt press type dehydrator has low processing capacity and takes a long time to process, and a large amount of washing water is used to wash the P fabric. It would be difficult to do that, and the missing amount would have to be loaded onto a truck, which would result in a heavy load as mentioned above.
,,.

本発明はこれKmみてベルト、プレス型脱水mt−長く
の人が取得している普通免許で運転できるトラックに搭
載し、且多臘に必要とされる洗浄水を循環再利用をする
ことにより上述の欠点を除去したもので、さらにポンプ
、脱水機等の駆動源を車輛のエンジンを利用した油圧式
として供給し、外部電力の供給を不用として給電設備の
ない処理場でも汚泥処理を可能としたものである。
The present invention is installed on a truck that can be driven by a long-term driver's license, such as belt, press type dehydration mt, and the above-mentioned method by circulating and reusing the washing water that is required for a large amount of time. In addition, the drive source for the pump, dehydrator, etc. is hydraulically powered by the vehicle's engine, eliminating the need for an external power supply, making sludge treatment possible even in treatment plants without power supply equipment. It is something.

以下本発明を図示の実施例に基づいて説明する。The present invention will be explained below based on illustrated embodiments.

図に於て0は普通運転免許で運転可能な普通トラックで
、該トラックに汚泥の脱水に必要なすべての装置が搭載
される。この脱水装置は第1図に示す構成よ構成る。
In the figure, 0 is a regular truck that can be driven with a regular driver's license, and this truck is equipped with all the equipment necessary for sludge dewatering. This dewatering apparatus is constructed as shown in FIG.

即ち下水処理場より1IlliI収された汚泥は給泥ポ
ンプ1にてラインミキサー3へ供給される。この時ライ
ンミキサー3の前後に、薬液槽5a、5bに貯留された
カチオン系高分子凝集剤とアニオン系或いはノニオン系
高分子凝集剤を収納しであるのを各薬液槽に接続された
薬注ポンプ2a、2bにて添加されるが、□1これは汚
泥が最適な凝集フロン、1::、、。
That is, the sludge collected from the sewage treatment plant is supplied to the line mixer 3 by the sludge pump 1. At this time, a cationic polymer flocculant and an anionic or nonionic polymer flocculant stored in chemical tanks 5a and 5b are stored before and after the line mixer 3, and a chemical inlet connected to each chemical tank is used. It is added by pumps 2a and 2b, but □1 is flocculation, which is most suitable for sludge.

りとなるようにレズその添加量は定められる。凝集剤の
添加後、ラインミキサー3にて急速攪拌を行なった後こ
れを前処理ドラム4へ供給される。
The amount of resin added is determined so that the After adding the flocculant, the mixture is rapidly stirred in the line mixer 3 and then supplied to the pretreatment drum 4.

この前処理ドラム4は外筒を40〜80メツシ^の全網
製のドラム形として濃縮槽とし、また内局を凝集混和槽
の二重式とし、この外筒を1〜2rpmのゆつ<J)し
た回転で回動させるようになし、この前処理ドラムの凝
集混和部4aで緩速攪拌が行なわれ、該ドラム内に供給
された凝集剤を添加された汚泥はここで強固で絨密なフ
ロックが形成され、次に濃縮部4bで5〜7%まで濃縮
され、これが次の脱水機6へ供給される。
This pre-treatment drum 4 has an outer cylinder that is a 40 to 80-mesh all-mesh drum shape and serves as a concentration tank, and an inner part that is a double type coagulation and mixing tank. J), and slow stirring is performed in the coagulation mixing section 4a of this pre-treatment drum, where the sludge to which the flocculant has been added, supplied into the drum, is solidified and compacted. A floc is formed, which is then concentrated to 5 to 7% in the concentrating section 4b, and then supplied to the next dehydrator 6.

この脱水機はエンドレス状の二枚のP布6aと6bが7
pツクの脱水が行えるよう互いに沿わせ且何回も折れ曲
がるようにして複数のローラ群にて導びかれるようにな
ってお9両戸布間にて強く挟圧されて所望の脱水が行な
われる。二枚のp布6a、6bのくさび状加圧脱水s4
 o内にて前処理ドラムの濃縮部より汚泥が供給される
とこのエンドレスベルト状p布の駆動によp該脱水部6
0で8〜15%まで脱水され、フロックは互いに凧密に
結合した板状となり、次に続く田−ラ加圧部6dにてさ
らに加圧脱水が行なわれる。このローラ加圧部のうち任
意のもの或いは後方側の加圧ローラ7(一本又は複数本
)内にトラックのエンジン排熱を導ひき、該排熱を利用
して40〜100℃に加熱し加圧ローラにて加圧脱水さ
れたケーキの水分をさらに脱水するようになす。このよ
うにして脱水後のケーキはエンドレスベルト状F布6a
、6’bの開放された排出部6eよシ排出され脱水ケー
キホッパー8内へ投入され一時的に貯留される〇 また脱水機のP布6a、6bは脱水機に附設された洗浄
後[9a、9bにて洗浄されるが、この洗浄後の洗浄水
と脱離水はホッパー90にて集受水し、これを循環ポン
プ10によυ前処理ドラムへ戻され該ドラムの洗浄水再
生部40にて88711度200 my/を以下に調整
された後これを洗浄水タンク11に貯水される。この洗
浄水タンク11の洗浄水は洗浄水ポンプ12にて上記洗
浄後@ 9 a 。
This dehydrator consists of two endless pieces of P cloth 6a and 6b.
They are placed along each other and bent many times to be guided by a group of rollers so that the water can be dehydrated, and then they are strongly pressed between the nine cloth cloths to achieve the desired dehydration. . Wedge-shaped pressurized dehydration s4 of two p cloths 6a and 6b
When sludge is supplied from the concentration section of the pre-treatment drum in the dewatering section 6, this endless belt-like cloth is driven.
The flocs are dehydrated to 8 to 15% at 0, and the flocs form a plate-like shape that is tightly bonded to each other.Then, the flocs are further pressurized and dehydrated in the subsequent field pressurizing section 6d. Exhaust heat from the truck's engine is introduced into any one of these roller pressure parts or into the pressure roller 7 (one or more) on the rear side, and the exhaust heat is used to heat the roller to 40 to 100°C. The moisture of the cake that has been pressurized and dehydrated using a pressure roller is further dehydrated. In this way, the cake after dehydration is made into an endless belt-like F cloth 6a.
, 6'b are discharged through the open discharge part 6e, and put into the dehydrating cake hopper 8 where it is temporarily stored. Also, the P cloths 6a and 6b of the dehydrating machine are cleaned after washing [9a attached to the dehydrating machine]. , 9b, and the washing water and desorbed water after washing are collected and received in a hopper 90, and returned to the υ pretreatment drum by the circulation pump 10, and then sent to the washing water regeneration section 40 of the drum. After adjusting the water to 88,711 degrees and 200 my/min, the water is stored in the wash water tank 11. The cleaning water in the cleaning water tank 11 is washed by the cleaning water pump 12 at @9a.

9bへ供給され一布の洗浄用として再利用されるが、汚
泥の脱水による分鵬水、添加凝集剤によp増えた量は洗
浄水タンク11よジオ−パフ賞jl、   。
The water is supplied to the washing water tank 11 and reused for washing the cloth, but the water separated by dewatering the sludge and the amount increased by the added flocculant are transferred to the washing water tank 11.

て処理場へ戻されるが、この場合SS6度200my/
を以下に清浄化されているので処理場の機能を損なうこ
とがない0 また本発明脱水装置に使用される凝集剤は処理場から供
給される水を利用して薬液槽内で所’ii!濃度に溶解
されるものである。
However, in this case, SS 6 degrees 200 my/
The flocculant used in the dewatering device of the present invention is purified in a chemical tank using water supplied from the treatment plant, so that it does not impair the functionality of the treatment plant. It is something that is dissolved in concentration.

上述の脱水装置すべての機器はその全体をケーシング(
アルミニウム等の)又は幌等のカバーにて覆うようにし
汚泥脱水時に発生する悪臭気を脱水車外へ発散しないよ
うになすと共にトラックのエンジンの種類によってはエ
ンジンへの給気をこの機器をおおったカバー内部の空気
を利用してエンジンへ供給し、燃焼して脱臭することも
可能である。
All of the above-mentioned dewatering equipment is constructed entirely in a casing (
This equipment is covered with a cover (made of aluminum, etc.) or a hood to prevent the bad odor generated during sludge dehydration from escaping outside the dehydration vehicle. It is also possible to use internal air to supply it to the engine and burn it to deodorize it.

第2図・第3図は本発明の一実施例図で有効ベル) 1
llli 1 mのベルトプレスを積載し、処理能力5
ハで、加熱p−ラの熱伝導、軽量化、耐蝕性を□ 考慮し、主要部を耐蝕アルミニウム製とし、脱水ケーキ
運搬量を約1トンとし、普通免許で運転可能なトラック
に搭載されている。
Figures 2 and 3 are illustrations of one embodiment of the present invention and are valid) 1
Loaded with lli 1 m belt press, processing capacity 5
In consideration of heat conduction, weight reduction, and corrosion resistance of the heating p-ra, the main parts are made of corrosion-resistant aluminum, the dehydrated cake carrying capacity is approximately 1 ton, and it is mounted on a truck that can be driven with a regular driver's license. There is.

また脱水機のベルト弐P布の駆動、各他ポンプの駆動は
車輛エンジンを利用した全油圧式とし給電設備のない処
理場に於ても汚泥の脱水処31 t−可能としたもので
ある〇 而して本発明による時は小規侠分敢型の下水処理場を巡
回して短時間で各下水処理場で発生する汚泥の脱水処理
が経済的に効率的に行えると共に汚泥の脱水に於て二成
分の薬剤が添力■されるので脱水率が向上し、しかもエ
ンジンの排熱利用にて戸布による脱水とさらに脱水を行
うようになしているので脱水ケーキの富水率が従来法に
比べ低下し、この脱水ケーキを処分するため運搬するホ
ッパーを備えているので他のダンプトラック等が不要と
なシ、各下水処理場に脱水設備が不要となる等数々の利
点を有する。
In addition, the drive of the dehydrator's belt and other pumps are fully hydraulic, using a vehicle engine, making it possible to dewater sludge even in treatment plants without power supply equipment. According to the present invention, the sludge produced at each sewage treatment plant can be economically and efficiently dehydrated in a short time by visiting the sewage treatment plants of the small-scale division type. Since the two-component agent is added in the process, the dehydration rate is improved, and since the exhaust heat of the engine is used to perform dehydration in the door cloth and further dehydration, the water richness of the dehydrated cake is lower than that of the conventional method. Since it is equipped with a hopper to transport this dehydrated cake for disposal, it has many advantages such as eliminating the need for other dump trucks and eliminating the need for dewatering equipment at each sewage treatment plant.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明による汚泥脱水処理工程を示す説明図、
第2図社実施例の正面図、第3図は同平面図である。 0・・・トラック ト・・給泥ポンプ 2a、2b・・・薬注ポンプ 3・・・ラインミキサー 4・・・前処理ドラム 4a・・・凝集混和部 4b・・・濃縮部 40・・・洗浄水再生部 5a、51)・・・薬液槽 6・・・脱水機 6F1.6b・・・P布 60・・・くさび状加圧部 6d・・・ローラ加圧部 6e・・・排出部 7・・・加熱ローラ 8・・・脱水ケーキホッパー 9a、9b・・・洗浄装置 90・・・ホッパー 10・・・循環ポンプ 11・・・洗浄水タンク 12・・・洗浄水ポンプ +、+Jl 外1名
FIG. 1 is an explanatory diagram showing the sludge dewatering process according to the present invention;
Figure 2 is a front view of the embodiment, and Figure 3 is a plan view of the same. 0...Tracked...Sludge feed pumps 2a, 2b...Chemical injection pump 3...Line mixer 4...Pretreatment drum 4a...Coagulation mixing section 4b...Concentration section 40... Cleaning water regeneration section 5a, 51)... Chemical tank 6... Dehydrator 6F1.6b... P cloth 60... Wedge-shaped pressure section 6d... Roller pressure section 6e... Discharge section 7...Heating roller 8...Dehydrated cake hoppers 9a, 9b...Cleaning device 90...Hopper 10...Circulation pump 11...Washing water tank 12...Washing water pump +, +Jl Outside 1 person

Claims (2)

【特許請求の範囲】[Claims] (1)給泥、P布洗浄等脱水作業に必要なポンプ、2.
4統の薬注装置、ラインミキサー、凝集混和部と濃縮部
及びP布の洗浄水再生部からなる前処理装置、加熱部を
付加したベルトプレス型脱水機、脱水ケーキホッパーを
全て積載し、車両のエンジンを利用して駆動することを
特徴とする移動型脱水車。
(1) Pumps necessary for dehydration work such as mud supply and P cloth cleaning, 2.
Four chemical dosing devices, a line mixer, a pretreatment device consisting of a flocculation mixing section, a concentration section, and a washing water regeneration section for P cloth, a belt press type dehydrator with a heating section, and a dehydration cake hopper are all loaded on the vehicle. A mobile dehydration vehicle characterized by being driven using an engine.
(2)  移動型脱水車を普通免許で運転できるトラッ
クとしたことを特徴とする特許請求の範囲第1項記載の
移動型脱水車。
(2) The mobile dehydration vehicle according to claim 1, wherein the mobile dehydration vehicle is a truck that can be driven with a regular driver's license.
JP57049305A 1982-03-26 1982-03-26 Moving type dehydration car Pending JPS58164843A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57049305A JPS58164843A (en) 1982-03-26 1982-03-26 Moving type dehydration car

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57049305A JPS58164843A (en) 1982-03-26 1982-03-26 Moving type dehydration car

Related Child Applications (1)

Application Number Title Priority Date Filing Date
JP59150349A Division JPS6041599A (en) 1984-07-18 1984-07-18 Movable dehydration truck

Publications (1)

Publication Number Publication Date
JPS58164843A true JPS58164843A (en) 1983-09-29

Family

ID=12827224

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57049305A Pending JPS58164843A (en) 1982-03-26 1982-03-26 Moving type dehydration car

Country Status (1)

Country Link
JP (1) JPS58164843A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015000380A (en) * 2013-06-17 2015-01-05 水ing株式会社 Apparatus and method for coagulating sludge, and sludge treatment apparatus

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015000380A (en) * 2013-06-17 2015-01-05 水ing株式会社 Apparatus and method for coagulating sludge, and sludge treatment apparatus

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