JPS6333440B2 - - Google Patents
Info
- Publication number
- JPS6333440B2 JPS6333440B2 JP58090874A JP9087483A JPS6333440B2 JP S6333440 B2 JPS6333440 B2 JP S6333440B2 JP 58090874 A JP58090874 A JP 58090874A JP 9087483 A JP9087483 A JP 9087483A JP S6333440 B2 JPS6333440 B2 JP S6333440B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- wastewater
- pipe
- circulation pump
- unit
- 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
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 117
- 239000002351 wastewater Substances 0.000 claims description 78
- 239000010802 sludge Substances 0.000 claims description 25
- 238000005188 flotation Methods 0.000 claims description 22
- 239000010865 sewage Substances 0.000 claims description 17
- 238000004065 wastewater treatment Methods 0.000 claims description 17
- 239000008213 purified water Substances 0.000 claims description 12
- 238000007599 discharging Methods 0.000 claims description 7
- 238000000746 purification Methods 0.000 claims description 7
- 230000003134 recirculating effect Effects 0.000 claims description 6
- 238000004891 communication Methods 0.000 claims description 3
- 238000004064 recycling Methods 0.000 claims description 2
- 239000000356 contaminant Substances 0.000 description 13
- 238000004140 cleaning Methods 0.000 description 6
- 239000007787 solid Substances 0.000 description 6
- 238000005202 decontamination Methods 0.000 description 4
- 230000003588 decontaminative effect Effects 0.000 description 4
- 230000005484 gravity Effects 0.000 description 3
- 239000012528 membrane Substances 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- 238000005352 clarification Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000011010 flushing procedure Methods 0.000 description 2
- 230000000717 retained effect Effects 0.000 description 2
- 230000001154 acute effect Effects 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000000701 coagulant Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000002427 irreversible effect Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 238000007790 scraping Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 230000009469 supplementation Effects 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/006—Regulation methods for biological treatment
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/24—Treatment of water, waste water, or sewage by flotation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/005—Black water originating from toilets
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/001—Build 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)
Description
【発明の詳細な説明】
本発明は概して廃水浄化処理技術に関し、更に
特別に下水処理装置に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates generally to wastewater purification technology, and more particularly to sewage treatment equipment.
本発明の特徴を実施化した装置は船舶又は下水
道本管に連結されていない建物及び建造物の廃水
処理に適用可能である。 Devices embodying features of the invention are applicable to the treatment of wastewater in ships or buildings and structures not connected to sewer mains.
現在、生活圏汚染問題は全世界的関心を喚起し
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、湖沼及び海洋へ投棄され
た船舶廃棄物の量を著しく増大させ、結果とし
て、廃水浄化、汚染除去装置を装備していない船
舶を領海から閉め出す措置を世界の諸国がとる事
態を招いた。「廃棄物、その他による海洋汚染防
止に関する協定」に依れば、船舶はそうした浄化
汚染除去装置を備えなければならない。現代の船
舶工学は船内廃水処理設備の自動的操縦を提供し
ている。従つて船内廃水の浄化と汚染除去のため
の、高性能且つ故障のない装置の発展に多大の関
心が寄せられている。建造中の船舶に適用可能な
廃水処理装置は現在多数知られている。しかし、
前述の協定の条件によれば、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容量の下水槽のみ
を備えた古い船舶に改良された設計の廃水処理方
式を装備するという問題を提起している。このよ
うな方式は広大な床面積を必要とし、一般に船内
下水槽とは別に設置されなければならない。 At present, the problem of pollution in living spaces is arousing worldwide attention. 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 significantly increased the amount of ship waste dumped into rivers, lakes, and oceans, and as a result, countries around the world have taken measures to exclude ships that are not equipped with wastewater purification and decontamination equipment from their territorial waters. This led to a situation where According to the Agreement on the Prevention of Marine Pollution from Waste and Other Sources, ships must be equipped with such purification and decontamination equipment. Modern marine engineering provides automatic steering of onboard wastewater treatment equipment. Accordingly, there is great interest in developing high performance and trouble-free equipment for the purification and decontamination of shipboard wastewater. Many wastewater treatment devices are currently known that can be applied to ships under construction. but,
Under the terms of the aforementioned agreement, both new and existing ships must be equipped with such wastewater treatment equipment, so this requirement usually applies to older ships with only limited capacity sewage tanks for improved designs. This raises the issue of equipping wastewater treatment methods. Such systems require extensive floor space and generally must be installed separately from the ship's sewage tanks.
「ネプテイマテイクーレトロ」として知られる
サレン・バテンノード社の廃水処理装置(1979年
7月16日発行、サレン・バテンノード、パンフレ
ツト第1号参照)が広く使用されているが、該装
置は船内下水槽内の上槽及び下層水位のレベル計
を含み、これらのレベル計から信号を受けると、
これに応じて該装置のスイツチを開閉する。該下
水槽は取水ユニツトをも擁し、このユニツトの廃
水の流入に面する先端部は取水ユニツトのハウジ
ングの壁と廃水の流れに対して垂直にある網で覆
われている。取水ユニツトの内側壁に取水管と未
処理水を再循環させる管を設ける。取水管は循環
ポンプの吸引端と連結する。該循環ポンプの圧力
端部は圧力管、圧力タンク及び一定の圧力供給管
を経て浮選ユニツトと通じ、該浮選ユニツトにお
いて廃水が浄化される。圧力タンクは未処理廃水
を再循環する管とも連絡している。圧力タンクに
廃水再循環管を連結する配管に排出器が設置さ
れ、この排出器は取水管を通過する水に通気する
よう意図される。該排出器はスラツジ収集器の気
相部分及び浄化水槽と連絡可能である。定量供給
圧力管は一般的に所定の長さで目盛りを付けた管
であり、廃水を所定の割合で浮選ユニツトに供給
する。 The Saren-Battennod wastewater treatment system known as the "Nepteimate Retro" (see Salen-Battennod, Brochure No. 1, published July 16, 1979) is widely used; It includes level meters for the upper and lower water levels in the water tank, and when it receives signals from these level meters,
The switch of the device is opened and closed accordingly. The sewage tank also has a water intake unit whose end facing the inlet of the wastewater is covered with a screen perpendicular to the wall of the housing of the water intake unit and the flow of the wastewater. An intake pipe and a pipe for recirculating untreated water are installed on the inside wall of the water intake unit. The water intake pipe is connected to the suction end of the circulation pump. The pressure end of the circulation pump communicates via a pressure line, a pressure tank and a pressure supply line with a flotation unit in which the waste water is purified. The pressure tank also communicates with pipes that recirculate untreated wastewater. A drain is installed in the piping connecting the wastewater recirculation pipe to the pressure tank, and this drain is intended to vent the water passing through the intake pipe. The discharger is in communication with the gas phase part of the sludge collector and with the clarification water tank. The metering pressure line is typically a length of graduated tube that supplies wastewater at a predetermined rate to the flotation unit.
FeCl3又はAl2(CO4)3の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。 Reagents such as FeCl 3 or Al 2 (CO 4 ) 3 are injected with a special pump to coagulate contaminants in the wastewater passing through the pressure tube.
浮選ユニツ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パ及び
浄化された水を排出する装置を含む。 The flotation unit includes a vessel for purifying the water, a scraper for removing flotsam formed during wastewater treatment, and a device for discharging the purified water.
該浮選ユニツトはスラツジ排出ポンプを備えた
スラツジ収集器及び浄化水排水ポンプを備えた浄
化水槽と連絡する。該装置は更に循環ポンプ、ス
ラツ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槽中の上層及び下層水
位レベル計を備える。 The flotation unit communicates with a sludge collector with a sludge discharge pump and a clarification tank with a clarified water drainage pump. The device further comprises a control section electrically coupled to a circulation pump, a sludge discharge pump and a purified water discharge pump, and upper and lower water level gauges in the sewage tank.
該装置の稼動中、循環ポンプは取水ユニツトの
ハウジング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ツトの網によ
つて留保される。約2又は3ata(絶対圧)の重圧
力が圧力タンク内で造り出される。圧力タンク内
の約60%の水が未処理廃水再循環管を通つて廃水
取水ユニツトのハウジングに戻される。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量の溶
解していない空気を含んでいる。約40%の廃水が
定量送出圧力管路によつて浮選ユニツトに送り出
される。この管路は目盛付き管として設計されて
いるので、圧力タンク内の一定の水圧下で、該定
量送出圧力管路内の流入量の割合は持続的あるい
は不変である。浮選ユニツトに送り出された水流
に凝固剤を注入し、その浮選ユニツトで重力下浮
選が生ずる。この過程で形成された浮きかすのス
ラツジはスクレーパによつてスラツジ収集器に移
され、他方浄化された水は処理水槽に吸引され
る。水流に汚染除去の溶剤を注入するための装備
もなされている。 During operation of the device, the circulation pump sucks wastewater from the housing of the water intake unit through the intake pipe and conveys the wastewater under pressure to the pressure tank. Large solids carried by the wastewater are then retained by a network of water intake units. A heavy pressure of about 2 or 3 ata (absolute pressure) is created in the pressure tank. Approximately 60% of the water in the pressure tank is returned to the housing of the wastewater intake unit through the raw 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% of the wastewater is delivered to the flotation unit via a metered delivery pressure line. This line is designed as a graduated tube, so that under constant water pressure in the pressure tank, the rate of inflow in the metering pressure line is constant or unchanged. A coagulant is injected into the water stream delivered to a flotation unit where gravity flotation occurs. The sludge of sludge formed in this process is transferred by a scraper to a sludge collector, while the purified water is sucked into a treatment water tank. Provisions are also made to inject decontamination solvents into the water stream.
大きな汚染物が網によつて留保されること、そ
して第1にこれらの大きな固体物が未処理廃水再
循環管を通つて、取水ユニツトに流入する廃水の
還流によつて流されるという事実によつて、上述
の装置は低性能の欠点を免がれない。反面、該網
は作業続行に伴い生ずる固体物で詰まつて来る。
該閉塞の結果、圧力タンクへの廃水送出量が減少
し、他方定量送出圧力管路による浮選ユニツトへ
の圧力タンクからの廃水排出量は一定している。
この為、再循環管を通つて廃水取水ユニツトのハ
ウジングに流入し、該網を流し又は掃除する水の
量は減少し、一層網の詰まりを増大させる。従つ
て循環ポンプによつて圧力タンクに供給される廃
水量は更に減少し、他方定量送出圧力管による圧
力タンクからの廃水排出量の割合は以前の水準を
保持し、これが循環管の還流径路を通つて下水タ
ンクに戻る水流量を再度減少させ、以下同様であ
る。上述の連鎖事象は不可逆であつて、循環ポン
プの故障を招く可能性もある。それを防ぐため、
稼動を中止し、外側の水の流れによつて網を洗わ
なければならない。 This is due to the fact that large contaminants are retained by the screen, and firstly due to the fact that these large solids are carried away by the return flow of wastewater entering the intake unit through the untreated wastewater recirculation pipe. Therefore, the above-mentioned devices suffer from the drawback of low performance. On the other hand, the net becomes clogged with solid matter generated as the work continues.
As a result of the blockage, the amount of waste water delivered to the pressure tank is reduced, while the amount of waste water discharged from the pressure tank to the flotation unit by the metered delivery pressure line remains constant.
This reduces the amount of water that enters the housing of the wastewater intake unit through the recirculation pipe and flushes or cleans the screen, further increasing the likelihood of blockage of the screen. Therefore, the amount of wastewater supplied to the pressure tank by the circulation pump is further reduced, while the proportion of wastewater discharged from the pressure tank by the metering pressure line remains at the previous level, which reduces the return path of the circulation line. The water flow rate through which the water flows back to the sewage tank is again reduced, and so on. The chain of events described above is irreversible and may even lead to failure of the circulation pump. To prevent this,
Operation must be stopped and the net washed with an external stream of water.
廃水取水ユニツトの網のより効果的洗浄によつ
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 screens of wastewater intake units.
この目的は、廃水の流れに沿つてそれぞれ順次
配列された、下水槽内に設けられたハウジングと
廃水の流れに面した該ハウジングの先端部を覆う
網とを有する廃水取水ユニツトと、廃水を取り入
れる取水管及び未処理の廃水を取水ユニツトに戻
す再循環管と、入口が水管によつて該取水管と連
結し出口が未処理の廃水の再循環管に連結する循
環ポンプと、定量送出圧力管路によつて循環ポン
プの出口と連結する浮選ユニツト、共に浮選ユニ
ツトと連絡して、それぞれスラツジ排出ポンプ及
び浄化した水を排出するポンプを有するスラツジ
収集器及び処理水槽、それぞれ該循環ポンプ、ス
ラツジを排出し浄化した水を排出するポンプ及び
下水槽内の上層及び下層水位のレベル計と電気的
に連結された制御区分とを含む廃水処理装置にし
て、さらに該制御区分と電気的に連結され、取水
管と循環ポンプの入口とを連結する水管に配置さ
れた水圧感知器を含む、該循環ポンプの出口は未
処理廃水を再循環させる管に直接連結され、該制
御区分に電気的に連結される自動閉鎖弁を定量送
出管路の循環ポンプ浮選ユニツトの間に配置した
ことを特徴とする該廃水処理装置を提供すること
によつて達せられる。 This purpose consists of a wastewater intake unit having a housing provided in the sewage tank and a net covering the tip of the housing facing the wastewater flow, each arranged sequentially along the wastewater flow; a water intake pipe and a recirculation pipe for returning untreated wastewater to the water unit; a circulation pump whose inlet is connected to the intake pipe by a water pipe and whose outlet is connected to the untreated wastewater recirculation pipe; and a metered delivery pressure pipe. a flotation unit connected by a channel to the outlet of the circulation pump; a sludge collector and a treatment water tank, both having a sludge discharge pump and a pump for discharging purified water, respectively, in communication with the flotation unit; A wastewater treatment device including a control section electrically connected to a pump for discharging sludge and discharging purified water, and a level meter for upper and lower water levels in a sewage tank, and further electrically connected to the control section. including a water pressure sensor located in a water pipe connecting the water intake pipe and the inlet of the circulation pump, the outlet of the circulation pump being connected directly to the pipe recirculating untreated wastewater, and electrically connected to the control section. This is achieved by providing the wastewater treatment device characterized in that a connected self-closing valve is arranged between the circulation pump flotation unit of the metering line.
廃水取水ユニツトは網の前面に緊締され、その
下方部に廃水通過のための開口部を有するケーシ
ングを含むことが望ましく、該取水ユニツトの網
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、循環ポンプによつて供給される未処
理水の流れは網を通過し、ケーシングから反転
し、網の表面に作用してその汚染物質を洗滌す
る。 Preferably, the waste water intake unit includes a casing which is fastened to the front of the screen and has openings in its lower part for the passage of waste water, and the screen of the water intake unit is oriented at an angle of 30 to 40 degrees to the waste water flow path. A stream of untreated water, inclined at an angle and supplied by a circulation pump, passes through the screen, reverses from the casing, and acts on the surface of the screen to wash it of contaminants.
廃水処理のための本装置を使用する場合、人員
が付き添わなくても、より確実な廃水浄化が保証
される。 When using the present device for wastewater treatment, a more reliable purification of wastewater is guaranteed without the need for personnel to be present.
本発明による廃水処理装置は廃水取水ユニツト
1(第1図)、船内下水槽4内の上層水位レベル
計2及び下層水位レベル計3を含む。該取水ユニ
ツト1は全体として符号5で示すハウジングを有
し、その下方側部に開口したケーシング部分6を
備える。廃水の流れに面したハウジング5の端部
は網7で覆われている。該取水ユニツト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
環させるための再循環管9を有する。該取水ユニ
ツト1は又網7を洗うための装置10も設けら
れ、この装置10はハウジング5の内部に設置さ
れ、自動的に作動する進入弁を経て、(明示され
ていない)外側の本水管と連絡する。 The wastewater treatment apparatus according to the present invention includes a wastewater intake unit 1 (FIG. 1), an upper water level gauge 2 and a lower water level gauge 3 in an onboard sewage tank 4. The water intake unit 1 has a housing, generally designated 5, with a casing part 6 open at its lower side. The end of the housing 5 facing the wastewater flow is covered with a screen 7. The water intake unit 1 has an intake pipe 8 for receiving incoming wastewater and a recirculation pipe 9 for recycling untreated wastewater. The water intake unit 1 is also provided with a device 10 for washing the screen 7, which device 10 is installed inside the housing 5 and is connected to the outside main water pipe (not explicitly shown) via an automatically actuated inlet valve. contact.
取水管8は水管12及び弁13を通して循環ポ
ンプ14の入口に連結する。該水管12は水圧感
知器15を収容する。循環ポンプ14は水管16
及び弁17を通して未処理廃水再循環管9と連結
する。水管16は自動作動弁19と流量調整膜2
0を備えた定量送出圧力管路18を介して浮選ユ
ニツト21と連絡する。該浮選ユニツト21は水
管22によつて処理済浄化水槽23と連結し、水
管24を介してフアン26を備えたスラツジ収集
器25と連結する。次に処理済浄化水槽23は水
管27によつて浄化水排出ポンプ28と連結し、
他方スラツジ収集器25はスラツジ排出ポンプ3
0と連結する。スラツジを該スラツジ収集器25
から、弁32を設けた水管31に沿つて下水槽4
へ、若しくは弁34を設けた水管33を経て船上
へ(明示していない)、排出することができる。 The water intake pipe 8 is connected to the inlet of a circulation pump 14 through a water pipe 12 and a valve 13. The water pipe 12 houses a water pressure sensor 15. The circulation pump 14 is a water pipe 16
and is connected to the untreated wastewater recirculation pipe 9 through a valve 17. The water pipe 16 has an automatic operating valve 19 and a flow rate adjustment membrane 2.
It communicates with the flotation unit 21 via a metering pressure line 18 with 0. The flotation unit 21 is connected via a water pipe 22 to a treated clarified water tank 23 and via a water pipe 24 to a sludge collector 25 equipped with a fan 26. Next, the treated purified water tank 23 is connected to a purified water discharge pump 28 via a water pipe 27,
On the other hand, the sludge collector 25 is connected to the sludge discharge pump 3.
Concatenate with 0. The sludge is collected in the sludge collector 25.
From there, a sewage tank 4 is installed along a water pipe 31 equipped with a valve 32.
It can be discharged to the vessel or via a water pipe 33 provided with a valve 34 onto the ship (not explicitly shown).
本装置は更に制御区分35を含み、これは上層
水位レベル計2、下層水位レベル計3、循環ポン
プ14、浄化水排出ポンプ28、スラツジ排出ポ
ンプ30、自動作動弁13,17,19、フアン
26並びに水圧感知器15と電線で連結されてい
る。 The device further includes a control section 35, which includes an upper water level gauge 2, a lower water level gauge 3, a circulation pump 14, a purified water discharge pump 28, a sludge discharge pump 30, automatically operated valves 13, 17, 19, and a fan 26. It is also connected to the water pressure sensor 15 by an electric wire.
取水ユニツト1の網7に詰まつた汚染物に対し
更に際立つた効果を上げ、流入する廃水を洗浄す
る能率を高めるため、網7(第2図)は廃水の流
れに対し30度ないし40度の傾斜で配置され、よつ
て、循環ポンプ14によつて再循環されて取水ユ
ニツト1に流れ込む未処理廃水の流れ36は網7
を通過し、網7の前面に設けられたケーシング6
から反転し、従つて網7の内側、外側両方の表面
に作用して汚染物を網から下水槽の底まで洗い流
す。 In order to have a more pronounced effect on the contaminants clogging the net 7 of the water intake unit 1 and to increase the efficiency of cleaning the incoming wastewater, the net 7 (Fig. 2) is set at an angle of 30 to 40 degrees with respect to the flow of the waste water. The stream 36 of untreated wastewater flowing into the water intake unit 1 after being recirculated by the circulation pump 14 is arranged at an inclination of
The casing 6 provided on the front side of the net 7
It then turns over, thus acting on both the inner and outer surfaces of the screen 7 and flushing the contaminants from the screen to the bottom of the sewage tank.
網7の傾斜角度は30度ないし45度の範囲が望ま
しい。何故なら取水ユニツト1のケーシング6か
ら反転される水流の力と共に、未処理廃水を再循
環させる管9から流入する未処理廃水の水流の力
及び重力が最も効果的になるのはこのような角度
によつてのみ保証されるからである。 The angle of inclination of the net 7 is preferably in the range of 30 degrees to 45 degrees. This is because it is at such an angle that the force of the water flow reversed from the casing 6 of the water intake unit 1, as well as the force and gravity of the water flow of the untreated wastewater entering from the pipe 9 recirculating the raw wastewater, are most effective. This is because it is guaranteed only by
網7の傾斜角度が45度を越えた場合、ケーシン
グ6から反転される水流によつて生ずるこすり取
る力の能率は著しく低下し、他方30度以下では重
力の急激な減少が起り、それによつてケーシング
6から反転される水流は網7の表面から汚染物を
こすり取ることができず、汚染物はさらに固着す
る傾向になる。 If the angle of inclination of the net 7 exceeds 45 degrees, the efficiency of the scraping force generated by the water flow reversed from the casing 6 decreases significantly, while below 30 degrees a sharp decrease in gravity occurs, thereby The water flow reversed from the casing 6 is unable to scrape the contaminants from the surface of the screen 7, and the contaminants tend to stick further.
本発明による廃水処理装置は次に述べるように
作動する。 The wastewater treatment device according to the invention operates as follows.
循環ポンプ14(第1図)は廃水取水ユニツト
1のハウジング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
が運んだ大型の汚染物又は固形物は網7を通過で
きず、他方ケーシング6は廃水中に浮遊する大き
な固体物が網7を通らないよう阻止する。循環ポ
ンプ14の入口に続く水管12中の所定の数値以
下の水圧下で廃水取水ユニツト1のハウジング5
に送られる水の普通の流量では、水圧感知器15
は制御区分35に伝える信号を起さず、従つて定
量送出圧力管路18の弁19は開かない。水管1
6に沿う水流は2つに分れる。流量の少ない部分
(約30%)は定量送出圧力管路18に入り、多い
部分(約70%は)は未処理廃水再循環の管9に還
流する。この水流分離は該定量送出圧力管路18
中に配置された薄膜20によつて確実になる。処
理中の廃水はこの圧力管路18を通過して浮選ユ
ニツト21に達し、ここで最終的に浄化され汚染
除去される。その結果生じたスラツジは浮選ユニ
ツト21から水管22を通つて処理済水槽23へ
と排出される。水管16から廃水取水ユニツト1
のハウジング5に水流が流入し網7から大型の固
体物を洗い流す。 The circulation pump 14 (FIG. 1) sucks wastewater from the housing 5 of the wastewater intake unit 1 through the net 7 and conveys it from the pipe 8 to the water pipe 16. Large contaminants or solids carried by the water flow cannot pass through the screen 7, while the casing 6 prevents large solids suspended in the wastewater from passing through the screen 7. Housing 5 of waste water intake unit 1 under water pressure below a predetermined value in water pipe 12 following the inlet of circulation pump 14
At normal flow rates of water delivered to the water pressure sensor 15
does not generate a signal to the control section 35 and therefore the valve 19 of the metering pressure line 18 does not open. Water pipe 1
The water flow along 6 is divided into two. The lower flow rate (approximately 30%) enters the metering pressure line 18, and the higher flow rate (approximately 70%) returns to the untreated wastewater recirculation line 9. This water flow separation is carried out by the quantitative delivery pressure line 18.
This is ensured by the membrane 20 placed therein. The wastewater being treated passes through this pressure line 18 to the flotation unit 21 where it is finally purified and decontaminated. The resulting sludge is discharged from flotation unit 21 through water pipe 22 to treated water tank 23. Waste water intake unit 1 from water pipe 16
A stream of water flows into the housing 5 and washes away large solid objects from the screen 7.
網7が汚染物によつて詰まり始めると、循環ポ
ンプ前の水管12における水圧が水圧感知器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。弁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て未処理廃水再
循環管9へ水管16を通して入り、そこから水は
廃水取水ユニツト1のハウジング5に戻る。結果
として、水管16によつて送られ網7に向う流量
は激しくなり、網7を効率よく洗い流すことを容
易にして、網から固着した汚染物を除去する。ケ
ーシング6の設置及び再循環水流の方向に対する
網の傾斜が網7の洗滌をさらに容易にしている。
網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)はケーシング6の壁から反転し
て網7の外側表面に対して鋭角度をなして流れ
る。そのため網7を塞ぐ汚染物は2つの側から作
用される。即ち、廃水の還流の流れ36はハウジ
ング5の内側から閉塞物に作用して該網から離れ
させ、他方ケーシング6から反転した流れ36は
網7の外側表面から汚染物をこすり落す傾向にあ
る。このような廃水還流の二重作用が網7の洗浄
効率を非常に高くする。こうして洗浄された網7
は下水槽4から廃水取水ユニツト1への流入率を
促進し、その結果生じた循環ポンプ14の入口
(第1図)における水圧の低下が水圧感知器15
の信号を再び始動させて制御区分35に伝える
と、制御区分35は定量送出圧力管路18の自動
弁19を開き、廃水の流れが浮選ユニツト21に
流入する。 When the screen 7 begins to become clogged with contaminants, the water pressure in the water pipe 12 in front of the circulation pump is detected by the water pressure sensor 15.
actuated to transmit a signal to the control section, which signals the valve 19 of the metering pressure line 18 to close. In the closed state of the valve 19, all water flow drawn up by the circulation pump 14 enters the untreated wastewater recirculation 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 flow of water directed by the water tube 16 toward the screen 7 is intense, facilitating efficient flushing of the screen 7 and removing entrenched contaminants from the screen. The arrangement of the casing 6 and the slope of the screen relative to the direction of the recirculating water flow further facilitate cleaning of the screen 7.
After passing through the open eyes of the screen 7, the recirculating water stream 36 (FIG. 2) turns away from the wall of the casing 6 and flows at an acute angle to the outer surface of the screen 7. The contaminants that block the mesh 7 are therefore acted upon from two sides. That is, the return flow 36 of wastewater acts on blockages from inside the housing 5 and forces them away from the screen, while the reversed flow 36 from the casing 6 tends to scrape contaminants from the outside surface of the screen 7. This dual effect of waste water circulation makes the cleaning efficiency of the net 7 very high. Net 7 cleaned in this way
promotes the inflow rate from the sewage tank 4 to the waste water intake unit 1, and the resulting drop in water pressure at the inlet of the circulation pump 14 (FIG. 1) causes the water pressure sensor 15 to increase.
When the signal is again activated and communicated to the control section 35, the control section 35 opens the automatic valve 19 in the metering pressure line 18 and the wastewater stream enters the flotation unit 21.
浮選ユニツト21内で廃水浄化過程で生じたス
ラツジは水管24によつてスラツジ収集器25に
運ばれ、ここから別の使用のために水管29沿い
にポンプ30によつて吸引される。 The sludge produced during the waste water purification process in the flotation unit 21 is conveyed by a water pipe 24 to a sludge collector 25, from where it is sucked by a pump 30 along a water pipe 29 for further use.
スラツジ収集器はフアン26によつて換気され
る。 The sludge collector is ventilated by a fan 26.
浮選ユニツト21から水管22沿いに処理済水
槽23に運ばれた浄化水は水管27を通つてポン
プ28によつて船上に排出される。 The purified water conveyed from the flotation unit 21 to the treated water tank 23 along the water pipe 22 is discharged onto the ship through the water pipe 27 by a pump 28.
上述の点から、提案の装置を使用することによ
つて、網7が汚染物で詰まつたとき、該装置に組
み込まれたシ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網7を自動的に洗い、
洗浄することが可能である。 In view of the above, it can be seen that by using the proposed device, when the net 7 becomes clogged with contaminants, it does not impede the reliable operation of the system incorporated in the device and does not require the intervention of the crew. Automatically wash the net 7 without
It is possible to wash it.
弁11を開いて洗滌液を網洗滌装置10に供給
することによつても網7を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の入口に水圧の増加が起らない場
合、網洗滌装置10が自動的に作動する。 The screen 7 can also be automatically cleaned by opening the valve 11 and supplying the cleaning liquid to the screen cleaning device 10, and within 3 minutes after starting the automatic valve 19, the inlet of the circulation pump 14 is If no increase in water pressure occurs, 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、本装置の船舶内での使
用は最小限の費用で現存の廃水処理設備への補充
を可能にする。例えば乗組員50名の船舶に対し
1.7cm3の容積とわずか0.7m2の面積しか必要としな
い。その上、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可能
である。 Moreover, since such a device can be easily installed in a relatively small space in a machinery room, its use onboard ships allows for the supplementation of existing wastewater treatment equipment at minimal cost. For example, for a ship with 50 crew members
Requires a volume of 1.7cm 3 and an area of only 0.7m 2 . Moreover, the present system can be operated using the existing sewage tank without disassembling and inspecting the sewage treatment equipment on board.
第1図は本発明による廃水取水ユニツトを備え
た廃水処理装置の機能的線図で、長軸方向の断面
図で示す。第2図は本発明による廃水処理装置の
廃水取水ユニツトの拡大断面図である。
1……廃水取水ユニツト、2……上層水位のレ
ベル計、3……下層水位のレベル計、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
再循環管、10……網洗滌装置、11,13,1
7,19,32,34……自動弁、12,16,
22,24,27,29,31,33……水管、
14……循環ポンプ、15……水圧感知器、18
……定量送出圧力管路、20……流量調整膜、2
1……浮選ユニツト、23……処理済水槽、25
……スラツジ収集器、26……フアン、28……
浄化水排出ポンプ、30……スラツジ排出ポン
プ、35……制御区分。
FIG. 1 is a functional diagram of a wastewater treatment device equipped with a wastewater intake unit according to the invention, shown in longitudinal section. FIG. 2 is an enlarged sectional view of the wastewater intake unit of the wastewater treatment apparatus according to the present invention. 1...Wastewater intake unit, 2...Level meter for upper water level, 3...Level gauge for lower water level, 4...Sewage tank, 5...Housing, 6...Casing, 7...
...Net, 8...Wastewater intake pipe, 9...Untreated wastewater recirculation pipe, 10...Net washing device, 11, 13, 1
7, 19, 32, 34... automatic valve, 12, 16,
22, 24, 27, 29, 31, 33... water pipe,
14...Circulation pump, 15...Water pressure sensor, 18
...Quantitative delivery pressure pipe line, 20...Flow rate adjustment membrane, 2
1...flotation unit, 23...treated water tank, 25
...Sludge Collector, 26...Juan, 28...
Purified water discharge pump, 30...Sludge discharge pump, 35...Control classification.
Claims (1)
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ツト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ツト
1に戻す再循環管9と、入口が水管12によつて
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、定量送出圧力
管路18によつて循環ポンプ14の出口と連結す
る浮選ユニツト21、共に浮選ユニツト21と連
絡して、それぞれスラツジ排出ポンプ30及び浄
化した水を排出するポンプ28を有するスラツジ
収集器25及び処理水槽23、それぞれ該循環ポ
ンプ14、スラツ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
水位のレベル計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させる管9に直接連
結され、該制御区分35に電気的に連結される自
動閉鎖弁19を定量送出管路18の循環ポンプ1
4浮選ユニツト21の間に配置したことを特徴と
する該廃水処理装置。 2 廃水取水ユニツト1が、網7の前面に緊締さ
れその下方部に廃水通過用開口部を有するケーシ
ング6を含み、該取水ユニツト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によつて供給される未処理廃
水の流れが網7を通過し、ケーシング6から反転
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項に記載
の廃水処理装置。[Scope of Claims] 1. Wastewater comprising housings 5 provided in the sewage tank 4 and a net 7 covering the tip of the housing 5 facing the wastewater flow, each sequentially arranged along the wastewater flow. A water intake unit 1, an intake pipe 8 for taking in waste water and a recirculation pipe 9 for returning untreated waste water to the water unit 1, an inlet connected to the intake pipe 8 by a water pipe 12 and an outlet for recycling untreated waste water. A circulation pump 14 connected to the circulation pipe 9 and a flotation unit 21 connected to the outlet of the circulation pump 14 by a metered delivery pressure line 18, both in communication with the flotation unit 21, and a sludge discharge pump 30 and a purification unit, respectively. A sludge collector 25 and a treatment water tank 23 each having a pump 28 for discharging purified water, the circulation pump 14, pumps 28, 30 for discharging sludge and discharging purified water, and level meters for the upper and lower water levels in the sewage tank. 2 and 3 and a control section 35 electrically connected to the control section 35, and a water pipe 12 electrically connected to the control section 35 and connecting the water intake pipe 8 and the inlet of the circulation pump 14. The circulation pump 14 includes a water pressure sensor 15 arranged therein.
The outlet of the circulation pump 1 of the metering line 18 is connected directly to the pipe 9 for recirculating the untreated wastewater, and the self-closing valve 19 is electrically connected to the control section 35.
The wastewater treatment device is arranged between four flotation units 21. 2. The waste water intake unit 1 includes a casing 6 which is fastened to the front side of a screen 7 and has an opening for passage of waste water in its lower part, and the screen 7 of the water intake unit 1 is oriented at 30 degrees to 40 degrees with respect to the flow path of the waste water. The flow of untreated wastewater, which is inclined at an angle of A wastewater treatment device according to claim 1, characterized in that:
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 JPS5949897A (en) | 1984-03-22 |
| JPS6333440B2 true 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) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE10126692B4 (en) * | 2001-06-01 | 2007-08-09 | Burmester, Hans Joachim | Process and installation for the treatment and recycling of bilge water from ship operation |
| DE102008046913B4 (en) * | 2008-09-12 | 2010-08-26 | Hamann Ag | Apparatus for wastewater treatment |
| CN113041684B (en) * | 2021-03-29 | 2022-10-21 | 内蒙古工业大学 | Chemical industry sewage solid-liquid separation equipment |
| 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 |
-
1982
- 1982-09-07 SU SU823482401A patent/SU1101414A1/en active
-
1983
- 1983-04-27 DE DE19833315193 patent/DE3315193A1/en active Granted
- 1983-04-28 FI FI831455A patent/FI72955C/en not_active IP Right Cessation
- 1983-04-29 SE SE8302438A patent/SE449860B/en not_active IP Right Cessation
- 1983-05-25 JP JP58090874A patent/JPS5949897A/en active Granted
- 1983-07-22 DD DD83253290A patent/DD242938A3/en unknown
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5949897A (en) | 1984-03-22 |
| DD242938A3 (en) | 1987-02-18 |
| FI831455A0 (en) | 1983-04-28 |
| DE3315193A1 (en) | 1984-03-08 |
| FI831455L (en) | 1984-03-08 |
| FI72955B (en) | 1987-04-30 |
| SU1101414A1 (en) | 1984-07-07 |
| SE8302438L (en) | 1984-03-08 |
| SE8302438D0 (en) | 1983-04-29 |
| SE449860B (en) | 1987-05-25 |
| DE3315193C2 (en) | 1988-03-24 |
| FI72955C (en) | 1987-08-10 |
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