CN201620053U - Ship ballast water treatment system - Google Patents
Ship ballast water treatment system Download PDFInfo
- Publication number
- CN201620053U CN201620053U CN2010201146084U CN201020114608U CN201620053U CN 201620053 U CN201620053 U CN 201620053U CN 2010201146084 U CN2010201146084 U CN 2010201146084U CN 201020114608 U CN201020114608 U CN 201020114608U CN 201620053 U CN201620053 U CN 201620053U
- Authority
- CN
- China
- Prior art keywords
- treatment system
- ballast water
- water treatment
- ship ballast
- pipeline
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Images
Landscapes
- Physical Water Treatments (AREA)
Abstract
The utility model relates to the technical field of environment protection and ship protection, and particularly relates to a ship ballast water treatment system which is characterized in that a ballast pump (1), a salinity sensor or an electric conductivity sensor (2), a filter (3), a flowmeter (4), an automatic control and alarm unit (5), an EUT unit (6), a total residual oxide sensor (7), a valve and a pipeline are included. The system adopts physical filtration technology, electrocatalysis technology and physical ultrasonic technology at the same time and has the benefits that pelagic flora and fauna, as well as other organisms in the ship ballast water can be killed more effectively; and no toxic by-products are produced, thereby realizing safer, environment-friendly and high reliable use.
Description
Technical field
The utility model relates to environment protection and hull protection technical field, especially a kind of ship ballast water treatment system.
Background technology
Water ballast can be guaranteed the correct center of gravity and the necessary balance and the stability of boats and ships.At present, nearly 10,000,000,000 tons of the water ballast that annual global boats and ships carry, have at least every day 7000 organisms etc. with the ballast water for ship oceangoing voyage to alien land.Species are invaded mutually, have aggravated the deterioration of marine ecology chain and environment.The ballast water yield that 190,000 tons of freighters of a load-carrying carry has surpassed 80,000 tons, the animals and plants that swim in the water ballast average every cubic metre up to 1.1 hundred million, the biology that every day, carried in water ballast in the whole world has surpassed 3000 kinds, and 300,000,000 of survival dinoflagellate packings are arranged in a water ballast tank.Portion investigation from Hong Kong shows: found 81 kinds of meiofauna and protozoons that the locality does not have in five ship water ballast water samples that selective examination is navigated.
Though severe environment such as that most of hydrobiont can't be stood is unglazed in the ballast tank, anoxic, iron content height are and dead on the road, minority " powerhouse " but can arrive the unballast waters smoothly, and bases oneself upon breeding in the locality, becomes the invader.The invasion of this adventive can cause the destruction of harbour state aquatic ecological, brings loss to local economy.Ballast water for ship also may carry the pathogenic agent with strict region epidemic characteristic, causes epiphytotics propagation, threatens the harbour state public's health.International Maritime Organizaton (International MaritimeOrganization, be called for short IMO) 2004 has formulated water ballast and settling management contract at the water ballast pollution present situation, requires various countries' boats and ships that ballast water treatment plant was installed after 2010 successively.
It is the focal issue of a global concern that IMO points out to administer the invasion of water ballast harmful organism, does not advocate different regions and adopts different improvement systems.Basic demand is: aboard ship handle; Cost is cheap, and equipment is small and exquisite, is convenient to operation; Nearshore waters, ocean environment not being formed new pollution, should be green harmless improvement novel method.For this reason, existing in the world multiple ballast water processing, they are mainly:
1, filtration method
In the ballast operating process,, can play the effect that prevents and reduce the harmful organism suction from water ballast by using the filtering system on the ship that a certain size biology is separated.
Filtering the validity that surpasses filter screen aperture object is 95%-98%, and the thickness aperture that generally is used for the wedge filter system of water ballast is respectively 500 μ m and 50 μ m.
2, ultraviolet method
Wavelength is that the ultraviolet ray of 253.7nm has killing action to biological and pathogenic agent.Because the organic solute in the seawater has the intensive sorption to the ultraviolet ray of this section wavelength, and suspended substance is to its barrier effect, so can influence treatment effect.Another shortcoming of this treatment process is that some little biologies may not obtain handling under the shadow than mcroorganism and just left the UV treatment unit, and turbid water can reduce ultraviolet penetrativity.Behind the large-scale microorganism of filtering with the UV treatment water ballast be a kind of effectively and the method that allows of environment, this technology all has no adverse effects to pipeline, pump etc.
3, electrolytic process
Chlorine is a kind of with a long history, sterilizing agent efficiently, extensively applies in the disinfecting of tap water.The disinfectant properties of chlorine is relevant with temperature and duration of contact.Domestic existing research electrolytic seawater obtains conclusion as the treatment process of water ballast: seawater can generate multiple material after by electrolysis, as ClO
-, Cl
2, strong oxidizing property material such as HClO, they are greater than the corrosion speed of hull in ortho-water to the corrosion speed of hull.Generated a series of toxic byproducts that have simultaneously, such material is discharged in the ocean can cause certain murder by poisoning to hydrobiont.
4, ozone method
Ozone is the very strong but unsettled oxygenant of a kind of oxidisability, and kill virus and bacterium comprise spore fast, and ozone can be decomposed into oxygen very soon, when water temperature 20 is spent, can lifetime in water less than 30min, so very little to the influence of environment.Producing of ozone is fairly simple, preparation in the air at sea.Compare with system chlorine device, the initial outlay total expenses of ozone equipment is higher relatively.When ozone dosage is big, can promote the corrosion of hull and equipment, and ozone can with the bromide reaction in the seawater, so use the ozonize water ballast to need very big dosage separately.
Above-mentioned 4 kinds of methods all have limitation separately, and the water ballast pact is approaching day by day execution date, and the ballast water treatment technology of anxious To be improved occurs, and this technology can reach the requirement of IMO water ballast pact, simultaneously safety and environmental protection, reliability height.
The utility model content
Defective at above-mentioned various ballast water treatment technology, the utility model has disclosed a kind of novel ship ballast water treatment system and has come processing ballast, this system has adopted physical filtering technology, electrocatalysis technology, materialization ultrasonic technique simultaneously, can kill swim animals and plants and individual littler other biological in the ballast water for ship efficiently; It is realized by the following technical solutions:
A kind of novel ship ballast water treatment system, it is characterized in that it comprises ballast pump 1, salinometer sensor or conductivity sensor 2, strainer 3, under meter 4, control and alarm unit 5, EUT (Electrocatalysis enhanced by Ultrasonic Technology refers to ultrasound-enhanced electrocatalysis technology) unit 6, total surplus oxide compound transmitter 7, valve and pipeline automatically; One side of ballast pump 1 connects the front end inlet channel, and opposite side connects the rear end inlet channel; Salinometer sensor or conductivity sensor 2 are installed on the inlet channel of rear end; The rear end inlet channel connects the water-in of strainer 3, the water outlet of strainer 3 is connected with a pipeline, and under meter 4 is installed on this pipeline, and this pipeline is connected with the inlet of EUT unit 6, the exit of EUT unit 6 is connected with a pipeline, and total surplus oxide compound transmitter 7 is installed on this pipeline.
Above-mentioned described strainer is by controlling backwash process with the pressure reduction of atmosphere formation.
Above-mentioned described strainer is many cartridge structures, and filtration and recoil are carried out simultaneously, are independent of each other.
Above-mentioned described filter element can be mesh grid, wedge shape net or sintering net.
The filter pore diameter of above-mentioned described strainer is the 10-100 micron.
Above-mentioned described EUT unit comprises electrocatalysis treating part and supersound process part.
Tabular or cylindric catalysis electrode is adopted in above-mentioned described electrocatalysis treating part.
Above-mentioned described supersound process partly adopts distributing ultra-sonic generator or energy-collecting ultrasonic producer.
Above-mentioned described energy-collecting ultrasonic frequency generator is 20-50KHz.
Above-mentioned described distributing ultra-sonic generator frequency is 20-80KHz.
Principle of the present utility model is: water enters the water ballast pipeline; Salinometer sensor or conductivity sensor test water inlet salinity or specific conductivity are transferred to automatic control section simultaneously; Automatically control and alarm unit are judged according to the data that transmission obtains, and output order is given the EUT unit, and the EUT unit produces quantitative hydroxyl free group according to instruction; Water by strainer, enters in the EUT unit earlier then, and hydroxyl radical free radical is killed organism in water; Water enters ballast tank or is discharged into the hull outside.In treating processes, total surplus oxide compound transmitter is detecting the concentration of oxidizing substance always, be transferred to automatic control and alarm unit simultaneously, if oxidizing substance concentration exceeds default value, automatically control and alarm unit can be given the EUT unit by output order, order it to reduce the concentration that produces hydroxyl free.If system breaks down, control and alarm unit can send sound and light alarm automatically, take corresponding emergency measures simultaneously.Physical filtering technology, electrocatalysis technology, materialization ultrasonic technique act on simultaneously in this system, can produce the hydroxyl radical free radical active group of high density, and this free group is killed living body biological in the water.Hydroxyl radical free radical is that hydrogen and oxygen element are formed, its oxidation capacity is only second to the material of fluorine, it can moment most of materials such as organism of oxidation contact, can moment kill biology, the hydroxyl radical free radical reduzate is carbonic acid gas and water, and is therefore all nontoxic to environment and human body.This system device can be implemented in swim animals and plants and the microorganism that line is efficiently killed the ballast water for ship kind.
The utlity model has following beneficial effect: can kill swim animals and plants and individual littler other biological in the ballast water for ship more efficiently; And can not produce toxic byproduct, therefore safety and environmental protection, reliability are more increased more.
Description of drawings
Fig. 1 is the system diagram of the part of the utility model embodiment;
Fig. 2 is the system diagram of another part of the utility model embodiment.
Embodiment
See also Fig. 1 and Fig. 2, the pipeline among Fig. 1 the A place be with Fig. 2 in pipeline at the B place for one.A kind of novel ship ballast water treatment system is characterized in that it comprises ballast pump 1, salinometer sensor or conductivity sensor 2, strainer 3, under meter 4, control and alarm unit 5, EUT unit 6, total surplus oxide compound transmitter 7, valve and pipeline automatically; One side of ballast pump 1 connects the front end inlet channel, and opposite side connects the rear end inlet channel; Salinometer sensor or conductivity sensor 2 are installed on the inlet channel of rear end; The rear end inlet channel connects the water-in of strainer 3, the water outlet of strainer 3 is connected with a pipeline, and under meter 4 is installed on this pipeline, and this pipeline is connected with the inlet of EUT unit 6, the exit of EUT unit 6 is connected with a pipeline, and total surplus oxide compound transmitter 7 is installed on this pipeline.
Above-mentioned described strainer is by controlling backwash process with the pressure reduction of atmosphere formation.
Above-mentioned described strainer is many cartridge structures, and filtration and recoil are carried out simultaneously, are independent of each other.
Above-mentioned described filter element can be mesh grid, wedge shape net or sintering net.
The filter pore diameter of above-mentioned described strainer is the 10-100 micron.
Above-mentioned described EUT unit comprises electrocatalysis treating part and supersound process part.
Tabular or cylindric catalysis electrode is adopted in above-mentioned described electrocatalysis treating part.
Above-mentioned described supersound process partly adopts distributing ultra-sonic generator or energy-collecting ultrasonic producer.
Above-mentioned described energy-collecting ultrasonic frequency generator is 20-50KHz.
Above-mentioned described distributing ultra-sonic generator frequency is 20-80KHz.
Principle of the present utility model is: water enters the water ballast pipeline; Salinometer sensor or conductivity sensor test water inlet salinity or specific conductivity are transferred to automatic control section simultaneously; Automatically control and alarm unit are judged according to the data that transmission obtains, and output order is given the EUT unit, and the EUT unit produces quantitative hydroxyl free group according to instruction; Water by strainer, enters in the EUT unit earlier then, and hydroxyl radical free radical is killed organism in water; Water enters ballast tank or is discharged into the hull outside.In treating processes, total surplus oxide compound transmitter is detecting the concentration of oxidizing substance always, be transferred to automatic control and alarm unit simultaneously, if oxidizing substance concentration exceeds default value, automatically control and alarm unit can be given the EUT unit by output order, order it to reduce the concentration that produces hydroxyl free.If system breaks down, control and alarm unit can send sound and light alarm automatically, take corresponding emergency measures simultaneously.Physical filtering technology, electrocatalysis technology, materialization ultrasonic technique act on simultaneously in this system, can produce the hydroxyl radical free radical active group of high density, and this free group is killed living body biological in the water.Hydroxyl radical free radical is that hydrogen and oxygen element are formed, its oxidation capacity is only second to the material of fluorine, and most of materials such as organism that it can the moment oxidation be contacted can kill biology moment, the hydroxyl radical free radical reduzate is carbonic acid gas and water, and is therefore all nontoxic to environment and human body.This system device can be implemented in swim animals and plants and the microorganism that line is efficiently killed the ballast water for ship kind.
The utlity model has following beneficial effect: can kill swim animals and plants and individual littler other biological in the ballast water for ship more efficiently; And can not produce toxic byproduct, therefore safety and environmental protection, reliability are more increased more.
This paper understands exemplary embodiment of the utility model and present preferred implementation specifically, should be appreciated that design of the present utility model can be by other various forms enforcement utilizations, and they drop in the protection domain of the present utility model equally.
Claims (9)
1. novel ship ballast water treatment system is characterized in that it comprises ballast pump (1), salinometer sensor or conductivity sensor (2), strainer (3), under meter (4), control and alarm unit (5), EUT unit (6), total surplus oxide compound transmitter (7), valve and pipeline automatically; One side of ballast pump (1) connects the front end inlet channel, and opposite side connects the rear end inlet channel; Salinometer sensor or conductivity sensor (2) are installed on the inlet channel of rear end; The rear end inlet channel connects the water-in of strainer (3), the water outlet of strainer (3) is connected with a pipeline, under meter (4) is installed on this pipeline, this pipeline is connected with the inlet of EUT unit (6), the exit of EUT unit (6) is connected with a pipeline, and total surplus oxide compound transmitter (7) is installed on this pipeline.
2. ship ballast water treatment system as claimed in claim 1 is characterized in that described strainer is many cartridge structures, and filtration and recoil are carried out simultaneously, are independent of each other.
3. ship ballast water treatment system as claimed in claim 1 is characterized in that described filter element is mesh grid or wedge shape net or sintering net.
4. ship ballast water treatment system as claimed in claim 1, the filter pore diameter that it is characterized in that described strainer is the 10-100 micron.
5. ship ballast water treatment system as claimed in claim 1 is characterized in that described EUT unit comprises electrocatalysis treating part and supersound process part.
6. ship ballast water treatment system as claimed in claim 5 is characterized in that described electrocatalysis treating part is tabular or cylindric catalysis electrode.
7. ship ballast water treatment system as claimed in claim 5 is characterized in that described supersound process partly is distributing ultra-sonic generator or energy-collecting ultrasonic producer.
8. ship ballast water treatment system as claimed in claim 7 is characterized in that described energy-collecting ultrasonic frequency generator is 20-50KHz.
9. ship ballast water treatment system as claimed in claim 7 is characterized in that described distributing ultra-sonic generator frequency is 20-80KHz.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201146084U CN201620053U (en) | 2010-02-10 | 2010-02-10 | Ship ballast water treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201146084U CN201620053U (en) | 2010-02-10 | 2010-02-10 | Ship ballast water treatment system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201620053U true CN201620053U (en) | 2010-11-03 |
Family
ID=43023510
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010201146084U Expired - Lifetime CN201620053U (en) | 2010-02-10 | 2010-02-10 | Ship ballast water treatment system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201620053U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102092814A (en) * | 2011-03-23 | 2011-06-15 | 青岛海德威科技有限公司 | Device for treating ship ballast water |
| CN102363544A (en) * | 2011-09-15 | 2012-02-29 | 南通海景船舶压载水处理系统股份有限公司 | Filter ultrasonic and electrolytic ultrasonic ship ballast water treatment equipment and treatment method |
| CN103507940A (en) * | 2013-09-12 | 2014-01-15 | 南通明德重工有限公司 | Bulk cargo ship with EP sign |
| CN104045198A (en) * | 2014-07-08 | 2014-09-17 | 曹学良 | Modularized ship ballast water treatment system |
-
2010
- 2010-02-10 CN CN2010201146084U patent/CN201620053U/en not_active Expired - Lifetime
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102092814A (en) * | 2011-03-23 | 2011-06-15 | 青岛海德威科技有限公司 | Device for treating ship ballast water |
| CN102092814B (en) * | 2011-03-23 | 2013-09-18 | 青岛海德威科技有限公司 | Device for treating ship ballast water |
| CN102363544A (en) * | 2011-09-15 | 2012-02-29 | 南通海景船舶压载水处理系统股份有限公司 | Filter ultrasonic and electrolytic ultrasonic ship ballast water treatment equipment and treatment method |
| CN103507940A (en) * | 2013-09-12 | 2014-01-15 | 南通明德重工有限公司 | Bulk cargo ship with EP sign |
| CN104045198A (en) * | 2014-07-08 | 2014-09-17 | 曹学良 | Modularized ship ballast water treatment system |
| CN104045198B (en) * | 2014-07-08 | 2016-01-13 | 曹学良 | A kind of Modular ship ballast water treatment system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Tsolaki et al. | Technologies for ballast water treatment: a review | |
| Gregg et al. | Review of two decades of progress in the development of management options for reducing or eradicating phytoplankton, zooplankton and bacteria in ship’s ballast water | |
| JP5127983B2 (en) | A kind of low current electrolysis sterilization algae device and method | |
| CN102933504B (en) | Emissions control system and method | |
| CN101068750B (en) | System and method for treatment of ballast water | |
| CN102515400A (en) | High-efficiency treatment method of ballast water in ship | |
| CN101918326A (en) | Ballast water treatment system and method | |
| CN101484389A (en) | Ballast water treatment plant having filter, disinfection, instrumentation and control unit | |
| CN101531410B (en) | Ocean vessel ballast water processing method and special system using same | |
| WO2011120250A1 (en) | Method and system for ship ballast water treatment | |
| CN101781043B (en) | Novel ballast water treatment method and device | |
| KR101923094B1 (en) | Ballast water treatment system with a low temperature water plasma device | |
| CN104016533A (en) | Ship ballast water treating method | |
| CN101519235A (en) | Ultrasonic intensified self-descaling micro-current electrolysis device for sterilizing and removing alga | |
| CN201620053U (en) | Ship ballast water treatment system | |
| JP2013525091A (en) | Ballast water treatment system using high efficiency electrolyzer | |
| CN202046961U (en) | Ship ballast water treatment system | |
| CN105617841B (en) | A kind of ship tail gas desulfurization and ballast water for ship integrated processing technique | |
| CN202717658U (en) | Ship ballasting water treatment device applicable to seawater/fresh water | |
| CN202337715U (en) | Ship ballast water treating system | |
| JP2016083627A (en) | Water purifier using photocatalyst | |
| Mesbahi | Latest results from testing seven different technologies under the EU MARTOB project-Where do we stand now | |
| CN104030504A (en) | Intelligent selection type ship ballast water treating method and apparatus | |
| CN202717657U (en) | Composite ship ballasting water treatment device | |
| CN202671338U (en) | Ship ballast water treatment equipment with filtering ultrasound and ultraviolet |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20101103 |
|
| CX01 | Expiry of patent term |