JPH09328093A - Sewage treatment equipment for ship or the like - Google Patents

Sewage treatment equipment for ship or the like

Info

Publication number
JPH09328093A
JPH09328093A JP16873096A JP16873096A JPH09328093A JP H09328093 A JPH09328093 A JP H09328093A JP 16873096 A JP16873096 A JP 16873096A JP 16873096 A JP16873096 A JP 16873096A JP H09328093 A JPH09328093 A JP H09328093A
Authority
JP
Japan
Prior art keywords
chamber
water
catalytic oxidation
air
water level
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP16873096A
Other languages
Japanese (ja)
Inventor
Tsuneo Takashina
経雄 高階
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.)
GOKOU SEISAKUSHO KK
Original Assignee
GOKOU SEISAKUSHO KK
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 GOKOU SEISAKUSHO KK filed Critical GOKOU SEISAKUSHO KK
Priority to JP16873096A priority Critical patent/JPH09328093A/en
Publication of JPH09328093A publication Critical patent/JPH09328093A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Abstract

PROBLEM TO BE SOLVED: To prevent the ocean from being contaminated by disposer waste water of high concentration by respectively providing an aeration air pipe communicated with pressure air source in a pre-treatment chamber and an aeration air pipe communicated with a pressure air source and a contact oxidization plate in a contact oxidization chamber. SOLUTION: A treatment tank 7 is filled with water beforehand, and waste water of high concentration discharged from a disposer is introduced to a pre- treatment chamber 8. On the other hand, pressure air from an air pipe 20 is supplied to an aeration air pipe 14, continuously jetted out into water from small holes after being changed into bubbles, water articles are broken by aeration action, a number of aerobic microbes are produced by the supplying of oxygen and organic materials are decomposed into carbonic acid gas and water. Also, contact oxidization plates 19 are arrayed on the full width of a first contact oxidization chamber 9, bubbles are divided into small pieces by clashing with a number of wrinkles, the concentration of oxygen solved in water is increased, aerobic microbes are produced in the contact oxidization plates 19 in a film shape and cleaning efficiency is improved by adding oxygen thereto.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本願発明は、船舶や艦船の生
活用雑廃水の処理装置であって、特に海洋の汚染を防止
する装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for treating domestic waste water for ships and ships, and more particularly to an apparatus for preventing marine pollution.

【0002】[0002]

【従来の技術】従来は、船舶や艦船における生活用雑廃
水は、生ごみや残飯などをデスポーザで粉砕した高濃度
の雑廃水をそのまま海中に投棄していた。
2. Description of the Related Art Conventionally, as domestic miscellaneous wastewater on ships and ships, high-concentration miscellaneous wastewater obtained by crushing food waste, leftover food and the like with a desposer was thrown into the sea as it is.

【0003】[0003]

【発明が解決しようとする課題】従って、このように高
濃度のデスポーザ廃水をそのまま海中に投棄すること
は、海洋を汚染するという環境上の問題があった。そこ
で、本願は上記した問題を解決することを特徴とするも
のである。
Therefore, the dumping of high-concentration desposer wastewater into the sea as it is has an environmental problem of polluting the ocean. Therefore, the present application is characterized by solving the above-mentioned problems.

【0004】[0004]

【課題を解決するための手段】本願は上記した目的を解
決するために、処理槽内の流れの方向に沿って、デスポ
ーザ廃水などの高濃度の雑廃水を受容し、かつ、上方が
開いた前処理室と、上方及び下方が開いた接触酸化室
と、この接触酸化室と下方が連通し、かつ、上方が開い
た沈澱室と、上部に濾過室を備え、かつ、水位制御器に
より水位が制御されると共に、放出管と連通した水位制
御室とを順次連設すると共に、前記前処理室内に、加圧
空気源と連通した暴気用空気管を、また前記接触酸化室
内に加圧空気源と連通した暴気用空気管及び接触酸化板
をそれぞれ配設したことを特徴とするものであり、好ま
しくは、前処理室と接触酸化室との間に、内部に加圧空
気源と連通した暴気用空気管と接触酸化板とを配設した
上方で開く前段接触酸化室を設ける。また上記におい
て、浄化作用を高めるために、暴気用空気管を、それぞ
れ各室の流れ方向の手前側に寄せて配設して成り、ま
た、処理槽外にバクテリア液タンクを備え、該タンクと
前段接触酸化室とを定量ポンプを介して連通する。さら
にまた低濃度の雑廃水を処理するために、水位制御室
に、手洗器などから排出される低濃度廃水を供給する流
入管を接続して成るものである。
In order to solve the above-mentioned object, the present application receives high-concentration miscellaneous wastewater such as desposer wastewater along the direction of flow in a treatment tank, and opens upward. The pretreatment chamber, the catalytic oxidation chamber whose upper and lower sides are open, the catalytic oxidation chamber communicating with the lower side, and the precipitation chamber whose upper side is open, and the filtration chamber on the upper side, and the water level controller controls the water level. Is controlled, and a water level control chamber communicating with the discharge pipe is sequentially installed, and an air pipe for assault communicating with a pressurized air source is further provided in the pretreatment chamber, and the contact oxidation chamber is also pressurized. It is characterized by disposing an air pipe for turbulence and a contact oxidation plate which are in communication with an air source, preferably, between the pretreatment chamber and the contact oxidation chamber, a pressurized air source inside and Pre-stage contact that opens above with a communicating air tube for air and a contact oxidation plate Providing an ionization chamber. Further, in the above, in order to enhance the purifying action, the air pipes for aeration are arranged close to the front side in the flow direction of the respective chambers, and a bacterial liquid tank is provided outside the treatment tank. And the pre-stage catalytic oxidation chamber are connected via a metering pump. Furthermore, in order to treat low-concentration miscellaneous wastewater, an inflow pipe for supplying low-concentration wastewater discharged from a handwasher or the like is connected to the water level control chamber.

【0005】[0005]

【発明の実施の形態】以下図面に基づいて、本願の実施
例を詳述すると、図1は船室の床1にデスポーザ2と手
洗器3、浴槽4、洗面器5、洗濯機6などを装備した場
合の構成を示しており、実際上は、これらの機器は、使
用人員に比例して設けられ、従ってそれらの機器から生
じる廃水量も使用人員にほぼ比例する。7は、床1の下
方位置に装備された処理槽であって、こ処理槽7は内部
に、流れの方向に沿って前処理室8と、第一接触酸化室
9と、第二接触酸化室10と、沈澱室11と、濾過室2
4を上部に備えた水位制御室12とを順次連続して設け
てあり、前処理室8は処理槽7の図中左側壁7a及びこ
れと対峙すると共に、下方が閉じて上方が開いた仕切壁
17によって形成され、該処理室8の上部には太径の雑
廃水管13と排気支管15aとが夫々接続してあり、前
記雑廃水管13には、開閉弁V1を介してデスポーザ
2、手洗器3などからの廃水支管13aが夫々接続して
あると共に、排気支管15aは排気ブロワ16を接続し
た排気管15に接続してある。また前処理室8の内底部
には、処理槽7の外部に設けられたエアーブロワ33に
エアーパイプ41を介して接続され、かつ、小穴を多数
配設した前後方向(流れ方向と直角方向)に延びる暴気
用空気管14が設けてある。
BEST MODE FOR CARRYING OUT THE INVENTION Referring to the drawings, an embodiment of the present invention will be described in detail. FIG. 1 shows a floor 1 of a cabin equipped with a desposer 2, a handwasher 3, a bathtub 4, a washbasin 5, a washing machine 6 and the like. The configuration is shown in the case of doing so, and in reality, these devices are provided in proportion to the number of users, and therefore the amount of waste water generated from those devices is also approximately proportional to the number of users. Reference numeral 7 denotes a treatment tank installed at a lower position of the floor 1. The treatment tank 7 has therein a pretreatment chamber 8, a first catalytic oxidation chamber 9, and a second catalytic oxidation chamber along the flow direction. Chamber 10, settling chamber 11 and filtration chamber 2
A water level control chamber 12 having an upper portion 4 is sequentially provided continuously, and the pretreatment chamber 8 faces the left side wall 7a of the treatment tank 7 in the drawing and the partition wall, and the lower portion is closed and the upper portion is opened. A thick waste water pipe 13 and an exhaust branch pipe 15a which are formed by a wall 17 are connected to the upper portion of the processing chamber 8, and the waste water pipe 13 is connected to the desposer 2 via an opening / closing valve V1. Waste water branch pipes 13a from the hand washing device 3 and the like are connected to each other, and an exhaust branch pipe 15a is connected to an exhaust pipe 15 to which an exhaust blower 16 is connected. Further, in the inner bottom portion of the pretreatment chamber 8, an air blower 33 provided outside the treatment tank 7 is connected via an air pipe 41, and a large number of small holes are provided in the front-back direction (direction perpendicular to the flow direction). An air tube 14 for aerial air that extends to the bottom is provided.

【0006】前記第一接触酸化室9は、前記仕切壁17
及びこれと対峙し、かつ、下方が閉じて上方が前記仕切
壁17よりも若干大きく開いた仕切壁18によって形成
され、内部には、前後方向に延び、かつ、表面積が広く
なるようにひだを有した塩化ビニールなどより成る多数
の接触酸化板19が左右方向で並行するように全幅にわ
たって配列されていると共に、内底部には前記エアーブ
ロワ33にエアーパイプ41を介して接続され、かつ、
小穴aを多数配設した前後方向に延びる暴気用空気管2
0が設けてある。
The first catalytic oxidation chamber 9 has a partition wall 17
It is formed by a partition wall 18 which is opposed to the partition wall and which is closed at the lower side and is opened at the upper side slightly larger than the partition wall 17, and is internally provided with a fold so as to extend in the front-rear direction and to have a large surface area. A large number of contact oxidation plates 19 made of vinyl chloride or the like are arranged over the entire width so as to be parallel to each other in the left-right direction, and are connected to the air blower 33 through the air pipe 41 at the inner bottom portion, and
An aerial air tube 2 extending in the front-rear direction and provided with a number of small holes a
0 is provided.

【0007】前記第二接触酸化室10は前記仕切壁18
及びこれと対峙し、かつ、上方と下方が夫々開いた仕切
壁21によって形成され、内部に前記接触酸化板19と
同様にひだを有した塩化ビニールなどより成る多数の接
触酸化板22が並行するように全幅にわたって配列され
ると共に、内底部には、前記エアーブロワ33とエアー
パイプ41を介して接続され、かつ、小穴を多数配設し
た前後方向に延びる暴気用空気管23が設けてある。
The second catalytic oxidation chamber 10 has the partition wall 18
And a large number of contact oxidation plates 22 made of vinyl chloride or the like which are formed by a partition wall 21 which is opposed to the partition wall 21 and which is open at the upper and lower sides, and which has a fold like the contact oxidation plate 19 inside. The air blower 33 is arranged over the entire width and is connected to the air blower 33 through the air pipe 41, and has an aerial air pipe 23 having a large number of small holes and extending in the front-rear direction. .

【0008】前記沈澱室11は、前記仕切壁21及びこ
れと対峙し、かつ、上方が前記仕切壁21よりも若干大
きく開いて下方が閉じた仕切壁25によって形成された
下部が前記第二接触酸化室10と連通する静水室から構
成されている。
The settling chamber 11 faces the partition wall 21 and the partition wall 21, and a lower part formed by a partition wall 25 which is opened a little larger than the partition wall 21 and is closed lower part is the second contact. It is composed of a still water chamber that communicates with the oxidation chamber 10.

【0009】前記濾過室24は前記仕切壁25の上部及
びこれと対峙し、かつ、上方と下方が夫々開いた仕切壁
26によって形成されると共に、下部には、多孔板28
が仕切板25と仕切板26間に取り外し可能に固定さ
れ、かつ、内部にはホーラチップなどの濾過材27が収
納してある。また濾過室24の上部には、排気管15と
連通する排気支管15bが、接続されている。
The filtration chamber 24 is formed by an upper portion of the partition wall 25 and a partition wall 26 which faces the partition wall 25 and which is open at the upper side and the lower side, and has a porous plate 28 at the lower side.
Is detachably fixed between the partition plate 25 and the partition plate 26, and a filter material 27 such as a hora chip is housed inside. An exhaust branch pipe 15b communicating with the exhaust pipe 15 is connected to the upper portion of the filtration chamber 24.

【0010】前記水位制御室12は、前記仕切壁25及
び処理槽7の図中右側壁7bとによって形成された前記
濾過室24よりの濾過水を貯留する室であって、内部に
は、深さ方向に沿って浮子スイッチ式の水位制御器2
9,30,31が夫々段階的に隔設してあり、これによ
ってその水位が制御される。
The water level control chamber 12 is a chamber which is formed by the partition wall 25 and the right side wall 7b of the processing tank 7 in the figure and stores the filtered water from the filtration chamber 24. Float switch type water level controller 2 along the vertical direction
9, 30, and 31 are respectively separated in stages, and the water level is controlled by this.

【0011】水位制御室12の上部には、浴槽4、手洗
器3、洗面器5、洗濯機6などよりの比較的低濃度廃水
が流入する流入管42を常時開の閉止弁V2を介して接
続した流入口32及びオーバーフロー管43を接続した
流出口34が夫々設けてあり、前記流入管42には手洗
器3などの流入支管42aが常時開の閉止弁V3を介し
て夫々接続され、また、このオーバーフロー管43は、
逆止弁V4,V5を介して廃水を船外に放出する放水管4
4に接続してある。
Above the water level control chamber 12, an inflow pipe 42 into which relatively low-concentration wastewater from the bathtub 4, handwasher 3, washbasin 5, washing machine 6, etc. flows in is provided with a normally-open stop valve V2. An inflow port 32 connected thereto and an outflow port 34 connected to an overflow pipe 43 are respectively provided, and an inflow branch pipe 42a such as the hand washing device 3 is connected to the inflow pipe 42 via a normally open stop valve V3, and , This overflow pipe 43
Water discharge pipe 4 for discharging wastewater to the outside of the ship via check valves V4 and V5
4 is connected.

【0012】前記前処理室8の底部には、常時閉の排出
弁V6が設けられ、これが連結管35及び常時開の閉止
弁V7を介して排水ポンプ36に接続されている。さら
に前記第一接触酸化室9と第二接触酸化室10との底部
にも、夫々常時開の排出弁V8,V9が、また前記水位制
御室12の底部にも常時開の排出弁V10が夫々設けてあ
り、これらが前記連結管35及び常時開の閉止弁V7を
介して、排水ポンプ36と接続されている。
A normally closed discharge valve V6 is provided at the bottom of the pretreatment chamber 8 and is connected to a drain pump 36 through a connecting pipe 35 and a normally open stop valve V7. Further, normally open discharge valves V8 and V9 are provided at the bottoms of the first catalytic oxidation chamber 9 and the second catalytic oxidation chamber 10, respectively, and normally open discharge valves V10 are also provided at the bottom of the water level control chamber 12. These are provided, and these are connected to the drainage pump 36 through the connecting pipe 35 and the normally open stop valve V7.

【0013】前記排水ポンプ36には圧力計37及び常
時閉の閉止弁V11及び逆止弁V12を接続した放水管44
に接続してあると共に、連結管35には前記閉止弁V7
と流れ方向の反対側位置に常時閉の閉止弁V13が設けて
あり、これが船舶の給水管45と接続されている。また
処理槽7の外部にはバクテリア液を内蔵したタンク38
が配置されており、該タンク38からバクテリア液が定
量ポンプ39によって、毎日1回程度定量のバクテリア
液を、第一接触酸化室9の上部の注入口40より注入さ
れる。
The drainage pump 36 is connected with a pressure gauge 37, a normally closed shutoff valve V11 and a check valve V12, and a water discharge pipe 44.
Is connected to the connecting pipe 35, and the stop valve V7 is connected to the connecting pipe 35.
A normally-closed shut-off valve V13 is provided at a position opposite to the flow direction and is connected to a water supply pipe 45 of the ship. In addition, a tank 38 containing a bacterial solution is provided outside the processing tank 7.
Is arranged, and a fixed amount of the bacterial solution is injected from the tank 38 by the constant amount pump 39 once a day through the inlet 40 at the upper part of the first catalytic oxidation chamber 9.

【0014】しかして使用に際し、処理槽7内を予め満
水状態としておき、この状態で食堂や調理室に設置され
ているデスポーザ2により排出される残飯や野菜くずな
どの粉砕物即ちデスポーザ2により排出される高濃度の
雑廃水を、廃水支管13aを介して雑廃水管13により
前処理室8に流入する。一方、エアーブロワ33は処理
槽7の使用中は24時間連続で運転され、加圧空気は調
整弁V15、圧力計46及びエアーパイプ41を経て、暴
気用空気管14に供給され、加圧空気は小穴から気泡と
なって、水中に連続して噴出し、この暴気作用によって
廃物は粉砕されると共に酸素の供給がなされて好気性微
生物が多数発生し、これにより有機物が炭酸ガスと水に
分解される。
In use, however, the treatment tank 7 is filled with water in advance, and in this state, it is discharged by a crushed product such as leftover food and vegetable scraps, that is, a desposer 2 which is discharged by a desposer 2 installed in a dining room or a cooking room. The high-concentration miscellaneous wastewater thus generated flows into the pretreatment chamber 8 through the miscellaneous wastewater pipe 13 via the wastewater branch pipe 13a. On the other hand, the air blower 33 is continuously operated for 24 hours while the processing tank 7 is in use, and the pressurized air is supplied to the aerial air pipe 14 through the regulating valve V15, the pressure gauge 46 and the air pipe 41 to pressurize the air. Air becomes bubbles from small holes and is continuously ejected into the water.By this aerobic effect, waste is crushed and oxygen is supplied, and a large number of aerobic microorganisms are generated, whereby organic matter becomes carbon dioxide and water. Is decomposed into.

【0015】上記において、暴気用空気管14を図示す
るように、前処理室8の流れ方向の手前側に寄せて設け
ることにより、気泡が上昇するとき、室内を回流する水
流に乗じて繰り返し酸素の供給がなされる。
In the above description, the aerating air pipe 14 is provided close to the front side in the flow direction of the pretreatment chamber 8 as shown in the drawing, so that when bubbles rise, the air flow for circulating the air in the pretreatment chamber 8 is repeated. Oxygen is supplied.

【0016】前処理室8をあふれた水は、仕切壁17を
越えて第一接触酸化室9に流入し、該室9においても前
記と同様に、その内底部に空気管20が配設してあるこ
とにより、その小穴から噴出する気泡の暴気作用によっ
て好気性微生物が多数発生すると共に、該第一接触酸化
室9内の全幅にわたって、接触酸化板19が配列してあ
るので気泡はその間を上昇し、また、接触酸化板19は
多数のしわを有するので、気泡はこのしわに衝突して細
分されて、水中に溶解する酸素濃度を高め、かつ、接触
酸化板19に好気性微生物を膜状に発生せしめ、これに
酸素を与えて浄化効率を著しく高める。
The water overflowing the pretreatment chamber 8 flows into the first catalytic oxidation chamber 9 over the partition wall 17, and in this chamber 9 as well, the air pipe 20 is arranged at the inner bottom portion thereof. Due to the presence of air bubbles, a large number of aerobic microorganisms are generated by the aerobic action of the bubbles ejected from the small holes, and the contact oxidation plates 19 are arranged over the entire width of the first catalytic oxidation chamber 9, so that the bubbles are present between them. In addition, since the catalytic oxidation plate 19 has many wrinkles, the bubbles collide with the wrinkles and are subdivided to increase the concentration of oxygen dissolved in the water, and the catalytic oxidation plate 19 contains aerobic microorganisms. It is generated in the form of a film and oxygen is given to this to remarkably enhance the purification efficiency.

【0017】さらに、暴気用空気管20を図示するよう
に第一接触酸化室9の流れ方向の手前側に寄せて設ける
ことによって、気泡が接触酸化板19間を上昇すると
き、室内を回流する水流に乗じて繰り返し、廃水の栄養
分(BOD成分)を接触酸化板19の表面に存在してい
る微生物に与えて浄化する。
Further, as shown in the figure, the air pipe 20 for turbulent air is provided close to the front side in the flow direction of the first catalytic oxidation chamber 9, so that when air bubbles rise between the catalytic oxidation plates 19, they are circulated in the chamber. The wastewater nutrient (BOD component) is repeatedly supplied to the microorganisms existing on the surface of the catalytic oxidation plate 19 to purify it.

【0018】この浄化作用は、第二接触酸化室10にお
いても同様に行なわれるが、該室10においては、下部
が沈澱室11と連通しており、沈澱室11は水が静止し
た状態にあるので、沈澱室11において固形分は沈澱分
離され、浄化水のみが上部より仕切壁25を越えて濾過
室24に流入する。濾過室24には、木質の多孔質のチ
ップ(ホーラチップ)などの濾過材27が充填してあ
り、この濾過材27による多孔質の空隙によって濾過室
24に流入した浄化水は濾過される。そして、空隙に残
留した固形分は、発生した微生物によって捕食されるの
で、水質は更に浄化されると共に、目詰まりを防止す
る。
This purifying action is similarly performed in the second catalytic oxidation chamber 10, but in the chamber 10, the lower part is in communication with the precipitation chamber 11, and the precipitation chamber 11 is in a state where water is stationary. Therefore, the solid content is precipitated and separated in the precipitation chamber 11, and only the purified water flows into the filtration chamber 24 from the upper part over the partition wall 25. The filter chamber 24 is filled with a filter material 27 such as wood porous chips (hola chips), and the purified water that has flowed into the filter chamber 24 is filtered by the porous voids of the filter material 27. Then, the solid content remaining in the voids is eaten by the generated microorganisms, so that the water quality is further purified and clogging is prevented.

【0019】濾過材27によって濾過された浄化水は多
孔板28により水位制御室12内に流下する。この水位
制御室12には、浮子式スイッチが深さ方向に段階的に
設けてあり、ポンプの運転開始の水位Mにまで水が溜ま
ると、中間位置の水位制御器29がONとなり、排水ポ
ンプ36が運転されると共に排出弁V10が開弁し、閉止
弁V7を介して水位制御室12内の水は放水管44によ
り船外に放出され、これにより水位が下がってポンプの
停止の水位Nまで下がると、下位置の水位制御器30が
ONとなって排水ポンプ36が停止すると共に排出弁V
10は閉弁して水の放出は停止する。上記において排水ポ
ンプ36などが故障して水位制御室12内の水位がオー
バー位置Lに達すると、上位置の水位制御器31がON
となって図示しないが警報信号を発する。
The purified water filtered by the filter material 27 flows down into the water level control chamber 12 by the porous plate 28. In this water level control chamber 12, a float type switch is provided stepwise in the depth direction, and when water is accumulated up to the water level M at the start of pump operation, the water level controller 29 at the intermediate position is turned on and the drainage pump 36 is operated and the discharge valve V10 is opened, and the water in the water level control chamber 12 is discharged to the outside of the ship by the water discharge pipe 44 through the shutoff valve V7, which lowers the water level and stops the water level N of the pump. Then, the water level controller 30 at the lower position is turned on, the drainage pump 36 is stopped, and the drain valve V
The valve 10 is closed and the discharge of water is stopped. When the drainage pump 36 or the like malfunctions and the water level in the water level control chamber 12 reaches the over position L, the water level controller 31 at the upper position is turned on.
Although not shown, an alarm signal is issued.

【0020】他方、比較的低濃度の雑廃水、例えば手洗
器3、洗面器5、洗濯機6などから廃水される50pp
m以下の廃水においては、該廃水を水位制御室12の上
部に流入管42により直接流入する。この場合も上記に
述べたように、水位制御器29,30,31により排水
ポンプ36の作動、停止及び警報信号の発生が行われ
る。
On the other hand, 50 pp of waste water having a relatively low concentration, such as hand wash 3, wash basin 5, washing machine 6 and the like.
In the case of waste water of m or less, the waste water directly flows into the upper part of the water level control chamber 12 through the inflow pipe 42. Also in this case, as described above, the water level controllers 29, 30 and 31 operate and stop the drainage pump 36 and generate an alarm signal.

【0021】なお、暴気用空気管14,20及び30よ
り噴出して暴気作用をもたらした空気及び処理槽1内で
発生したガスは排水ブロワ16によって、排気管15か
ら船外の高所に排気される。また、毎日1回程度のバク
テリア液が第一接触酸化室9に定量ポンプ39により自
動的に注入される。また実験結果によれば、入り口位置
のBOD成分が3000〜8000ppmである食品の
デスポーザ廃水の場合、出口位置で50ppm以下に浄
化された。
The air blown out from the aeration air pipes 14, 20 and 30 and causing the aeration action and the gas generated in the treatment tank 1 are discharged from the exhaust pipe 15 to a high place outside the vessel by the drain blower 16. Exhausted to. Further, the bacterial solution is injected into the first catalytic oxidation chamber 9 once a day automatically by the metering pump 39. Further, according to the experimental results, in the case of the food desposer wastewater having a BOD component of 3000 to 8000 ppm at the inlet position, it was purified to 50 ppm or less at the outlet position.

【0022】[0022]

【発明の効果】以上のように本願によれば、処理槽の前
処理部において、暴気作用によって廃棄物を粉砕して排
出浄化を容易にし、且つ、好気性微生物によって、廃水
中の溶解成分を炭酸ガスと水に分解すると共に、次段の
接触酸化室における暴気作用により廃水はさらに分解浄
化されて沈澱室に於て固形分を分離沈澱し、更に、濾過
室において、微生物濾過を行なうことにより、高濃度の
デスポーザ廃水を著しく浄化することができて海洋投棄
においても海洋汚染をもたらす惧れはなく、かつ、接触
酸化板に微生物を固定できるので、船の揺れで水が流出
しても微生物は流出せず性能が維持し得るという利点を
有する。
As described above, according to the present invention, in the pretreatment section of the treatment tank, the waste is crushed by the aerobic action to facilitate the discharge purification, and the aerobic microorganisms dissolve the dissolved components in the wastewater. Is decomposed into carbon dioxide gas and water, and the wastewater is further decomposed and purified by the aerobatic action in the next-stage catalytic oxidation chamber to separate and precipitate solids in the precipitation chamber, and microbial filtration is performed in the filtration chamber. As a result, high-concentration desposer wastewater can be significantly purified, there is no risk of causing marine pollution even at the time of dumping into the sea, and since microorganisms can be fixed on the contact oxidation plate, water will flow out due to shaking of the ship. Also has the advantage that the performance can be maintained without the outflow of microorganisms.

【0013】また請求項2記載の構成によれば、2段の
接触酸化室により分解浄化効率をより高めることがで
き、また、請求項3記載の構成によれば、気泡が水流に
乗じて繰り返し廃水のBOD成分を微生物に与えて浄化
効率を高めることができ、また、請求項4記載の構成に
よれば、バクテリア液タンクより、バクテリア液を注加
することにより、バクテリアが少ない食品廃棄物の場合
でも微生物による浄化作用が促進されると共に、バクテ
リアが多くいればこれを食する大形の原正動物も増加し
て、浄化効率を著しく高めることができ、さらにまた、
請求項5記載の構成によれば、低濃度雑廃水を、水位制
御室に流入させることにより、同一の廃水ポンプで排出
できて、船内のスペースを節約できるなどの利点を有す
る。
According to the second aspect of the present invention, the decomposition and purification efficiency can be further increased by the two-stage catalytic oxidation chamber. Further, according to the third aspect, the bubbles are repeatedly multiplied by the water flow. The BOD component of waste water can be given to microorganisms to enhance purification efficiency, and according to the configuration of claim 4, by pouring the bacterial solution from the bacterial solution tank, food waste containing less bacteria can be obtained. Even in the case where the purification action by microorganisms is promoted, the number of large protozoa eating the bacteria increases, and the purification efficiency can be significantly increased.
According to the configuration of claim 5, low-concentration miscellaneous wastewater can be discharged by the same wastewater pump by flowing into the water level control chamber, which has an advantage that the space in the ship can be saved.

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

【図1】総体図Fig. 1 Overall figure

【図2】要部の断面図FIG. 2 is a sectional view of a main part

【符号の説明】[Explanation of symbols]

2 デスポーザ 3 手洗器 7 処理槽 8 前処理室 9 第一接触酸化室 10 第二接触酸化室 11 沈澱室 12 水位制御室 13 雑廃水管 14,20,23 暴風用空気管 17,18,21,25 仕切壁 19,22 接触酸化板 24 濾過室 29,30,31 水位制御器 33 エアーブロワ 36 排水ポンプ 38 バクテリア液タンク 39 定量ポンプ 42 流入管 44 放出管 2 Desposer 3 Handwasher 7 Treatment tank 8 Pretreatment chamber 9 First contact oxidation chamber 10 Second contact oxidation chamber 11 Precipitation chamber 12 Water level control room 13 Miscellaneous wastewater pipe 14, 20, 23 Storm air pipe 17, 18, 21, 25 Partition Wall 19,22 Contact Oxidation Plate 24 Filtration Chamber 29,30,31 Water Level Controller 33 Air Blower 36 Drain Pump 38 Bacterial Liquid Tank 39 Metering Pump 42 Inflow Pipe 44 Release Pipe

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 処理槽内の流れの方向に沿って、デスポ
ーザ廃水などの高濃度の雑廃水を受容し、かつ、上方が
開いた前処理室と、上方及び下方が開いた接触酸化室
と、この接触酸化室と下方が連通し、かつ、上方が開い
た沈澱室と、上部に濾過室を備え、かつ、水位制御器に
より水位が制御されると共に、放出管と連通した水位制
御室とを順次連設すると共に、前記前処理室内に、加圧
空気源と連通した暴気用空気管を、また前記接触酸化室
内に加圧空気源と連通した暴気用空気管及び接触酸化板
をそれぞれ配設したことを特徴とする船舶などの生活用
雑廃水処理装置。
1. A pretreatment chamber that receives high-concentration miscellaneous wastewater such as desposer wastewater along the direction of flow in a treatment tank and that has a pretreatment chamber that is open at the top and a catalytic oxidation chamber that is open at the top and bottom. A water level control chamber that is in communication with the catalytic oxidation chamber at the bottom and a precipitation chamber that is open at the top and a filtration chamber at the top, and the water level is controlled by a water level controller, and that is in communication with the discharge pipe. And an air pipe for storm air communicating with a pressurized air source in the pretreatment chamber, and an air pipe for storm air and a contact oxidization plate communicating with the pressurized air source in the contact oxidation chamber. A domestic wastewater treatment device for ships and the like, which is characterized by being installed respectively.
【請求項2】 前処理室と接触酸化室との間に、内部に
加圧空気源と連通した暴気用空気管と接触酸化板とを配
設した上方で開く前段接触酸化室を設けて成る請求項1
記載の船舶などの生活用雑廃水処理装置。
2. A pre-stage catalytic oxidation chamber is provided between the pretreatment chamber and the catalytic oxidation chamber, in which a turbulent air tube communicating with a pressurized air source and a catalytic oxidation plate are provided inside and which opens upward. Claim 1 consisting of
Wastewater treatment equipment for daily life such as ships described.
【請求項3】 暴気用空気管を、それぞれ各室の流れ方
向の手前側に寄せて配設して成る請求項1または記載の
船舶などの生活用雑廃水処理装置。
3. The household wastewater treatment device for ships and the like according to claim 1 or 2, wherein the air pipes for storm are arranged close to the front side in the flow direction of each chamber.
【請求項4】 処理槽外にバクテリア液タンクを備え、
該タンクと前段接触酸化室とを定量ポンプを介して連通
して成る請求項2または3記載の船舶などの生活用雑廃
水処理装置。
4. A bacterial liquid tank is provided outside the processing tank,
The household wastewater treatment device for ships and the like according to claim 2 or 3, wherein the tank and the pre-stage catalytic oxidation chamber are communicated with each other via a metering pump.
【請求項5】 水位制御室に、手洗器などから排出され
る低濃度廃水を供給する流入管を接続して成る請求項
1,2,3または4記載の船舶などの生活用雑廃水処理
装置。
5. The household wastewater treatment device for ships and the like according to claim 1, 2, 3 or 4, wherein an inflow pipe for supplying low-concentration wastewater discharged from a handwasher or the like is connected to the water level control room. .
JP16873096A 1996-06-10 1996-06-10 Sewage treatment equipment for ship or the like Pending JPH09328093A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16873096A JPH09328093A (en) 1996-06-10 1996-06-10 Sewage treatment equipment for ship or the like

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16873096A JPH09328093A (en) 1996-06-10 1996-06-10 Sewage treatment equipment for ship or the like

Publications (1)

Publication Number Publication Date
JPH09328093A true JPH09328093A (en) 1997-12-22

Family

ID=15873364

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16873096A Pending JPH09328093A (en) 1996-06-10 1996-06-10 Sewage treatment equipment for ship or the like

Country Status (1)

Country Link
JP (1) JPH09328093A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007054789A (en) * 2005-08-26 2007-03-08 Gokou Seisakusho:Kk Apparatus for treating daily liquid waste material of vessel
CN104648623A (en) * 2013-11-20 2015-05-27 北京易寻方达科技有限责任公司 Marine sewage discharge control device
KR102019195B1 (en) * 2018-05-29 2019-09-06 창원환경산업 주식회사 Apparatus for on-site treating night soil in vessels

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007054789A (en) * 2005-08-26 2007-03-08 Gokou Seisakusho:Kk Apparatus for treating daily liquid waste material of vessel
JP4589203B2 (en) * 2005-08-26 2010-12-01 株式会社五光製作所 Liquid waste treatment equipment for ship life
CN104648623A (en) * 2013-11-20 2015-05-27 北京易寻方达科技有限责任公司 Marine sewage discharge control device
KR102019195B1 (en) * 2018-05-29 2019-09-06 창원환경산업 주식회사 Apparatus for on-site treating night soil in vessels

Similar Documents

Publication Publication Date Title
US6383369B2 (en) Waste and wastewater treatment and recycling system
CA1072018A (en) Ship waste water treating with flotation and membrane permeation
US6207047B1 (en) Wastewater treatment system
BG103743A (en) System for the treatment of residential waste waters
KR20010039527A (en) Method and device for purifying and/or treating communal and/or industrial waste water
JPH09328093A (en) Sewage treatment equipment for ship or the like
US3311239A (en) Aerobic waste treatment system
JP4589203B2 (en) Liquid waste treatment equipment for ship life
US3899423A (en) Sewage treatment system
JP2011245916A (en) Sanitary sewage decomposition treatment device for ships
JP5171800B2 (en) Manure purification equipment
USRE26931E (en) Aerobic waste treatment system
JP3343611B2 (en) Wastewater treatment equipment for food processing
JP5444449B2 (en) Manure purification equipment
JPS60193596A (en) Treating apparatus of sewage
JP2005163411A (en) Circulating flush toilet system
JPS6019097A (en) Sewage treating apparatus
JPS586555B2 (en) human waste septic tank
US3817848A (en) Effluent treatment
KR101592066B1 (en) Strong alkaline water and anions hydroxyl radicals preserving decomposition using the device
JP3473377B2 (en) Control structure of garbage processing equipment
JPS6010714Y2 (en) septic tank
JP2003200182A (en) Cleaning treatment device and cleaning treatment method
JPS6110797Y2 (en)
JPH05253595A (en) Apparatus for treating organic waste