CN202717657U - Composite ship ballasting water treatment device - Google Patents
Composite ship ballasting water treatment device Download PDFInfo
- Publication number
- CN202717657U CN202717657U CN 201220202036 CN201220202036U CN202717657U CN 202717657 U CN202717657 U CN 202717657U CN 201220202036 CN201220202036 CN 201220202036 CN 201220202036 U CN201220202036 U CN 201220202036U CN 202717657 U CN202717657 U CN 202717657U
- Authority
- CN
- China
- Prior art keywords
- water
- removal device
- algae removal
- sterilization algae
- ballast
- 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 - Fee Related
Links
Images
Abstract
The utility model discloses a composite ship ballasting water treatment device, which is arranged among a ship outer main water taking port, a ballasting water cabin with a water filling port and a water drainage port and a ship outer main discharging port, and the composite ship ballasting water treatment device also comprises a primary sterilizing algae removal device with an electrolysis device and a first ultrasonic device and a secondary sterilizing algae removal device with a ultraviolet device and a second ultrasonic device, a water inlet of a ballasting pump is simultaneously connected with the ship outer main water taking port and the water discharging port, a water outlet of the ballasting pump is simultaneously connected with a water inlet of the filter, a water inlet of the secondary sterilizing algae removal device and the ship outer main discharging port, the water outlet of the filter is connected with a water inlet of the primary sterilizing algae removal device, a water outlet of the primary sterilizing algae removal device is connected with the water inlet of the secondary sterilizing algae removal device, and the water outlet of the secondary sterilizing algae removal device is simultaneously connected with the water filling port and the ship outer main discharging port. Processing units of the composite ship ballasting water treatment device can form different combination, so that the form is diversified, the application range is wide, and the sterilizing algae removal effect is thorough.
Description
Technical field
The utility model belongs to the ballast for cruising water-treatment technology field, especially relates to a kind of apparatus for treating ship ballast water.
Background technology
At present the quantum of international trade is that transportation by oceangoing vessel realizes more than 90%, when ballast water for ship without processing or process when thoroughly just not carrying out the strange land discharging, will very likely cause the alien species invasion.As have " ctenophore event ", " vibrio cholerae pollution incident " of Typical Representative etc.Halobiontic invasion has non-reversibility, and its caused environmental hazard can grow in intensity along with the transition of time, is therefore classified as four greatly one of harm that the ocean faces by International Maritime Organizaton (IMO).
Carry out the harm that the discharging of ballast water and sediment strange land brings for effectively controlling oceangoing vessel, member states's diplomacy conference that IMO holds has been passed through " Management of Ships ' Ballast Water and settling management and control pact " on February 13rd, 2004 in London, this pact has been opened for various countries' official approval on June 1st, 2004 and accepted.
China is as the category-A member of the UN Security Council of shipping big country and IMO, the present oceangoing vessel tons gross of China accounts for 3.4% of world tonnage, it is second-biggest-in-the-world sea transport state, industrialization lags behind may meet with technical monopoly and trade barrier, exploitation has independent intellectual property right and practical ballast water treatment technology, and tool is of great significance.
Different according to the route of ship's navigation and zone, the ballast water type also has difference, and water ballast may be fresh water, brackish water or seawater.The biological species that contains in the water ballast mainly contains algae, bacterium, fungi, mould, virus, fish-egg, protozoon etc., easily discharges the algae toxin when wherein algae is killed under conventional means, causes secondary pollution; Part bacterium and fungi can form gemma and spore under certain unfavourable condition, activity recovery gradually again when adverse environment is removed, so be difficult to kill fully.
Ballast water treatment technology commonly used comprises the methods such as traditional filtering method, Ozonation, electrolytic process, ultraviolet disinfection at present, and prior art is the processing for seawater ballast water mostly, when the route of ship's navigation and area change, the ballast water type also will change, and single treatment process can't be processed it.
The traditional filtering method is after water ballast is carried out coagulation-flocculation treatment, filter with filtering layer, thereby purify water, but its clearance to be limited, especially then can't remove fully the less bacterium of particle diameter, fungi, virus.
The ozone oxidation method for disinfection mainly is by the required enzyme of the inner glucose of decomposing bacteria, or organoid and DNA, the RNA of destruction bacteriophage, or in the intrusion cell, act on lipoprotein and the inner lipopolysaccharides of adventitia, make the distortion of bacterium generation permeability and dissolving death.But the problem that exists is that occupation area of equipment is larger, installs restricted on the ship; Ozonated sea water can produce the objectionable impuritiess such as bromate, may produce secondary pollution.
Ultraviolet sterilizing method mainly is with the function of destroying nucleic acid microorganism to be caused death by the radiation injury to microorganism (pathogenic agent such as bacterium, virus, gemma), thereby reaches the purpose of sterilization.The problem that ultraviolet ray is used for the processing existence of water ballast is: 1, seawater contains a large amount of suspended matter meeting shielding of ultraviolet to the irradiation of biology and pathogenic agent, affect treatment effect, and energy consumption is very large; 2, the treatment effect quality depends on the size and geometric of microorganism to a great extent, such as seaweeds, because its size and color, the dose ratio bacterium that needs is large, bluish-green marine alga is to ultraviolet resistivity extra-heavy, kills large 2 one 3 grades of the quantity that radiation quantity that its needs needs than killing bacteria; 3, some microorganism has possessed stronger self-repairing capability in long-term natural evolution process, can be to anti-ultraviolet processing, and some bacteriums and plant plankton also have similar repair ability, and treatment effect is undesirable.
Electrolytic process is to utilize the Cl that produces when electrolysis
2, C1O
2, HC1O, C1O
-Microorganism is killed or press down to be lived etc. efficient oxygenant, chlorine ion concentration is the important operating parameter of electrolytic process in the water.Boats and ships are different because of the waters of its navigation, and the characteristic of its water ballast is also different, mainly it can be divided into seawater, fresh water and brackish water.Brackish water is because of its residing geographical position, the exchanging form with seawater, evaporated, precipitation, freeze, the impact of ice-melt and land runoff, distribution of the salinity is uneven.Be determined by experiment chlorine ion concentration comparatively suitable preparing chlorine by electrolysis more than 15000mg/L, chlorine ion concentration is still feasible greater than 8000mg/L, but efficient is lower, and energy consumption is higher, chlorine ion concentration is not suitable for electrolysis less than 8000mg/L, need to replenish salt such as the need electrolysis and improve its chloride ion content.
Ultrasonic sterilization is a sterilizing and algae-removing technology of development in recent years, the heat effect that it utilizes the ultrasonic cavitation effect to be accompanied by, mechanical effect, chemical effect, biological effect comes deactivation biological, can produce up to the high temperature of 1900 ~ 5200K at ul-trasonic irradiation bubble and small interface place and surpass the high pressure of 50MPa, temperature can raise 10% at per second, and with strong shockwave and the speed per hour jet up to 400km/h, these conditions can be to open the algae air bag, destroy cell wall breaking, impel the zoogloea depolymerization, add its water burning, pyrolytic decomposition and very strong OH and the H of generation oxidisability
2O
2Material, thus effectively realize the bioinactivation of ballast water for ship.But supersonic method has the duration sterilization effect because containing chlorine residue unlike electrolytic process.
Some built-up type sterilising plants also appear at present, as electrolysis, ultrasonic wave and microwave, ultraviolet one or more serial or parallel connections are used, but because ballast water for ship relates to seawater, fresh water and brackish water, and the biological species that may comprise is various, the bad adaptability that causes the device of these combination techniques, can not process thoroughly various types of water ballasts, treatment effect is undesirable.
Summary of the invention
The purpose of this utility model provides a kind of compound apparatus for treating ship ballast water, uses same set of device just can process the water ballast of seawater, fresh water or brackish water, and adaptability is extensive, treatment effect good.
The technical solution of the utility model device is: a kind of compound apparatus for treating ship ballast water, be arranged on the total intake of outboard, have between the water ballast tank and the total discharge outlet of outboard of water filling port and water port, comprise ballast pump, strainer, elementary sterilization algae removal device and secondary sterilization algae removal device, wherein elementary sterilization algae removal device comprises electrolyzer and the first ultrasonic equipment that is arranged in the housing, secondary sterilization algae removal device comprises ultraviolet equipment and the second ultrasonic equipment that is arranged in the housing, the water inlet of described ballast pump connects the total intake of described outboard and described water port simultaneously, the water outlet of described ballast pump connects water inlet and the total discharge outlet of described outboard of strainer simultaneously, the water outlet of strainer connects the water inlet of elementary sterilization algae removal device, the water inlet of secondary sterilization algae removal device connects the water outlet of elementary sterilization algae removal device and the water outlet of described ballast pump simultaneously, and the water outlet of secondary sterilization algae removal device connects described water filling port and the total discharge outlet of described outboard simultaneously.
Electrolyzer in the elementary sterilization algae removal device can with seawater electrolysis, produce Cl
2, ClO
2, HC1O, C1O
-, OH, H
2O
2Etc. efficient oxygenant material, the ultrasonic cavitation effect can produce with the chlorine reaction oxidation operation of trichloromethane, destroy the air bag of algae, destroy the hypopuss such as spore, gemma, electrolysis and ultrasonic wave cooperate, and sterilization and disinfection energy force rate monotechnics is high, can be short in the reaction times, in the less situation of electric current, reach except the algae sterilising effect.The ultrasonic cavitation effect can also further be destroyed large zoogloea and be single microbial, destroys cell walls, and collaborative ultraviolet equipment is realized thoroughly killing organism within the extremely short time; The mechanical effect of vibration of ultrasonic wave cleans the incrustation on the negative electrode of electrolyzer, ultraviolet quartz socket tube surface in addition, makes the operation that system can be continual and steady.Seawater is through above-mentioned processing, and organism is thoroughly killed, and can realize direct discharging; For the fresh water water ballast, can utilize ultrasonic cavitation effect and ultraviolet equipment to cooperate, realization is thoroughly killed organism, during discharging, passes through ultrasonic cavitation and ultra-violet sterilization again, realizes safety dumping.In same set of device, electrolyzer, ultrasonic equipment and ultraviolet equipment can be used in combination, its strong adaptability, the sterilization algae removal that goes for seawater, fresh water or brackish water water ballast is processed, the sterilization algae removal time is short, contents of residual chlorine is low, and light to the erosion infringement of equipment, insect killing effect is thorough.
Between the total intake of described outboard and described ballast pump water inlet, between described water port and the described ballast pump water inlet, between described ballast pump water outlet and the total water port of described outboard, between described ballast pump water outlet and the described strainer water inlet, between described ballast pump water outlet and the described secondary sterilization algae removal device water inlet, between described secondary sterilization algae removal device water outlet and the described water filling port, be respectively equipped with valve between described secondary sterilization algae removal device water outlet and the total water port of described outboard.Realize processing to the different salinity water ballast by the opening and closing of controlling each valve.
The another kind of technical solution of the utility model device is: a kind of compound apparatus for treating ship ballast water, be arranged on the total intake of outboard, have between the water ballast tank and the total discharge outlet of outboard of water filling port and water port, comprise ballast pump, strainer, elementary sterilization algae removal device and secondary sterilization algae removal device, wherein elementary sterilization algae removal device comprises electrolyzer and the first ultrasonic equipment that is arranged in the housing, secondary sterilization algae removal device comprises ultraviolet equipment and the second ultrasonic equipment that is arranged in the housing, the water inlet of described ballast pump connects the total intake of described outboard and described water port simultaneously, the water outlet of described ballast pump connects the water inlet of strainer simultaneously, the water inlet of elementary sterilization algae removal device and the total discharge outlet of described outboard, the water outlet of strainer connects the water inlet of elementary sterilization algae removal device, the water outlet of elementary sterilization algae removal device connects the water inlet of secondary sterilization algae removal device, and the water outlet of secondary sterilization algae removal device connects described water filling port and the total discharge outlet of described outboard simultaneously.
Between the total intake of described outboard and described ballast pump water inlet, between described water port and the described ballast pump water inlet, between described ballast pump water outlet and the total water port of described outboard, between described ballast pump water outlet and the described strainer water inlet, between described ballast pump water outlet and the described elementary sterilization algae removal device water inlet, between described secondary sterilization algae removal device water outlet and the described water filling port, be respectively equipped with valve between described secondary sterilization algae removal device water outlet and the total water port of described outboard.Realize processing to the different salinity water ballast by the opening and closing of controlling each valve.
Electrolyzer in the sterilization algae removal chamber can with seawater electrolysis, produce Cl
2, ClO
2, HC1O, C1O
-, OH, H
2O
2Etc. efficient oxygenant material, the oxidation operation that the ultrasonic cavitation effect can produce with the chlorine reaction trichloromethane destroys the air bag of algae, destroy the hypopuss such as spore, gemma, electrolysis and ultrasonic wave cooperate, and sterilization and disinfection energy force rate monotechnics is high, reaction times is short, and chlorinity is low; The ultrasonic cavitation effect can also further be destroyed large zoogloea and be single microbial, destroys cell walls, and collaborative ultraviolet equipment is realized thoroughly killing organism within the extremely short time; The mechanical effect of vibration of ultrasonic wave cleans the incrustation on the negative electrode of electrolyzer, ultraviolet quartz socket tube surface in addition, makes the operation that system can be continual and steady.Seawater is through above-mentioned processing, and organism is thoroughly killed, and can realize direct discharging; For the fresh water water ballast, can utilize ultrasonic cavitation effect and ultraviolet equipment to cooperate, realization is thoroughly killed organism, during discharging, passes through ultrasonic cavitation and ultra-violet sterilization again, realizes safety dumping.Electrolyzer, ultrasonic equipment and ultraviolet equipment are used in combination, its strong adaptability, the sterilization algae removal time is short, and contents of residual chlorine is low, and light to the erosion infringement of equipment, insect killing effect is good.
Be provided with salinity measurement instrument or chlorion detector at the total intake of described outboard between the water inlet of described elementary sterilization algae removal chamber.The salinity that is used for the rapid detection water intaking, the suitable processing mode of convenient selection.
The utility model has the advantages that: need not to add other medicaments, non-secondary pollution is environmentally friendly technology; According to the characteristic of water ballast, can be combined to form different processing units, thoroughly kill contaminants of biological origin in the water ballast, flexible form, applied widely.Combination electrolysis and ultrasonic wave and ultraviolet ray and ultrasonic technology carry out multistage algae removal sterilization to water ballast, can be low at residual chlorine concentration, biological pollutant is carried out multistage killing under the condition that the reaction times is short, remove thoroughly, and prevent simultaneously the corrosion to equipment.
Description of drawings
Accompanying drawing 1 is the structure principle chart of the utility model embodiment 1;
Accompanying drawing 2 is the syndeton synoptic diagram of elementary sterilization algae removal device and secondary sterilization algae removal device among the utility model embodiment 1;
Accompanying drawing 3 is the structure principle chart of the utility model embodiment 2 embodiment 2;
1, the total intake of outboard, 2, the total discharge outlet of outboard, 3, ballast pump, 4, water ballast tank, 5, water filling port, 6, water port, 7, salinity measurement instrument or chlorion detector, 8, strainer, 9, electrolyzer, the 10, first ultrasonic equipment, 11, ultraviolet sterilizing lamp, 12, the second ultrasonic equipment, 13, elementary sterilization algae removal device, 14, secondary sterilization algae removal device, 15, housing, 16, housing, 17, anode, 18, negative electrode, 19, electrolysis power, 20, ballast power, 21, quartz socket tube, K1-K7, valve.
Embodiment
Embodiment 1:
Pipeline between total intake 1 and ballast pump 3 water inlets is provided with control valve K1 overboard, between the water inlet of the water outlet of ballast pump 3 and strainer 8, be provided with salinity measurement instrument or chlorion detector 7 and control valve K2, pipeline is provided with control valve K3 between the water outlet of secondary sterilization algae removal device 14 and water filling port 5, pipeline is provided with control valve K4 between the water inlet of water port 6 and ballast pump 3, be provided with control valve K5 at the water outlet of ballast pump 3 and the pipeline between secondary sterilization algae removal device 14 water inlets, be provided with control valve K6 at the water outlet of ballast pump 3 and the pipeline between the total discharge outlet 2 of outboard, the pipeline between secondary sterilization algae removal device 14 water outlets and the total discharge outlet 2 of outboard is provided with control valve K7.
Consult Fig. 2, in the present embodiment, elementary sterilization algae removal device 13 and secondary sterilization algae removal device 14 are separately positioned on two independently in the housing, wherein the electrolyzers 9 in the elementary sterilization algae removal device 13 comprise and are arranged on anode 17, the negative electrode 18 in the housing 15 and are arranged on the outer electrolysis power 19 of housing 15, the first ultrasonic equipment 10 be positioned at anode 17 and negative electrode 18 under, mechanical effect anticathode 18 surface dirts that utilize vibration of ultrasonic wave to produce are removed.Ultraviolet sterilizing lamp 11 in the secondary sterilization algae removal device 14 is set in the quartz socket tube 21 that is arranged in the housing 16, rectifier power supply 20 is arranged on outside the housing 16, the second ultrasonic equipment 12 is arranged on over against the side of quartz socket tube 21, utilizes mechanical effect that ultrasonic vibration produces that the surface dirt of quartz socket tube 21 is cleaned.
The present embodiment device is for water intaking and to the water ballast tank water filling time, open valve K1, K2, K3, all the other valve closess, the water ballast that extracts through ballast pump 3 filters through strainer 8, biology and the rubbish of size more than 50 μ m is removed, and detect by the chlorine ion concentration in salinity measurement instrument or 7 pairs of water ballasts of chlorion detector, choose the sterilizing treatmenting process of different water filling and draining according to detectable level, when chlorine ion concentration was greater than 15000mg/L in the water intaking, only optional step A processed; When chlorine ion concentration is less than 8000mg/L in the water intaking, can select step B1 or step B2 to process; When chlorine ion concentration is 8000mg/L-15000mg/L in the water intaking, can select steps A, step B1 or step B2 to process, wherein steps A is: water intaking is through filtering, by behind electrolyzer 9, the first ultrasonic equipment 10, ultraviolet sterilizing lamp 11 and the second ultrasonic equipment 12 sterilization algae removals, send in the water ballast tank 4 as water filling successively; Step B1 is: water intaking by behind ultraviolet sterilizing lamp 11 and the second ultrasonic equipment 12 sterilization algae removals, is sent in the water ballast tank 4 as water filling successively through filtering; Step B2 is: water intaking by behind the first ultrasonic equipment 10, ultraviolet sterilizing lamp 11 and the second ultrasonic equipment 12 sterilization algae removals, is sent in the water ballast tank 4 as water filling successively through filtering.
When water ballast tank 4 carried out draining, water ballast was extracted out from water port 6, and through ballast pump 3, chlorine ion concentration scope in the water intaking during corresponding water filling, when chlorine ion concentration was greater than 15000mg/L in the water intaking, only optional step A processed; When chlorine ion concentration is less than 8000mg/L in the water intaking, can select step B1 or step B2 to process; When chlorine ion concentration is 8000mg/L-15000mg/L in the water intaking, can select steps A, step B1 or step B2 to process.Particularly, the steps A during draining is: Open valve K4, K6, and all the other valve closess, water ballast is through directly discharging by the total discharge outlet 2 of outboard behind the ballast pump 3; Step B1 during draining is: Open valve K4, K5, K7, all the other valve closess, water ballast is sent in the secondary sterilization algae removal device 14 by ballast pump 3, enables ultraviolet sterilizing lamp 11 and the second ultrasonic equipment 12, after carrying out the sterilization algae removal processing, discharge by the total discharge outlet 2 of outboard.Step B2 during draining is: Open valve K4, K5, K7, all the other valve closess, water ballast is sent into elementary sterilization algae removal device 13 by ballast pump 3, enter again in the secondary sterilization algae removal device 14, enable ultraviolet sterilizing lamp 11 and the second ultrasonic equipment 12, after carrying out the sterilization algae removal processing, discharge by the total discharge outlet 2 of outboard.
In the present embodiment, for step B1 and step B2, its drainage processing method is only by i.e. discharging behind ultraviolet sterilizing lamp 11 and the second ultrasonic equipment 12 sterilization algae removals, processing mode when difference is water filling is different, step B2 is only by ultraviolet sterilizing lamp 11 and the second ultrasonic equipment 12 sterilization algae removals, and step B1 just carries out water filling by the first ultrasonic equipment 10, ultraviolet sterilizing lamp 11 and the second ultrasonic equipment 12 sterilization algae removals.
Embodiment 2:
Consult Fig. 3, be the compound apparatus for treating ship ballast water of another kind, be arranged on the total intake 1 of outboard, have between the water ballast tank 4 and the total discharge outlet 2 of outboard of water filling port 5 and water port 6, comprise ballast pump 3, strainer 8, elementary sterilization algae removal device 13 and secondary sterilization algae removal device 14, wherein elementary sterilization algae removal device 13 comprises housing 15, electrolyzer 9 and the first ultrasonic equipment 10, secondary sterilization algae removal device 14 comprises housing 16, ultraviolet sterilizing lamp 11 and the second ultrasonic equipment 12, the water inlet of ballast pump 3 is the outer total intake 1 of connected boat and water port 6 simultaneously, the water outlet of ballast pump 3 connects the water inlet of strainer 8 simultaneously, the total discharge outlet 2 of the water inlet of elementary sterilization algae removal device 13 and outboard, the water outlet of strainer 8 connects the water inlet of elementary sterilization algae removal device 13, the water outlet of elementary sterilization algae removal device 13 connects the water inlet of secondary sterilization algae removal device 14, and the water outlet of secondary sterilization algae removal device 14 connects water filling port 5 and the total discharge outlet 2 of outboard simultaneously.Solid line represents waterflood-transmission line among the figure, and dotted line represents water discharge line.
Pipeline between total intake 1 and ballast pump 3 water inlets is provided with control valve K1 overboard, pipeline between the water inlet of the water outlet of ballast pump 3 and strainer 8 is provided with salinity measurement instrument or chlorion detector 7 and control valve K2, pipeline is provided with control valve K3 between the water outlet of secondary sterilization algae removal device 14 and water filling port 5, pipeline is provided with control valve K4 between the water inlet of water port 6 and ballast pump 3, be provided with control valve K5 at the water outlet of ballast pump 3 and the pipeline between elementary sterilization algae removal device 13 water inlets, be provided with control valve K6 at the water outlet of ballast pump 3 and the pipeline between the total discharge outlet 2 of outboard, the pipeline between secondary sterilization algae removal device 14 water outlets and the total discharge outlet 2 of outboard is provided with control valve K7.
Consult Fig. 2, in the present embodiment, elementary sterilization algae removal device 13 and secondary sterilization algae removal device 14 are separately positioned on two independently in the housing, wherein the electrolyzers 9 in the elementary sterilization algae removal device 13 comprise and are arranged on anode 17, the negative electrode 18 in the housing 15 and are arranged on the outer electrolysis power 19 of housing 15, the first ultrasonic equipment 10 be positioned at anode 17 and negative electrode 18 under, mechanical effect anticathode 18 surface dirts that utilize vibration of ultrasonic wave to produce are removed.Ultraviolet sterilizing lamp 11 in the secondary sterilization algae removal device 14 is set in the quartz socket tube 21 that is arranged in the housing 16, rectifier power supply 20 is arranged on outside the housing 16, the second ultrasonic equipment 12 is arranged on over against the side of quartz socket tube 21, utilizes mechanical effect that ultrasonic vibration produces that the surface dirt of quartz socket tube 21 is cleaned.
The present embodiment device is for water intaking and to the water ballast tank water filling time, open valve K1, K2, K3, all the other valve closess, the water ballast that extracts through ballast pump 3 filters through strainer 8, biology and the rubbish of size more than 50 μ m is removed, and detect by the chlorine ion concentration in salinity measurement instrument or 7 pairs of water ballasts of chlorion detector, choose the sterilizing treatmenting process of different water filling and draining according to detectable level, when chlorine ion concentration was greater than 15000mg/L in the water intaking, only optional step A processed; When chlorine ion concentration was less than 8000mg/L in the water intaking, optional step B2 or step B3 processed; When chlorine ion concentration is 8000mg/L-15000mg/L in the water intaking, can select steps A or step B2 or B3 to process, wherein steps A is: water intaking is through filtering, by behind electrolyzer 9, the first ultrasonic equipment 10, ultraviolet sterilizing lamp 11 and the second ultrasonic equipment 12 sterilization algae removals, send in the water ballast tank 4 as water filling successively; Step B2 is: water intaking by behind the first ultrasonic equipment 10, ultraviolet sterilizing lamp 11 and the second ultrasonic equipment 12 sterilization algae removals, is sent in the water ballast tank 4 as water filling successively through filtering; Step B3 is: water intaking by behind the first ultrasonic equipment 10, ultraviolet sterilizing lamp 11 and the second ultrasonic equipment 12 sterilization algae removals, is sent in the water ballast tank 4 as water filling successively through filtering.
When water ballast tank 4 carried out draining, water ballast was extracted out from water port 6, and through ballast pump 3, chlorine ion concentration scope in the water intaking during corresponding water filling, when chlorine ion concentration was greater than 15000mg/L in the water intaking, only optional step A processed; When chlorine ion concentration was less than 8000mg/L in the water intaking, optional step B2 or step B3 processed; When chlorine ion concentration is 8000mg/L-15000mg/L in the water intaking, can select steps A or step B2 or B3 to process.Particularly, the steps A during draining is: Open valve K4, K6, and all the other valve closess, water ballast is through directly discharging by the total discharge outlet 2 of outboard behind the ballast pump 3; Step B2 during draining is: Open valve K4, K5, K7, all the other valve closess, water ballast is sent into elementary sterilization algae removal device 13 by ballast pump 3, enter again in the secondary sterilization algae removal device 14, enable ultraviolet sterilizing lamp 11 and the second ultrasonic equipment 12, after carrying out the sterilization algae removal processing, discharge by the total discharge outlet 2 of outboard; Step B3 during draining is: Open valve K4, K5, K7, all the other valve closess, water ballast is sent into elementary sterilization algae removal device 13 by ballast pump 3, enable the first ultrasonic equipment 10, enter again in the secondary sterilization algae removal device 14, enable ultraviolet sterilizing lamp 11 and the second ultrasonic equipment 12, carry out discharging by the total discharge outlet 2 of outboard after sterilization algae removal processes.
In the present embodiment, for step B2 and step B3, its water flood treatment method is by the first ultrasonic equipment 10, ultraviolet sterilizing lamp 11 and the second ultrasonic equipment 12 sterilization algae removals, processing mode when difference is draining is different, only by i.e. discharging behind ultraviolet sterilizing lamp 11 and the second ultrasonic equipment 12 sterilization algae removals, also need among the step B3 by just discharging after the first ultrasonic equipment 10, ultraviolet sterilizing lamp 11 and the processing of the second ultrasonic equipment 12 sterilization algae removals among the step B2.
Current density is 10～2500A/m during electrolysis
2, ultrasonic frequency is 15～500KHz, ultraviolet wavelength is: 180-400nm.
The water ballast that chloride ion content is high enters elementary sterilization algae removal device after filtering, carries out the sterilization algae removal processing first time.Water ballast can produce Cl when electrolysis
2, ClO
2, HC1O, C1O
-Etc. efficient oxygenant material, with the biocidal in the ballast water for ship or press down to live, if can produce following four problems when the efficient oxidation agent dose that produces is excessive: 1, with water in organism form high carcinogenic disinfection byproduct (DBP) trichloromethane; 2, strengthen the microorganism resistance; 3, cause and smell flavor; 4, invalid to the microorganism of zoogloea inside, but when being used in combination, electrolysis and ultrasonic technology can change this situation, can be in the less situation of electric current, reinforcement removes the algae sterilising effect.The OH that under electrolytic action, produces, H
2O
2Preferentially can produce with chlorine reaction the oxidation operation of trichloromethane on particle, ultrasonic wave is to the air bag of algae, the hypopuss such as spore, gemma, and the destruction of cell wall breaking, zoogleic unzipping is much larger than chlorine class sterilizing agent.The collaborative electrochemical oxidation of ultrasound oxidation technology forms advanced oxidation processes, the increase that the degradation rate of the energy force rate monotechnics of sterilization and disinfection will improve 7 to 9 orders of magnitude, and namely speed of response is incited somebody to action necessarily even several hundred million increases.Even electrolysis+ultrasonic wave combination technique is short in the reaction times; also can reach good water ballast in the low situation of chlorinity except the algae sterilising effect; in addition; in actual use; slowly after the fouling, electrolytic efficiency also can reduce gradually, even the interpolar of cathode and anode can be blocked fully on the negative electrode of electrolysis; to shut down to root out at last fouling, or the chemical pickling scale removal.And when adopting electrolysis+ultrasonic wave combination technique, two kinds of technology act in a covering device, and hyperacoustic mechanical effect cleans the negative electrode fouling in the collaborative electrochemical electrolysis, can realize continuous electrolysis and then reach the purpose of continuous processing ballast.
The UV radiation technology for sterilization non-secondary pollution, little to environmental influence, in the sterilization process of sanitary sewage, adopt more, when applying to the ballast for cruising water treatment, it mainly contains following problem: 1, enter the sanitary sewage SS content of disinfecting steps generally at 10-20mg/l, and the SS content of seawater is far above this numerical value, a large amount of suspended matter meeting shielding of ultraviolet affect treatment effect, and energy consumption is very large to the irradiation of biological and pathogenic agent; 2, depend on to a great extent the size and geometric of microorganism, such as the reason of marine alga owing to its size and color, the dose ratio bacterium that needs is large, and bluish-green marine alga is to ultraviolet resistivity extra-heavy, kills large 2-3 grades of the quantity that radiation quantity that its needs needs than killing bacteria; And ultraviolet sterilization can only be killed the outer microtube biology, can't kill for the microorganism that is attached to solid particulate matter and spore inside; 3, some microorganism has formed the self-regeneration function in long-term natural evolution process, and behind the environment that leaves ultraviolet radiation, some microorganisms of being killed and wounded can be repaired the dna molecular of damage automatically, realize regeneration.And UV radiation technology for sterilization and ultrasonic technology are united when using, under the hyperacoustic effect of low frequency, the jet that hyperacoustic periodicity concussion and acoustic cavitation form forms mechanical shearing in water, large zoogloea can be destroyed and be single microbial, increase ultrasonic power and then can destroy cell walls, strengthen disinfection efficacy of ultraviolet ray.As only can within 5s, colibacillus of excrement being reduced to 1600CFU/100ml from 450000 with ultraviolet ray, and the ultrasonic wave of 50w is acted synergistically with it, can within 5s, colibacillus of excrement be reduced to 250CFU/100ml, ultrasonic wave and ultraviolet ray synergy with 310w can be reduced to 100CFU/100ml with colibacillus of excrement within 5s.In addition, in actual use, utilize hyperacoustic mechanical effect that ultraviolet quartz socket tube incrustation is cleaned, the transmittance of raising has guaranteed the sterilization effect that continues.As for the brackish water of chloride ion content between seawater and fresh water, during as water ballast, the treatment step that adopts can be selected respectively steps A, step B1, B2 or B3 according to the power of device, the ballast water capacity that needs processing and the requirement of energy consumption, all can guarantee preferably sterilization algae removal effect.
When adopting the treatment process of water intaking-filtration-(electrolysis+ultrasonic wave)+(ultraviolet ray+ultrasonic wave)-water tank water filling-water tank draining, the ballast water body that enters boats and ships still contains certain density available chlorine and H
2O
2Material continues to suppress the again breeding of objectionable impurities, still conformance with standard requirement when guaranteeing discharge of ballast water in ballast tank.When adopting the treatment process of water intaking-filtration-ultrasonic wave-(ultraviolet ray+ultrasonic wave)-water tank water filling-(ultraviolet ray+ultrasonic wave)-water tank draining or water intaking-filtration-(ultraviolet ray+ultrasonic wave)-water tank water filling-(ultraviolet ray+ultrasonic wave)-water tank draining or water intaking-filtration-ultrasonic wave-(ultraviolet ray+ultrasonic wave)-water tank water filling-ultrasonic wave-(ultraviolet ray+ultrasonic wave)-water tank draining, water ballast before the discharging can carry out a sterilization algae removal again and process still conformance with standard requirement when guaranteeing discharge of ballast water.
Through the water ballast of seawater, brackish water or fresh water after the technical finesse of multistage composite type, discharge after finally reaching the standard-required of IMO " Management of Ships ' Ballast Water and sediment monitoring and management contract " D2.
Above-listed detailed description is that this embodiment limits claim of the present utility model for the specifying of the utility model possible embodiments, and does not allly break away from the equivalence that the utility model does and implements or change, all should be contained in the claim of this case.
Claims (5)
1. compound apparatus for treating ship ballast water, be arranged on the total intake of outboard, have between the water ballast tank and the total discharge outlet of outboard of water filling port and water port, comprise ballast pump, strainer, it is characterized in that: it also comprises elementary sterilization algae removal device and secondary sterilization algae removal device, wherein elementary sterilization algae removal device comprises electrolyzer and the first ultrasonic equipment that is arranged in the housing, secondary sterilization algae removal device comprises ultraviolet equipment and the second ultrasonic equipment that is arranged in the housing, the water inlet of described ballast pump connects the total intake of described outboard and described water port simultaneously, the water outlet of described ballast pump connects water inlet and the total discharge outlet of described outboard of strainer simultaneously, the water outlet of strainer connects the water inlet of elementary sterilization algae removal device, the water inlet of secondary sterilization algae removal device connects the water outlet of elementary sterilization algae removal device and the water outlet of described ballast pump simultaneously, and the water outlet of secondary sterilization algae removal device connects described water filling port and the total discharge outlet of described outboard simultaneously.
2. compound apparatus for treating ship ballast water according to claim 1 is characterized in that: between the total intake of described outboard and described ballast pump water inlet, between described water port and the described ballast pump water inlet, between described ballast pump water outlet and the total water port of described outboard, between described ballast pump water outlet and the described strainer water inlet, between described ballast pump water outlet and the described secondary sterilization algae removal device water inlet, between described secondary sterilization algae removal device water outlet and the described water filling port, be respectively equipped with valve between described secondary sterilization algae removal device water outlet and the total water port of described outboard.
3. compound apparatus for treating ship ballast water, be arranged on the total intake of outboard, have between the water ballast tank and the total discharge outlet of outboard of water filling port and water port, comprise ballast pump, strainer, it is characterized in that: it also comprises elementary sterilization algae removal device and secondary sterilization algae removal device, wherein elementary sterilization algae removal device comprises electrolyzer and the first ultrasonic equipment that is arranged in the housing, secondary sterilization algae removal device comprises ultraviolet equipment and the second ultrasonic equipment that is arranged in the housing, the water inlet of described ballast pump connects the total intake of described outboard and described water port simultaneously, the water outlet of described ballast pump connects the water inlet of strainer simultaneously, the water inlet of elementary sterilization algae removal device and the total discharge outlet of described outboard, the water outlet of strainer connects the water inlet of elementary sterilization algae removal device, the water outlet of elementary sterilization algae removal device connects the water inlet of secondary sterilization algae removal device, and the water outlet of secondary sterilization algae removal device connects described water filling port and the total discharge outlet of described outboard simultaneously.
4. compound apparatus for treating ship ballast water according to claim 3 is characterized in that: between the total intake of described outboard and described ballast pump water inlet, between described water port and the described ballast pump water inlet, between described ballast pump water outlet and the total water port of described outboard, between described ballast pump water outlet and the described strainer water inlet, between described ballast pump water outlet and the described elementary sterilization algae removal device water inlet, between described secondary sterilization algae removal device water outlet and the described water filling port, be respectively equipped with valve between described secondary sterilization algae removal device water outlet and the total water port of described outboard.
5. according to claim 1,2,3 or 4 described compound apparatus for treating ship ballast water, it is characterized in that: be provided with salinity measurement instrument or chlorion detector at the total intake of described outboard between the water inlet of described elementary sterilization algae removal chamber.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220202036 CN202717657U (en) | 2012-05-07 | 2012-05-07 | Composite ship ballasting water treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220202036 CN202717657U (en) | 2012-05-07 | 2012-05-07 | Composite ship ballasting water treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202717657U true CN202717657U (en) | 2013-02-06 |
Family
ID=47619486
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220202036 Expired - Fee Related CN202717657U (en) | 2012-05-07 | 2012-05-07 | Composite ship ballasting water treatment device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202717657U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105130074A (en) * | 2015-09-29 | 2015-12-09 | 哈尔滨工业大学（威海） | Electro-catalysis /ultraviolet composite ship ballast water treatment method and equipment |
| CN113226917A (en) * | 2018-08-31 | 2021-08-06 | 斯凯孚海运有限公司 | Reactor with a reactor shell |
-
2012
- 2012-05-07 CN CN 201220202036 patent/CN202717657U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105130074A (en) * | 2015-09-29 | 2015-12-09 | 哈尔滨工业大学（威海） | Electro-catalysis /ultraviolet composite ship ballast water treatment method and equipment |
| CN113226917A (en) * | 2018-08-31 | 2021-08-06 | 斯凯孚海运有限公司 | Reactor with a reactor shell |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| 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 | |
| Tsolaki et al. | Technologies for ballast water treatment: a review | |
| US6802956B2 (en) | Electrolytic treatment of aqueous media | |
| KR101256896B1 (en) | A micro-current electrolysis sterilization algaecide device and method | |
| CN101786748B (en) | Efficient inactivation and energy-saving ship ballast water process method and system | |
| CN101781043B (en) | Novel ballast water treatment method and device | |
| CN102642960A (en) | Device and method for ship ballast water processing and applied to seawater/freshwater | |
| CN102515400A (en) | High-efficiency treatment method of ballast water in ship | |
| CN205313291U (en) | Refrigeration cycle water integrated processing system | |
| WO2011016781A1 (en) | Emissions control system and method | |
| CN202717658U (en) | Ship ballasting water treatment device applicable to seawater/fresh water | |
| CN202936278U (en) | Comprehensive treatment device for ballast water | |
| CN104016533A (en) | Ship ballast water treating method | |
| CN102120661A (en) | Equipment and method for treating ship domestic sewage through electrolytic process | |
| US6875363B2 (en) | Process and device for the treatment of water, particularly for ships | |
| Vorkapić et al. | Shipboard ballast water treatment systems on seagoing ships | |
| CN106946325A (en) | The method and system of hydroxyl radical free radical advanced oxidation prevention and control ocean invasive plants | |
| Taylor et al. | Preventive treatment and control techniques for ballast water | |
| CN202717657U (en) | Composite ship ballasting water treatment device | |
| CN102491569B (en) | Marine ballast water treatment system | |
| CN102774938A (en) | Device for treating living creatures in ship ballast water by utilizing sinusoidal pulse electric field | |
| CN204939160U (en) | Marine plankton inactivating device | |
| CN105130074A (en) | Electro-catalysis /ultraviolet composite ship ballast water treatment method and equipment | |
| CN201161945Y (en) | Ultrasonic reinforced fine current electroanalysis disinfect algae removal apparatus | |
| JPH0427493A (en) | Cleaning and sterilizing device for water and method for utilizing cleaned and sterilized water |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130206 Termination date: 20180507 |