JPS6130837B2 - - Google Patents

Info

Publication number
JPS6130837B2
JPS6130837B2 JP57030942A JP3094282A JPS6130837B2 JP S6130837 B2 JPS6130837 B2 JP S6130837B2 JP 57030942 A JP57030942 A JP 57030942A JP 3094282 A JP3094282 A JP 3094282A JP S6130837 B2 JPS6130837 B2 JP S6130837B2
Authority
JP
Japan
Prior art keywords
tank
sludge
water
overwater
flocculant
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.)
Expired
Application number
JP57030942A
Other languages
Japanese (ja)
Other versions
JPS58150490A (en
Inventor
Hideaki Oomori
Akira Izawa
Tetsuo Kato
Keiichi Fujita
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.)
Tokyu Car Corp
Original Assignee
Tokyu Car Corp
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 Tokyu Car Corp filed Critical Tokyu Car Corp
Priority to JP57030942A priority Critical patent/JPS58150490A/en
Publication of JPS58150490A publication Critical patent/JPS58150490A/en
Publication of JPS6130837B2 publication Critical patent/JPS6130837B2/ja
Granted legal-status Critical Current

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  • Filtration Of Liquid (AREA)
  • Sewage (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Description

【発明の詳細な説明】 本発明は、浄化槽その他の槽に貯留された汚泥
水を凝集剤液を用いて処理する浄化槽等の汚泥水
処理車に関するもので、浄化槽その他の槽の所在
の場所に於いて、汚泥水を凝集剤液を用いつつ凝
集汚泥と過水とに効果的に分離し、種汚泥の死
滅のない過水を張水として浄化槽その他の槽に
戻すことができるため、凝集汚泥のみを運搬すれ
ば良く、浄化槽等の管理も容易であり、小型化が
可能であり、さらに操作が容易である等、従来の
汚泥水汲取車に比し画期的な効果を奏する浄化槽
等の汚泥水処理車を提供するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a sludge water treatment vehicle for a septic tank or other tank that treats sludge water stored in a septic tank or other tank using a flocculant solution. Sludge water can be effectively separated into flocculated sludge and overwater using a flocculant solution, and the overwater, which does not kill the seed sludge, can be returned to the septic tank or other tank as water. Septic tanks, etc., have revolutionary effects compared to conventional sludge and water pumping trucks, such as only needing to be transported, septic tanks, etc. are easy to manage, can be made smaller, and are easier to operate. It provides a sludge water treatment vehicle.

即ち、本発明は、 1つのタンク内を2つの区画壁により区画して
凝集剤液槽、過水槽、及び撹拌機構を備え且つ
上記凝集剤液槽と連通し得る汚泥水槽を設けた汚
泥水処理タンクと、 上記過水槽と上記汚泥水槽との間にそれぞれ
に連通可能に配され、上記汚泥水槽内で凝集剤液
と撹拌混合され固形分がブロツク状に凝集された
汚泥水を、過水と凝集汚泥とに分離する過装
置と、 真空ポンプ及び四方切換コツクを用いて構成し
た一つの加圧・減圧装置と、 切換コツクを介して上記汚泥水槽又は上記過
水槽に連通し得る吸排水ホースと を装備してなり、 上記加圧・減圧装置は、上記凝集剤液槽、上記
過水槽、及び上記汚泥水槽それぞれに連通して
該三槽それぞれの内部を減圧・加圧可能になして
あり、 上記凝集剤液槽と上記汚泥水槽との間には、上
記汚泥水槽内への凝集剤液の移行量を計測する流
量計を設けてあり、 上記過装置は、俯仰自在な横型の回転式スク
リーン筒と、その下方に配備し上記汚泥水槽に連
通し得る過水受タンクと、上記スクリーン筒で
分離された凝集汚泥を収容する汚泥槽とからなつ
ている ことを特徴とする浄化水槽等の汚泥水処理車を
提供するものである。
That is, the present invention provides a sludge water treatment in which one tank is divided by two partition walls and provided with a flocculant liquid tank, a superhydric tank, and a sludge tank that is equipped with a stirring mechanism and that can communicate with the flocculant liquid tank. A tank is arranged so as to be able to communicate with each other between the above-mentioned superwater tank and the above-mentioned sludge tank, and the sludge water in which the solid content is agglomerated into blocks by being stirred and mixed with the flocculant liquid in the sludge tank is mixed with the superwater tank and the sludge tank. A filtration device that separates flocculated sludge into flocculated sludge, a pressurization/depressurization device configured using a vacuum pump and a four-way switching tank, and a suction/drainage hose that can communicate with the sludge tank or the overwater tank via the switching tank. The pressurization/depressurization device is connected to each of the flocculant liquid tank, the overwater tank, and the sludge tank, and is capable of depressurizing and pressurizing the inside of each of the three tanks, A flow meter is provided between the flocculant liquid tank and the sludge tank to measure the amount of flocculant liquid transferred into the sludge tank. Sludge in a septic water tank, etc., comprising a cylinder, an overwater receiving tank disposed below the cylinder and communicating with the sludge tank, and a sludge tank that accommodates flocculated sludge separated by the screen cylinder. The company provides water treatment vehicles.

以下、本発明の浄化槽等の汚泥水処理車を図面
に示す一実施例について説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of a sludge water treatment vehicle such as a septic tank according to the present invention shown in the drawings will be described below.

第1図〜第3図において、1は車体中央部に搭
載した汚泥水処理タンクで、第4図に示す2つの
区画壁1′,1′により内部を区画して前方より順
次凝集剤液槽A、過水槽B、及び汚泥水槽Cを
設けてある。そして該凝集剤液槽Aの内壁にはエ
ポキシ樹脂が塗布してあり、該汚泥水槽Cには第
4図に示す如く3枚羽根2を回転軸に2段階に設
けてなる撹拌機構C′を配してある。又Dは上記
汚泥水処理タンク1の左側後方に配置した過装
置、Eはその前方に配置した汚泥槽、Fは上記汚
泥水処理タンク1の右側方に配置した清水タン
ク、Gは上記汚泥水処理タンク1の後部上方に配
置した吸排水ホース用ホースリール、Jは洗滌ホ
ース用ホースリールであり、その他第1図〜第3
図に図示していないが本発明の浄化槽等の汚泥水
処理車には第4図に示す如く必須要件として真空
ポンプHを具備させてある。このように各槽等を
構成し配置することにより、本発明の汚泥水処理
車は小型化が可能となり、積載重量4t未満の小型
自動車への適用をもつて狭い道路を自由に走行す
ることが可能となる。
In Figures 1 to 3, 1 is a sludge water treatment tank mounted in the center of the vehicle body, and the interior is divided by two partition walls 1' and 1' shown in Figure 4, and the flocculant liquid tank is sequentially placed from the front. A, a water tank B, and a sludge tank C are provided. The inner wall of the flocculant liquid tank A is coated with epoxy resin, and the sludge tank C is equipped with a stirring mechanism C' having three blades 2 installed in two stages on a rotating shaft as shown in FIG. It is arranged. Also, D is a filtration device placed on the left rear side of the sludge water treatment tank 1, E is a sludge tank placed in front of it, F is a clean water tank placed on the right side of the sludge water treatment tank 1, and G is the sludge water A hose reel for the suction and drainage hose placed above the rear of the treatment tank 1, J is a hose reel for the cleaning hose, and other
Although not shown in the figure, the sludge water treatment vehicle such as a septic tank according to the present invention is equipped with a vacuum pump H as an essential requirement, as shown in FIG. By configuring and arranging each tank etc. in this way, the sludge water treatment vehicle of the present invention can be downsized, and can be applied to small vehicles with a loading weight of less than 4 tons and can freely travel on narrow roads. It becomes possible.

而して、上記各構成の配管関係を、上記各構成
の一部の詳細及び上記各構成以外の構成とともに
第4図に基づいて説明すると、凝集剤液槽A、
過水槽B、及び汚泥水槽Cは四方切換コツクIを
介して真空ポンプHに連通させてあり、四方切換
コツクIと上記各槽A、B、Cとを結ぶパイプ3
にはエアークリーナー4を設け、パイプ3の一端
は3つに分岐させてそれぞれ二方切換コツク5,
6,7を介して上記各槽A、B、Cに接続してあ
る。又四方切換コツクIと真空ポンプHは、2本
のパイプ8,9によつて閉ループを形成し一つの
加圧、減圧装置を構成するように接続してあり、
上記パイプ9にはオイルセパレーター10及び空
気安全弁11を設けてある。又四方切換コツクI
に一端を接続した別のパイプ12はその他端にお
いて2つに分岐させてあり、その一方は二方切換
コツク13を介して大気中に開放してあり、他方
は二方切換コツク14を介して汚泥水槽Cに接続
してある。
The piping relationship of each of the above components will be explained based on FIG. 4 along with some details of each of the above components and components other than the above components.
The overwater tank B and the sludge tank C are connected to a vacuum pump H via a four-way switching tank I, and a pipe 3 connects the four-way switching tank I to the tanks A, B, and C.
is provided with an air cleaner 4, and one end of the pipe 3 is branched into three parts, each of which has a two-way switch 5,
It is connected to the above-mentioned tanks A, B, and C via 6 and 7. Furthermore, the four-way switching tank I and the vacuum pump H are connected to form a closed loop through two pipes 8 and 9 to constitute one pressurization and depressurization device.
The pipe 9 is provided with an oil separator 10 and an air safety valve 11. Four-way switching Kotoku I
Another pipe 12 connected at one end to the other end is branched into two parts, one of which is open to the atmosphere via a two-way switching socket 13, and the other is open to the atmosphere via a two-way switching socket 14. It is connected to sludge tank C.

又、15は凝集剤液槽Aに一端を接続したパイ
プで、二方切換コツク16を介して大気中に開放
させてあり、該切換コツク16の開放時に凝集剤
液を外部(系外)から吸引できるようになしてあ
る。17は凝集剤液槽Aと汚泥水槽Cとの間に設
けた凝集剤液移行のためのパイプで、流量計18
及び二方切換コツク19を設けてある。そして
又、20,21はそれぞれ二方切換コツク22,
23を介して過水槽B及び汚泥水槽Cに一端を
接続したパイプで、点24において合流し、該合
流点24においてパイプ25及びパイプ26に分
岐させてある。分岐させた一方のパイプ25は吸
排水ホース用ホースリールGに捲かれた吸排水ホ
ース27に二方切換コツク28を介して接続して
あり、他方のパイプ26は二方切換コツク29を
介して過装置Dの一端に接続してある。又過
装置Dの他端は二方切換コツク30を有する透明
なパイプ31を介して過水槽Bに接続してあ
る。
A pipe 15 has one end connected to the flocculant liquid tank A, and is opened to the atmosphere via a two-way switch 16. When the switch 16 is opened, the flocculant liquid is removed from the outside (outside the system). It is designed so that it can be inhaled. 17 is a pipe for transferring the flocculant liquid between the flocculant liquid tank A and the sludge tank C, and the flow meter 18
and a two-way switching cock 19. Also, 20 and 21 are two-way switching tips 22,
It is a pipe whose one end is connected to the overwater tank B and the sludge tank C via a pipe 23, which joins at a point 24, and branches into a pipe 25 and a pipe 26 at the junction 24. One of the branched pipes 25 is connected to a suction/drainage hose 27 wound around a hose reel G for suction/drainage hoses via a two-way switching socket 28, and the other pipe 26 is connected via a two-way switching socket 29. It is connected to one end of the filter device D. The other end of the filtration device D is connected to the filtration tank B via a transparent pipe 31 having a two-way switching pot 30.

上記パイプ21,26,31を介して過水槽
Bと汚泥槽Cとの間に連通した過装置Dは、
過水受タンク32と、該過水受タンク32上方
に回転自在に配置した横型の回転式スクリーン筒
33と、該回転式スクリーン筒33の上方に配置
した洗滌ノズル34′とを主体として構成してあ
り、該回転式スクリーン筒33と洗滌ノズル3
4′とは下方及び前方の開口した透明な外筐34
(第2図参照)内に収納してある。回転式スクリ
ーン筒33は厳密にはその前端33′を上記外筐
34の前方へ突出させて汚泥槽Eの汚泥収入部3
5上に位置させてあり、上記外筐34後端の軸支
部を中心として上記外筐34前端を油圧シリンダ
ー52等で上下動させることにより、上記外筐3
4と共に俯仰自在(第4図及び第8図比較参照)
となしてある。又上記回転式スクリーン筒33
は、40〜100メツシユの金網、ナイロン製鋼等の
網体で構成してあり、その内側面には内部の汚泥
やその他の夾雑物を回転に伴つて前端33′方向
へ押出す螺旋プレード(図示せず)を設けてあ
る。そして又回転式スクリーン筒33は上記外筐
34に設けた回転式スクリーン筒支持ロール(図
示せず)の一部を油圧モーター(図示せず)によ
り回転速度調節可能に駆動できるようになしてあ
る。尚、前述した過装置Dへの連通パイプ2
6,31は、それぞれ回転式スクリーン筒33内
及び過水受タンク32内に開口させてある。又
36,36は汚泥槽の汚泥取出用ハツチである。
The filtration device D communicates between the filtration tank B and the sludge tank C via the pipes 21, 26, and 31.
It mainly consists of an overwater receiving tank 32, a horizontal rotary screen cylinder 33 rotatably arranged above the overwater receiving tank 32, and a cleaning nozzle 34' arranged above the rotary screen cylinder 33. The rotary screen tube 33 and the cleaning nozzle 3
4' is a transparent outer casing 34 with openings at the bottom and front.
(See Figure 2). Strictly speaking, the rotary screen cylinder 33 has its front end 33' protruding forward of the outer casing 34, and is connected to the sludge receiving section 3 of the sludge tank E.
By moving the front end of the outer casing 34 up and down with a hydraulic cylinder 52 or the like around the shaft support at the rear end of the outer casing 34, the outer casing 3
4 and can be raised and raised freely (see comparison of Figures 4 and 8)
It is said that In addition, the rotary screen tube 33
is composed of a mesh body made of wire mesh, nylon steel, etc. with 40 to 100 meshes, and on its inner surface there is a spiral plate (Fig. (not shown) is provided. Further, the rotary screen tube 33 is configured such that a part of a rotary screen tube support roll (not shown) provided in the outer casing 34 can be driven by a hydraulic motor (not shown) so that the rotation speed can be adjusted. . In addition, the communication pipe 2 to the above-mentioned filter device D
6 and 31 are opened into the rotary screen cylinder 33 and the overwater receiving tank 32, respectively. Further, 36, 36 are hatches for removing sludge from the sludge tank.

又清水タンクFは、プランジヤーポンプ37を
介し、二方切換コツク38を有するパイプ39に
よつて洗滌ノズル34′に連通させてあり、且つ
パイプ39から分岐させた洗滌ホース40に連通
させてある。該洗滌ホース40は洗滌ホース用ホ
ースリールJに捲かれており、その開放端に二方
切換コツク41を具備させてあつて、各槽の洗滌
その他の洗滌に用い得るようになしてある。
The fresh water tank F is connected to the cleaning nozzle 34' via a plunger pump 37 and a pipe 39 having a two-way switching socket 38, and is also connected to a cleaning hose 40 branched from the pipe 39. . The cleaning hose 40 is wound around a hose reel J for cleaning hoses, and has a two-way switching socket 41 at its open end so that it can be used for cleaning each tank and other cleaning purposes.

尚、第1〜3図において、42は操作レバー群
であり、上述した各種の切換コツク、ポンプ、回
転式スクリーン筒、ホースリール、撹拌機構等を
油圧により遠隔操作できるようになしてある。勿
論上記各構成の内の一部、例えば切換コツクは手
動により操作するものであつても良い。又各槽に
は目視可能な液量目盛計(図示せず)を設けてあ
り、パイプの一部は透明にしてその内部を通過す
る液体の性状を目視できるようになしてある。
In FIGS. 1 to 3, reference numeral 42 denotes a group of operating levers, which enable remote control of the various switching levers, pumps, rotary screen tubes, hose reels, stirring mechanisms, etc. described above using hydraulic pressure. Of course, some of the above-described components, such as the switching knob, may be operated manually. Each tank is provided with a visually visible liquid level scale (not shown), and a portion of the pipe is made transparent so that the properties of the liquid passing through it can be visually observed.

次に、以上のように構成した本発明の浄化槽等
の汚泥水処理車における作動の態様を説明する。
本発明の汚泥水処理車の走行状態においては第4
図に示す如く全ての切換コツクは閉成状態にあ
り、浄化槽等所在の場所に走行するに先立つて、
まず凝集剤液Kを凝集剤液槽Aに第5図に示す如
く吸引収容する。即ち、第5図に示す如く、二方
切換コツク5,13,16を開放し且つ四方切換
コツクIを設定すると共に、真空ポンプHを作動
させれば、太い実線で示す如く凝集剤液槽A内の
空気がパイプ3,12を介して大気中に放出さ
れ、これによる凝集剤液槽Aの減圧に伴つてパイ
プ15を介して凝集剤液Kが系外から凝集剤液槽
A内に吸引収容される。吸引収容する凝集剤液K
としてはカチオン性ポリアクリルアミド系高分子
凝集剤の0.1〜0.3%水溶液が好ましい。凝集剤液
Kを吸引収容したら、二方切換コツク16を閉成
すると共に四方切換コツクIを切換えて凝集剤液
槽A内を大気圧下とし、しかる後二方切換コツク
5,13を閉成してから、浄化槽等所在の場所ま
で走行する。尚、この場合本発明の浄化槽等の汚
泥水処理車は積載重量4t未満の小型自動車となす
ことが可能であるから、狭い道路でも自由に走行
できる。
Next, the mode of operation of the sludge water treatment vehicle such as a septic tank according to the present invention constructed as described above will be explained.
In the running state of the sludge water treatment vehicle of the present invention, the fourth
As shown in the figure, all the switching points are in the closed state, and before traveling to the location where the septic tank is located,
First, the flocculant liquid K is sucked into the flocculant liquid tank A as shown in FIG. That is, as shown in FIG. 5, by opening the two-way switching sockets 5, 13, and 16 and setting the four-way switching socket I, and operating the vacuum pump H, the flocculant liquid tank A is opened as shown by the thick solid line. The air inside is released into the atmosphere through the pipes 3 and 12, and as the pressure in the flocculant tank A is reduced, the flocculant liquid K is sucked into the flocculant tank A from outside the system through the pipe 15. be accommodated. Coagulant liquid K to be sucked and stored
A 0.1 to 0.3% aqueous solution of a cationic polyacrylamide polymer flocculant is preferable. After the flocculant liquid K is sucked and contained, the two-way switching tank 16 is closed, and the four-way switching tank I is switched to bring the inside of the flocculant liquid tank A to atmospheric pressure, and then the two-way switching sockets 5 and 13 are closed. Then, drive to the location where the septic tank, etc. is located. In this case, the vehicle for treating sludge water such as a septic tank according to the present invention can be made into a small vehicle with a loading weight of less than 4 tons, so it can be freely driven even on narrow roads.

浄化槽等所在の場所に到着したら、、第6図に
示す如く、吸排水ホース用ホースリールGから吸
排水ホース27を繰り出し、その先端を浄化槽L
に挿入し、浄化槽L内の汚泥水Mを汚泥水槽C内
に収容吸引する。即ち、第6図に示す如く、二方
切換コツク7,13を開放し且つ四方切換コツク
Iを切換え、真空ポンプHを作動させる一方、二
方切換コツク23,28を開放すれば汚泥水槽C
内の空気が太い実線で示す如くパイプ3,12を
介して大気中に放出され、これによる汚泥水槽C
の減圧に伴なつて、パイプ21,25及び吸排水
ホース27を介して浄化槽L内の汚泥水Mが汚泥
水槽C内に吸引収容される。
When you arrive at the location of the septic tank, etc., as shown in Fig. 6, let out the suction and drainage hose 27 from the hose reel G for the suction and drainage hose, and connect the tip of the hose to the septic tank L.
The sludge water M in the septic tank L is contained and sucked into the sludge tank C. That is, as shown in FIG. 6, by opening the two-way switching sockets 7 and 13 and switching the four-way switching socket I to operate the vacuum pump H, while opening the two-way switching sockets 23 and 28, the sludge tank C is opened.
The air inside is released into the atmosphere through the pipes 3 and 12 as shown by the thick solid line, and the resulting sludge tank C
As the pressure is reduced, the sludge water M in the septic tank L is sucked into the sludge tank C via the pipes 21, 25 and the suction/drainage hose 27.

汚泥水Mの上記吸引収容作業が終了したら、第
7図に示す如く、上記二方切換コツク23,28
のみを開放状態から閉成状態とし、二方切換コツ
ク7,13、四方切換コツクI、及び真空ポンプ
Hを第6図の状態としたまま、二方切換コツク1
9を開放して凝集剤液槽A中の凝集剤液Kを太い
実線で示す如くパイプ17を介して汚泥水槽C内
に吸引収容する。汚泥水槽C内への凝集剤液Kの
吸引収容は汚泥水槽Cが減圧下におかれているこ
とによつて行なわれ、又吸引収容すべき凝集剤液
Kは流量計18で計量すれば良く、所定量の凝集
剤液Kを汚泥水槽Cに吸引収容した後二方切換コ
ツク19を閉成すれば凝集剤液Kの吸引収容は終
了する。凝集剤液Kの吸引収容量(使用量)は、
凝集剤液Kとして前述の如くカチオン性ポリアク
リルアミド系高分子凝集剤の0.1〜0.3%水溶液を
用いた場合、汚泥水槽C内の汚泥水Mに対し2.1
〜4容量%とするのが好ましい。尚、汚泥水槽C
内の汚泥水Mの量は前述したように汚泥水槽Cに
設けた液量目盛りによつて測定されている。
When the suction and storage work of the sludge water M is completed, as shown in FIG.
The two-way switching socket 7, 13, the four-way switching socket I, and the vacuum pump H remain in the state shown in FIG. 6.
9 is opened, and the flocculant liquid K in the flocculant liquid tank A is sucked into the sludge tank C through the pipe 17 as shown by the thick solid line. The flocculant liquid K is sucked and stored in the sludge tank C by keeping the sludge tank C under reduced pressure, and the flocculant liquid K to be sucked and stored can be measured using a flow meter 18. After a predetermined amount of the flocculant liquid K is sucked and stored in the sludge tank C, the two-way switching pot 19 is closed, and the suction and storage of the flocculant liquid K is completed. The suction capacity (amount used) of flocculant liquid K is:
When a 0.1 to 0.3% aqueous solution of a cationic polyacrylamide polymer flocculant is used as the flocculant liquid K as described above, the sludge water M in the sludge tank C has a concentration of 2.1%.
It is preferable to set it as 4 volume %. Furthermore, sludge tank C
The amount of sludge water M in the sludge tank C is measured by the liquid volume scale provided in the sludge tank C as described above.

次いで、このように汚泥水槽C内に凝集剤液K
を吸引収容したら、撹拌機構C′を用いて凝集剤
液K及び汚泥水Mを撹拌混合して汚泥水M中の固
形分をフロツク状に凝集させ、この一次処理汚泥
水Nを第7図に示す如く汚泥水槽C内に形成す
る。このような撹拌混合は、二方及び四方切換コ
ツクを前述した第6図に示す状態におくことによ
り行うこともでき、この場合は空になつた浄化槽
Lから吸排水ホース27、パイプ25,21を介
して汚泥水槽C内に吸引された空気によつて、汚
泥水槽C内の凝集剤液K及び汚泥水Mが撹拌混合
される。尚、撹拌機構C′による撹拌混合と空気
による撹拌混合は併用しても、或は何れか一方を
用いても良い。
Next, the flocculant liquid K is poured into the sludge tank C in this way.
After suction and storage, the flocculant liquid K and the sludge water M are stirred and mixed using the stirring mechanism C' to flocculate the solid content in the sludge water M, and this primary treated sludge water N is prepared as shown in Fig. 7. It is formed in the sludge tank C as shown. Such agitation and mixing can also be performed by placing the two-way and four-way switching pots in the state shown in FIG. The flocculant liquid K and the sludge water M in the sludge tank C are stirred and mixed by the air sucked into the sludge tank C through the sludge tank C. Note that the stirring and mixing by the stirring mechanism C' and the stirring and mixing by air may be used together, or either one of them may be used.

汚泥水槽C内の上記一次処理汚泥水Nは次い
で、第8図に示す如く過装置Dに移行してここ
で凝集汚泥Oと過水Pとに分離し、凝集汚泥O
は汚泥槽Eに収容する一方、過水Pは過水槽
Bに収容する。この切換操作は、汚泥水槽C内の
撹拌混合終了後第7図において四方切換コツクI
を切換えてパイプ12,3を介し汚泥水槽Cを大
気圧化とした後、第8図に示す如く四方切換弁I
を再び切換えると共に、二方切換コツク13,7
を閉成する一方二方切換コツク6,4,23,2
9,30を開放し、且つ回転式スクリーン筒33
を駆動することにより行ない得る。即ち、このよ
うにすれば、汚泥水槽Cを加圧状態とすることが
できるから、汚泥水槽C内の一次処理汚泥水Nを
パイプ21,26を介して過装置Dにおける回
転式スクリーン筒33に圧送することができる。
横型の回転式スクリーン筒33の一端から圧送さ
れた一次処理汚泥水Nは回転式スクリーン筒33
の回転に伴いスクリーン面によつて過水Pと凝
集汚泥Oとに分離され、分離された凝集汚泥Oは
スクリーンの内側面に設けた前記螺旋プレードに
よつて押出されつつ含有水分を更に分離され、他
端33′より落下して汚泥槽E内に汚泥取入部3
5から収容される一方、過水Pはそのスクリー
ン面より過水受タンク32内に流下する。そし
て過水受タンク内に流下した過水Pは、過
水槽Bが減圧下におかれているから、透明なパイ
プ31を介して過水槽B内に吸引され且つ収容
される。尚、この場合の凝集剤の使用量は極めて
微量であり、凝集剤は、分離された凝集汚泥O中
に取り込まれるため、実質的に過水P中に残存
せず、過水P中の種汚泥を死滅させる惧れがな
いため、これを張水として使用した場合、浄化槽
Lは正常に機能する。また、横型の回転式スクリ
ーン筒33は前述の如く回転速度調節可能となし
てあるから、その回転速度を遅くすることによ
り、或は回転式スクリーン筒33を第8図に示す
如く仰状態とすることにより、凝集汚泥Oの搬送
速度を遅らせて分離効果を高めることができ、特
に回転式スクリーン筒33を実施例の如く俯仰自
在となすことにより、坂道(下り坂)に浄化槽等
の汚泥水処理車を停止させて作業を行なう場合、
横型の回転式スクリーン筒33を俯仰自在とせず
固定したものと比較し、より一層分離効果を高め
ることができる。また、上記過装置Dにおいて
は外筐34を透明となしてあるから回転式スクリ
ーン筒33の目詰り状態等を観察でき、又外筐3
4により回転止スクリーン筒33を囲んであるか
ら過水の飛散を防止でき、更にはパイプ31を
透明となしてあるからその内部を通過する過水
の性状を観察できる。
The primary treated sludge water N in the sludge tank C is then transferred to the filtration device D as shown in FIG. 8, where it is separated into flocculated sludge O and perwater P.
is stored in the sludge tank E, while the overwater P is stored in the overwater tank B. This switching operation is performed after the stirring and mixing in the sludge tank C is completed.
After switching the sludge tank C to atmospheric pressure via the pipes 12 and 3, the four-way switching valve I is turned on as shown in FIG.
At the same time, two-way switching tips 13, 7 are switched again.
6, 4, 23, 2
9, 30 are opened, and the rotary screen cylinder 33 is opened.
This can be done by driving the . That is, by doing this, the sludge tank C can be pressurized, and the primary treated sludge water N in the sludge tank C can be passed through the pipes 21 and 26 to the rotary screen tube 33 in the filtration device D. Can be pumped.
The primary treated sludge water N, which is pressure-fed from one end of the horizontal rotary screen tube 33, is transferred to the rotary screen tube 33.
As the screen rotates, the screen surface separates the superhydrate P and flocculated sludge O, and the separated flocculated sludge O is pushed out by the spiral blades provided on the inner surface of the screen, while the water content is further separated. , the sludge intake part 3 falls from the other end 33' and enters the sludge tank E.
5, while the excess water P flows down into the excess water receiving tank 32 from the screen surface. Since the overwater tank B is placed under reduced pressure, the overwater P that has flowed down into the overwater receiving tank is sucked into the overwater tank B through the transparent pipe 31 and stored therein. In this case, the amount of flocculant used is extremely small, and since the flocculant is taken into the separated flocculated sludge O, it does not substantially remain in the superhydrate P, and the seeds in the superwater P Since there is no risk of killing the sludge, the septic tank L will function normally if this is used as water filling. Further, since the rotational speed of the horizontal rotary screen tube 33 is adjustable as described above, by slowing down the rotational speed, the rotary screen tube 33 can be placed in an upright position as shown in FIG. By this, the conveyance speed of the flocculated sludge O can be slowed down and the separation effect can be enhanced. In particular, by making the rotary screen cylinder 33 freely tiltable as in the embodiment, sludge water treatment such as a septic tank can be carried out on a slope (downhill). When performing work with the vehicle stopped,
The separation effect can be further enhanced compared to a horizontal rotary screen cylinder 33 that is fixed and not tiltable. In addition, in the above-mentioned filter device D, the outer casing 34 is made transparent, so that it is possible to observe the clogging state of the rotary screen tube 33, and the outer casing 34 is transparent.
4 surrounds the anti-rotation screen cylinder 33, which prevents excess water from scattering.Furthermore, since the pipe 31 is transparent, the properties of the excess water passing through it can be observed.

上述の如くして過水槽B内に過水Pを収容
したら、第8図の状態において二方切換コツク2
3,29,30を閉成し、四方切換コツクIを切
換え、且つ二方切換コツク13を開放して汚泥水
槽C及び過水槽Bを大気圧下とした後、第9図
に示す如く、過水槽B内の過水Pを浄化槽L
に圧送する。即ち、第9図に示す如く四方切換コ
ツクIを切換え、且つ二方切換えコツク13,
6,22,28のみを開放状態におけば、真空ポ
ンプHの作動によりパイプ12,8,9,3を介
して空気が過水槽B内に圧送され、この圧送に
よる過水槽Bの加圧状態に伴つて、過水槽B
内の過水Pは、パイプ20,25及び吸排水ホ
ース27を介して浄化槽L内に張水として圧送さ
れる。
After storing the excess water P in the excess water tank B as described above, the two-way switching tank 2 is opened in the state shown in FIG.
3, 29, and 30, switch the four-way switching pot I, and open the two-way switching pot 13 to bring the sludge water tank C and the excess water tank B to atmospheric pressure, as shown in FIG. Excess water P in water tank B is removed from septic tank L.
to be pumped to. That is, as shown in FIG. 9, the four-way switching socket I is switched, and the two-way switching socket 13,
If only 6, 22, and 28 are left open, air is forced into the overwater tank B through the pipes 12, 8, 9, and 3 by the operation of the vacuum pump H, and the pressurized state of the overwater tank B is caused by this pressure feeding. Accordingly, overwater tank B
The excess water P inside is pumped into the septic tank L through the pipes 20, 25 and the suction/drainage hose 27 as filled water.

以上の操作が終了したら、四方及び二方切換コ
ツクその他を第4図に示す状態に戻し、次の浄化
槽まで走行し、再び上述の如き操作を多数槽につ
いて繰り返し、汚泥槽E中に凝集汚泥Oが満され
た時点で、汚泥水処理場に凝集汚泥Oを運べば良
い。このようにすれば汚泥水処理場では凝集汚泥
のみを処理すれば良いから、生し尿用に造られた
汚泥水処理場に、汚泥濃度の少ない浄化槽の汚泥
水を投入することが防止され、且つその能力がオ
ーバーフロー気味だつたのが解消される。尚、第
9図に示す如く二方切換コツク38を開放するこ
とにより、洗滌ノズル34′から高圧の清水Qを
噴出させて回転式スクリーン筒33を洗滌するこ
とができ、又二方切換コツク41を開放すること
により、洗滌ホース40の先端から高圧の清水を
噴出させて各所を洗滌することができる。
When the above operation is completed, return the four-way and two-way switching pots and others to the state shown in Figure 4, drive to the next septic tank, repeat the above operation for multiple tanks, and put the flocculated sludge into the sludge tank E. When this is satisfied, the flocculated sludge O can be transported to the sludge treatment plant. In this way, only flocculated sludge needs to be treated at the sludge water treatment plant, which prevents sludge water from a septic tank with a low sludge concentration from being input into a sludge water treatment plant built for raw human waste. The fact that the ability was overflowing has been resolved. Incidentally, by opening the two-way switching pot 38 as shown in FIG. By opening the cleaning hose 40, high-pressure clean water can be jetted out from the tip of the cleaning hose 40 to clean various areas.

叙上の如く、本発明の浄化槽等の汚泥水処理車
は、処理タンク本体に凝集剤液槽、過水槽、及
び汚泥水槽の三槽を具備させた操作容易且つ小型
化可能なもので、且つ真空ポンプ及び四方切換コ
ツクを用いて構成した減圧・加圧装置により上記
三槽の減圧・加圧状態を造り出すこと等によつて
効果的な汚泥水処理を行ない得るものであつて、
処理すべき汚泥水にその濃度に応じて凝集剤液を
撹拌混合してフロツクを形成することにより汚泥
水の処理能率を高めることができ、又従来のよう
に汚泥水汲取車による浄化槽その他の槽と汚泥水
処理場との頻雑な往復作業に頼ることなく、浄化
槽その他の槽所在の場所において、浄化槽その他
の槽の汚泥水の処理を行なうと同時に、過装置
で俯仰自在な回転スクリーン筒により簡便に且つ
効率良く分離し過水槽に吸引収容した過水を
張水として浄化槽に還流させ浄化槽を正常に機能
させることができる等、浄化槽等の管理及び汚泥
水処理作業を容易且つ迅速に行なうことができる
他、汚泥水処理場の能力がオーバーフロー気味な
のを防止することができ、又濃い汚泥水処理用と
して造られている汚泥水処理場に、うすい浄化槽
の汚泥水がそのまま混入されるのを防止すること
ができる等の極めて多大な効果を有するものであ
る。
As mentioned above, the sludge water treatment vehicle such as a septic tank of the present invention is easy to operate and can be made compact, as the treatment tank body is equipped with three tanks: a flocculant liquid tank, an overwater tank, and a sludge water tank. Effective sludge water treatment can be carried out by creating a depressurized and pressurized state in the three tanks using a depressurizing and pressurizing device configured using a vacuum pump and a four-way switching cock,
Sludge water treatment efficiency can be increased by stirring and mixing flocculant liquid according to the concentration of the sludge water to be treated to form a floc. Sludge water from septic tanks and other tanks can be treated at the location where the septic tank and other tanks are located, without relying on frequent back and forth work between the septic tank and the sludge water treatment plant. To easily and quickly manage septic tanks, etc. and treat sludge water by easily and efficiently separating superfluous water and suctioning it into a superfluous tank and returning it to the septic tank as water, allowing the septic tank to function normally. In addition, it is possible to prevent the capacity of the sludge water treatment plant from overflowing, and it is also possible to prevent sludge water from a thin septic tank from being mixed directly into the sludge water treatment plant, which is built to treat thick sludge water. It has extremely great effects such as being able to prevent

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

第1図、第2図、及び第3図はそれぞれ本発明
の一実施例の平面図、側面図、及び背面図であ
り、第4図、第5図、第6図、第7図、第8図、
及び第9図はそれぞれ本発明の一実施例の循環系
統の概略を示す、走行状態、凝集剤液槽への凝集
剤液吸引状態、汚泥水吸引状態、汚泥水槽への凝
集剤液吸引状態、過分離状態、及び過水注入
状態でのフローシートである。 1…汚泥水処理タンク、1′…区画壁、A…凝
集剤液槽、B…過水槽、C…汚泥水槽、C′…
撹拌機構、D…過装置、E…汚泥槽、H…真空
ポンプ、I…四方切換コツク。
1, 2, and 3 are a plan view, a side view, and a back view, respectively, of an embodiment of the present invention, and FIGS. 4, 5, 6, 7, and Figure 8,
and FIG. 9 schematically show a circulation system according to an embodiment of the present invention, respectively: running state, coagulant liquid suction state to the flocculant liquid tank, sludge water suction state, flocculant liquid suction state to the sludge water tank, This is a flow sheet in an over-separated state and an over-water injection state. 1... Sludge water treatment tank, 1'... Compartment wall, A... Coagulant liquid tank, B... Overwater tank, C... Sludge water tank, C'...
Stirring mechanism, D...filtration device, E...sludge tank, H...vacuum pump, I...four-way switching pot.

Claims (1)

【特許請求の範囲】 1 1つのタンク内を2つの区画壁により区画し
て凝集剤液槽、過水槽、及び撹拌機構を備え且
つ上記凝集剤液槽と連通し得る汚泥水槽を設けた
汚泥水処理タンクと、 上記過水槽と上記汚泥水槽との間にそれぞれ
に連通可能に配され、上記汚泥水槽内で凝集剤液
と撹拌混合され固形分がブロツク状に凝集された
汚泥水を、過水と凝集汚泥とに分離する過装
置と、 真空ポンプ及び四方切換コツクを用いて構成し
た一つの加圧・減圧装置と、 切換コツクを介して上記汚泥水槽又は上記過
水槽に連通し得る吸排水ホースと を装備してなり、 上記加圧・減圧装置は、上記凝集剤液槽、上記
過水槽、及び上記汚泥水槽それぞれに連通して
該三槽それぞれの内部を減圧・加圧可能になして
あり、 上記凝集剤液槽と上記汚泥水槽との間には、上
記汚泥水槽内への凝集剤液の移行量を計測する流
量計を設けてあり、 上記過装置は、俯仰自在な横型の回転式スク
リーン筒と、その下方に配備し上記汚泥水槽に連
通し得る過水受タンクと、上記スクリーン筒で
分離された凝集汚泥を収容する汚泥槽とからなつ
ている ことを特徴とする浄化水槽等の汚泥水処理車。
[Scope of Claims] 1. Sludge water in which one tank is divided by two partition walls, and a sludge tank is provided with a coagulant liquid tank, an overwater tank, and a sludge tank that is equipped with a stirring mechanism and can communicate with the coagulant liquid tank. A treatment tank is arranged so as to be able to communicate with each other between the above-mentioned superwater tank and the above-mentioned sludge water tank, and the sludge water in which the solid content has been agitated and mixed with the flocculant liquid in the sludge tank to coagulate into blocks is a filtration device that separates the sludge and flocculated sludge; a pressurization/depressurization device configured using a vacuum pump and a four-way switching tank; and a suction/drainage hose that can communicate with the sludge tank or the overwater tank via the switching tank. The pressurization/depressurization device is connected to each of the flocculant liquid tank, overwater tank, and sludge tank, and is capable of depressurizing and pressurizing the inside of each of the three tanks. A flow meter is provided between the flocculant liquid tank and the sludge tank to measure the amount of flocculant liquid transferred into the sludge tank. A septic water tank, etc., comprising a screen tube, an overwater receiving tank disposed below the screen tube and communicating with the sludge tank, and a sludge tank that accommodates the flocculated sludge separated by the screen tube. Sludge water treatment vehicle.
JP57030942A 1982-02-27 1982-02-27 Vehicle for treating sludgy water in purifying tank or the like Granted JPS58150490A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57030942A JPS58150490A (en) 1982-02-27 1982-02-27 Vehicle for treating sludgy water in purifying tank or the like

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57030942A JPS58150490A (en) 1982-02-27 1982-02-27 Vehicle for treating sludgy water in purifying tank or the like

Publications (2)

Publication Number Publication Date
JPS58150490A JPS58150490A (en) 1983-09-07
JPS6130837B2 true JPS6130837B2 (en) 1986-07-16

Family

ID=12317728

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57030942A Granted JPS58150490A (en) 1982-02-27 1982-02-27 Vehicle for treating sludgy water in purifying tank or the like

Country Status (1)

Country Link
JP (1) JPS58150490A (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60257899A (en) * 1984-06-05 1985-12-19 Arai Seisakusho:Kk Apparatus for removing precipitate in treatment tank such as purification tank
KR20010108858A (en) * 2000-05-31 2001-12-08 정홍섭 Mobile waste water treatment system and method therefor
KR20030076009A (en) * 2002-03-22 2003-09-26 이성헌 A garbage truck having a waste water disposal plant
JP4749365B2 (en) * 2007-03-19 2011-08-17 新明和工業株式会社 Sludge concentrator and sludge concentrator
JP4999710B2 (en) * 2007-08-20 2012-08-15 新明和工業株式会社 Sludge concentrator and sludge concentrator

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5460758A (en) * 1977-09-30 1979-05-16 Stigebrandt Ake Method of and device for treating sludge water

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5460758A (en) * 1977-09-30 1979-05-16 Stigebrandt Ake Method of and device for treating sludge water

Also Published As

Publication number Publication date
JPS58150490A (en) 1983-09-07

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