Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPS625028B2 - - Google Patents
[go: Go Back, main page]

JPS625028B2 - - Google Patents

Info

Publication number
JPS625028B2
JPS625028B2 JP57116370A JP11637082A JPS625028B2 JP S625028 B2 JPS625028 B2 JP S625028B2 JP 57116370 A JP57116370 A JP 57116370A JP 11637082 A JP11637082 A JP 11637082A JP S625028 B2 JPS625028 B2 JP S625028B2
Authority
JP
Japan
Prior art keywords
tank
sludge water
water treatment
overwater
sludge
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
JP57116370A
Other languages
Japanese (ja)
Other versions
JPS596998A (en
Inventor
Akira Izawa
Tetsuo Kato
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 JP57116370A priority Critical patent/JPS596998A/en
Publication of JPS596998A publication Critical patent/JPS596998A/en
Publication of JPS625028B2 publication Critical patent/JPS625028B2/ja
Granted legal-status Critical Current

Links

Landscapes

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

Description

【発明の詳細な説明】 本発明は、汚泥水処理及び張水返送車による浄
化槽等の汚泥水処理方法に関するもので、一台の
車両により、浄化槽等の汚泥水の抜き取りと張水
とを可能ならしめた新規な汚泥水処理方法に関す
るものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for treating sludge water in a septic tank, etc. using a sludge water treatment and water-filling return vehicle, and it is possible to remove sludge water from a septic tank, etc. and fill it with water using a single vehicle. This paper relates to a new sludge water treatment method.

従来、浄化槽等の管理を目的として浄化槽等の
汚泥水を処理する場合、浄化槽等の汚泥水をバキ
ユームカー等で引抜いた後、家庭用の水道水で張
水を行なうか、或は他のタンク車で張水を運搬し
て来て張水を行なつていたため、張水作業に労力
を要する等の不都合があつた。
Conventionally, when treating sludge water from a septic tank, etc. for the purpose of managing the septic tank, etc., the sludge water from the septic tank, etc. is drawn out with a vacuum car, etc., and then the water is filled with household tap water, or another tank car is used. Because the water was brought in and filled with water, there were inconveniences such as the labor required to fill the water.

本発明は、叙上の点に鑑みなされたものであ
り、一台の車両によつて、汚泥水の抜き取りと張
水とを可能とし、もつて浄化槽等の管理を容易と
することができる新規な汚泥水処理方法を提供す
るものである。
The present invention has been made in view of the above-mentioned points, and is a novel product that enables the removal and filling of sludge water with a single vehicle, thereby facilitating the management of septic tanks, etc. This provides a method for treating sludge water.

即ち、本発明は、車輌に、吸排水ホース、汚泥
水と凝集剤とを撹拌混合する撹拌機構内部に備え
た汚泥水処理タンク、過水タンク、固液分離を
行なう回転式スクリーン筒とその下方に配設した
過水受タンクとを備えた過装置、及び真空ポ
ンプ及び四方切換弁を用いて構成され上記汚泥水
処理タンクと過水タンクとの内圧をそれぞれ別
個に加圧、減圧し得る加圧、減圧装置を装備さ
せ、上記吸排水ホースをそれぞれ汚泥水処理タン
クと過水タンクとに連通させ、且つ過装置を
汚泥水処理タンクと過水タンクとのの間に接続
させてなる汚泥水処理及び張水返送車を用いる浄
化槽等の汚泥水処理方法であつて、過水タンク
に予め過水を収容しておき、加圧、減圧装置に
より汚泥水処理タンクを減圧して吸排水ホースを
介し浄化槽等の汚泥水を汚泥水処理タンク内に吸
引収容した後、上記加圧、減圧装置により過水
タンクを加圧して過水タンク内の過水を、汚
泥水処理タンクに吸引収容した汚泥水の量に等し
い量を上記吸排水ホースを介して浄化槽等に排出
する一方、上記汚泥水処理タンク内の汚泥水を凝
集剤と共に撹拌機構により撹拌混合して汚泥水処
理タンク内にフロツク(水中汚泥のコロイドが持
つ電荷(−)と凝集剤分子の有する電荷(+)が
中和し、汚泥コロイドが引き合わされ(架橋現
象)て、海綿状群となつたもの)を形成し、斯く
して得られたフロツクを含む汚泥水処理タンク内
の一次処理水を、上記汚泥水処理タンクを加圧、
減圧装置により加圧して上記過装置に圧送して
過装置により固液分離し、上記過水受タンク
内に分離された過水を、上記加圧減圧装置によ
り過水タンクを減圧して過水タンク内に吸引
収容し、必要に応じ該過水を過水受タンクか
ら浄化槽等に排出することを特徴とする汚泥水処
理及び張水返送車による浄化槽等の汚泥水処理方
法を提供するものである。
That is, the present invention provides a vehicle with a suction/drainage hose, a sludge water treatment tank and a water permeation tank provided inside a stirring mechanism that stirs and mixes sludge water and a coagulant, a rotary screen tube that performs solid-liquid separation, and a rotary screen cylinder below the same. A pressurizing system is constructed using a filtration device equipped with an overwater receiving tank located in the sludge water treatment tank and an overwater tank, and a vacuum pump and a four-way switching valve, and is capable of pressurizing and reducing the internal pressure of the sludge water treatment tank and overwater tank separately. The sludge water is equipped with a pressure and decompression device, the suction and drainage hoses are connected to the sludge water treatment tank and the overwater tank, and a filtration device is connected between the sludge water treatment tank and the overwater tank. A sludge water treatment method using a septic tank, etc. that uses a treatment and water-filling return vehicle, in which overwater is stored in an overwater tank in advance, the sludge water treatment tank is depressurized using a pressurization/reduction device, and the suction/drainage hose is connected. After suctioning and storing sludge water from a septic tank, etc. into a sludge water treatment tank, the overwater tank is pressurized by the above-mentioned pressurization and decompression device, and the overwater in the overwater tank is sucked and stored into the sludge water treatment tank. An amount equal to the amount of water is discharged to a septic tank etc. through the suction and drainage hose, while the sludge water in the sludge water treatment tank is stirred and mixed with a flocculant by a stirring mechanism to form flocs (underwater) in the sludge water treatment tank. The charge (-) of the sludge colloid and the charge (+) of the flocculant molecules are neutralized, and the sludge colloids are drawn together (cross-linking phenomenon) to form a spongy group. The primary treated water in the sludge water treatment tank containing the obtained flocs is pressurized into the sludge water treatment tank.
Pressure is increased by the pressure reduction device, the pressure is sent to the above-mentioned filtration device, solid-liquid separation is carried out by the filtration device, and the separated superwater is placed in the above-mentioned superhydration receiving tank. The present invention provides a method for treating sludge water in a septic tank, etc. using a water filling and return vehicle, which is characterized by suctioning and storing superfluous water in a tank, and discharging the excess water from an overwater receiving tank to a septic tank, etc., as necessary. be.

以下、本発明方法の実施態様を図面に沿つて説
明する。
Embodiments of the method of the present invention will be described below with reference to the drawings.

まず、本発明方法に用いる汚泥水処理及び張水
返送車について説明すると、図面はかかる車両の
配管系統図を示すものであつて、図面において、
1は開閉コツク10,11を有する吸排水ホー
ス、2は汚泥水と凝集剤とを撹拌混合する撹拌機
構2′を内部に備えた汚泥水処理タンク、3は
過水タンク、4は過装置、5は上記汚泥水処理
タンク2と過水タンク3との内圧をそれぞれ別
個に加圧、減圧し得る加圧、減圧装置、6は凝集
剤液タンクでこれらは車両(図示せず)に装備さ
せてある。
First, to explain the sludge water treatment and water charging return vehicle used in the method of the present invention, the drawing shows a piping system diagram of such a vehicle, and in the drawing,
1 is a suction/drainage hose having opening/closing handles 10 and 11; 2 is a sludge water treatment tank equipped with a stirring mechanism 2' for stirring and mixing sludge water and flocculant; 3 is a water tank; 4 is a filter device; Reference numeral 5 denotes a pressurization and depressurization device capable of pressurizing and depressurizing the internal pressures of the sludge water treatment tank 2 and overwater tank 3, respectively, and 6 denotes a flocculant liquid tank, which is installed in a vehicle (not shown). There is.

而して、上記吸排水ホース1は、ホースリール
12に巻かれており、それぞれ開閉コツク13を
有するパイプ30、及び開閉コツク14を有する
パイプ31を介して汚泥水処理タンク2及び過
水タンク3の底部に連通させてある。尚、この場
合、上記パイプ30,31は直接吸排水ホース1
に接続してはなく、パイプ30はパイプ32を介
して、又パイプ31はパイプ32及びパイプ33
を介して吸排水ホース1に接続してある。
The suction and drainage hose 1 is wound around a hose reel 12, and is connected to the sludge water treatment tank 2 and the overwater tank 3 via a pipe 30 having an opening/closing socket 13 and a pipe 31 having an opening/closing socket 14, respectively. It is connected to the bottom of the. In this case, the pipes 30 and 31 are directly connected to the suction and drainage hose 1.
pipe 30 is connected to pipe 32, and pipe 31 is connected to pipe 32 and pipe 33.
It is connected to the suction and drainage hose 1 via.

又、上記汚泥水処理タンク2及び過水タンク
3には、それぞれ内部の汚泥水及び過水の性状
等を確認するための窓2″,3″を設けてある。
The sludge water treatment tank 2 and overwater tank 3 are provided with windows 2'' and 3'' for checking the properties of the sludge and overwater, respectively.

又、上記装置4は、固液分離のための横型の
回転式スクリーン筒4′と、その下方に配設した
過水受タンク4″とで構成してある。回転式ス
クリーン筒4′は、その一端部から排出される汚
泥水(汚泥水処理タンク2において後述のように
浄化槽等の汚泥水を凝集剤と凝集反応させて得ら
れるフロツクを含む一次処理水)をそのスクリー
ン面で固液分離するもので、分離される汚泥を、
その内側面に設けた螺旋ブレード(図示せず)に
より他端部から汚泥槽(図示せず)に排水する一
方、分離される過水を過水受タンク4″内に
流下又は滴下するようになしてある。尚、回転式
スクリーン筒4′は、傾斜地における過作業を
円滑に行なう等の観点からその他端部において俯
仰自在な構成となしてある。而してこのように構
成された過装置4は、開閉コツク15を有する
パイプ34、及び開閉コツク16を有するパイプ
35を介して汚泥水処理タンク2と過水タンク
3との間に接続してある。更に詳述すると、過
装置4は、その回転式スクリーン筒4′の一端部
を、パイプ34,33,30を介して汚泥水処理
タンク2の底部に接続してあり、又過水タンク
4″をパイプ36,35を介して過水タンク3
の上部に接続してある。又開閉コツク15を有す
るパイプ34には少なくともその一部に透明部3
4′を設けてある。
The device 4 is composed of a horizontal rotary screen cylinder 4' for solid-liquid separation, and a water receiving tank 4'' disposed below the horizontal screen cylinder 4'.The rotary screen cylinder 4' includes: The sludge water discharged from one end (primary treated water containing flocs obtained by flocculating reaction of sludge water from a septic tank etc. with a flocculant in the sludge water treatment tank 2 as described later) is separated into solid and liquid on its screen surface. The sludge that is separated is
A spiral blade (not shown) provided on the inner surface drains water from the other end to a sludge tank (not shown), while allowing the separated excess water to flow or drip into the excess water receiving tank 4''. The rotary screen tube 4' is constructed so that it can be tilted up and down at the other end in order to smoothly carry out overwork on slopes. 4 is connected between the sludge water treatment tank 2 and the filtration tank 3 via a pipe 34 having an opening/closing socket 15 and a pipe 35 having an opening/closing socket 16. , one end of the rotary screen cylinder 4' is connected to the bottom of the sludge water treatment tank 2 via pipes 34, 33, 30, and the filtration tank 4'' is connected to the bottom of the sludge water treatment tank 2 via pipes 36, 35. water tank 3
It is connected to the top of the. In addition, the pipe 34 having the opening/closing knob 15 has a transparent part 3 at least in a part thereof.
4' is provided.

又、上記加圧、減圧装置5は、真空ポンプ5
0、四方切換弁51、圧力調整バルブ52等を主
体として構成してある。即ち、四方切換弁に4本
のパイプ53,54,55、及び56の一端部を
接続し、パイプ53及び54の他端部間に真空ポ
ンプ50を接続し、パイプ56をその先端部を分
岐させてそれぞれ開閉コツク57を有するパイプ
58、及び開閉コツク59を有するパイプ60を
介して過水タンク3及び汚泥水処理タンク2の
上部に接続し、パイプ55をその先端に三方切換
コツクよりなる圧力調整バルブ52を接続し、且
つ圧力調整バルブ52に、大気中に開放するパイ
プ61及び汚泥水処理タンク2に連通するパイプ
62を接続して構成してある。而して、上記の如
き構成によれば、真空ポンプ50の作動下におい
て四方切換弁51を切換えることにより、パイプ
55及び56を、その一方を加圧状態としたとき
他方を減圧状態とすることができる。従つて、こ
の状態下において、まず、開閉コツク57,59
を操作すれば、汚泥水処理タンク2及び過水処
理タンク3の何れか一方又は双方の内圧を加圧又
は減圧することができる。又、パイプ55及び6
2が連通するように圧力調整バルブ52を調整
し、且つ開閉コツク59を閉鎖する一方、開閉コ
ツク57を開放して、四方切換弁51を切換えれ
ば、汚泥水処理タンク2及び過水タンク3の一
方を減圧状態とし、他方を加圧状態とすることが
できる。即ち、上記加圧、減圧装置5によれば、
汚泥水処理タンク2と過水タンク3との内圧を
一台の真空ポンプ50を用いてそれぞれ別個又は
同時に加圧、減圧することができる。尚、上記の
説明では、加圧、減圧装置5の機能を理解し易す
くするため、四方切換コツク51、開閉コツク5
7等の操作順序は実際の操作順序と異ならせてあ
る。また、上記加圧、減圧装置5によれば、圧力
調整バルブ52を調整してバルブ61及びパイプ
62それぞれへのパイプ55の連通度合を調整す
ることにより、汚泥水処理タンク2の加圧圧力及
び加圧圧力を調整することができる。特に加圧圧
力を調整できることは重要であり、これによつて
後述のようにフロツクを破損することなく汚泥水
処理タンク2から過装置4に圧送することが可
能となる。尚、圧力調整バルブ52は2つの二方
切換コツク(開閉コツク)を用いて構成すること
もできる。又、63はオイルセパレーター、64
は空気安全弁、65はエアークリーナーである。
Further, the pressurization and depressurization device 5 includes a vacuum pump 5
0, a four-way switching valve 51, a pressure regulating valve 52, and the like. That is, one end of four pipes 53, 54, 55, and 56 are connected to a four-way switching valve, a vacuum pump 50 is connected between the other ends of pipes 53 and 54, and the tip of pipe 56 is branched. It is connected to the upper part of the overwater tank 3 and the sludge water treatment tank 2 through a pipe 58 having an opening/closing socket 57 and a pipe 60 having an opening/closing socket 59, respectively, and a pipe 55 is connected to the top of the pipe 55 with a three-way switching socket. A regulating valve 52 is connected to the pressure regulating valve 52, and a pipe 61 that opens to the atmosphere and a pipe 62 that communicates with the sludge water treatment tank 2 are connected to the pressure regulating valve 52. According to the above configuration, by switching the four-way switching valve 51 while the vacuum pump 50 is operating, when one of the pipes 55 and 56 is in a pressurized state, the other is in a depressurized state. I can do it. Therefore, under this condition, first, the opening/closing tips 57, 59
By operating this, the internal pressure of either or both of the sludge water treatment tank 2 and the water treatment tank 3 can be increased or decreased. Also, pipes 55 and 6
If the pressure adjustment valve 52 is adjusted so that the sludge water treatment tank 2 and the overwater tank 3 are connected, and the opening/closing knob 59 is closed, the opening/closing knob 57 is opened and the four-way switching valve 51 is switched. One of them can be in a reduced pressure state and the other can be in a pressurized state. That is, according to the pressurization and decompression device 5,
The internal pressures of the sludge water treatment tank 2 and the overwater tank 3 can be pressurized and depressurized separately or simultaneously using one vacuum pump 50. In the above explanation, in order to make it easier to understand the functions of the pressurization and depressurization device 5, the four-way switching pot 51 and the opening/closing pot 5 are used.
The order of operations such as No. 7 is different from the actual order of operations. Further, according to the pressurization and depressurization device 5, by adjusting the pressure adjustment valve 52 and adjusting the degree of communication of the pipe 55 to the valve 61 and the pipe 62, the pressurization pressure and Pressure pressure can be adjusted. In particular, it is important to be able to adjust the pressurizing pressure, which makes it possible to forcefully feed the flocs from the sludge water treatment tank 2 to the filtration device 4 without damaging the flocs, as will be described later. Note that the pressure regulating valve 52 can also be configured using two two-way switching sockets (opening/closing sockets). Also, 63 is an oil separator, 64
is an air safety valve, and 65 is an air cleaner.

又、上記凝集剤液タンク6は、流量計17及び
開閉コツク18を有するパイプ37を介して汚泥
水処理タンク2の上部に連通させてあり、この場
合、車両外の凝集剤液タンク19から車両外のポ
ンプ20を用いて移送した凝集剤液を、上記流量
計17で測定しつつ汚泥水処理タンク2内に所定
量供給できるようになしてある。
The flocculant liquid tank 6 is connected to the upper part of the sludge water treatment tank 2 via a pipe 37 having a flow meter 17 and an opening/closing cock 18. In this case, the flocculant liquid tank 19 outside the vehicle is connected to the top of the sludge water treatment tank 2. A predetermined amount of the flocculant liquid transferred using the external pump 20 can be supplied into the sludge water treatment tank 2 while being measured by the flow meter 17.

又、7は、前記吸排水ホース1と過装置4の
間に設けたポンプで、過装置4で分離された
過水を吸排水ホース1を介して直接排出できるよ
うになしてある。更に詳述すると、上記ポンプ7
は、開閉コツク21と共にパイプ38に設けてあ
り、該パイプ38の一端を吸排水ホース1に、又
他端をパイプ36を介して過装置4における
過水受タンク4″にそれぞれ接続してある。又3
9はポンプ7によらず、重力により過水を排出
する重力排出口であり、ポンプ7と過装置4と
の間に、この場合パイプ36を分岐させ且つ開閉
コツク22を具備させて設けてある。
Further, reference numeral 7 denotes a pump provided between the suction and drainage hose 1 and the filter device 4, so that the excess water separated by the filter device 4 can be directly discharged through the suction and drainage hose 1. To explain in more detail, the pump 7
is provided on a pipe 38 together with the opening/closing pot 21, and one end of the pipe 38 is connected to the suction and drainage hose 1, and the other end is connected to the overwater receiving tank 4'' in the overflow device 4 through the pipe 36. .Mata 3
Reference numeral 9 denotes a gravity discharge port for discharging excess water by gravity, not by the pump 7, and is provided between the pump 7 and the filter device 4, in this case with a branched pipe 36 and an opening/closing pot 22. .

この他、図面中23はドレン排出用開閉コツク
である。
In addition, 23 in the drawing is an opening/closing pot for drain discharge.

而して、以上の構成からなる汚泥水処理及び張
水返送車を用いれば、以下の如く本発明の汚泥水
処理方法を実施できる。
By using the sludge water treatment and water filling return vehicle having the above configuration, the sludge water treatment method of the present invention can be carried out as follows.

即ち、まず本発明の基本的な実施態様において
は、浄化槽等の所在の場所まで上記車両を走行さ
せた後、ホースリール12より吸排水ホース1を
操り出してこれを浄化槽等の汚泥水中に挿入し、
加圧、減圧装置5により汚泥水処理タンク2を減
圧状態とし、開閉コツク10,11、及び13を
開放して吸排水ホース1、パイプ32,30を介
して浄化槽等の汚泥水を汚泥水処理タンク2内に
吸引収容する。そして、これと前後し開閉コツク
18を開放して凝集剤液タンク6から、液量計1
7で測定しつつ所定量の凝集剤液をパイプ37を
介して汚泥水処理タンク2内に吸引収容する。こ
のようにして汚泥水処理タンク2内に所定量の汚
泥水及び凝集剤液を吸引収容したら、撹拌機構
2′を作動させ、汚泥水を汚泥水処理タンク2内
で凝集反応させ、フロツクを形成する。
That is, in the basic embodiment of the present invention, first, after driving the vehicle to a location where a septic tank or the like is located, the suction and drainage hose 1 is pulled out from the hose reel 12 and inserted into the sludge water of the septic tank or the like. death,
The sludge water treatment tank 2 is depressurized by the pressurization and depressurization device 5, and the opening/closing pots 10, 11, and 13 are opened to treat sludge water from a septic tank, etc., via the suction/drainage hose 1 and pipes 32, 30. It is sucked and accommodated in the tank 2. Then, around this time, the opening/closing pot 18 is opened and the flocculant liquid tank 6 is drained from the liquid level meter 1.
A predetermined amount of flocculant liquid is sucked into the sludge water treatment tank 2 through the pipe 37 while being measured at step 7. After a predetermined amount of sludge water and coagulant liquid are sucked and stored in the sludge water treatment tank 2 in this way, the stirring mechanism 2' is operated to cause the sludge water to undergo a flocculation reaction in the sludge water treatment tank 2 to form flocs. do.

フロツクが形成されたら、加圧、減圧装置5に
より汚泥水処理タンク2を加圧状態とする一方、
過水タンク3を減圧状態とし、且つ過装置4
を作動させると共に開閉コツク13,15及び1
6を開放する。このようにすれば、フロツクを含
む汚泥水処理タンク2内の一次処理水を、パイプ
30,33、及び34を介して過装置4におけ
る回転式スクリーン筒4′に圧送することがで
き、回転式スクリーン筒4′で分離され過水受
タンク4″内に流下又は滴下する過水を、パイ
プ36及び35を介し過水タンク3内に吸引収
容させることができる。そして、上記の一次処理
水の圧送過程において、パイプ34における透明
部34′から、その内部を通過するフロツクの性
状等を観察しつつ、加圧、減圧装置5の圧力調整
バルブ52を調整すれば、汚泥水処理タンク2の
加圧圧力を前述の如く調整することができるか
ら、フロツクを損傷させることなく微少圧力で
過装置4に圧送することができる。
Once the flocs are formed, the sludge water treatment tank 2 is pressurized by the pressurization/depressurization device 5, while
The excess water tank 3 is brought into a reduced pressure state, and the excess water tank 3 is brought into a depressurized state, and the
13, 15 and 1.
Open 6. In this way, the primary treated water in the sludge water treatment tank 2 containing flocs can be sent under pressure to the rotary screen cylinder 4' in the filtration device 4 via the pipes 30, 33, and 34, and the rotary The super water separated by the screen tube 4' and flowing down or dripping into the super water receiving tank 4'' can be sucked and stored in the super water tank 3 via the pipes 36 and 35. During the pressure feeding process, if the properties of the flocs passing through the transparent part 34' of the pipe 34 are observed, and the pressure adjustment valve 52 of the pressurization/depressurization device 5 is adjusted, the pressure in the sludge water treatment tank 2 can be adjusted. Since the pressure can be adjusted as described above, the flocs can be fed to the filtration device 4 under very low pressure without damaging the flocs.

次いで、過水タンク3を加圧、減圧装置5に
より加圧状態とし、且つ開閉コツク14,11及
び10を開放する。このようにすれば、過水タ
ンク3内の過水をパイプ31,33及び32、
並びに吸排水ホース1を介して浄化槽等に排水す
ることができる。
Next, the overwater tank 3 is brought into a pressurized state by the pressurization/decompression device 5, and the opening/closing pots 14, 11, and 10 are opened. In this way, the excess water in the excess water tank 3 can be removed from the pipes 31, 33 and 32.
In addition, water can be drained to a septic tank or the like via the suction/drainage hose 1.

尚、以上の説明及び以下の説明では、開放した
開閉コツク以外の開閉コツクは全て閉鎖してあ
る。又、上記の基本的な実施態様は浄化槽等の
SV調整時に主として用いられる。
In addition, in the above explanation and the following explanation, all the opening/closing doors other than the open opening/closing door are closed. In addition, the above basic embodiment is suitable for septic tanks, etc.
Mainly used when adjusting SV.

ところで、上記の基本的な実施態様では、過
装置4との固液分離完了後、分離された過水を
浄化槽等に排出している。しかし、過装置4で
は、汚泥が分離されているから、最初に吸引した
浄化槽等の汚泥水と排出する過水との量は一致
せず、排出する過水の量が不足する。このよう
な不都合を解消するためには、過水タンク3内
に予め過水(張水)を吸引収容しておけば良
く、このようにすれば、上記の如く過水が不足
することがない。即ち、本発明においてこのよう
に予め過水を過水タンク3内に収容しておけ
ば、上記の実施態様により汚泥水を処理しても、
過水タンク3から排出される過水は不足する
ことがないし、又、汚泥水タンク2への汚泥水吸
引直後、加圧、減圧装置により過水タンク3を
加圧すれば、過水タンク3内に予め収容されて
いる過水を、パイプ31,33及び32、並び
に吸排水ホース1を介して直ちに排出できる。
By the way, in the above basic embodiment, after the solid-liquid separation with the filtration device 4 is completed, the separated filtrate is discharged to a septic tank or the like. However, in the filtration device 4, since the sludge is separated, the amount of the sludge water sucked into the septic tank or the like and the superfluous water to be discharged do not match, and the amount of superfluous water to be discharged is insufficient. In order to eliminate this inconvenience, it is sufficient to suction and store overwater (filled water) in the overwater tank 3 in advance, and in this way, there will be no shortage of overwater as described above. . That is, in the present invention, if the superhydrant is stored in the superhydric tank 3 in advance in this way, even if the sludge water is treated according to the above embodiment,
There is no shortage of superfluous water discharged from the superfluous tank 3, and if the superfluous tank 3 is pressurized by the pressurization/reducing device immediately after the sludge water is sucked into the sludge water tank 2, the superfluous water tank 3 The excess water previously stored inside can be immediately discharged via the pipes 31, 33 and 32 and the suction/drainage hose 1.

尚、上記の如き実施態様と異なり、浄化槽等の
清掃のため、浄化槽等の汚泥水の全量引抜きが必
要な場合には、汚泥水処理タンク2だけでなく
過水タンク3にも浄化槽等の汚泥水を吸引収容す
る。汚泥水処理タンク2への汚泥水の吸引収容は
前述の通りであり、過水タンク3へ汚泥水を吸
引収容するには、加圧、減圧装置5により過水
タンク3を減圧状態とし、且つ開閉コツク10,
11及び14を開放すれば良く、このようにすれ
ば吸排水ホース1並びにパイプ32,33及び3
1を介して浄化槽等の汚泥水を過水タンク3内
に吸引収容できる。汚泥水処理タンク2及び過
水タンク3に汚泥水吸引収容したら、まず汚泥水
処理タンク2内の汚泥水を前述の基本的な実施態
様に従つて処理し、過装置4における過水受
タンク4″内に過水を得る。過水受タンク
4″内の過水は、過水タンク3内にこの場合
汚泥水が収容されているから、上記の基本的実施
態様によつては排出できず、開閉コツク21を開
放し且つポンプ7を作動させ、パイプ36及び3
8、並びに吸排水ホース1を介して直接排出す
る。尚、ポンプ7によるポンピングが必要のない
場合には開閉コツク22を開放して重力排出口3
9から過水を排出する。而して、汚泥水処理タ
ンク2内の汚泥水を処理、排出したら、過水タ
ンク3内の汚泥水を汚泥水処理タンク2内に移行
し、これを上記の如き基本的実施態様で過装置
4を介して、或はポンプ7を介して吸排水ホース
1から排出する。この場合において、過水タン
ク3から汚泥水処理タンク2への汚泥水の移行
は、加圧、減圧装置5により、汚泥水処理タンク
2を減圧状態とする一方、過水タンク3を加圧
状態とし、且つ開閉コツク14及び13を開放す
ることにより、パイプ31,33及び30を介し
て行なうことができる。
Note that, unlike the embodiments described above, if the entire amount of sludge water from the septic tank, etc. needs to be withdrawn for cleaning the septic tank, etc., the sludge from the septic tank, etc. will be removed not only from the sludge water treatment tank 2 but also from the overwater tank 3. Suction and containment of water. The suction and storage of sludge water into the sludge water treatment tank 2 is as described above. In order to suction and store sludge water into the overwater tank 3, the overwater tank 3 is brought into a depressurized state by the pressurization and decompression device 5, and Opening/closing trick 10,
11 and 14, and in this way, the suction and drainage hose 1 and the pipes 32, 33, and 3
1, sludge water from a septic tank or the like can be sucked and stored in the overwater tank 3. After the sludge water is sucked and stored in the sludge water treatment tank 2 and the overwater tank 3, the sludge water in the sludge water treatment tank 2 is first treated in accordance with the basic embodiment described above, and then transferred to the overwater receiving tank 4 in the filtration device 4. The excess water in the excess water receiving tank 4'' cannot be discharged according to the above-mentioned basic embodiment because sludge water is stored in the excess water tank 3 in this case. , open the opening/closing pot 21 and operate the pump 7, and then open the pipes 36 and 3.
8, as well as direct discharge via the suction and drainage hose 1. In addition, when pumping by the pump 7 is not necessary, open the opening/closing pot 22 and close the gravity outlet 3.
Drain excess water from 9. After the sludge water in the sludge water treatment tank 2 has been treated and discharged, the sludge water in the sludge water treatment tank 3 is transferred to the sludge water treatment tank 2, and the sludge water is transferred to the filtration apparatus in the basic embodiment as described above. 4 or from the suction/drainage hose 1 via the pump 7. In this case, the sludge water is transferred from the overwater tank 3 to the sludge water treatment tank 2 by bringing the sludge water treatment tank 2 into a depressurized state using the pressurization and decompression device 5, while the overwater tank 3 is brought into a pressurized state. This can be done via the pipes 31, 33, and 30 by opening the opening/closing tips 14 and 13.

叙上の如く、本発明の汚泥水処理方法によれ
ば、一台の車両を用いるだけで、汚泥水の抜き取
りと張水とを可能とすることができ、本発明で用
いる過装置及び加圧・減圧装置による効果と相
俟つて浄化槽等の管理を容易に実施できる等の効
果が奏される。
As described above, according to the sludge water treatment method of the present invention, it is possible to remove and fill the sludge water with just one vehicle, and the sludge water treatment method and pressurization device used in the present invention・Coupled with the effects of the pressure reduction device, it is possible to easily manage septic tanks, etc.

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

図面は本発明に用いられるの汚泥水処理及び張
水返送車の配管系統図を示すものである。 1……吸排水ホース、2……汚泥水処理タン
ク、2′……撹拌機構、3……過水タンク、4
……過装置、5……加圧、減圧装置。
The drawing shows a piping system diagram of the sludge water treatment and water return vehicle used in the present invention. 1... Suction and drainage hose, 2... Sludge water treatment tank, 2'... Stirring mechanism, 3... Overwater tank, 4
...pressure device, 5...pressurization, depressurization device.

Claims (1)

【特許請求の範囲】 1 車輌に、吸排水ホース、汚泥水と凝集剤とを
撹拌混合する撹拌機構内部に備えた汚泥水処理タ
ンク、過水タンク、固液分離を行なう回転式ス
クリーン筒とその下方に配設した過水受タンク
とを備えた過装置、及び真空ポンプ及び四方切
換弁を用いて構成され上記汚泥水処理タンクと
過水タンクとの内圧をそれぞれ別個に加圧、減圧
し得る加圧、減圧装置を装備させ、上記吸排水ホ
ースをそれぞれ上記汚泥水処理タンクと上記過
水タンクとに連通させ、且つ上記過装置を上記
汚泥水処理タンクと上記過水タンクとの間に接
続させてなる、汚泥水処理及び張水返送車を用い
て浄化槽等の汚泥水を処理する方法であつて、 上記過水タンクに予め過水を収容してお
り、上記加圧、減圧装置により上記汚泥水処理タ
ンクを減圧して上記吸排水ホースを介し浄化槽等
の汚泥水を上記汚泥水処理タンク内に吸引収容し
た後、上記加圧、減圧装置により上記過水タン
クを加圧して上記過水タンク内の過水を、上
記汚泥水処理タンクに吸引収容した汚泥水の量に
等しい量を上記吸排水ホースを介して浄化槽等に
排出する一方、上記汚泥水処理タンク内の汚泥水
を凝集剤と共に撹拌機構により撹拌混合して上記
汚泥水処理タンク内にフロツクを形成し、斯くし
て得られたフロツクを含む上記汚泥水処理タンク
内の一次処理水を、上記汚泥処理タンクを上記加
圧、減圧装置により加圧して、上記過装置に圧
送して固液分離し、上記過水受タンク内に分離
された過水を、上記加圧減圧装置により上記
過水タンクを減圧して上記過水タンク内に吸引
収容し、必要に応じ該過水を上記過水受タン
クから浄化槽等に排出することを特徴とする汚泥
水処理及び張水返送車による、浄化槽等の汚泥水
処理方法。
[Scope of Claims] 1. A vehicle includes a suction and drainage hose, a sludge water treatment tank and a superhydrant tank provided inside a stirring mechanism that stirs and mixes sludge water and a flocculant, a rotary screen cylinder that performs solid-liquid separation, and its It is constructed using a filtration device equipped with an overwater receiving tank disposed below, a vacuum pump, and a four-way switching valve, and is capable of pressurizing and depressurizing the internal pressure of the sludge water treatment tank and overwater tank, respectively. Equipped with a pressurization and depressurization device, connecting the suction and drainage hoses to the sludge water treatment tank and the overwater tank, and connecting the filtration device between the sludge water treatment tank and the overwater tank. This is a method of treating sludge water in a septic tank, etc. using a sludge water treatment and water filling and return vehicle, in which the above-mentioned overwater tank is previously filled with superfluous water, and the above-mentioned pressurization and depressurization device is used to After depressurizing the sludge water treatment tank and sucking and storing sludge water from the septic tank, etc. into the sludge water treatment tank through the suction and drainage hose, the overwater tank is pressurized by the pressurization and depressurization device to remove the overwater. An amount of excess water in the tank equal to the amount of sludge sucked and stored in the sludge water treatment tank is discharged to a septic tank etc. through the suction and drainage hose, while the sludge water in the sludge water treatment tank is treated with a flocculant. The primary treated water in the sludge water treatment tank containing the flocs thus obtained is stirred and mixed by a stirring mechanism to form flocs in the sludge water treatment tank, and the sludge treatment tank is pressurized. The overwater is pressurized by the decompression device and sent to the above-mentioned filtration device for solid-liquid separation, and the separated overwater is placed in the overwater receiving tank. A method for treating sludge water in a septic tank or the like using a sludge water treatment and water-filling return vehicle, characterized in that the superfluous water is sucked into a tank and discharged from the superwater receiving tank to a septic tank or the like as required.
JP57116370A 1982-07-05 1982-07-05 Treatment of sludgy water in purifier tank, etc. and treatment of sludgy water by vehicle for returning filling water Granted JPS596998A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57116370A JPS596998A (en) 1982-07-05 1982-07-05 Treatment of sludgy water in purifier tank, etc. and treatment of sludgy water by vehicle for returning filling water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57116370A JPS596998A (en) 1982-07-05 1982-07-05 Treatment of sludgy water in purifier tank, etc. and treatment of sludgy water by vehicle for returning filling water

Publications (2)

Publication Number Publication Date
JPS596998A JPS596998A (en) 1984-01-14
JPS625028B2 true JPS625028B2 (en) 1987-02-03

Family

ID=14685289

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57116370A Granted JPS596998A (en) 1982-07-05 1982-07-05 Treatment of sludgy water in purifier tank, etc. and treatment of sludgy water by vehicle for returning filling water

Country Status (1)

Country Link
JP (1) JPS596998A (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55119844A (en) * 1979-08-31 1980-09-13 Seibu Polymer Kasei Kk Joint for culvert
JPS6291297A (en) * 1985-10-16 1987-04-25 Tokyu Car Corp Sludge water treatment unit mountable on vehicle
JP4749365B2 (en) * 2007-03-19 2011-08-17 新明和工業株式会社 Sludge concentrator and sludge concentrator
IT1394556B1 (en) * 2009-06-08 2012-07-05 Jurop S P A APPARATUS AND METHOD FOR THE RECYCLING OF SLUDGE WATER, IN PARTICULAR FOR SERVICE VEHICLES FOR CLEANING OF PIPELINES OF SEIZED SEWAGE PIPELINES
JP6105220B2 (en) * 2011-07-12 2017-03-29 高砂熱学工業株式会社 Treatment method of flushing waste water from piping system of equipment with galvanized steel pipes

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SE7710986L (en) * 1977-09-30 1979-03-31 Stigebrandt Ake METHOD AND DEVICE FOR TREATMENT OF THE SLUDGE WATER CONTENT IN SEWER WELLS AND DYLIKT

Also Published As

Publication number Publication date
JPS596998A (en) 1984-01-14

Similar Documents

Publication Publication Date Title
US5819776A (en) Liquid de-icer production apparatus and method
CN108455817B (en) Sewage suction purification vehicle
CA2486137A1 (en) Mobile slurrying and cleaning system for residual oil contaminated sand
CA2465585A1 (en) Concrete recovery method and system
JPS625028B2 (en)
JPS6291297A (en) Sludge water treatment unit mountable on vehicle
JP3627809B2 (en) Sludge concentration apparatus and sludge concentration method
CN209411838U (en) A kind of equipment of low energy consumption sewage treatment
CN215799048U (en) High-efficient muddy water intelligence purifier
JPS6115114Y2 (en)
CN211676594U (en) Electric suction filtration device
CN216472584U (en) Landfill leachate concentrate pretreatment equipment
US4705755A (en) Apparatus for collecting lysozyme from egg white by adsorption
GB2300576A (en) Device for and method of separating suspended solids from liquids
CN222586452U (en) Intelligent full-automatic emulsion guarantee system
JP4749365B2 (en) Sludge concentrator and sludge concentrator
RU104936U1 (en) CIRCUIT WATER CLEANING SYSTEM WHEN WASHING CARS
JPS58150490A (en) Vehicle for treating sludgy water in purifying tank or the like
DE590848C (en) Liquid conveying device
CN219991404U (en) Vehicle-mounted sludge dewatering device
CN214880726U (en) Total nitrogen treatment equipment for wastewater
SU1393883A2 (en) Machine for removing solid drifts from drain wells
CN218058672U (en) A water resource recycling device
CN212595524U (en) Environment-friendly precipitator conveying system
CN219849132U (en) Emulsion liquid phase mixing device