KR100663332B1 - Control apparatus for electrolytic sterilization system of ballast water of a ship - Google Patents

Control apparatus for electrolytic sterilization system of ballast water of a ship Download PDF

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KR100663332B1
KR100663332B1 KR1020060068536A KR20060068536A KR100663332B1 KR 100663332 B1 KR100663332 B1 KR 100663332B1 KR 1020060068536 A KR1020060068536 A KR 1020060068536A KR 20060068536 A KR20060068536 A KR 20060068536A KR 100663332 B1 KR100663332 B1 KR 100663332B1
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seawater
ballast water
electrolytic
residual chlorine
chlorine ion
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김경희
이경란
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아쿠아셀 주식회사
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/467Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction
    • C02F1/4672Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction by electrooxydation
    • C02F1/4674Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction by electrooxydation with halogen or compound of halogens, e.g. chlorine, bromine
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B63SHIPS OR OTHER WATERBORNE VESSELS; RELATED EQUIPMENT
    • B63JAUXILIARIES ON VESSELS
    • B63J4/00Arrangements of installations for treating ballast water, waste water, sewage, sludge, or refuse, or for preventing environmental pollution not otherwise provided for
    • B63J4/002Arrangements of installations for treating ballast water, waste water, sewage, sludge, or refuse, or for preventing environmental pollution not otherwise provided for for treating ballast water
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104Devices therefor; Their operating or servicing
    • C02F1/46109Electrodes
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104Devices therefor; Their operating or servicing
    • C02F1/46109Electrodes
    • C02F2001/46119Cleaning the electrodes
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/008Originating from marine vessels, ships and boats, e.g. bilge water or ballast water
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/46Apparatus for electrochemical processes
    • C02F2201/461Electrolysis apparatus
    • C02F2201/46105Details relating to the electrolytic devices
    • C02F2201/4612Controlling or monitoring
    • C02F2201/46125Electrical variables
    • C02F2201/4613Inversing polarity
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/46Apparatus for electrochemical processes
    • C02F2201/461Electrolysis apparatus
    • C02F2201/46105Details relating to the electrolytic devices
    • C02F2201/4612Controlling or monitoring
    • C02F2201/46125Electrical variables
    • C02F2201/4614Current
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/46Apparatus for electrochemical processes
    • C02F2201/461Electrolysis apparatus
    • C02F2201/46105Details relating to the electrolytic devices
    • C02F2201/4612Controlling or monitoring
    • C02F2201/46145Fluid flow
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/04Disinfection

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  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
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  • Chemical Kinetics & Catalysis (AREA)
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  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

A control apparatus of an electrolytic sterilization system of ballast water of a ship is provided to effectively perform the sterilization of the ballast water. The electrolytic sterilization apparatus(10) includes two titan insoluble electrodes(11,12). The residual chlorine ion concentration sensing sensor(21) is installed at the inside of a ballast tank, senses the residual chlorine ion of sea water and generates an electric signal in proportion to the sensed concentration. A flow sensing sensor(22) is installed at the pipe of a pump, senses the inflow amount of the sea water and generates an electric signal in proportion to the sensed result.

Description

선박 밸러스트수 전해살균시스템의 제어장치{Control apparatus for electrolytic sterilization system of ballast water of a ship}Control apparatus for electrolytic sterilization system of ballast water of a ship}

도 1은 본 발명에 따른 선박 밸러스트수 전해살균시스템의 제어장치 블록도.1 is a control block diagram of a ship ballast water electrolytic sterilization system according to the present invention.

도 2는 본 발명에 따른 선박 밸러스트수 전해살균시스템의 제어흐름도.2 is a control flow chart of the ship ballast water electrolytic sterilization system according to the present invention.

[도면의 주요부분에 대한 부호의 설명][Explanation of symbols on the main parts of the drawings]

10 : 전해살균장치 11, 12 : 불용성 전극10: electrolytic sterilizer 11, 12: insoluble electrode

20 : 전해살균제어부 21 : 잔류염소이온 농도감지센서20: electrolytic sterilization control unit 21: residual chlorine ion concentration sensor

23 : 콘트롤부 24 : 전류제어부23: control unit 24: current control unit

25 : 극성전환부 26 : 펄스발생기25: polarity switching unit 26: pulse generator

본 발명은 선박의 선체 안정을 유지하기 위해 배의 바닥에 싣는 밸러스트(ballast)의 해수(海水) 전해살균장치에 관한 것으로써, 더욱 상세하게는 전해살균장치의 양극(+)과 음극(-) 모두에 티탄 소재 불용성 전극을 설치하고, 극성전환부, 전류조절부 및 유량감지센서, 펄스발생기, 잔류염소이온농도감지센서를 각각 부가함으로써 양극과 음극의 극성을 주기적으로 전환시켜 차아염소산나트륨을 중단 없이 생성되도록 하는 한편, 해수의 유입량과 차아염소산나트륨의 농도에 의해 전해량을 조절하여 차아염소산나트륨 농도를 조절할 수 있을 뿐만 아니라, 음극에 수산화염화합물이 부착되는 것을 방지하여 밸러스트수의 살균을 효과적으로 이루어질 수 있도록 하는 전해장치를 이용한 선박의 밸러스트 해수 살균장치에 관한 것이다.The present invention relates to a seawater electrolytic sterilizer of ballast (ballast) to be mounted on the bottom of the ship in order to maintain the hull stability of the ship, more specifically the positive (+) and the negative (-) of the electrolytic sterilizer Titanium-based insoluble electrodes were installed on all of them, and the polarity switching part, current control part, flow rate sensor, pulse generator, and residual chlorine ion concentration sensor were added respectively to periodically change the polarity of the positive electrode and the negative electrode to stop sodium hypochlorite. In addition to controlling the amount of sodium hypochlorite by controlling the amount of electrolyte by the inflow of seawater and the concentration of sodium hypochlorite, the sterilization of ballast water can be effectively prevented by preventing the attachment of the hydroxide compound to the cathode. The present invention relates to a ballast seawater sterilization apparatus of a ship using an electrolytic apparatus.

1992년 유엔환경개발회의는 비토착 생물의 확산 방지를 위하여 국제해사기구에 밸러스트수(Ballast water)의 방출에 관한 제도적인 규제를 요청하였으며, 이에 따라 국제해사기구에서는 밸러스트수에 의한 생태계 파괴 및 오염을 방지하기 위한 방안으로 선박이 항만 내에 입항하기 전 일정한 해역에서 밸러스트수를 교환하는 방안과, 적재하고 있는 밸러스트수를 물리, 화학적인 방법으로 살균이나 소독하는 두 가지 방안을 제시하였다.In 1992, the United Nations Conference on Environment and Development asked the International Maritime Organization to systematically regulate the release of ballast water in order to prevent the spread of non-indigenous organisms. In order to prevent this problem, two methods of exchanging ballast water in a certain sea area before the ship enters the harbor, and two methods of disinfecting or disinfecting the ballast water loaded by physical and chemical methods were proposed.

상기의 두 가지 방안 중 밸러스트수를 물리, 화학적으로 살균 또는 소독하는 방법은 선박에 적재되는 밸러스트수 양이 대용량이므로 처리효율이 떨어져서 대양에서 밸러스트수를 교환하는 방안에 대하여 검토가 집중적으로 이루어져 왔으나, 대양에서의 밸러스트수 교환 작업은 많은 시간과 노력이 필요하며 선박안전에 위험을 초래할 가능성이 있고 근거리 항해 중에는 작업이 불가능하므로 실용적인 밸러스트수 처리장치의 개발이 요구 및 제안되고 있다.Among the above two methods, the method of physically, chemically sterilizing or disinfecting the ballast water has been intensively examined for the method of exchanging the ballast water in the ocean due to the low processing efficiency because the amount of ballast water loaded on the ship is large. Since ballast water exchange work in the ocean requires a lot of time and effort, it may pose a danger to the safety of ships, and it is impossible to work during close voyage, so the development of a practical ballast water treatment device is required and proposed.

상기와 같은 종래의 밸러스트수 처리장치는 일본공개특허 제2005- 342626호(공개일자:2005.12.15)(발명의 명칭:밸러스트 수처리방법 및 장치, 해당 장치를 탑재한 선박)에서 충격수압장치를 구비하여 밸러스트 탱크 내부로 해수가 유입될 때 바다생물을 걸러내는 막여과장치의 세척수에 충격수압을 가하고, 이 충격수압에 의 해 수생 생물의 사멸 효과를 발휘할 수 있도록 하고, 또한 막여과장치의 전.후단에 자외선 조사장치나 전해장치를 구비하여 살균을 실시한 것이 제안되었다.The conventional ballast water treatment apparatus as described above is provided with a shock-hydraulic device in Japanese Patent Laid-Open No. 2005-342626 (published date: December 15, 2005) (name of the invention: a ballast water treatment method and apparatus, a vessel equipped with the apparatus). Thus, when the seawater enters the ballast tank, the impact water pressure is applied to the water of the membrane filter system that filters the sea creatures, and the impact water pressure is used to exert the killing effect of the aquatic organisms. It has been proposed to sterilize with a UV irradiation apparatus or an electrolytic apparatus at the rear stage.

또한, 대한민국 공개특허 제2004-0066971호(공개일자:2004.07.30)(발명의 명칭 : 선박용 밸라스트수 처리장치)에서는 밸러스트 탱크 내부로 해수가 유입될 때 바다생물을 걸러내는 여과장치 내부에 회전식 여과필터를 설치하고, 청소솔로 회전식 여과필터에 부착된 이물질을 연속적으로 제거하고, 상기 여과장치 후단부에 자외선-전해살균처리장치를 설치한 것이 제안되었다.In addition, the Republic of Korea Patent Publication No. 2004-0066971 (published date: 2004.07.30) (name of the invention: the ballast water treatment device for ships) in the rotary system inside the filtration device to filter the sea creatures when seawater is introduced into the ballast tank It has been proposed to install a filtration filter, to continuously remove foreign substances attached to the rotary filtration filter with a cleaning brush, and to install an ultraviolet-electrolytic sterilization treatment device at the rear end of the filtration device.

상기와 같은 종래의 선박용 밸라스트수 처리장치는 양극(+)에 불용성 티탄전극을, 음극(-)에는 스텐레스전극을 설치하여 양극에서의 전해로 인해 차아염소산나트륨이 생성되어 밸러스트수에 포함된 각종 세균을 살균하도록 되어 있는 전해살균장치를 포함하고 있다. The conventional vessel ballast water treatment apparatus as described above has insoluble titanium electrodes at the positive electrode (+), and stainless steel electrodes at the negative electrode (-), so that sodium hypochlorite is generated by electrolysis at the positive electrode and thus included in the ballast water. Electrolytic sterilization device for sterilizing bacteria is included.

일반적으로 해수를 전기분해할 경우 양극과 음극에는 반응식(1)과 같은 주 반응과 반응식 (2)와 같은 부반응이 진행된다. In general, when seawater is electrolyzed, a main reaction as shown in Scheme (1) and a side reaction as shown in Scheme (2) proceed to the anode and the cathode.

Figure 112006052131653-pat00001
반응식(1)
Figure 112006052131653-pat00001
Scheme (1)

Figure 112006052131653-pat00002
반응식(2)
Figure 112006052131653-pat00002
Scheme (2)

해수의 전기분해가 일어나는 동안 양극에서는 차아염소산 혹은 차아염소산나트륨이 생성되고, 음극에서는 수소 발생과 아울러 생성된 수산화 이온(OH-)으로 인하여 강알카리성으로 변하게 되고, 생성된 수산화이온은 해수중 용존되어 있는 나 트륨이온과 반응하여 NaOH가 생성되게 된다. In the positive electrode for the electrolysis of water takes place hypochlorite or sodium hypochlorite is generated, in the negative electrode as well as the generated hydroxide ions (OH -) and hydrogen generation is changed into due strong alkali, the resulting hydroxide ions are dissolved in the seawater NaOH is produced by reacting with sodium ion.

이때, 해수중 다량 용존되어 있는 마그네슘이온(Mg2+)와 칼슘이온(Ca2+) 등이 NaOH와 반응하여 불용성 침전물이 생성되는데 이러한 물질이 음극의 전극 표면에 부착되는 현상이 나타난다.At this time, magnesium ions (Mg 2+ ) and calcium ions (Ca 2+ ) dissolved in a large amount of sea water react with NaOH to generate an insoluble precipitate, which is a phenomenon in which these substances adhere to the electrode surface of the cathode.

이와 같이 해수 전해장치에서 전해가 일어나는 동안 음극 표면에 부착된 수산화염화합물 피막은 전해반응기의 전류효율을 저하시킴에 따라 전해장치의 성능을 급격히 저하시키는 한편, 양극과 음극 두 전극간의 저항이 증가하여 정전압 모드로 운전할 경우 전류밀도가 감소하게 됨으로써 전해살균장치의 성능저하 현상이 나타나게 될 뿐만 아니라, 정전류 모드로 운전을 할 경우에는 저항 증가로 인해 일정 전류를 공급하기 위해선 전압을 상승시켜야 하므로 전력비 상승을 초래하게 된다.As such, the hydroxyaluminum compound film attached to the surface of the cathode during electrolysis in the seawater electrolyzer degrades the electrolytic reactor's current efficiency rapidly, while increasing the resistance between the anode and cathode electrodes. When operating in the constant voltage mode, the current density decreases, resulting in the degradation of the electrolytic sterilizer. In addition, when operating in the constant current mode, the voltage must be increased to supply a constant current due to the increased resistance. Will result.

따라서 전술한 종래 밸러스트수 처리장치에서의 전해살균장치의 경우 양극으로 사용된 티탄 소재 불용성 전극에서 염소생성으로 인한 살균제가 생성되고 음극에서의 수산화염화합물이 부착되는 현상이 나타나면 주기적으로 전원을 단속(斷續)하여 음극을 산성용액으로 세척 한 후 전해가 계속 이루어지도록 하고 있으나, 이럴 경우 세척에 필요한 염산 등의 산용액을 이용함에 따라 위험성이 큰 산 용액을 선적하여 관리해야하는 안전성의 문제 뿐만 아니라 세척시 발생되는 폐수처리를 해야 하므로 폐수처리에 필요한 시설 및 약품등이 요구되는 문제가 발생되며, 또한 음극의 주기적인 세척으로 인하여 불필요한 인력이 소요되는 문제점을 안고 있다. Therefore, in the case of the above-described electrolytic sterilizer in the conventional ballast water treatment apparatus, when a disinfectant produced by chlorine is generated in the titanium insoluble electrode used as the anode and a hydroxide compound is attached at the cathode, the power is periodically interrupted ( Iii) After the negative electrode is washed with acidic solution, the electrolysis is continued.In this case, however, the acidic solution, such as hydrochloric acid, is used to clean the solution. Since the wastewater treatment that is generated at the time needs to be a problem that requires facilities and chemicals required for wastewater treatment, and also has a problem that unnecessary manpower is required due to the periodic cleaning of the cathode.

본 발명은 상기와 같은 문제점인 음극 표면에 부착되는 수산화염화합물이 약산성 분위기에서 용해된다는 사실에 착안하여 양극(+)과 음극(-) 모두에 티탄 소재 불용성 전극을 각각 설치하고, 양극과 음극의 극성을 일정 주기로 반복 전환함으로써 음극 표면에 부착된 수산화염화합물이 양극으로 전환되었을 때 약산성 분위기에서 수산화염화합물을 재 용해시켜 제거하여 전극상태를 원래의 상태로 회복시켜줌으로써 밸러스트수의 살균효과를 지속적으로 높일 수 있도록 하는 것을 기술적 과제로 한다. The present invention focuses on the fact that the hydroxide compound attached to the surface of the negative electrode, which is the above problem, is dissolved in a weakly acidic atmosphere, and a titanium-based insoluble electrode is installed on both the positive electrode and the negative electrode, respectively. By repeating the polarity at regular intervals, when the hydroxide compound attached to the surface of the cathode is converted to the anode, it dissolves and removes the hydroxide compound in a weak acid atmosphere to restore the electrode state to its original state. It is a technical subject to make it possible to raise.

또한, 본 발명의 밸러스트수 전해살균장치는 펄스발생기를 부가하여 상기 극성변환장치에 의해 양극과 음극에 특정 펄스를 인가하여 이 펄스에 의하여 전극표면에 미세 진동을 발생시켜 극성 변환시에 미 제거된 미량의 수산화염화합물의 탈착과 아울러 음극에서 생성되는 수소로 인한 농도 분극 및 수소 취성으로 인하여 전극의 수명이 단축되는 것을 방지함으로써 전류 및 전해효율을 극대화 할 수 있도록 하는 것을 기술적 과제로 한다.In addition, the ballast water electrolytic sterilizer of the present invention adds a pulse generator to apply a specific pulse to the positive electrode and the negative electrode by the polarity conversion device to generate fine vibration on the electrode surface by this pulse, which is not removed at the time of polarity conversion. The technical task is to maximize the current and electrolytic efficiency by preventing the desorption of the hydroxide compound and the life of the electrode is shortened due to concentration polarization and hydrogen embrittlement due to hydrogen generated in the cathode.

또한, 본 발명의 밸러스트수 전해살균장치는 전류조절장치를 부가하여 밸러스트 탱크내에 유입되는 해수의 량에 따라 전극에 인가되는 전류를 조절할 수 있어 차아염소산나트륨의 농도를 자동 제어할 수 있도록 하고, 해수가 밸러스트 탱크 내에 유입되기 전 원활한 살균이 이루어지도록 하는 것을 기술적 과제로 한다. In addition, the ballast water electrolytic sterilization apparatus of the present invention can adjust the current applied to the electrode according to the amount of seawater flowing into the ballast tank by adding a current regulator to automatically control the concentration of sodium hypochlorite, seawater The technical problem is to ensure smooth sterilization before the gas is introduced into the ballast tank.

또한, 본 발명의 밸러스트수 전해살균장치는 밸러스트 탱크내의 잔류 염소이온농도를 센싱하여 유입된 밸러스트수의 량에 비례하여 차아염소산나트륨의 농도를 일정하게 유지시켜 살균이 지속적으로 이루어지도록 함으로서 밸러스트수를 보다 효과적으로 살균할 수 있도록 하는 것을 기술적 과제로 한다.In addition, the ballast water electrolytic sterilization apparatus of the present invention senses the residual chlorine ion concentration in the ballast tank and maintains the concentration of sodium hypochlorite in proportion to the amount of the ballast water introduced, so that the sterilization is continuously carried out. Technical task is to make sterilization more effective.

본 발명은 티탄소재 불용성 전극이 구비된 전해살균장치에 의한 해수의 전기분해로 차아염소산나트륨를 생성하여 해수에 포함된 세균을 살균하는 선박 밸러스트수 전해살균시스템에 있어서, 상기 전해살균장치는 해수를 전기 분해시키는 두개의 티탄 소재 불용성 전극으로 이루어지고, 밸러스트탱크 내에 설치되어 해수의 잔류염소이온농도를 센싱하여 그에 비례하는 전기적신호를 발생하는 잔류염소이온 농도감지센서와, 밸러스트탱크 내에 해수를 유입시키는 펌프의 배관에 설치되어 해수의 유입량을 센싱하여 그에 비례하는 전기적신호를 발생하는 유량감지센서와, 상기 불용성 전극에 연결되어 일정한 주기로 양극과 음극의 극성을 변환시켜 전기 분해시키는 극성전환부와, 상기 극성전환부의 입력단에 연결되어 상기 불용성 전극에 공급되는 전류를 조절하는 전류제어부와, 상기 불용성 전극에 연결되어 수산화염화합물이 음전극 표면에 부착되는 것을 방지하기 위해 미세진동을 발생시키는 펄스발생기와, 상기 잔류염소이온 농도감지센서 및 유량감지센서의 출력신호에 의해 상기 전류제어부, 극성전환부, 펄스발생기를 제어하는 콘트롤부로 이루어지는 것을 특징으로 한다.In the present invention, in the marine ballast water electrolytic sterilization system for generating sodium hypochlorite to sterilize bacteria contained in seawater by electrolysis of seawater by an electrolytic sterilization apparatus equipped with a titanium-carbon insoluble electrode, the electrolytic sterilization apparatus is used to electrolyze seawater. It is composed of two titanium insoluble electrodes to decompose and is installed in the ballast tank to detect residual chlorine ion concentration in seawater and generate an electrical signal proportional to it, and a pump to introduce seawater into the ballast tank. A flow rate sensor installed at a pipe of the sensor to sense an inflow of seawater and generate an electrical signal proportional thereto, and a polarity switching unit connected to the insoluble electrode to convert the polarity of the positive electrode and the negative electrode at regular intervals and electrolyze the polarity; Connected to an input of a switching unit and supplied to the insoluble electrode A current control unit for controlling the flow, a pulse generator connected to the insoluble electrode to generate micro vibrations to prevent the hydroxide compound from adhering to the surface of the negative electrode, and an output signal of the residual chlorine ion concentration sensor and the flow sensor It characterized by consisting of a control unit for controlling the current control unit, the polarity switching unit, the pulse generator.

이하 본 발명에 따른 선박 밸러스트수 전해살균시스템의 제어장치를 첨부된 도 1 및 도 2에 의해 상세히 설명하면 다음과 같다.Hereinafter, a control device of a ship ballast water electrolytic sterilization system according to the present invention will be described in detail with reference to FIGS. 1 and 2.

도 1은 본 발명에 따른 선박 밸러스트수 전해살균시스템의 제어장치 블록도이며, 도 2는 본 발명에 따른 선박 밸러스트수 전해살균시스템의 제어흐름도로서, 해수를 전기분해하여 차아염소산 및 차아염소산나트륨의 생성하는 전해살균장치(10)는 양극과 음극 모두에 티탄 소재 불용성 전극(11) (12)이 설치되어 있으며, 밸러스트탱크 내에 설치되어 있는 해수의 잔류염소이온농도를 감지하는 잔류염소이온 농도감지센서(21)와 밸러스트탱크 내에 해수를 유입시키는 펌프의 배관에 설치되어 해수의 유입량을 감지하는 유량감지센서(22)가 구비된다.1 is a block diagram of a control device for a ship ballast water electrolytic sterilization system according to the present invention, and FIG. 2 is a control flow chart of a ship ballast water electrolytic sterilization system according to the present invention, wherein seawater is electrolyzed to dissolve hypochlorous acid and sodium hypochlorite. The electrolytic sterilizer 10 to be produced is provided with titanium insoluble electrodes 11 and 12 at both the positive electrode and the negative electrode, and a residual chlorine ion concentration sensor for detecting residual chlorine ion concentration in seawater installed in the ballast tank. 21 and the flow rate sensor 22 is installed in the pipe of the pump for introducing the seawater into the ballast tank to detect the inflow of the seawater.

상기 불용성 전극(11)(12)에는 수산화염화합물이 음전극 표면에 부착되지 않도록 하기 위한 미세진동을 발생시키는 펄스발생기(26)가 연결되고, 또한 일정한 주기로 전극의 극성을 변환하여 극성을 주기적으로 변환시키는 극성전환부(25)가 연결되어 있다.The insoluble electrodes 11 and 12 are connected with a pulse generator 26 for generating a micro vibration for preventing the hydroxide compound from adhering to the surface of the negative electrode, and also periodically changing the polarity by changing the polarity of the electrode at regular intervals. The polarity switching section 25 is connected.

상기 잔류염소이온 농도감지센서(21) 및 유량감지센서(22)의 출력단에는 시스템 전체 제어하는 콘트롤부(23)에 연결되고, 상기 콘트롤부(23)의 출력단에는 미세진동을 발생시키는 펄스발생기(26)와, 유량감지센서(22)로부터 출력되는 해수의 유입량에 따라 전해살균장치(10)의 불용성 전극(11) (12)에 전류를 공급하는 전류제어부(24)가 연결된다.The output terminal of the residual chlorine ion concentration sensor 21 and the flow rate sensor 22 is connected to a control unit 23 for controlling the entire system, and a pulse generator for generating fine vibration at the output end of the control unit 23 ( 26 and a current control unit 24 for supplying current to the insoluble electrodes 11 and 12 of the electrolytic sterilizer 10 according to the inflow amount of the seawater output from the flow rate sensor 22.

상기 전류제어부(24)의 출력단에는 전해살균장치(10)의 불용성 전극(11)(12)을 양극과 음극으로 극성 변환하여 교대로 전기 분해시키는 극성전환부(25)가 접속된다.At the output terminal of the current control unit 24, a polarity switching unit 25 for polarizing the insoluble electrodes 11 and 12 of the electrolytic sterilizing device 10 into a positive electrode and a negative electrode is alternately connected.

상기와 같은 구성으로 이루어진 본 발명에 따른 선박 밸러스트수 전해살균시스템의 제어과정을 도 1 및 도 2에 의해 상세히 설명하면 다음과 같다.The control process of the ship ballast water electrolytic sterilization system according to the present invention having the above configuration will be described in detail with reference to FIGS. 1 and 2 as follows.

먼저, 본 발명의 선박 밸러스트수 전해살균시스템의 제어장치에 전원이 공급 되면 콘트롤부(23)에서는 시스템을 초기화(단계 100)시킨 후, 전류제어부(24), 극성전환부(25), 펄스발생기(26)를 각각 인에이블 상태로 만들어(단계 101) 동작하게 만든 다음, 잔류염소이온 농도감지센서(21)와 유량감지센서(22)로부터 출력되는 신호를 차례로 읽어(단계 102)들이게 된다.First, when power is supplied to the control device of the ship ballast water electrolytic sterilization system of the present invention, the control unit 23 initializes the system (step 100), and then the current control unit 24, the polarity switching unit 25, the pulse generator Each of 26 is enabled (step 101) to operate, and then the signals output from the residual chlorine ion concentration sensor 21 and the flow rate sensor 22 are sequentially read (step 102).

상기 유량감지센서(22)는 미도시된 펌프를 통해 밸러스트탱크 내에 유입되는 해수의 유속에 비례한 전기적신호를 아날로그 형태로 출력하게 되며, 콘트롤부(23)에서는 상기 유량감지센서(22)로부터 신호가 수신됨이 판단(단계 103)되면 그 신호를 디지털 데이터로 변환 후 비교 분석하여 유입량을 산출하고, 그 유입량에 따라 전해살균장치(10)의 불용성 전극(11)(12)에 공급하는 전류 값을 산출(단계 104)하여 결정하게 된다.The flow rate sensor 22 outputs an electrical signal in analog form proportional to the flow rate of the seawater flowing into the ballast tank through a pump (not shown), and the controller 23 outputs a signal from the flow rate sensor 22. Is determined (step 103), the signal is converted into digital data and then analyzed for comparison to calculate the inflow amount, and the current value supplied to the insoluble electrodes 11 and 12 of the electrolytic sterilizer 10 according to the inflow amount. It is determined by calculating (step 104).

이와 같이 유량감지센서(22)로부터 출력되는 해수의 유입량에 따라 불용성 전극(11)(12)에 공급하는 전류량은 콘트롤부(23)에 아래의 표 1과 같이 테이블화되어 저장된다.As described above, the amount of current supplied to the insoluble electrodes 11 and 12 according to the inflow amount of the seawater output from the flow rate sensor 22 is stored in a table as shown in Table 1 below.

(표 1) 밸러스트탱크 내의 해수 유입량에 따라 불용성 전극(11)(12)에 공급되는 전류값. Table 1 Current values supplied to the insoluble electrodes 11 and 12 according to the inflow of seawater in the ballast tank.

유량(m3/min)Flow rate (m 3 / min) 전류값(A:암페어)Current value (A: Ampere) L1L1 A1A1 L2L2 A2A2 L3L3 A3A3 L4L4 A4A4

이와 같이 콘트롤부(23)에서는 유량감지센서(22)로부터 출력되는 유입량에 따라 불용성 전극(11)(12)에 공급하는 전류 값을 산출한 후, 그 제어 전류값을 전류제어부(24)로 전송(단계 105)하게 되고, 상기 전류제어부(24)에서는 그에 비례한 전류값을 극성전환부(25)를 통해 전해살균장치(10)의 불용성 전극(11)(12)에 인가(단계 106)하게 됨으로써 해수를 전기분해하게 된다.In this way, the control unit 23 calculates the current value supplied to the insoluble electrodes 11 and 12 according to the inflow amount output from the flow rate sensor 22, and then transfers the control current value to the current control unit 24. In step 105, the current control unit 24 applies a current value proportional thereto to the insoluble electrodes 11 and 12 of the electrolytic sterilizer 10 through the polarity switching unit 25 (step 106). As a result, seawater is electrolyzed.

상기 극성전환부(25)는 콘트롤부(23)에 의해 인에이블 상태가 되면 일정 주기 마다 불용성 전극(11)(12)의 극성을 양극과 음극으로 변환시키게 되며, 이에 따라 전류제어부(24)에서 출력되는 전류가 극성전환부(25)에서 변환되는 극성에 전류를 실어 불용성 전극(11)(12)에 인가함으로써 상기 불용성 전극(11)(12)은 극성전환부(25)에 의해 일정한 주기로서 교대로 해수를 전기 분해시키게 된다.When the polarity switching unit 25 is enabled by the control unit 23, the polarity switching unit 25 converts the polarities of the insoluble electrodes 11 and 12 into a positive electrode and a negative electrode at regular intervals. The output current is applied to the insoluble electrodes 11 and 12 by applying a current to the polarity converted by the polarity switching unit 25 so that the insoluble electrodes 11 and 12 are maintained at a constant period by the polarity switching unit 25. In turn, seawater is electrolyzed.

이때, 전해살균장치(10)의 불용성 전극(11)(12) 중에서 어느 한쪽 전극에서는 양극반응에 의해 차아염소산 및 차아염소산나트륨이 중단 없이 지속적으로 생성된다.At this time, any one of the insoluble electrodes 11, 12 of the electrolytic sterilizer 10 is continuously produced without interruption by the hypochlorite and sodium hypochlorite by the anodic reaction.

여기에서 상기 극성전환부(25)에 의한 불용성 전극(11)(12)의 극성변화 주기는 실험결과 수산화염화합물이 부착될 수 없는 5~10분 간격이 바람직한 것으로 나타났다.In this case, the polarity change period of the insoluble electrodes 11 and 12 by the polarity switching part 25 was found to be preferably 5 to 10 minutes apart from which the hydroxide compound could not be attached.

한편, 상기 펄스발생기(26)는 콘트롤부(23)에 의해 인에이블 상태가 되면 8~15KHz 대역의 펄스를 출력하여 불용성 전극(11)(12)에 미세한 진동을 지속적으로 인가함으로써 미제거된 수산염 화합물을 전극표면으로부터 제거하고 또한 전극표면에 부착되는 것을 방지하게 된다.Meanwhile, when the pulse generator 26 is enabled by the controller 23, the pulse generator 26 outputs a pulse of 8 to 15 KHz to continuously apply minute vibrations to the insoluble electrodes 11 and 12, thereby removing oxalate. The compound is removed from the electrode surface and prevented from adhering to the electrode surface.

상기의 펄스발생기(26)는 불용성 전극(11)(12)에 8~15KHz 대역의 펄스를 인가할 경우 수산화염화합물이 부착되지 않는 최적의 주파수 범위임을 많은 실험을 통해 확인하였으며, 이러한 펄스발생기(26)의 회로구성은 발진기(OSC), NE555 집적 회로 등을 조합하여 구성할 수 있는 통상의 공지기술로서 자세한 구성과 설명은 생략한다.The pulse generator 26 has been confirmed through a number of experiments that the pulse generator (26) is an optimal frequency range to which the hydroxide compound is not attached when a pulse of 8-15KHz band is applied to the insoluble electrode (11) (12). The circuit configuration of 26) is a conventional publicly known technique that can be configured by combining an oscillator (OSC), an NE555 integrated circuit, and the like, and detailed configuration and description thereof will be omitted.

한편, 상기 콘트롤부(23)에서는 유량감지센서(22)로부터 유량 유입신호가 없을 경우에는 펌프의 가동이 중단되어 밸러스트탱크 내부에 해수가 유입되지 않는 저장 상태임을 인지하게 되며, 이때에는 잔류염소이온 농도감지센서(21)의 출력신호를 읽어 들여 밸러스트탱크 내부에 유입된 밸러스트수의 차아염소산나트륨의 농도를 일정하게 유지하는 과정을 수행하게 된다.On the other hand, when there is no flow inflow signal from the flow rate sensor 22, the control unit 23 recognizes that the pump is stopped and the storage state does not flow into the ballast tank, the residual chlorine ion at this time By reading the output signal of the concentration sensor 21 to perform a process of maintaining a constant concentration of sodium hypochlorite of the ballast water introduced into the ballast tank.

즉, 상기 잔류염소이온 농도감지센서(21)는 밸러스트 탱크 내 잔류 염소이온 농도를 센싱하여 그에 비례하는 전기적 아날로그 신호를 콘트롤부(23)로 출력하게 되며, 상기 콘트롤부(23)에서는 잔류염소이온 농도감지센서(21)로부터 출력되는 신호를 디지털 데이터로 변환 및 비교 분석하여 잔류염소이온농도에 따라 전해살균장치(10)의 구동을 결정하게 된다.That is, the residual chlorine ion concentration detection sensor 21 senses the residual chlorine ion concentration in the ballast tank and outputs an electrical analog signal proportional thereto to the control unit 23, and the residual chlorine ion in the control unit 23. The signal output from the concentration sensor 21 is converted into digital data and compared and analyzed to determine the driving of the electrolytic sterilizer 10 according to the residual chlorine ion concentration.

상기 콘트롤부(23)에서 측정한 잔류염소이온농도에 기준 농도에 미치지 못하는 것으로 판단(단계 107)되면 세팅된 전류데이터 값을 전류제어부(24)와 극성전환부(25)를 통해 불용성 전극(11)(12)에 전류를 공급(단계 108)함에 따라 전기분해를 발생시켜 지속적으로 차아염소산나트륨을 생성하도록 하고, 상기 콘트롤부(23)에서 측정한 잔류염소이온농도에 기준 농도에 도달할 경우 전류제어부(24)를 오프시켜(단계 109) 전기분해를 중단시킴으로써 밸러스트탱크내의 차아염소산나트륨의 농도를 일정하게 유지되도록 하여 살균효과를 극대화 한 것이다. If it is determined that the residual chlorine ion concentration measured by the control unit 23 does not reach the reference concentration (step 107), the set current data value is insoluble electrode 11 through the current control unit 24 and the polarity switching unit 25. By supplying a current to step (12) (step 108), electrolysis is generated to continuously generate sodium hypochlorite, and when the residual concentration of chlorine ion measured by the control unit 23 reaches a reference concentration, the current The control unit 24 is turned off (step 109) to stop electrolysis so that the concentration of sodium hypochlorite in the ballast tank is kept constant to maximize sterilization effect.

이와 같이 본 발명은 전기 분해가 이루어지는 동안 표면 오염이 일어나는 음 극에 펄스전압이 인가되어 운전되므로 높은 전위차에 의해 기존의 전해법 보다 살균효율이 향상되며, 전극의 오염을 방지하게 됨으로써 전해살균장치의 전류효율을 최적화 할 수 있어 성능을 일정하게 유지하는 것이 가능하게 되는 것이다.As described above, since the present invention operates by applying a pulse voltage to the cathode where surface contamination occurs during electrolysis, the sterilization efficiency is improved by the high potential difference and prevents contamination of the electrode. By optimizing the current efficiency, it is possible to keep the performance constant.

또한, 전극의 오염을 방지하는 펄스발생기로 인하여 정전류 및 정전압 운전이 가능하여 전력비가 기존의 전기분해법에 비해 저렴하고 약품 사용 시에 비해 유지비가 현저히 절감될 뿐만 아니라, 이로 인해 일정한 전류효율이 유지됨에 따라 유지 관리가 용이하여 수질관리를 위한 인력이 필요 없게 되는 것이다.In addition, constant current and constant voltage operation are possible due to the pulse generator that prevents contamination of the electrode, so that the power cost is lower than that of the conventional electrolysis method, and the maintenance cost is considerably reduced compared to the use of chemicals, thereby maintaining a constant current efficiency. Therefore, it is easy to maintain, so that no manpower for water quality management is required.

또한, 밸러스트수 살균에 적용되는 약품을 이용한 방법보다 전극오염방지 설비가 부착된 전해살균장치가 안전하며, 안정적으로 짧은 시간에 살균하여 국제해사기구에서 밸러스트수에 의한 생태계 파괴 및 오염을 방지하기 위한 방안을 만족 시킬 수 있는 것이다.In addition, the electrolytic sterilizer equipped with electrode contamination prevention equipment is safer than the method using the chemicals applied to the ballast water sterilization, and it is sterilized in a short time stably to prevent the destruction of the ecosystem by the ballast water in the ecosystem by the International Maritime Organization. You can satisfy the room.

이상에서 상술한 바와 같이 본 발명은 전해살균장치를 양극(+)과 음극(-) 모두 티탄 소재 불용성 전극을 각각 설치하고, 극성변환장치에 의해 양극과 음극을 일정 주기로 극성을 전환하여 전해하도록 함으로써 차아염소산나트륨을 중단 없이 생성하여 살균효과를 지속적으로 높이는 효과가 있는 것이다.As described above, in the present invention, the electrolytic sterilizer is provided with an insoluble electrode of titanium material for both the positive electrode (+) and the negative electrode (-), and the positive electrode and the negative electrode are switched to each other at regular intervals by the polarity conversion device to perform electrolysis. Sodium hypochlorite is produced without interruption to increase the sterilization effect continuously.

또한, 본 발명은 펄스발생기를 부가하여 상기 극성변환장치에 의해 양극과 음극이 일정한 주기로 극성이 전환되어 전해가 이루어질 때 음극에 펄스를 인가하고, 이 펄스에 의한 미세 진동을 발생시켜 전극의 표면에 수산화염화합물이 부착되는 것을 방지함으로써 전류 및 전해효율을 높이는 효과가 있는 것이다.In addition, the present invention, by adding a pulse generator, the polarity of the positive electrode and the negative electrode is switched by a certain period of time by the polarity conversion device to apply a pulse to the cathode when the electrolysis is performed, and generates a fine vibration by the pulse to the surface of the electrode By preventing the attachment of the hydroxide compound is effective to increase the current and electrolytic efficiency.

또한, 본 발명은 전류조절장치를 부가하여 밸러스트 탱크내에 유입되는 해수의 량에 따라 전극에 인가되는 전류를 증감하여 차아염소산나트륨의 농도를 자동 제어함으로써 해수가 밸러스트 탱크 내에 유입되기 전 원활한 살균이 이루어지는 효과가 있는 것이다. In addition, the present invention by adding a current regulator to increase or decrease the current applied to the electrode according to the amount of seawater flowing into the ballast tank to automatically control the concentration of sodium hypochlorite smooth sterilization before seawater is introduced into the ballast tank It works.

또한, 본 발명은 밸러스트 탱크내의 잔류염소이온농도를 센싱하여 유입된 밸러스트수의 량에 비례하여 차아염소산나트륨의 농도를 일정하게 유지시켜 살균이 지속적으로 이루어지도록 함으로서 선박의 선체 안정을 유지하기 위해 배의 바닥에 싣는 밸러스트수를 보다 효과적으로 살균하는 효과가 있는 것이다.In addition, the present invention senses the residual chlorine ion concentration in the ballast tank to maintain a constant concentration of sodium hypochlorite in proportion to the amount of ballast water introduced to maintain the ship's hull stability by maintaining sterilization It is effective to sterilize the ballast water on the bottom of the ball more effectively.

Claims (1)

티탄소재 불용성 전극이 구비된 전해살균장치(10)에 의한 해수의 전기분해로 차아염소산나트륨를 생성하여 해수에 포함된 세균을 살균하는 선박 밸러스트수 전해살균시스템에 있어서,In the marine ballast water electrolytic sterilization system which sterilizes bacteria contained in seawater by generating sodium hypochlorite by electrolysis of seawater by an electrolytic sterilizer 10 equipped with a titanium carbon insoluble electrode, 상기 전해살균장치(10)는 해수를 전기 분해시키는 두개의 티탄 소재 불용성 전극(11)(12)으로 이루어지고,The electrolytic sterilizer 10 is composed of two titanium-based insoluble electrodes (11, 12) for electrolyzing sea water, 밸러스트탱크 내에 설치되어 해수의 잔류염소이온농도를 센싱하여 그에 비례하는 전기적신호를 발생하는 잔류염소이온 농도감지센서(21)와,Residual chlorine ion concentration sensor 21 is installed in the ballast tank and senses the residual chlorine ion concentration of seawater and generates an electrical signal in proportion thereto; 밸러스트탱크 내에 해수를 유입시키는 펌프의 배관에 설치되어 해수의 유입량을 센싱하여 그에 비례하는 전기적신호를 발생하는 유량감지센서(22)와,A flow rate sensor 22 installed in a pipe of a pump for introducing seawater into the ballast tank and sensing an inflow amount of seawater to generate an electrical signal proportional thereto; 상기 불용성 전극(11)(12)에 연결되어 일정한 주기로 양극과 음극(11)(12)의 극성을 변환시켜 전기 분해시키는 극성전환부(25)와,A polarity switching unit 25 connected to the insoluble electrodes 11 and 12 and converting the polarity of the positive electrode and the negative electrode 11 and 12 at regular intervals to electrolyze; 상기 극성전환부(25)의 입력단에 연결되어 상기 불용성 전극(11)(12)에 공급되는 전류를 조절하는 전류제어부(24)와,A current control unit 24 connected to an input terminal of the polarity switching unit 25 to adjust a current supplied to the insoluble electrodes 11 and 12; 상기 불용성 전극(11)(12)에 연결되어 수산화염화합물이 음전극 표면에 부착되는 것을 방지하기 위해 미세진동을 발생시키는 펄스발생기(26)와,A pulse generator 26 connected to the insoluble electrodes 11 and 12 to generate micro vibrations to prevent the hydroxide compound from adhering to the negative electrode surface; 상기 잔류염소이온 농도감지센서(21) 및 유량감지센서(22)의 출력신호에 의해 상기 전류제어부(24),극성전환부(25), 펄스발생기(26)를 제어하는 콘트롤부(23)로 이루어지는 것을 특징으로 하는 선박 밸러스트수 전해살균시스템의 제어장치.By the output signal of the residual chlorine ion concentration detection sensor 21 and the flow rate detection sensor 22 to the control unit 23 for controlling the current control unit 24, the polarity switching unit 25, the pulse generator 26 Control device for ship ballast water electrolytic sterilization system, characterized in that made.
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US11027991B2 (en) 2017-10-05 2021-06-08 ElectroSea, LLC Electrolytic biocide generating system for use on-board a watercraft
US11718542B2 (en) 2017-10-05 2023-08-08 ElectroSea, LLC Electrolytic biocide generating system for use on-board a watercraft
KR101828598B1 (en) 2017-11-27 2018-02-12 임한귀 Seawater Electrolyer not using Acid Cleaning
US11345621B2 (en) 2019-02-11 2022-05-31 ElectroSea, LLC Self-treating electrolytic biocide generating system with recirculation
US11866351B2 (en) 2019-02-11 2024-01-09 ElectroSea, LLC Self-treating electrolytic biocide generating system with recirculation
US11498855B2 (en) 2019-04-09 2022-11-15 ElectroSea, LLC Electrolytic biocide-generating unit

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