JPH0612130A - Drainage system for ballast water in oil tank - Google Patents
Drainage system for ballast water in oil tankInfo
- Publication number
- JPH0612130A JPH0612130A JP4189923A JP18992392A JPH0612130A JP H0612130 A JPH0612130 A JP H0612130A JP 4189923 A JP4189923 A JP 4189923A JP 18992392 A JP18992392 A JP 18992392A JP H0612130 A JPH0612130 A JP H0612130A
- Authority
- JP
- Japan
- Prior art keywords
- oil tank
- current
- galvanic anode
- anticorrosion
- ballast water
- 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
Links
Landscapes
- Loading And Unloading Of Fuel Tanks Or Ships (AREA)
- Prevention Of Electric Corrosion (AREA)
- Control Of Non-Electrical Variables (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、陸上、海洋または地下
に設置された石油タンク、もしくはタンカーのスロップ
オイルタンクに溜まるバラスト水等の排水装置に関する
ものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a drainage device for ballast water or the like stored in an oil tank installed on land, in the ocean or underground, or in a slop oil tank of a tanker.
【0002】[0002]
【従来の技術】元々、原油中には若干の水分が混入して
おり、また、タンカーのスロップオイルタンク中にもバ
ラスト水が介在しているので、これらの水分は原油と共
に石油タンク中に荷揚げされる。この原油中に含まれて
いる水分またはバラスト水が原油と共に製油所に2次輸
送されると、製油装置における精製過程において塩分が
析出し、バルブや熱交換器等を閉塞する恐れがある。従
って、石油タンク中において充分に水切りをしておくこ
とが肝要である。このために、石油タンクには底板に近
い所に水切り用のドレンパイプが設けられており、この
ドレンパイプに設けられたバルブの開閉操作とドレンポ
ンプの作動・停止によって、石油タンク底部に溜まって
いるバラスト水等の排水を行っている。しかし、原油と
バラスト水等との境界を確実に検知したうえで排水を行
わないと、バラスト水等の排水が不充分であったり、ま
たは、原油までバラスト水等と一緒に排出してしまう恐
れもある。この原油とバラスト水等との境界面を探知す
る装置としては可搬油水界測定器等があり、電解液中で
石油タンクを構成する金属と異なる電位を示す金属、例
えばマグネシウム合金から成る電極にリード線とメジャ
ーを接続し、このリード線の端部を直流電流計のマイナ
ス端子に接続すると共に直流電流計のプラス端子と石油
タンクをリード線で接続しておき、前記電極を石油タン
ク中に降ろして直流電流計の指示値を読み、この指示値
によって前記電極が原油中にあるのかバラスト水中にあ
るのかを判定し、そのときの深さを前記メジャーによっ
て測るものである。また、バラスト水等により石油タン
クの底部が腐食されるのを防止するために、石油タンク
の底板に流電陽極特性を有する金属体により構成した電
気防食装置が取り付けられることがある。この場合にお
いてバラスト水等をほぼ完全に排出すると、流電陽極体
が抵抗率の高い原油で覆われることになり、流電陽極体
から発生する防食電流が制限されて防食効果を発揮でき
なくなるという問題点があった。2. Description of the Related Art Originally, a small amount of water was mixed in crude oil, and ballast water was also present in the slop oil tank of the tanker. To be done. When the water or ballast water contained in this crude oil is secondarily transported to the refinery together with the crude oil, salt may be precipitated during the refining process in the oil refiner, which may block valves and heat exchangers. Therefore, it is important to drain the water sufficiently in the oil tank. For this reason, a drain pipe for draining water is installed near the bottom plate in the oil tank, and the oil is collected at the bottom of the oil tank by opening and closing the valve installed in this drain pipe and operating and stopping the drain pump. Drains ballast water that is present. However, if drainage is not performed after the boundary between crude oil and ballast water, etc. is reliably detected, the ballast water, etc. may be insufficiently drained, or even crude oil may be discharged together with ballast water, etc. There is also. As a device for detecting the boundary surface between this crude oil and ballast water, there is a portable oil / water field measuring instrument, etc., and a metal having a potential different from that of the metal constituting the oil tank in the electrolyte, for example, an electrode made of a magnesium alloy, is used. Connect the lead wire and measure, connect the end of this lead wire to the negative terminal of the DC ammeter, and also connect the positive terminal of the DC ammeter to the oil tank with the lead wire. It is taken down, the reading value of the DC ammeter is read, and it is judged whether the electrode is in crude oil or ballast water by this reading value, and the depth at that time is measured by the measure. Further, in order to prevent the bottom portion of the oil tank from being corroded by ballast water or the like, a cathodic protection device made of a metal body having galvanic anode characteristics may be attached to the bottom plate of the oil tank. In this case, if the ballast water or the like is almost completely discharged, the galvanic anode body will be covered with crude oil having a high resistivity, and the anticorrosion current generated from the galvanic anode body will be limited and the anticorrosion effect will not be exhibited. There was a problem.
【0003】[0003]
【発明が解決しようとする課題】上述した可搬油水界測
定器等で原油とバラスト水との境界を検出しておいて
も、この境界値に基づいてバルブ、ポンプ等の排水設備
の運転を制御しないと、排出したバラスト水に原油が混
入することは避けられなかった。また、原油タンクの底
板に取り付けた流電陽極体が抵抗率の高い原油等に覆わ
れて流電陽極体から発生する防食電流が制限され、防食
効果を発揮できないという問題点を解決する手段として
は、実公平3−51335号公報に開示されているよう
に、流電陽極体が完全に浸漬されるように石油タンク側
面に設けられた貯蔵液出入口ノズルの下方まで電解液を
張り込む方法もあるが、この方法では電解液にバラスト
水等が多量に加わると防食範囲の増大を招き、防食電流
が不足して充分な防食効果が得られないという欠点があ
った。Even if the boundary between crude oil and ballast water is detected by the above-mentioned portable oil / water level measuring instrument, etc., the operation of drainage facilities such as valves and pumps can be performed based on this boundary value. Without control, it was inevitable that crude oil would be mixed into the discharged ballast water. Further, as a means for solving the problem that the galvanic anode body attached to the bottom plate of the crude oil tank is covered with crude oil having a high resistivity, the anticorrosion current generated from the galvanic anode body is limited, and the anticorrosion effect cannot be exhibited. As disclosed in Japanese Utility Model Publication No. 3-51335, there is also a method of pouring the electrolyte solution to the lower side of the storage solution inlet / outlet nozzle provided on the side surface of the oil tank so that the galvanic anode body is completely immersed. However, this method has a drawback in that when a large amount of ballast water or the like is added to the electrolytic solution, the anticorrosion range is increased, and the anticorrosion current is insufficient to obtain a sufficient anticorrosion effect.
【0004】[0004]
【課題を解決するための手段】本発明は、上述した従来
方法の欠点を解決するためになされたものであって、石
油タンク内面における所定の位置に流電陽極を取り付
け、前記石油タンク内面と流電陽極との接続部に石油タ
ンク内面と流電陽極とを流れる防食電流を検出する手段
を設け、前記手段により検出した電流値に基づいて前記
石油タンクの残留水をドレンノズルから自動的に排出さ
せ、前記残留水のレベルを所定のレベルに保持するよう
にしたものである。SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned drawbacks of the conventional method, in which a galvanic anode is attached at a predetermined position on the inner surface of an oil tank to form an inner surface of the oil tank. A means for detecting the anticorrosion current flowing through the inner surface of the oil tank and the galvanic anode is provided at the connection with the galvanic anode, and the residual water in the oil tank is automatically discharged from the drain nozzle based on the current value detected by the means. The residual water level is maintained at a predetermined level.
【0005】[0005]
【作用】石油タンク内面に取り付けられた流電陽極と前
記石油タンクとの接続部に設けられた防食電流測定器に
よって石油タンク内面と流電陽極とを流れる防食電流を
検出し、この検出値に基づいて排水設備の制御を行う。
即ち、原油から分離したバラスト水のレベルが流電陽極
の設置点以上に上昇すると防食電流が流れることを防食
電流測定器によって検出して排水設備を運転させ、バラ
スト水のレベル低下に伴って前記流電陽極が原油によっ
て覆われるようになると防食電流が流れなくなることを
検出して排水設備の運転を停止させる。[Function] The anticorrosion current flowing through the inner surface of the oil tank and the galvanic anode is detected by the anticorrosion current measuring device provided at the connecting portion between the galvanic anode mounted on the inner surface of the oil tank and the oil tank, and the detected value is detected. Based on this, the drainage facilities are controlled.
That is, when the level of the ballast water separated from the crude oil rises above the installation point of the galvanic anode, the drainage facility is operated by detecting that the anticorrosion current flows by the anticorrosion current measuring instrument, and the level of the ballast water decreases with the above. When the galvanic anode becomes covered with crude oil, it detects that the anticorrosion current stops flowing and stops the operation of the drainage facility.
【0006】[0006]
【実施例】以下、本発明の実施例を図面を参照しながら
説明する。図1は本発明の一実施例を示す石油タンクに
おけるバラスト水の排水装置の構成を示す概略図であ
り、電流測定用流電陽極を石油タンク内面の1箇所に取
り付けたものである。図1において、石油タンク1の側
面下部にはドレンノズル2が石油タンク1の側面を貫通
して取り付けられており、このドレンノズル2の少し上
の石油タンク1の内面には亜鉛、アルミニウム、マグネ
シウムまたはこれらの合金から成る電流測定用流電陽極
31が取り付けられている。この電流測定用流電陽極3
1の芯金31aには防食電流計測用分流器またはホール
素子から構成される防食電流測定器4が取り付けられて
おり、前記電流計測用流電陽極31の芯金31aを流れ
る防食電流は前記防食電流測定器4によって検出されて
電流検出器6に入力される。この電流検出器6に入力さ
れた防食電流が予め設定した値と一致したときは、リレ
ー回路7が作動するように回路が構成されている。ま
た、ドレンノズル配管2′の途中に取り付けたドレンポ
ンプ10およびバルブ11の駆動制御部9,9′と電源
12′間の回路には、前記リレー回路7によって作動す
るスイッチ8,8′が組み込まれている。Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a schematic diagram showing the configuration of a ballast water drainage device in an oil tank showing an embodiment of the present invention, in which a galvanic anode for current measurement is attached to one location on the inner surface of the oil tank. In FIG. 1, a drain nozzle 2 is attached to a lower part of a side surface of an oil tank 1 so as to penetrate through a side surface of the oil tank 1, and zinc, aluminum, magnesium, or these is provided on an inner surface of the oil tank 1 slightly above the drain nozzle 2. The galvanic anode 31 for electric current measurement made of the above alloy is attached. This galvanic anode for current measurement 3
The core metal 31a of No. 1 is provided with the anticorrosion current measuring device 4 composed of a shunt or a hall element for measuring the anticorrosion current, and the anticorrosion current flowing through the core metal 31a of the galvanic anode 31 for current measurement is the anticorrosion current. The current is detected by the current measuring device 4 and input to the current detector 6. The circuit is configured so that the relay circuit 7 is activated when the anticorrosion current input to the current detector 6 matches a preset value. Switches 8 and 8'operated by the relay circuit 7 are incorporated in the circuit between the drive control units 9 and 9'of the drain pump 10 and the valve 11 and the power source 12 'which are installed in the drain nozzle pipe 2'. ing.
【0007】図2は、本発明のもう一つの実施例であっ
て、石油タンク1の内面の上下2箇所に電流測定用流電
陽極31,32を取り付け、さらに、前記石油タンク1
の底板1aの内面に防食用流電陽極5を取り付けた石油
タンクにおけるバラスト水の排水装置の構成を示す概要
図である。前記電流測定用流電陽極31の上部における
所定の位置に電流測定用流電陽極31と同じ材質と形状
を備えた電流測定用流電陽極32が石油タンク1の内面
に取り付けられている。また、前記電流測定用流電陽極
32の芯金32aには防食電流計測用分流器またはホー
ル素子から構成される防食電流測定器4′が取り付けら
れており、石油タンク1の底板1aの内面には前記電流
測定用流電陽極31よりも低い位置に防食用流電陽極5
が設置されている。前記電流測定用流電陽極31の芯金
31aを流れる防食電流と前記電流測定用流電陽極32
の芯金32aを流れる防食電流は前記防食電流測定器4
と4′で検出されて電流検出器6に入力され、この電流
検出器6に入力された防食電流が予め設定した値と一致
したときはリレー回路7が作動するように回路が構成さ
れている。以上説明した構成要素より他の構成要素は図
1におけるものと同一であるので説明は省略する。FIG. 2 shows another embodiment of the present invention, in which galvanic anodes 31 and 32 for current measurement are attached to upper and lower two positions on the inner surface of the oil tank 1, and further, the oil tank 1
FIG. 3 is a schematic view showing the configuration of a ballast water drainage device in an oil tank in which an anticorrosion galvanic anode 5 is attached to the inner surface of the bottom plate 1 a of FIG. A current measuring galvanic anode 32 having the same material and shape as that of the current measuring galvanic anode 31 is attached to the inner surface of the oil tank 1 at a predetermined position above the current measuring galvanic anode 31. Further, a corrosive current measuring shunt or a corrosive current measuring device 4'consisting of a Hall element is attached to the core metal 32a of the galvanic anode 32 for current measurement, and is attached to the inner surface of the bottom plate 1a of the oil tank 1. Is an anticorrosion galvanic anode 5 at a position lower than the galvanic anode 31 for current measurement.
Is installed. The anticorrosion current flowing through the core metal 31a of the galvanic anode 31 for measuring current and the galvanic anode 32 for measuring current.
The anticorrosion current flowing through the core metal 32a of the
The circuit is configured so that the relay circuit 7 is activated when the anticorrosion current input to the current detector 6 matches the preset value. . The components other than the components described above are the same as those in FIG.
【0008】次に、本発明により石油タンクにおけるバ
ラスト水の排水装置の動作を簡単に説明する。図1にお
いて、石油タンク1に海水を張ると電流測定用流電陽極
31と石油タンク1の内面には電位差が生じ、電流測定
用流電陽極31と石油タンク1との間にある一定の防食
電流が流れる。また、石油タンク1に海水を僅か混入さ
せた原油を張ると、電流測定用流電陽極31の周囲の接
水抵抗率は高くなり、前記電流測定用流電陽極31と石
油タンク1との間には防食電流は殆ど流れなくなる。そ
こで、電流測定用流電陽極31の芯金31aを流れる防
食電流が電流検出器6に予め設定した値以上になったと
きにスイッチ8と8′がオンとなり、前記防食電流が電
流検出器6の設定値以下になったときは前記スイッチ8
と8′はオフとなるように電流検出器6の電流を設定し
ておく。石油タンク1に注入された海水を含んだ原油は
静置しておくと海水と原油とは分離し、原油は上に、海
水は下に溜まる。従って、電流測定用流電陽極31が海
水に覆われる状態になるとスイッチ8と8′はオンとな
り、駆動制御部9と9′の作動によってドレンポンプ1
0が作動し、バルブ11が開いて石油タンク1内の海水
がドレンノズル配管2′の出口から排出され、石油タン
ク1内の海水レベルが下がる。海水レベルの低下に伴っ
て電流測定用流電陽極31が原油で覆われるようになる
とスイッチ8と8′はオフとなり、ドレンポンプ10が
停止すると共にバルブ11も閉じて石油タンク1からの
排水が止まる。Next, the operation of the ballast water drainage device in the oil tank according to the present invention will be briefly described. In FIG. 1, when seawater is filled in the oil tank 1, a potential difference occurs between the galvanic anode 31 for current measurement and the inner surface of the oil tank 1, and a certain anticorrosion between the galvanic anode 31 for current measurement and the oil tank 1 is performed. An electric current flows. Further, when crude oil containing a small amount of seawater mixed therein is filled in the oil tank 1, the water contact resistivity around the amperometric anode 31 for current measurement becomes high, and the galvanic anode 31 for current measurement and the oil tank 1 are separated from each other. Almost no anti-corrosion current flows through. Therefore, when the anticorrosion current flowing through the core metal 31a of the galvanic anode 31 for current measurement exceeds a value preset in the current detector 6, the switches 8 and 8'are turned on and the anticorrosion current is detected by the current detector 6. When it is less than the set value of, switch 8
And 8'set the current of the current detector 6 so as to be turned off. If the crude oil containing the seawater injected into the oil tank 1 is left to stand, the seawater and the crude oil are separated, and the crude oil accumulates on the top and the seawater accumulates on the bottom. Therefore, when the galvanic anode 31 for current measurement is in a state of being covered with seawater, the switches 8 and 8'are turned on, and the drain pump 1 is activated by the operation of the drive control units 9 and 9 '.
0 operates, the valve 11 is opened, the seawater in the oil tank 1 is discharged from the outlet of the drain nozzle pipe 2 ', and the seawater level in the oil tank 1 is lowered. When the galvanic anode 31 for current measurement comes to be covered with crude oil due to the decrease in seawater level, the switches 8 and 8 ′ are turned off, the drain pump 10 is stopped, and the valve 11 is closed so that the drainage water from the oil tank 1 is discharged. Stop.
【0009】図2において、石油タンク1に海水を張る
と電流測定用流電陽極31,32と石油タンク1の内面
には電位差が生じ、電流測定用流電陽極31,32と石
油タンク1との間にある一定の防食電流が流れる。ま
た、石油タンク1に海水を僅か混入させた原油を張る
と、電流測定用流電陽極31と32の周囲の接水抵抗率
は高くなり、前記電流測定用流電陽極31と32と石油
タンク1との間には防食電流は殆ど流れなくなる。そこ
で、電流測定用流電陽極32の芯金32aを流れる防食
電流が電流検出器6に予め設定した値以上になったとき
にスイッチ8,8′がオンとなり、電流測定用流電陽極
31の芯金31aを流れる防食電流が前記電流検出器6
に予め設定した値以下になったときにスイッチ8,8′
がオフとなるように電流検出器6の電流を設定してお
く。海水を含んだ原油を石油タンク1に注入して静置し
ておくと海水と原油は分離し、原油は上に、海水は下に
溜まる。この海水が電流測定用流電陽極32にまで上昇
するとスイッチ8,8′がオンとなり、駆動制御部9,
9′の作動に伴ってドレンポンプ10が作動し、バルブ
11が開いて石油タンク1内の海水がドレンノズル配管
2′の出口から排出され、石油タンク1内の海水レベル
が下がる。海水レベルの低下に伴って電流測定用流電陽
極31が原油に覆われるようになるとスイッチ8と8′
はオフとなり、ドレンポンプ10が停止すると共にバル
ブ11も閉じて石油タンク1からの排水が止まる。In FIG. 2, when seawater is filled in the oil tank 1, a potential difference occurs between the galvanic anodes 31 and 32 for current measurement and the inner surface of the petroleum tank 1, and the galvanic anodes 31 and 32 for current measurement and the petroleum tank 1 are connected. A certain anticorrosion current flows between the two. Further, when crude oil containing a small amount of seawater mixed therein is filled in the oil tank 1, the water contact resistivity around the current measuring galvanic anodes 31 and 32 becomes high, and the current measuring galvanic anodes 31 and 32 and the oil tanks. Almost no anticorrosion current flows between 1 and. Therefore, when the anticorrosion current flowing through the cored bar 32a of the galvanic anode 32 for current measurement exceeds a value preset in the current detector 6, the switches 8 and 8'are turned on, and the galvanic anode 31 for current measurement is turned on. The anticorrosion current flowing through the core metal 31a is the current detector 6
Switch 8 and 8'when the value becomes less than the value preset in
The current of the current detector 6 is set so that is turned off. When crude oil containing seawater is poured into the oil tank 1 and left to stand still, the seawater and the crude oil are separated, the crude oil accumulates at the top and the seawater accumulates at the bottom. When this seawater rises to the galvanic anode 32 for current measurement, the switches 8 and 8'are turned on, and the drive control unit 9 and
Along with the operation of 9 ', the drain pump 10 is operated, the valve 11 is opened, the seawater in the oil tank 1 is discharged from the outlet of the drain nozzle pipe 2', and the seawater level in the oil tank 1 is lowered. When the galvanic anode 31 for current measurement comes to be covered with crude oil as the seawater level decreases, the switches 8 and 8 '
Is turned off, the drain pump 10 is stopped, the valve 11 is closed, and the drainage from the oil tank 1 is stopped.
【0010】以上の説明から明らかなように、図1に示
す実施例においては、海水レベルが電流測定用流電陽極
31の設置点以上に上昇すると排水を開始し、電流測定
用流電陽極31の設置点以下に低下すると排水を停止す
る。また、図2に示す実施例においては電流測定用流電
陽極32の設置点以上に海水レベルが上昇したときに排
水を開始し、電流測定用流電陽極31の設置点以下に海
水レベルが低下すると排水を停止する。As is clear from the above description, in the embodiment shown in FIG. 1, when the seawater level rises above the installation point of the galvanic anode 31 for current measurement, drainage is started and the galvanic anode 31 for current measurement is started. When the temperature drops below the installation point, the drainage will be stopped. In the embodiment shown in FIG. 2, drainage is started when the seawater level rises above the installation point of the current measurement galvanic anode 32, and the seawater level drops below the installation point of the current measurement galvanic anode 31. Then the drainage is stopped.
【0011】[0011]
【発明の効果】以上説明したように、本発明による石油
タンクにおけるバラスト水の排水装置は、石油タンク内
面における所定の位置に流電陽極を取り付け、前記石油
タンク内面と流電陽極とを流れる防食電流を検出する防
食電流測定器を石油タンク内面と流電陽極との接続部に
設け、検出した電流値によって排水設備の運転を制御
し、前記石油タンク内の油を排出することなく残留水の
みをドレンノズルから自動的に排出するものである。ま
た、石油タンク内のバラスト水等のレベルを一定範囲に
制御できるので、バラスト水等の増加に伴う防食範囲の
増大によって防食電流が不足して充分な防食効果を得ら
れないという問題点を解消でき、防食用流電陽極が抵抗
率の高い原油等に覆われて流電陽極から発生する防食電
流が制限され、防食効果を発揮できなくなる問題点もな
くなる。As described above, in the ballast water drainage device for an oil tank according to the present invention, a galvanic anode is attached at a predetermined position on the inner surface of the oil tank to prevent corrosion that flows between the inner surface of the oil tank and the galvanic anode. An anticorrosion current measuring device that detects the current is installed at the connection between the inner surface of the oil tank and the galvanic anode, and the operation of the drainage facility is controlled by the detected current value, and only the residual water is discharged without discharging the oil in the oil tank. Is automatically discharged from the drain nozzle. In addition, since the level of ballast water etc. in the oil tank can be controlled within a certain range, the problem that the anticorrosion current is insufficient and the sufficient anticorrosion effect cannot be obtained due to the increase of the anticorrosion range accompanying the increase of ballast water etc. is solved. Therefore, the anticorrosion galvanic anode is covered with crude oil or the like having a high resistivity, and the anticorrosion current generated from the galvanic anode is limited, so that there is no problem that the anticorrosion effect cannot be exhibited.
【図1】本発明の一実施例を示す石油タンクにおけるバ
ラスト水排水装置の構成を示す概略図。FIG. 1 is a schematic diagram showing a configuration of a ballast water drainage device in an oil tank showing an embodiment of the present invention.
【図2】本発明のもう一つの実施例を示す石油タンクに
おけるバラスト水排水装置の構成を示す概略図。FIG. 2 is a schematic diagram showing a configuration of a ballast water drainage device in an oil tank showing another embodiment of the present invention.
1 石油タンク 1a 石油タンク底板 2 ドレンノズル 2′ ドレンノズル配管 31,32 電流測定用流電陽極 32a,32b 電流測定用流電陽極の芯金 4,4′ 防食電流測定器 5 防食用流電陽極 6 電流検出器 7 リレー回路 8,8′ スイッチ 9,9′ 駆動制御部 10 ドレンポンプ 11 バルブ 12,12′ 電源 1 Oil tank 1a Oil tank bottom plate 2 Drain nozzle 2'Drain nozzle pipe 31, 32 Current measuring galvanic anode 32a, 32b Current measuring galvanic anode core metal 4, 4'Corrosion protection current measuring instrument 5 Corrosion protection galvanic anode 6 Current Detector 7 Relay circuit 8,8 'Switch 9,9' Drive controller 10 Drain pump 11 Valve 12, 12 'Power supply
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 C23F 13/00 8414−4K ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 5 Identification code Office reference number FI technical display location C23F 13/00 8414-4K
Claims (1)
を取り付けると共に前記石油タンク内面と流電陽極とを
流れる防食電流を検出する手段を前記石油タンク内面と
流電陽極との接続部に設け、前記手段により検出した電
流値を予め電流検出器に設定した基準値と比較すること
により前記石油タンクに付帯する排水設備の運転を制御
し、前記石油タンクの残留水をドレンノズルから自動的
に排水させることにより前記残留水のレベルを所定のレ
ベルに制御することを特徴とする石油タンクにおけるバ
ラスト水の排水装置。1. A means for attaching a galvanic anode to a predetermined position on the inner surface of an oil tank and detecting means for detecting an anticorrosion current flowing through the inner surface of the oil tank and the galvanic anode is provided at a connecting portion between the inner surface of the oil tank and the galvanic anode. Provided, the operation of the drainage equipment incidental to the oil tank is controlled by comparing the current value detected by the means with a reference value preset in the current detector, and the residual water in the oil tank is automatically discharged from the drain nozzle. A drainage device for ballast water in an oil tank, wherein the level of the residual water is controlled to a predetermined level by draining.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP18992392A JP3290205B2 (en) | 1992-06-24 | 1992-06-24 | Ballast water drainage in oil tanks |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP18992392A JP3290205B2 (en) | 1992-06-24 | 1992-06-24 | Ballast water drainage in oil tanks |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0612130A true JPH0612130A (en) | 1994-01-21 |
JP3290205B2 JP3290205B2 (en) | 2002-06-10 |
Family
ID=16249475
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP18992392A Expired - Fee Related JP3290205B2 (en) | 1992-06-24 | 1992-06-24 | Ballast water drainage in oil tanks |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3290205B2 (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5845735A (en) * | 1995-12-23 | 1998-12-08 | Daimler-Benz Ag | Control element arrangement for controlling the longitudinal movement and/or the lateral movement of a motor vehicle |
KR101346237B1 (en) * | 2011-03-10 | 2014-01-03 | 삼성중공업 주식회사 | Wastewater treatment system of a vessel |
CN107512500A (en) * | 2016-11-16 | 2017-12-26 | 高翔 | More storage tanks are concentrated and cut water and oil return method and system |
US11965818B1 (en) * | 2020-05-28 | 2024-04-23 | Mopeka Products Llc | Corrosion monitor |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103231878B (en) * | 2013-04-28 | 2015-02-25 | 南京工业大学 | Automatic water system of cutting of oil tank |
-
1992
- 1992-06-24 JP JP18992392A patent/JP3290205B2/en not_active Expired - Fee Related
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5845735A (en) * | 1995-12-23 | 1998-12-08 | Daimler-Benz Ag | Control element arrangement for controlling the longitudinal movement and/or the lateral movement of a motor vehicle |
US6446747B1 (en) | 1995-12-23 | 2002-09-10 | Daimlerchrysler Ag | Control element arrangement for controlling the longitudinal movement and/or the lateral movement of a motor vehicle |
KR101346237B1 (en) * | 2011-03-10 | 2014-01-03 | 삼성중공업 주식회사 | Wastewater treatment system of a vessel |
CN107512500A (en) * | 2016-11-16 | 2017-12-26 | 高翔 | More storage tanks are concentrated and cut water and oil return method and system |
CN107512500B (en) * | 2016-11-16 | 2018-11-09 | 高翔 | More storage tank concentrations cut water and oil return method and system |
US11965818B1 (en) * | 2020-05-28 | 2024-04-23 | Mopeka Products Llc | Corrosion monitor |
Also Published As
Publication number | Publication date |
---|---|
JP3290205B2 (en) | 2002-06-10 |
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