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JPS5949897A - Waste water disposal plant - Google Patents

Waste water disposal plant

Info

Publication number
JPS5949897A
JPS5949897A JP58090874A JP9087483A JPS5949897A JP S5949897 A JPS5949897 A JP S5949897A JP 58090874 A JP58090874 A JP 58090874A JP 9087483 A JP9087483 A JP 9087483A JP S5949897 A JPS5949897 A JP S5949897A
Authority
JP
Japan
Prior art keywords
water
wastewater
pipe
circulation pump
net
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.)
Granted
Application number
JP58090874A
Other languages
Japanese (ja)
Other versions
JPS6333440B2 (en
Inventor
ゲナンジイ−・セルゲイビイツチ・ゼ−ニン
セミヨン・アレクサンドロビイツチ・ボガ−トイフ
アナト−リイ・チイモフエ−ビイツチ・ソロビイエフ
ウラジイ−ミル・アナトリイエビイツチ・メドヴエ−ジエフ
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.)
LE TEKUNOROJICHIESUKII I KOROD
RENINGURAADOSUKII TEKUNOROJICHIESUKII INST KORODEIRUNOI PUROMUSHIRENNOSUTEI
Original Assignee
LE TEKUNOROJICHIESUKII I KOROD
RENINGURAADOSUKII TEKUNOROJICHIESUKII INST KORODEIRUNOI PUROMUSHIRENNOSUTEI
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 LE TEKUNOROJICHIESUKII I KOROD, RENINGURAADOSUKII TEKUNOROJICHIESUKII INST KORODEIRUNOI PUROMUSHIRENNOSUTEI filed Critical LE TEKUNOROJICHIESUKII I KOROD
Publication of JPS5949897A publication Critical patent/JPS5949897A/en
Publication of JPS6333440B2 publication Critical patent/JPS6333440B2/ja
Granted legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/006Regulation methods for biological treatment
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/24Treatment of water, waste water, or sewage by flotation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/005Black water originating from toilets
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/001Build in apparatus for autonomous on board water supply and wastewater treatment (e.g. for aircrafts, cruiseships, oil drilling platforms, railway trains, space stations)

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Molecular Biology (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Microbiology (AREA)
  • Health & Medical Sciences (AREA)
  • Physical Water Treatments (AREA)
  • Filtration Of Liquid (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)

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】 ・)・宅明は屯して廃水浄化すj、:t!J技術に関1
2、更に待X]1に1・−水処理装置に関する。
[Detailed description of the invention] ・)・Takumei goes back and purifies wastewater. :t! J Technology 1
2.Furthermore, regarding the water treatment equipment.

を疵IM明の″1.マ徴を実施化した装(代は船舶又・
汀[水道水Pi K−東結されていない建物及び建1告
物の廃水処理VC過+!1 I’ll能である。
IM Ming's ``1.''
[Tap water Pi K-Wastewater treatment of buildings and buildings that are not connected to the east VC exceeds! 1 I'll be able to do it.

1見(1:、、生活圏19卆問題は全巨界的関心を喚起
1−。
1 view (1:,, The problem of living sphere 19 volumes has aroused the interest of the whole world 1-.

ている。河川、湖沼及び海洋への廃物投棄は生活圏の全
体的汚染の中でも特別な位置を占める。船舶の躍進的発
達は河川、湖沼及び海洋・\投東ざ力。
ing. Dumping of waste into rivers, lakes and oceans occupies a special place in the overall pollution of living areas. The rapid development of ships has led to the expansion of rivers, lakes, and oceans.

だ船舶廃東物の喰を著し7く増大させ、結果として、廃
水浄化、汚染除去装置を装fiift l、−Cいない
船舶を領rlrjから閉め出−J−tバhfを世界の諸
国がとる事態を招いた。[廃柄物、その曲による海洋汚
染防止に関する協定1に依れば、船舶(dそうした浄上
汚染除去装置を備えなければならない。現代の船舶下学
に1船内廃水処理設備〕)自動的操縦を提供している。
This has significantly increased the consumption of ship waste, and as a result, countries around the world have shut out ships that are not equipped with wastewater purification and decontamination equipment from the territory. This led to a situation where [According to Agreement 1 on the Prevention of Marine Pollution by Waste Materials, Ships (d) must be equipped with such purification and decontamination equipment. Modern ships must be equipped with onboard wastewater treatment equipment] to operate automatically. providing.

従って船内廃水の浄化と汚染除去のだめの、高件能叶つ
故障のない装置4の発展に多友の関心が寄せらり、てい
る。建造中の船舶に部用I拝能な1i6水処理装(4は
現庄多数知られている。しかし、前1JSの協定の条r
1−によfl、げ、新造船と現存船の双方ともそうした
廃水処理装置を備えねばならないので、この要請は普通
限られた6耽のF水槽のみを備えた古い船舶に改良され
た設計の廃水処理)1式を装備するという問題を提起し
7ている。このような万民は広大な床面積を必要とし、
一般に船内[:水槽とは別に設置されなければならない
Therefore, Tatomo is interested in the development of a high-performance, failure-free device 4 for purifying and removing contaminants from shipboard wastewater. 1i6 water treatment system which can be used on ships under construction (4 is currently well known. However, the provisions of the previous 1JS agreement
1- Since both new ships and existing ships must be equipped with such wastewater treatment systems, this requirement is usually applied to older ships with only a limited 6-hole F tank for improved designs. The issue of installing one set of wastewater treatment (waste water treatment) has been raised. Such people require a large amount of floor space,
In general, it must be installed separately from the aquarium.

[不)”テユマティク・−レトロ」として知られ、るサ
レ7・パチンノード社の廃水処理装+i’V11979
年7月16日発行、サレン・パテ7ノード、・よシフ1
/2ト第1号参照)が広く使用はれでいるが、該装置、
は船内[水槽内の土層及び下層水位・l)レベル計を庁
み、これらのレベル泪から信号を受けると、これに応じ
て該装置のスイッチを開閉する。
[Un) Known as "Teyumatic-Retro", wastewater treatment system +i'V11979 from Rusale 7 Pachinode Co., Ltd.
Published on July 16th, Saren Pate 7 nodes, Yoshifu 1
2) is widely used, but the device,
monitors the level meters on board (the soil layer and lower water level in the water tank), and when it receives signals from these level gauges, it opens and closes the switches of the device accordingly.

該下水槽は取水ユニットをも擁し、このユニ、トの廃水
の流入に面する先端部は取水ユニ、トのノ・ウジノブの
壁と廃水の流れに対して垂直にある網で叫われている。
The sewage tank also has a water intake unit, the end of which faces the inflow of wastewater is connected by a net perpendicular to the wall of the intake unit and the wastewater flow. .

取水1ニツトの内側壁に取水管と、を処理求を再循環を
せる管を設ける。取水管は循環ポツプの吸引端と連結す
る。該循環ポンプの11:、万端]ζli t、J、 
’IE勾管、圧カタ〕/り及び一定の圧力供給管を経て
l′Y選コー二1.トと通じ、該浮選1−、−、−)ト
F(おい−C廃)kが浄化シれる。圧力タンクは未処理
廃水を11循環する管とも連絡1−ている。IEカタン
クに廃水再循環管を連結する配管に排出器が設置され、
この排出器(は取tj<管を通過する水に通気するよう
意図される。該排出器はクラ1.ジ収集器の気相部分及
び浄化水槽と連絡可能である。定量供給圧力管(・よ一
般的に所定の長さで目盛りを付けた管であり、l5J6
水を所定の割合で浮選ユニ1.トに供給する。
A water intake pipe and a pipe for recirculating the processed water are installed on the inner wall of the water intake unit. The water intake pipe is connected to the suction end of the circulation pop. 11 of the circulation pump:, all things possible] ζli t, J,
'IE gradient pipe, pressure kata] / and constant pressure supply pipe to l'Y selection conduit 1. The flotation 1-, -, -) and F (Oi-C waste) are purified. The pressure tank is also connected to a pipe that circulates untreated wastewater. A drain was installed on the pipe connecting the wastewater recirculation pipe to the IE Katank.
This ejector is intended to vent the water passing through the pipe. The ejector can communicate with the gas phase part of the collector and with the clarified water tank. It is generally a tube marked with a scale at a predetermined length, and is 15J6.
1. Flotate water at a predetermined ratio. supply to customers.

yect、又はに4 (804) 3 ”ような試薬を
圧力管を通過する廃水の汚染物質を凝固させるため特別
なポンプで注入する。
A special pump injects a reagent such as yect, or ni4 (804) 3'' to coagulate contaminants in the wastewater passing through the pressure tube.

浮選ユニ7トは水を浄化する容器、廃水処理中に形成さ
れた浮きかすを除去するスクレーノく及び浄化濱れた水
を排出する装置を含む。
The flotation unit 7 includes a vessel for purifying the water, a drain for removing the flotsam formed during wastewater treatment, and a device for discharging the purified water.

該浮選ユニ、トはスラッジ排出ポンプを備えたスラッジ
収集器及び浄化水排水ポンプを備えだ浄化水槽と連絡す
る。該装置は更に循環ポツプ、スラッジ排出ポンプ及び
浄化水排出ポンプと電気的に結合した制御区分と下水漕
中のト層及びF層水位レベル計を備える。
The flotation unit communicates with a sludge collector equipped with a sludge discharge pump and a clarification tank equipped with a clarified water drainage pump. The apparatus further includes a control section electrically connected to the circulation pop, sludge discharge pump and purified water discharge pump, and level gauges for the To and F layers in the sewage tank.

該装置の稼動中、循環ポツプは取水ニー、トの・・ウジ
ノブから取水管を通して廃水を吸引し、重圧下で該廃水
を圧力タンクに搬送する。その際廃水が運んだ大きな固
体物は取水ユニットの網1′こよって留保きれる。約2
又は3ata(絶対ICE)の重圧勾が圧力タンク内で
造り出される。圧カタノク内の約60係の水が未処理廃
水再循環管を通って廃水取水1ニツトのノ・ウジノブに
戻される。未処理廃水再循環管に連結する排出器が廃水
に空気を通し、圧力タンクに送られたその廃水は相当鼠
の溶解していない空気を含んでいる。約40チの廃水が
定数送出圧力管路によって浮選ユニ+)pc送り出され
る。この管路は目盛付き管として設計きれているので、
圧力タンク内の一定の水圧下で、接定間送出圧力管路内
の流入計の割合は持続的あるいは不変である。浮選ユニ
ットだ送り出された水流に凝固剤を注入し、その浮選ユ
ニ、トで重力1:浮選が′1ミする。この過程で形成さ
れた浮きかすのスラッジはスクレーパによってスラッジ
収集器に移され、曲刃浄化さり、だ水は処理水槽に吸引
さ!+、る。水流に汚染除去の溶剤を注入するだめの装
備もな烙れている。
During operation of the device, the circulation pop sucks wastewater from the intake knee, through the intake pipe, and conveys the wastewater under heavy pressure to the pressure tank. In this case, large solid objects carried by the wastewater can be retained by the net 1' of the water intake unit. Approximately 2
Or a heavy pressure gradient of 3 ata (absolute ICE) is created in the pressure tank. Approximately 60 liters of water in the pressure tank is returned to the wastewater intake port through an untreated wastewater recirculation pipe. An ejector connected to the raw wastewater recirculation line aerates the wastewater, and the wastewater sent to the pressure tank contains a significant amount of undissolved air. Approximately 40 g of waste water is delivered to the flotation unit by a constant delivery pressure line. This pipe is designed as a graduated pipe, so
Under constant water pressure in the pressure tank, the rate of inflow meter in the delivery pressure line during contact is constant or unchanged. A coagulant is injected into the water stream sent out by the flotation unit, and the flotation becomes 1:1 gravity. The floating sludge formed in this process is transferred to the sludge collector by a scraper, purified by a curved blade, and the sludge is sucked into the treated water tank! +、ru. Equipment for injecting decontamination solvents into water streams is also in disrepair.

友きな汚染物が網によって留保をれること、そして第1
にこれらの入きな固体物が未処理廃水再循環管を通って
、取水ユニットf流入する廃水の璧随によって流きれる
という事実によって、−上述の装置6.は低性能の欠点
を免かれない。反面、該網は作も続行に伴い生ずる固体
物で詰斗って来る。
Friendly contaminants are retained by the net, and the first
Due to the fact that these solids are washed away by the stream of wastewater entering the water intake unit f through the untreated wastewater recirculation pipe - the above-described device 6. does not suffer from the drawback of low performance. On the other hand, the net becomes clogged with solid matter that is produced as the crop continues.

該閉寒の結果、圧力夕/りへの帳水送出敗が減少し、他
方室間へ出圧力管路による浮選ユニットへのjE月タン
クか1〕)の廃水排出には一定している。
As a result of the closed cold, the discharge of waste water to the pressure tank is reduced, while the discharge of waste water from the tank to the flotation unit by the pressure pipe between the chambers is constant. .

この為、再循環管を1市って廃水取水ユニットのハウジ
ングに流入り、、該網を流し又は掃除する水の量(桃減
少し、一層網の詰まりを増太さ1)る。従って循環ポン
プによって圧力タンクに供1拾をノ1−る廃水縁は更に
減少し、他方定量送出圧力管tてよる圧力タンクからの
廃水排出鼠の割合は1:J、前のIk準を1呆持し、こ
れが循環管の還流径路を通ってF水タンクに戻る水流量
を再度減少させ、μ下回様である。上述の連鎖事象は不
可逆であって、循環−1ミンプの故障を招く可能性もあ
る。それを防ぐため、稼動を中東12、外側の水の流れ
によって網を洗」つなければならない。
This reduces the amount of water that flows through the recirculation pipe into the housing of the waste water intake unit and flushes or cleans the screen (reducing the amount of water and increasing the amount of water that clogs the screen). Therefore, the amount of waste water supplied to the pressure tank by the circulation pump is further reduced, and on the other hand, the ratio of waste water discharged from the pressure tank by the metered-rate delivery pressure pipe is 1:J, compared to the previous Ik standard. This causes the flow rate of water returning to the F water tank through the return path of the circulation pipe to decrease again, below μ. The chain of events described above is irreversible and may even lead to failure of the circulating-1 minp. To prevent this, the net must be washed by an external stream of water during operation.

廃水取水ユニットの網のより効果的洗浄(でよって廃水
処理装置の性能を改良することが本発明の目的である。
It is an object of the present invention to improve the performance of wastewater treatment equipment by more effective cleaning of the mesh of the wastewater intake unit.

この目的は、1傷水の流れに沿ってそれぞれIIM’r
 y′)ζ配列をれた、下水槽内に設けら11.たノ・
ウンングと廃水の流れに面した該ノ・ウンングの先端部
kldう網とを有する廃水取水ユニットと、廃水をil
’Vり入れる取水管及び未処理の廃水を取水ユニ、トに
戻す再循環管と、人口が水管によって該取水管と連結し
出口が未処理の廃水の再循環材に連結する循環ゼンブと
、定漬送出出力管路によって循環ポンプの出1」と連結
する浮選ユニ、ト、共に浮選ユニ2トと連絡1.て、そ
れぞれスラ、ジ排出ポノグ及び浄化した水を排出するポ
ンプを有するスラッジ11M琳器及び処理水槽、そノt
ぞれ該循環ポツプ、スラ、)をjJF出1.浄化した水
を排出増−るボノグ及びトー水槽内の−L層及び下層水
位のレベル計と電気的に連結を九だ制御区分とを含む廃
水処理装置にして、′:yらに該制御区分と電気的に連
結され、取水庁と循Jgボノグの人口とを連結する水管
に配置さり、た水王感田器を倉み、該循環ポンプの出I
」は未処理廃水を再循j4さする管に直接連結きil、
該制御区分に電気的に、小結される自動閉鎖弁を定+1
送出資路の循JRj?ノゾ浮、西ユニットの間に配fi
t l、たことを特徴とJ−る該廃水処理装置4を提供
することによって達すられる。
This objective is to carry out each IIM'r along the flow of one wound.
11. Tano・
a wastewater intake unit having a winding and a mesh at the tip of the winding facing the wastewater flow;
a water intake pipe that takes in the water, a recirculation pipe that returns untreated wastewater to the water supply unit, and a circulation pipe that connects the intake pipe with the water pipe and whose outlet connects to the untreated wastewater recirculation material; The flotation unit, which is connected to the output 1 of the circulation pump by a constant immersion delivery output pipe, is connected to the flotation unit 2.1. A 11M sludge vessel and a treated water tank each have a sludge, a discharge pump, and a pump for discharging purified water.
1. A wastewater treatment device including a control section electrically connected to a level meter for the -L layer and lower water level in the Bonog and To water tank for increasing the discharge of purified water, and the control section is connected to the It is electrically connected to the water pipe that connects the water intake agency and the population of the circulating Jg Bonog, and holds the water tank, and the output I of the circulation pump.
” can be connected directly to pipes that recirculate untreated wastewater,
A self-closing valve electrically connected to the control section is fixed +1.
Circulation of transmission route JRj? Nozouki, distributed between the west unit
This is achieved by providing the wastewater treatment device 4 characterized by the following characteristics.

廃水取水ユニットは網の前+hiに緊締され、そのド)
5郡M+帳水通過のだめの開口部を有する1−7ングを
Jゼrことが望ましく、該取水ユニットの網は廃、/に
の流路Qこ村して30度な・・)し40度の角度で傾側
しでいで、循環2ングによつで供給′さノする未処理水
の流れは網を1市過し、ケー/ノグから反転し、網の表
面に作用してその汚染物質dhを洗滌する。
The wastewater intake unit is tightened in front of the net +hi, and its de)
It is desirable to have a 5-gun M + 1-7 ring with an opening for water passage, and the net of the water intake unit is discarded, and the flow path Q is 30 degrees...) and 40 The stream of untreated water fed by the circulation ring, which is inclined at an angle of 100°, passes through the screen, is reversed from the cage, and acts on the surface of the screen, contaminating it. Wash the substance dh.

廃水処理のだめの本装置を使11Jする場合、人員が付
〜添わなくても、より確実な廃水浄化が保tiIEされ
る。
When using this apparatus for wastewater treatment, more reliable wastewater purification can be maintained even without the presence of personnel.

本発明による廃水処理装置は廃水取水ユニット1(第1
図)、船内下水槽4内のに層水Eヶレベル計2及びド層
水位レベル計3を含む。該取水ユニ、]・1は全体とし
て符号5で示ずハウジングを有し、その下方側部に開口
したケー7ング部分6を(、lえる。、廃水の流れに面
したハウジング5の端部は網Tで覆われている。該取水
ユニ、ト1は流入する廃水を取入れる取水管8と未処理
廃水を再循環させるだめの再循環管9を有する。該取水
ユニリド1は又網7を洗うだめの装置10も設けられ、
この装置10はハウジング5の内部に設置wをれ、自動
的に作動する進入弁を経て、(明示はれていない)外側
の木水管と連絡する。
The wastewater treatment device according to the present invention includes a wastewater intake unit 1 (first
(Figure), includes a layer water level meter 2 and a layer water level meter 3 in the ship's sewage tank 4. The water intake unit 1 has a housing, generally designated 5, with a casing part 6 opening at its lower side, the end of the housing 5 facing the waste water flow. is covered with a mesh T. The water intake unit 1 has an intake pipe 8 for receiving incoming wastewater and a recirculation pipe 9 for recirculating untreated wastewater. A device 10 for washing is also provided,
This device 10 is installed inside the housing 5 and communicates with the outside water pipe (not explicitly shown) via an automatically actuated inlet valve.

取水管8は水管12及び弁13を通して循環ボ7ダ14
の人りに連結する。咳水管12は水圧感知器15を収容
する。循19ボノグ14は水管16位び′tF−17を
通して未処理廃水再循環′1ff9と連結−1°2q。
The water intake pipe 8 passes through the water pipe 12 and the valve 13 to the circulation body 14.
Connect to people. Cough water tube 12 houses a water pressure sensor 15 . Circulation 19 Bonog 14 is connected to untreated wastewater recirculation '1ff9 through water pipe 16'tF-17 -1°2q.

水’ff 16 ist自動作動卯19と流計調整膜2
゜を備えたiに14送出千力管路18を介して浮選1ニ
ツト21と連絡する。該I″IiAIiAユニ1 i4
水管221cよって処理(前浄化水槽23と連結12、
水管24全介l〜て)丁ン2Bを備えたスラッジ収集器
25と連結する。次に処理済浄化水槽23は水管27p
ζよつ−C浄化水排出ポンプ28と連結17、曲与スラ
1.ジ収’イ各器25はスラ、ジ排出ボ/ブ3゜と司5
結する。スラッジを核スラ、ジ収イト器25がら、1e
32を設+tjだ1(り管31に沿−ンて「水槽4へ、
符しく+、1井34を・没けた水管33を経て船り一\
(明示1.ていなl/−1)、排出することができる。
Water 'ff 16 ist automatic operation rabbit 19 and flow meter adjustment membrane 2
14 is connected to the flotation unit 21 via a delivery line 18. The I″IiAIiA Uni 1 i4
Processed by water pipe 221c (connection 12 with pre-purification water tank 23,
The water pipe 24 is connected to the sludge collector 25 equipped with a pipe 2B. Next, the treated septic water tank 23 has water pipe 27p.
ζyotsu-C purified water discharge pump 28 and connection 17, curved slurry 1. Each container 25 has a slurry, a discharge tube 3゜ and a holder 5.
conclude. 1e
32, along the pipe 31,
+, 1 well 34, the boat 1 via the sunken water pipe 33\
(Explanation 1. Tena l/-1), can be discharged.

本1q ロク゛l・L史に制御JI+区、)35を^み
、これはトハづk 117:レベル計2、ド層水位レベ
ル計3、循ipポンプ14、/P if二水排出ポノグ
28、スラッジ排出ボ5/フ”30、自−1山作車jJ
’1″l 3 、17 、19、フ丁ノ2611(2び
に水圧感知器15と電線で連結をtlてし)る。
Book 1q: Control JI + District in the history of Rokil/L, ) 35, this is tohazuk 117: Level meter 2, layer water level meter 3, circulation IP pump 14, /Pif 2 water discharge ponog 28, Sludge discharge bo 5/fu” 30, self-1 mountaineering car jJ
'1''l 3, 17, 19, Futono 2611 (connect with 2 and water pressure sensor 15 with electric wire).

取水ユニ1.ト1の網1に詰まった汚染物にχ・↑し更
に際立った効果をにげ、流入する廃水を洗浄する能率を
高めるため、網7(第2図) i、;[l弘水の流れに
対し30度ないし40度の傾斜で配:6され、よって、
循1貝ポンプ14に、よって丙循lυ1−で取水ユニッ
ト1に流れ内む未処理廃水の流れ36は網7を通過j〜
、網Tの前面に設けらfしたケーンノブ6から反転し、
従って網Tの内側、外側両)jの表面1C作用1.て汚
染物を網から下水槽の底まで洗い流す。
Water intake unit 1. In order to have a more pronounced effect on the pollutants clogging the net 1 of the net 1 and increase the efficiency of cleaning the inflowing wastewater, the net 7 (Fig. 2) i,; It is arranged at an inclination of 30 degrees to 40 degrees to
The stream 36 of untreated wastewater flowing into the water intake unit 1 in the circulation 1 shell pump 14 and thus into the water intake unit 1 in the circulation lυ1- passes through the net 7 j~
, reverse from the cane knob 6 provided on the front of the net T,
Therefore, both the inner and outer sides of the net T) j's surface 1C action 1. to flush contaminants from the screen to the bottom of the sewage tank.

網Tの傾斜角度は30度ないし45度の範囲が望ましい
。何故なら取水ユニ、ト1のケーンノブ6から反転され
る水流の力と共に、未処理昨水を再循環ざ亡る管9から
流入する未処理廃水の水流のり及び1r力が最も効果的
になるのけこのしすな角度によってのみ保証きれるから
である。
The angle of inclination of the net T is preferably in the range of 30 degrees to 45 degrees. This is because, along with the force of the water flow reversed from the cane knob 6 of the water intake unit 1, the force of the water flow and 1r force of the untreated wastewater flowing in from the pipe 9 where the untreated waste water is recirculated becomes the most effective. This is because it can only be guaranteed by a certain angle.

網7の傾斜角度が45度を越えた嚇合、ケーシング6か
ら反転される水流によって生ずるこすり取る勾の能率は
著しく低Fし、他方30度以下では重力の急激な減少が
起り、それによってケーンノブ6から反転される水流は
網7の表面から汚染吻をこすりをることができず、汚染
物はさらに固着する。n向Vこ々る。
When the angle of inclination of the net 7 exceeds 45 degrees, the efficiency of the scraping slope caused by the water flow reversed from the casing 6 becomes extremely low, while when the angle of inclination of the net 7 is less than 30 degrees, a sudden decrease in gravity occurs, which causes the cane knob to The water flow reversed from 6 cannot scrape the contaminants from the surface of the net 7, and the contaminants are further stuck. n mukai v kokoru.

本発明による廃欠処理装置は次に述べZ、ように1乍動
する。
The waste processing apparatus according to the present invention operates as described below.

循j衰ボ/プ14(第1図)は廃水取水に、ト1の・・
ウジ7・グ5から網7を通して廃水を吸引し、管8から
水管16に該廃水を搬送する。水流が運んだ友ノ(すの
汚染物又は固体物は凋7を通過で〜v1イ11シ方ケー
/7グ6は廃水中に浮遊する(きな固体I勿が・悄7を
ynらないよう阻IFする。f盾項ボンフ゛14の人1
」に続く水管12中の所定の数値以丁の水圧Fで廃水取
IKに、ト1のハウジング5に送ら9る水の杵1山の流
¥i、でに−1、水圧感知器15は制御区分35に伝え
る信号を起さず、従って定鼠送出圧ツノ1青路1Bのブ
「19は開かない。水管1’6IC沿う水流は2つに分
れる。流電の少ない部分(約30%)は定晴送出圧力管
路IBK入り、多い部分(約TOチ)は未処理廃水再循
環の管9に還流する。
The circulation pipe 14 (Fig. 1) is used for wastewater intake, and the circulation pipe 14 (Fig. 1)
Waste water is sucked from the maggots 7 and 5 through the net 7, and is conveyed from the pipe 8 to the water pipe 16. Contaminants or solid substances carried by the water flow pass through the wastewater and become suspended in the wastewater. I will prevent it from happening.f shield term bomb 14 person 1
At a predetermined water pressure F in the water pipe 12 following ``, the flow of water is sent to the waste water intake IK to the housing 5 of the t1, and the water pressure sensor 15 is It does not generate a signal to be transmitted to the control section 35, and therefore the valve 19 of the constant delivery pressure horn 1 Aoji 1B does not open.The water flow along the water pipe 1'6IC divides into two parts. %) enters the constant discharge pressure line IBK, and a large portion (approximately TO) is returned to the untreated wastewater recirculation line 9.

この水流分離は該定瞼送出圧力管路1日中、゛で配置さ
れた薄膜20によって確実になる。処理中の廃水はこの
圧力管路18を通τ尚して浮4ユニ、ト21に達し、こ
こで最終的に浄化され汚染除ガきノする。
This water flow separation is ensured throughout the day in the constant eyelid delivery pressure line by the membrane 20 placed at . The wastewater being treated passes through this pressure pipe 18 and reaches the float 21, where it is finally purified and decontaminated.

その結果生じたスラッジは浮選ツー二、ト21から水管
22を通って処理済水槽23へと排出さハ、る。
The resulting sludge is discharged from the flotation tank 21 through a water pipe 22 to a treated water tank 23.

水管16から廃水取水ユニ、)1の・・ウジング5に水
流が流入し網7から大型の固体物を洗い流す。
A water flow flows from the water pipe 16 into the waste water intake unit () 1...using 5 and washes away large solid objects from the net 7.

網1が汚染物によって詰まり始めると、循環ボング前の
水管12における水圧が水IE感知器15に働いて信号
を制御区分に伝達させ、該制御区分は定量送出圧力管路
18の弁19を閉鎖するよう信号を発する。井19が閉
じた状態では、循環ポンプ14が吸い上げた水流はすべ
−r未処理廃水ド)i盾環管9へ水管16を通して入り
、そこから水は廃水取水ユニット1のハウジング5に戻
る。結果として、水管16によって送られ・141に向
う成畦は激しくなり、網7を効率よく洗いbl[すこと
全容易K 12て、網から固着した汚染物゛を除去する
。ケ−ノング6の設置及び再循環水流の方向[24する
網の傾斜が網7の洗滌をさらに容易にしている。
When the mesh 1 becomes clogged with contaminants, the water pressure in the water pipe 12 before the circulation bong acts on the water IE sensor 15 to transmit a signal to the control section, which closes the valve 19 of the metering pressure line 18. give a signal to do so. In the closed state of the well 19, all the water flow sucked up by the circulation pump 14 enters the untreated wastewater pipe 9 through the water pipe 16, from where it returns to the housing 5 of the wastewater intake unit 1. As a result, the growth directed towards the water pipe 16 becomes more intense, making it easier to wash the net 7 efficiently and remove any stuck contaminants from the net. The installation of the canongs 6 and the slope of the screen according to the direction of the recirculating water flow further facilitate the cleaning of the screen 7.

@7の閉塞していない目を通過後、再循環水の流れ36
(第2図)はケー/ング6の壁から反転しr J147
 fZ)外側表面だ吋I7て鏡角度をなして流れる。
Flow of recirculated water after passing through the unoccluded eyes of @7 36
(Fig. 2) is reversed from the wall of the cage 6.
fZ) flows at a mirror angle on the outer surface.

そのため網7を塞ぐ汚染′吻k」2つの側から作用きれ
る。叩1.、廃lkの璧流の流れ36はハウジング5の
内四から閉塞ノ吻に作用1ノで政綱から離り、さす、四
方ケー/7グ6から反転した流it 36は網Tの外側
表面から汚染′吻をこすり落す傾向にある。このような
)V水gt fif+、・7)二直作用がi司1の洗浄
効率を非常に高くrる。こう1.て洗浄さiulこ網7
はF水槽4から1所求i反水ユニ、ト1への流入率を促
進12、その結宋生した循」■ボンダ14の人11(第
1図)にひける/に圧の低Fが水圧感り」1器15の信
号を再び始動をi−て制御区、>35に伝、えると、制
御区分35は定i^送出1tE:JノイU路18の自I
IIJIJP19を開き、+fF、水のjili、ノ?
、 7>i浮1九ユニ、 ト211・で流入する。
Therefore, the contamination blocking the net 7 can be acted upon from two sides. Hit 1. , the flow 36 of the waste lk acts on the blockage nozzle from the inner four of the housing 5, leaves the line at one point, and the flow it 36 reversed from the four-way cage/7 g 6 flows from the outer surface of the mesh T. Contaminants tend to rub off on their proboscises. Such a ) V water gt fif+, ·7) two-direction action makes the cleaning efficiency of i-1 very high. This 1. Cleaned the net 7
1 from the F tank 4 to the water tank 4, which promotes the inflow rate to the tank 12, resulting in a low pressure F compared to the person 11 of the bonder 14 (Fig. 1). When the signal from the water pressure sensor 15 is transmitted again to the control section >35, the control section 35 outputs a constant i^ sending 1tE: J Neu U road 18's own I
Open IIJIJP19, +fF, water jili, no?
, 7>i floats 19 units, and flows in at 211.

4選ユニ1.トス1内で(イ^水?p化渦桿で生じたス
ラッジ(+、[水11724にょっでスラッジ収集器2
5ににポツプ3OKよって吸引される。
4 selection Uni 1. In Toss 1, (I^Water?Sludge generated in the p-conversion vortex rod (+, [Water 11724Nyodde Sludge Collector 2
5 is sucked by pop 3 OK.

スラッジ収集器はファン26によって換気される。The sludge collector is ventilated by a fan 26.

浮選ユニ、ト21から水管22沿いに処理断木槽23に
運ばれた浄化水は水管27を眞ってポンプ2Bによって
船上に排出される。
The purified water carried from the flotation unit 21 to the treated tree tank 23 along the water pipe 22 is discharged onto the ship by the pump 2B through the water pipe 27.

上述の点から、提案の装置を使用することによって、網
Tが汚染物で詰1つだとき、該装置に組み込まれだンス
テムの確実な稼動を阻害せず、乗組員の介入を必要とせ
ずにM137を自動的(・こ洗い、洗浄することが可能
である。
In view of the above, by using the proposed device, when the net T is clogged with contaminants, it will not disturb the reliable operation of the system incorporated in the device and will not require the intervention of the crew. It is possible to automatically clean the M137.

弁11を開いて洗滌液を網洗滌装置10に供給すること
によっても網T全自動的に洗浄することができ、自動作
動弁19の始動後3分以内に、循環ポンプ14の人口に
水圧の増1〕(1が起らない場合、網洗滌装置10が自
動的に作動する。
It is also possible to completely automatically clean the net T by opening the valve 11 and supplying the cleaning liquid to the net cleaning device 10. Increase 1] (If 1 does not occur, the screen washing device 10 will automatically operate.

更にこのような装置は機械室に比較的狭い空間で容易に
設置できるので、本装置6.の船舶内ごの使用は最小限
の費用で現存の廃水処理装置への補充を可能にする。例
えば乗組員50名の船舶に対し1、7 msの容積とわ
ずか0.7rr?の面積しか必要としない。そのに、船
内の下水処理設備を分解検査せずに、現存の下水槽を使
用して本装置の稼動が61能である。
Furthermore, since such a device can be easily installed in a relatively narrow space in a machine room, this device 6. On-board use of the system allows replenishment of existing wastewater treatment systems at minimal cost. For example, for a ship with 50 crew members, a volume of 1.7 ms and only 0.7 rr? only requires an area of In addition, the system can be operated using the existing sewage tank without disassembling the sewage treatment equipment on board.

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

第1図は本発明による廃水取水” 二y トを備えだ廃
水処理装置の機能的線図で、長袖方向の断面図C示す。 第2図j4本発明だよる廃水処理装置の廃水取水ユニ、
トの拡大断面図である。 1・・・廃水取水ユニ、ト、2・・・混層水位のレベル
計、3・・・F廃水(Xrのレベル計、4・・下水槽、
5・・・ハウジング、6・・ケーシング、7・・・網、
8・・・廃水の取水管、9・・・未処理廃水の再循壌箸
、1o・・・網洸滌装J  11,13.1?、19,
32.34・・・自動弁、12,16,22,24,2
7,29゜31.33・・・水管、14・・・循頃ポツ
プ、15・・・水圧感知器、18・・・定冴送出王力管
路、20−i量、閘整嘆、21・・γ!N廓ユニ、ト、
23・・・処J里済水槽、25・・・クラ1.ジ収集器
、26・・ファン、2B・・・浄化水排出ポンプ、30
・・・スラッジ排出ポンプ、35・・・制御区分。 第1頁の続き 0発 明 者 ウラシイ−ミル・アナトリイエビイッチ
・メドヴ工−ジエフ ソヴイエト連邦しニングラード ・ウリツツア・グロモーヴア6 ケーブイ50 568−
Fig. 1 is a functional diagram of a wastewater treatment device equipped with a wastewater intake unit according to the present invention, and is shown in a cross-sectional view C in the long sleeve direction.
FIG. 1...Wastewater intake unit, 2...Level meter for mixed layer water level, 3...F wastewater (Xr level meter, 4...Sewage tank,
5...Housing, 6...Casing, 7...Net,
8...Wastewater intake pipe, 9...Untreated wastewater recirculation chopstick, 1o...Network Service J 11,13.1? ,19,
32.34...Automatic valve, 12,16,22,24,2
7,29゜31.33...Water pipe, 14...Circulation pop, 15...Water pressure sensor, 18...Standing power delivery line, 20-i quantity, lock adjustment, 21 ...γ! N-Uni, To,
23...Tokoro J Risai Aquarium, 25...Kura 1. collector, 26...fan, 2B...purified water discharge pump, 30
...Sludge discharge pump, 35...Control classification. Continued from page 1 0 Inventor Vlasii-Mir Anatolyevich Medov Engineering-Ziv Soviet Union Ningrad Ulitsya Gromovar 6 Cavei 50 568-

Claims (1)

【特許請求の範囲】 H)  1′96水の流れに沿ってそれぞれ順次配列さ
れた、下水槽(4)内に設けられたハウジング(5)と
廃水の流れに面した該ハウジング(5)の先端部を覆う
網(7)とを有する廃水取水ユニット(1)と、廃水を
取り入れる取水管(8)及び未処理の廃水を取水ユニッ
ト(1)に戻す再循環¥1(9)と、人【コが水管(1
2)によって該取水管(8)と連結し出口が未処理の廃
水の再循環管(9)に連結する循環ポンプ(14)と、
定檄送出+IH力・R路(18)によって循環ポンプ(
14)の出口と連結する浮選ユニット(21)、共に浮
選ユニッ1−(21)と連絡して、それぞれスラッジ排
出ポンプ(30)及び浄化1〜だ水を排出するポンプ(
28)を有するスラッジ収集器(25)及び処理水槽(
23)、それぞれ該〔盾環ボンフ”(14)、スラッジ
を排出し浄化した水を排出するポンプ(28,30)及
び下水槽内の上層及び下層水位のI/ペル計(2,3)
と電気的に連結された制御区分(35)とを含む廃水処
理装置にして、さらに該制御1II1区分(35)と電
気的に連結され、取水管(8)と循環ポンプ(14)の
入口とを連結する水管(12)に配置された水圧感知器
(15)を含み、該循環ポンプ(14)の出口は未処理
廃水を再循環きせる管(9)に直接連結され、該制御区
分(35)Vct気的に連結される自動閉鎖弁(19)
を定駿医出管路(18)の循環ポンプ(14)浮選ユニ
、)(21)の間に配置道シたことを特徴上する該廃水
処理装置。 (2)廃水取水ユニット(1)が、網(7)の前面に緊
締されそのF刃部に廃水通過相開1コ部を有するケーシ
ング(6)を含み、該取水ユニ2ト(1)の網(7)は
廃水の流路に対して30度ないし40度の角度で傾斜し
ていて、循環ポンプ(14)によって供給される未処理
廃水の流れが網1)を通過し、ケーシング(6)から1
i転し、網(7)の表面に作用してその汚染物質を洗滌
することを特徴とする特許請求の範囲第1項r記・;あ
の廃水処哩装(召。
[Scope of Claims] H) 1'96 Housings (5) provided in the sewage tank (4) and housings (5) facing the wastewater flow, each arranged sequentially along the water flow. a wastewater intake unit (1) having a net (7) covering the tip, an intake pipe (8) for taking in the wastewater and recirculation for returning untreated wastewater to the water unit (1); [This is a water pipe (1)
a circulation pump (14) connected to the water intake pipe (8) by 2) and whose outlet is connected to the untreated wastewater recirculation pipe (9);
Circulation pump (
A flotation unit (21) is connected to the outlet of the flotation unit 1-(21), and a sludge discharge pump (30) and a pump (30) for discharging sludge water are connected to the flotation unit 1-(21), respectively.
28) with a sludge collector (25) and a treated water tank (
23), a pump (28, 30) for discharging sludge and discharging purified water, and an I/pel meter (2, 3) for the upper and lower water levels in the sewage tank, respectively.
and a control section (35) electrically connected to the control section (35), further electrically connected to the control section (35) and connected to the intake pipe (8) and the inlet of the circulation pump (14). the outlet of the circulation pump (14) is directly connected to a pipe (9) for recirculating untreated wastewater; ) Vct pneumatically connected self-closing valve (19)
The wastewater treatment apparatus is characterized in that the circulation pump (14), the flotation unit, ) (21) are disposed between the circulation pump (14) and the discharge pipe (18). (2) The wastewater intake unit (1) includes a casing (6) which is fastened to the front surface of the net (7) and has one wastewater passage phase opening in its F blade part, and the wastewater intake unit (1) The screen (7) is inclined at an angle of 30 to 40 degrees to the wastewater flow path, so that the flow of untreated wastewater supplied by the circulation pump (14) passes through the screen 1) and the casing (6). ) to 1
Claim 1(r): The waste water treatment device is characterized in that it acts on the surface of the net (7) and washes the pollutants therefrom.
JP58090874A 1982-09-07 1983-05-25 Waste water disposal plant Granted JPS5949897A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
SU3482401 1982-09-07
SU823482401A SU1101414A1 (en) 1982-09-07 1982-09-07 Apparatus for treating effluents

Publications (2)

Publication Number Publication Date
JPS5949897A true JPS5949897A (en) 1984-03-22
JPS6333440B2 JPS6333440B2 (en) 1988-07-05

Family

ID=21026307

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58090874A Granted JPS5949897A (en) 1982-09-07 1983-05-25 Waste water disposal plant

Country Status (6)

Country Link
JP (1) JPS5949897A (en)
DD (1) DD242938A3 (en)
DE (1) DE3315193A1 (en)
FI (1) FI72955C (en)
SE (1) SE449860B (en)
SU (1) SU1101414A1 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113041684A (en) * 2021-03-29 2021-06-29 内蒙古工业大学 A chemical wastewater solid-liquid separation device
CN113209702A (en) * 2021-06-09 2021-08-06 北京市城远市政工程有限责任公司 Construction process of municipal sewage purification system
CN113209702B (en) * 2021-06-09 2022-07-12 北京市城远市政工程有限责任公司 Municipal sewage treatment device

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SE8302438L (en) 1984-03-08
FI831455L (en) 1984-03-08
SE8302438D0 (en) 1983-04-29
DD242938A3 (en) 1987-02-18
FI72955C (en) 1987-08-10
DE3315193C2 (en) 1988-03-24
FI72955B (en) 1987-04-30
DE3315193A1 (en) 1984-03-08
SE449860B (en) 1987-05-25
JPS6333440B2 (en) 1988-07-05
SU1101414A1 (en) 1984-07-07
FI831455A0 (en) 1983-04-28

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