유류 오염토 현장 처리용 정화선
The present invention refers to marine pollutants in soil for recovering a relates to search techniques environment, oil-polluted stratified clay in particular marine in the orginal speech signal can be reconstructed from the field for restoring earth contaminants is purifying relates to a water craft. According to data disclosed years 2004 - 2009 of rust bases mukho anti, anti samch'ok, kuryongp'o anti, going south by-product, from a such as anti ulsan 15 the main ports along one area, but inferior to it in a severe pollution levels. The various pathway, so that contamination marine. through. In particular, for heavy in process, oil, organic contaminants of a polyimide resin, such deposited charge Image deposition of PMs pier to be serious dirty, its geometric toe are known as HMG-COa reductase KIPO &. Speculative and marine the wastewater coming from river in addition through the contaminant is Yan is deposited. Yan nitrogen-based odorant deposit where such spills due to the generation of bad smell as well as at night, the contaminated with oil is fish or shellfish the power that the processor consumes nobody else shall might inflict KIPO & severe. In addition, fish due to deposit nitrogen-based odorant while is disturb ecosystem have a roasted fishery such as atmosphere individual door generate point number. While, for the purpose of triggers number stratified clay contamination in harbor and large ship marine periodically for ocular which dredging stratified clay, annual the amount of dredged sediment base hemp cloth amounting to at KIPO & only 3000. Oil as said a dredged, by dietary fiber and starch can be intolerable for meanihgfui recycling is contaminating have required either water treatment should in. Among other things, for purifying dredged in order that the water treatment and fluorescent indication can be for transferring dredged, since has extremely high cost transfer substantially dredged transferred overall cost processing for purifying the proportion of cost in addition, the treatment is of dredged sediment. a specific timbre of difficulty. I.e., compo-nent pumping together sea and dredged in dredging harbor, 10 - 20% a dredged from positive to dredging entire sea which the persons can just of wet liquid to flow down majority to 80 - 90%. Sea water dredged both relays and transfers them to an treatment facility hence cost transfer with adjacent to the Bulletin window, defined within a purification must perform on himself is processed in a number chamber malls in real-time automatically operated or stopped repeatedly dredged collision for the purification of the door is of hope appeared. is number. The oil contaminated with a marine stratified clay level and a culture medium using the same conjunction with techniques the orginal speech signal can be reconstructed, shape and includes an annular dredged are ready for treatment in facilities is desired in which the container has KIPO &. Registration number 10 - 0958067 patent 25th which [prior art literature] (notification date 2010. 5. 13) Of a door for the present invention refers to said addresses the point number, a dredging stratified clay in Yan in jobsite after directly water treatment is formed at the upper, a contaminated with oil in particular to such a level that can recycling stratified clay orginal speech signal can be reconstructed, water treatment facilities to a water craft having joint groove in joint earth oil-polluted mounted on the number line for under public affairs heat exchanger.. The present invention according to said opens the folder of his/her line for oil-polluted earth having joint groove in joint, sea (lake, reservoir) (Yan ') or river with dredged in dredging in the case and stores water dredging, the suction is formed received on deck to the reservoir, said unit and an outlet for supplying air water dredging vessel which is intended is formed; and said non-thrombogenic heparin derivatives dredged and water treatment water, treated dredging water is exhausted to the outlet of said ship purge processing system; is provided with, the, is connected to non-thrombogenic heparin derivatives dredged dredger flows in water, said status a dredged screening unit and extractor extracts plurality of groups, said sorting unit is safe to skin without any side at a group of dredged is non-thrombogenic heparin derivatives while the water flows into the water, a dredged said status plurality of groups so that the screening device and a cyclone, said cyclone device during groups at relatively small particle size flows in water dredging and dredged having, said soil of dredged sediment is attached particles and oil to generate microbubbles for that desorbs number 2 oil of dredged sediment said bubble generator is connected to an auxiliary performing detachmentcontrol trillion and, said auxiliary which treats coming from dredged receives temporarily water dredging and, during said dredged the heavier particles to precipitate 7S, said ship of a of pairing a predefined settling separation trillion and, said settling separation trillion water dredging and fine particles not precipitated in flows in said aggregation number number aggregation is connected to tank through a main for agglomerating particles fine said control trillion and, and bubble generator 99 90001566999 to generate microbubbles, which treats main said agglomerated said microparticles and dredging the case and stores water which, said number 1 receive a supply of bubble generator bubbles from said fine particles floating separates the inoculating activated microorganisms injury, said recessed in said floating increasing dissolved injuries in settling separation trillionwith fall-out providing a of injury is the main exhaust stream, such as internal dehydration to thereby said dryer and receives water dredging reparing over-number is levitation filters the conductive metal for blocking electromagnetic wave outlet of said ship in that it comprises at filter unit is connected to the semiconductor layer.. The present invention according to line for oil-polluted earth having joint groove in joint, to a water craft water treatment system contaminants out of the exhaust gas the marine or river instantaneous dredging stratified clay and water treatment in situ again wastewater treatment process of rotating in a first direction and wherein the load of logistics the speech signal can be reconstructed, mirror signal controller unit is off member and the spraying member are number. In addition in the present invention oil, with different contaminations by dietary fiber and starch can be terminal unit source and to be vertically movable.. In addition in the present invention cyclone device and a, using microorganism the waste compares contour line values to progressing directions waste can be due to buried land of 2 difference pollution can be connected a contact point is turned off. One in the embodiment according to Figure 1 of the present invention for line oil-polluted earth having joint groove in joint is electrophotographic number of threads. Disclosure also also Figure 2 shows a oil-polluted earth having joint groove in joint 1 to a multiplex line for. component. 1 also also shown in Figure 3 shows a oil-polluted earth having joint groove in joint system for purifying at an adequate temperature, to line for performed at is stream multiplex water treatment. it became at the time of to 3 also also Figure 4 shows a sorting unit (drum screen) is electrophotographic number of threads. Figure 5 shows a number chamber separator 2 also also number 1 is electrophotographic it became at the time of to magnetic force. Also 6a and 6b has door 2 shown in cyclone device is configuration and number of threads. it became at the time of to number 2 2 also also Figure 7 shows a magnetic force is electrophotographic number chamber separator. Figure 8 shows a number chamber settling separation mourningit became at the time of to also electrophotographic is also 2. it became at the time of to 2 also also Figure 9 shows a main dehydrator (multistage cyclone to) is electrophotographic number of threads. crisis mourning levitation it became at the time of 2 to also also Figure 10 shows a is electrophotographic number chamber. Figure 11 shows a centrifugal separator it became at the time of to also spin-dryer chamber 2 also is electrophotographic number. Also also shown in Figure 12 shows a 2 is surface an approximate filter sand. In the embodiment one Figure 13 of the present invention liquid microorganism use in. foil distribution of microorganisms in the culture bottle. Also the present invention according to Figure 16 shows a to 14 also for oil-polluted earth having joint groove in joint which is applicable to, in this line as in which the results of experiments on biological water treatment, which foil provided well! in efficiency number organic Figure 14, Figure 15 total order which foil is provided to treatment water number, a total 16. foil provided well! in efficiency number. The present applicant Korean marine technology promotion circle of the bases rust deflector 'future offshore industry technology development business' of, a difference between both scales is marine or river is a contaminant upon the monitoring dredging stratified clay after purifying treatment in situ, on dredging recycles a aggregate which contains sand on pumped water (hereinafter, ' dredging can ' assembling and welding steps) for restoring the capable of rotating in a first direction is again a decontamination duct for earth having joint groove in joint seal, and a development line for adaptation small number to number. Also the 1 'large characteristic 15 call' having joint groove in joint earth contaminants designated for electrophotographic number of thread line is disclosed.. 'large characteristic 15 call' the length 63m per hour scale tone 1,100 to 500 tone (400 - 450 ton seawater, 50 - 100 ton dredged) member while changing number was small. The present invention refers to number number chamber rather than predetermined development techniques based on line purifying work it was completed is a diarylaminosilane, a triarylaminosilane, a patent application. Hereinafter, reference to drawing with an, oil-polluted earth having joint groove in one of the present invention in the embodiment according to for line (hereinafter 'purifying line' photolithography) concave unit, and the water treatment for the pulsating current is a described. Disclosure also also Figure 2 shows a oil-polluted earth having joint groove in joint 1 to a multiplex line for of configuration, (a) coarse of the cleaned gas is plane view, (b) is of multiplex line the cleaned gas. In addition, also also shown in Figure 3 shows a oil-polluted earth having joint groove in joint 1 for line system for purifying at an adequate temperature, to multiplex water treatment performed at is stream. Also with a 2 and 3, one of the present invention in the embodiment according to purifying line (900) a ship (800) and purification system (700) comprises an ultra-. Ship (800) the, as said, approximately 1,100 ton having a length of at 62m is scale. The vessel's (800) the which the treated dredging water again for marine or river-situ with an outlet (not shown) is formed. In addition ship (800) at a center portion of a vehicle for held together water dredging and dredged reservoir for (in settling separation trillion be used in the the after alcoholic beverage it will do) is formed. Receiving bath ship (800) deck is formed of any concave. System for purifying (700) a selected unit (10, drum screen) comprises an ultra-. Sorting unit (10) non-thrombogenic heparin derivatives dredged pumped from the dredger receives water. of selecting foreign from dredged soil. Sorting unit in the present invention (10) by separating the status for the dredged foreign which triggers number, specifically 3 on drum screen (10) and according to at, treated for 500 ton per hour. 3 on drum screen (10) the, of Figure 4 as shown in electrophotographic drum screen, cylindrical mesh network consisting of top elid processing device is provided with screen of 2. Number 1 a is arranged at the center portion on screen (11) the 13 mm hereinafter a particle size of at particle to allow for the passage of a KIPO & only. Number 1 screen (11) envelop a disposed screen number 2 (12) the only particles of to allow for the passage of a KIPO & 4 mm hereinafter. Drum screen (10) whereof the rotation non-thrombogenic heparin derivatives dredged by the centrifugal and is urged toward inner wall of screen water, number 1 screen (11) of wastes in 13 mm or more filtering out impurities contained which, number 1 screen (11) through the screen number 2 a of dredged sediment (12) in gravel, such as shell 4 mm or more filtering out impurities contained.. Remaining, number 2 water dredging sand screen (12) through the is stage. 4 mm or more materials collected by a conveyor belt (not shown) are transported after land station. Main load stably a wafer even when soil contaminants oil when including part of heavy metals is general rule, . Number 1 in the embodiment is in the the after alcoholic beverage it will do in magnetic force separator (20) and a number 2 magnetic force separator (50) in earth oil-polluted through the process that triggers number heavy metals can be selectively adds. Just, through automatic analysis sample would be if there is no heavy metal contamination, number 1 magnetic force separator (20) such as steel or iron, in current number of relatively large size foreign number 2 and triggers number only magnetic force separator (50) is connected, steps three through five, heavy metals iron, is that no contamination on number when a mobile station is determined to number 1 would be magnetic force separator (20) and number 2 magnetic force separator (50) without incorporation into an a process may be. Number 1 number 2 interposing a magnetic force does not pass through the separator magnetic force would be, drum screen (10), which pass through the dredging water a dredged the after alcoholic beverage it will do cyclone device (30) is directly into the to. In the embodiment of oil-polluted cripto hereinafter in a moment when a polluted composite heavy metals number before the number 1 magnetic force separator (20) and number 2 magnetic force separator (50) through the detaching process magnetic force of the antenna in case that the optionally additional to the disclosed. As said, drum screen (10) the foreign substance a cutting device and vertically dredged screen the drum natural dropping water dredging and (10) the number 1 magnetic force separator (20) is introduced into. The present invention refers to purification system (700) the vessel's (800) loading a form, it is possible to minimize the powered since each device locating corresponding advertisement based on the shown list, number 1, a difference between both scales is the same magnetic force separator (20) a drum screen (10) according to driving of the first liquid natural dredged water dredging the drop the. minimizes the use a motive power by. Number 1 magnetic force separator (20) is shown in a 5 a of.. In the present invention using wet magnetic force separator (20) as the publicly known device of cylindrical magnet (21) belt in a form is wound on the magnet of the rotary scroll which is cyclically belt while, during dredged the overlying belt by using magnetism without directly seeing the magnet the materials is a driver attached to magnetic belt, when moved into an off influence of separated from one another belt with respect to the base. The materials one non magnetism not attached to a magnet rotating since descended on the end of magnet in separated from one another. The belt from separating from demagnetizer in order to make for hereinafter using (demagnetizer) may be loaded with. The present in the embodiment when the magnets (21) has the and release the magnetic force of approximately 3,000 - 4,000 gauss, 2. 2 magnets class 2 kw 500 ton per time arranged for treated. Just, number 1 magnetic force separator (20) all magnetic material are not from separating, mainly steel current, related thereto is measured during each test current number iron, which are weak in magnetic by dietary fiber and starch can be the after alcoholic beverage it will do material separated from one another in separator magnetic force number 2. Number 1 magnetic force separator (20) magnetic material such as steel isolated from a conveyor belt (not shown) is conveyed into a land is collected by which, magnet (21) cyclone the after alcoholic beverage it will do materials not attached to a device (30) is transferred to. The present in the embodiment device cyclone at the time (30) also is configuration and number of threads 6b and 6a. shown in an. Cyclone device (30) the number 1 magnetic force separator (20) from vented dredged status receive a supply of is separating. The present cyclone device (30) to a plurality of cyclone (31) and a vibration screen (32) and return pipe (33) has a. To cyclone (31) the 5 dog a unit respectively, to two 5 a dredged flux of cyclone gas (31) particle size as it passes through sequentially separated from one another. To cyclone (31) the top of the cylindrically, formed from a conical lower, is formed the cylindrical unit through an inlet of dredged sediment propelled at a high speed by dredging and to cyclone water dredging and dredged surface while the water flows into the water (31) inner wall of which lowered after-processing, while they are rotating, conical portion that is lighter in which the guide vans for generating a rise materials to cyclone (31) the upper part of the are discharged with the, to cyclone materials heavy (31). an arrangement is stage. The present in the embodiment about cyclone in 0. 8 - 1. 2kg/Cm2is during traveling pressure operation of. First disposed cyclone in protruded from a required side of the second material is a 5 is fed into the cyclone disposed two final through sequentially group flux of cyclone gas cyclone is disposed approximately 0. 075 mm hereinafter with a particle size of at is protruded from a required side of the particles. More particularly, two 5 to flux of cyclone gas (31) sequentially in 0. Particles greater than 1 mm, 0. 095 mm particles greater than, 0. 09 mm particles greater than, 0. 08 mm particles greater than, 0. The lower portion of the cyclone particles greater than 075 mm. is discharged. Particle size 0. The upper portion of the cyclone particles are of 075 mm hereinafter. is discharged. Plurality of cyclone to (31) separated through the lower portion of 0. 075 mm particles are largely exceeds sand component is reusable, to cyclone (31) the upper part the 0. 075 mm hereinafter particles of a clay, or [...], organic, oil, heavy contaminant such as (hereinafter, for the sake of convenience of 0. 075 mm hereinafter, of a clay, meter or injecting a fine ceramic particle 'fine earth' him. them) is. And 0. 075 mm or more with a a particle size of at, to cyclone (31) stage to cyclone particles are (31) of the signal recording layer provided on one side vibration screen (32) is transferred. Vibration screen (32) network mesh sand on film is made by a mesh network (particle diameter 0. 074 mm hereinafter to allow passage therethrough of granules of of) the overlying state after dehydration while vibration in, a recycling as aggregate moved at a land. Sand during particle size of 0. 075 mm hereinafter fine toga which deionized water, these have sometimes vibrated screen (32) mesh network through the vibration screen (32) after collected in the lower of, anodizing membrane pipe (33) to several through the flux of cyclone gas (31) to again for conducting the separations by particle size, particle size of 0. And isolated maximum stratified clay fine 075 mm hereinafter. As said fine toe itself or contaminants, a large contact surface area a clay or [...] to the typical particles soil, soil is attached much contaminant is the above particle as well as, for also separated from microparticles contaminants hereinafter do not go. In the present invention 0. 075 mm hereinafter with contamination stratified clay of which treats auxiliary the after alcoholic beverage it will do defined, and, floating increasing dissolved in treating a. Cyclone device (30) the light passed through the 0. 075 mm hereinafter which treats auxiliary water dredging lightweight of (40) is introduced into. And cyclone device (30) the auxiliary which treats (40) may be placed on objects, goods top of dredging water without depending on additional power, to cyclone (31) which treats from (40) is introduced into. Just, as said, oil contaminated with fine toga composite heavy contaminated fine lightweight dredging water to cyclone (31) via a bypass line from the number 2 the after alcoholic beverage it will do magnetic force separator (50), from which, after magnetic force again through the auxiliary which treats (40) is introduced into. Would be if there is no heavy metal contamination, which treats sub water dredging particles and soil (40) is introduced into. When contaminated composite heavy first relates to. Mineral particles or, in earth fine including iron oxide a variety of heavy metals that is fitted with an aperture. Number 2 magnetic force separator (50) in number 1 magnetic force separator (20) are practically non-separated in and isolated heavy metals. The present in the embodiment number 2 number chamber separator magnetic force a employed in electrophotographic a 7. shown in an. Number 2 magnetic force separator (50) the grade magnetic separation (HGMC, High Gradient Magnetic Separation) is publicly known as device of, the present in the embodiment 6,000 - 7,000 gauss in a permanent magnet having high magnetic force by using a at high levels of heavy. Number 2 magnetic force separator (50) also number 1 magnetic force separator (20) similarly to the toga wetting units by the belt to form a fine surface to reach the active area the magnetic force, is attached to magnet magnetic material has a nonmagnetic octenyl succinate anhydride transfer to a concave use. In addition, the present in the embodiment utilizes toga number 2 magnetic force separator (50) prior to its entry to magnetization and a number dispersion by mixing a number the objective compound. separation efficiency. The number dispersion joining is formed is intended dispersing fine stratified clay. I.e., fine cripto included in the iron oxide, manganese oxide, or the like, that has to of charges to be in soil environments, consists of generally, PZC soil environments, consists of the pH (point of zero charge) of strong such as phosphate from hereinafter an anionic out by absorption of said surface, is secondary to iron oxide of lines having micro-toga. is completely separating repellency. Magnetization in addition number tank (51) are ready for employment of a finer supplied with number magnetization from may magnetize stratified clay. Number of a heavy-input of magnetization for the particles mineral containing magnetic force in order to achieve a high separation efficiency, magnetization of soil particles is to increase the power (magneticsusceptibility). Heavy force magnetization of soil particles exhibits and correlation high content. Magnetization low mineral high force and received by using the mineral containing heavy metals amount of. means that the X and Y axis. In addition, iron oxide oxide and manganese oxide, silicate mineral residual form of heavy metals (silicate mineral or silicates) compared to relatively high magnetization force, to render them preferably, vortex type magnetic field is later number can be purifying stratified clay fine triggers. Soil has number of magnetization in a magnetic force particles (mainly mineral) which by which it is possible to convert, magnetization force mineral weak magnetization of. serve to increase the force. Magnetization as number, ferromagnetism mineral character season stone( Fe3O4)as a tower or an Image, scissors character season nickel soil in the soil particles overall magnetic installed inside the main body a. Wherein,, a triarylaminosilane, a tetraarylaminosilane and itself crosslinks to stone character season addition, character seasonin three containing iron (Fe) component is dissolved nickel soil serves to crosslinked to the magnetic. may also be installed inside the main body. In addition, magnetization salt - alkenylcephem compounds 1, 2 as number( FeCl2, FeCl3, FeSO4such as) a solvent dissolved alkali pH system adjusts then followed by elevated temperature have a water air, discharging commodities by throwing a cripto fine soil particles is method for the magnetization m. Wherein, nickel soil component in addition Fe the crosslinked to. by using magnetism without directly seeing the. As said, in the embodiment of the present invention/number dispersion in the handwritten or number one and number 2 by injecting magnetic force separator (50) in soil including heavy metals can be authored in the first client by a number from air by photocatalytic particles. Number 2 magnetic force separator (50) isolated from heavy metals or heavy metals including fine toe after collected via a conveyor belt is conveyed into a land which, remaining fine toe dredging the controller washes the auxiliary which treats (40) is introduced into. Number 2 magnetic force separator (50) the auxiliary which treats (40) is arranged at the upper portion of an interconnection part floriculture and dredging water by at least one naturally, without power which treats (40) is introduced into. Eliminate a point, to cyclone toga fine isolated from polluted by heavy metals, and if the data number 2 magnetic force separator (50) but via, if there is no heavy metal contamination would be fine toe cyclone device (30) which treats from (40) to directly into the performed in such a manner that. Auxiliary which treats (40) fine lightweight dredging the case and stores water containing characteristic purification processing KIPO &. I.e., auxiliary which treats (40) the number 2 bubble generator (41) is connected the item may be supply fine bubbles. The auxiliary which treats (40) with minute in agitator to dilution water is decreased stratified clay (43) is provided. The present invention, such as soil contaminated with oil is a treatment object main, auxiliary which treats (40) the fine bubbles detachment trillion oil for that desorbs oil discharging commodities by throwing a.. Auxiliary which treats (40) which treats auxiliary when a utilized with detachment trillion oil is (40) to centurial gun ultrafine (micro bubble) is supplied to. Bubble generator number 2 (41) in 3-10 μm which treats auxiliary generating aquaculture system of ultra-fine size (40) supplied to. Contaminant particles and soil centurial gun ultrafine (in particular oil, organic) soil contaminants to penetrate and between pipe includes a projection part curved upward from particles. I.e., soil between contaminant particles and penetrate into the ultrafine magnetic centurial gunin pressure strange phenomenon by generating a shock wave which while descending, is soil contaminant is by shock wave is from particles. As said, oil (and/or organic) contaminated with fine toe auxiliary which treats (40) the after alcoholic beverage it will dosettling separation trillionit became detachment contaminant is in state (60) is transferred to. settling separation trillion (60) electrophotographic a number of threads. shown in an 8. Ship (800) of deck made any concave settling separation trillion a receiving the reservoir (60) is used as, at least approximately 20m are formed flatly, dredging water be precipitated particles that are heavy sufficient hydraulics. under public affairs residence time in number. Heavier particles are settling separation trillion (60) but precipitated in, auxiliary which treats (40) oil/it became detachment in organics settling separation trillion splitter is lighter than water (60) can dredging without being precipitated in suspended therein and maintaining the state in which.. Electrophotographic of Figure 8 consults a surface, auxiliary which treats (40) 2, which is connected to two pipe line (61) and fine togasettling separation trillion can dredging through (60) central feed tower (64) is transferred to. settling separation trillion (60) is formed in the shape of the upper part of the bed upper end a number corresponding to the number of structure (62) are provided on. Number structure (62) is disposed a constant height settling separation trillion (60) first water level is of utensils, the first structure number water dredging surface (62) which treats main the after alcoholic beverage it will do through (90) is transferred to. Number structure (62) of the tops of teeth (63) such that every other period the floating things is intended. In addition, settling separation trillion (60) on a lower end of a rotating truck (65) is provided. Truck (65) the settling separation trillion (60) is at least two bodies separated width bottom of a length which is settling separation trillion the shape corresponding to the shape (60) for reciprocally moving bottom of.. Truck (65) the settling separation trillion (60) settling separation trillionfall-out precipitated in the bottom of (60) of an lower unit lifts up/down (not shown) to pipeline (not shown) through main dehydrator the after alcoholic beverage it will do (80) are delivered by means of.. settling separation trillion (60) precipitated in fall-out clay, silt, contaminant is main and changes resistance value by, main dehydrator (80) particle size dewatering and in separated from one another. Main dehydrator (80) the settling separation trillion (60) precipitated in fall-out again together with action and dehydrating a. for conducting the separations particle size. Main dehydrator (80) a electrophotographic number of threads is shown in a KIPO & 9. Main dehydrator (80) has a multi-step cyclone consisting of an said in a cyclone device (30) .the same. However, main dehydrator (80) two 3 in the as a unit group of cyclone gas said a cyclone device (30) is formed in a cool compared to. for separating particles soil. First disposed to cyclone number 1 (81) in particle size 0. 074 mm hereinafter particles of separate the input grooves from the output, second disposed to cyclone number 2 (82) to cyclone number 1 in (81) substance transported from 0 particle size particles. 03 mm hereinafter and separating particles of, finally disposed to cyclone number 3 (83) in 0. And isolated particles of 01 mm hereinafter. Main dehydrator (80) for supplying the cyclone each of a screen (not shown) are covered with a cylindrical lower electrode, the screen the 0. Particles of 01 mm hereinafter film is made by network mesh passing, soil passes through the screen and again through pipe anodizing membrane particles are separated from one another particle size in cyclone. Suffering from screen and fine earth are collected and dehydration after land station is transferred. Main dehydrator (80) 0 finally in. 01 mm hereinafter toe fine classification to a particle size of at most a. is in many cases. The occurrence of minute toe main which treats (90) that is fed to it is generally designated on a but, connected to its upper discharge opening of each in the method, the step of exhaust line disposable through can be processed. E.g., to cyclone number 2 (82) in opposite direction at 0. 03 mm hereinafter specific is substantially particles of pollutants are if an, to cyclone number 2 (82) on top of connecting the separate exhaust line for storing and collecting contaminants may discard an KIPO &. Main which treats (90) (clarifying) the dredging can and do not precipitate and a fine togasettling separation trillion (60) flows in from, 0. 01 mm hereinafter toe fine classification to a particle size of at main dehydrator (80), the treatment fluid is introduced from is. Main which treats (90) has flocculation number tank (42) from aggregation number can dredging receive a supply of suspended therein and a soil particles, organic, like an of pairing a predefined aggregation functions, agglomeration, contaminants. Aggregation number the calcium, magnesium, such as charged is a cationic coagulant number is used. Aggregation number number aggregation lightweight fine a shift fork is pulled, is charged into the lower agitating. assembly the fine particles. The microparticles a large contact surface area and the wafer which adsorbed thereto when the air is filled in the, easily by gravity or divided does not selected aggregation the second scattered reflection can dredging through microfabrication in number for agglomerating particles are later. hereinafter for separation. Aggregation number by soil particles and agglomerated contaminants.. However, main which treats (90) agitator continue in (91) is being, long time to residence from a in an agglomerated particle are and do not precipitate and the after alcoholic beverage it will do floating increasing dissolved (100) is transferred to. Levitation increasing dissolved (100, also 10 reference) which treats the main has (90) fine particles agglomerated in (mainly organic or oil-polluted water) then injuries using for bubble-number triggers. for. For injuries increasing dissolved (100) the bubble generator number 1 (101) is connected. Bubble generator number 1 (101) the above-mentioned number 2 the bubble generator (41) similarly to the 0. 0003 - 0. Increasing dissolved out by the opposing team bubbles of 001 mm (100), and the clocks are supplied to. Micro fine particles agglomerated bubbles attached to the substrate surface waters with the first base station which serves to fasten the (so-called 'bubble entrainment action') performs. In addition, as said, magnetic pressure strange phenomenon for separating contaminants in earth the cassette holder performs, which also serves to. Method micro injuries increasing dissolved (100) of sleep in floating the pollutants and fine particles for triggers number injuries increasing dissolved (100) the upper part of the skimmer (102) is provided. Skimmer (102) has of injury increasing dissolved (100) of G1 the longer side of the cross section is formed in the shape of bar, levitation increasing dissolved (100) is arranged in the vicinity of of sleep is movable reciprocating. Skimmer (102) has a reciprocating the movement of injuries increasing dissolved (100) of sleep hopper contaminants the substrate (not shown) forced into the. triggers number. Dehydrator hopper centrifuge (70) and a are connected. Dehydrator centrifugal separator (70) the use of centrifugal force, while a rotating a dehydration contaminants. Been eliminated and easily discard the collected contaminants 30 - 40% a function of rate which has an upper side and a sludge cake is conveyed into a land is formed is resulting from the. Levitation increasing dissolved (100) from vented dredging water filter unit (110, also 12) is the filtration of the slurry suspension is resulting through, ship (800) a vent port (not shown) through the is-situ with an river sea. Accepted plurality filter unit in the present invention is filter is used. Sand filter (110) has within a housing sand light filtration material are filled with, dredging water sand are pressed against the sand in the fuel filter is filtering while passing through the connector. Final the dredging heavy the can, oil and organic matter is substantially number reparing over-state required by law thereby, it satisfy an with required quality level. While, in the present invention, as said, physical, heavy metals by means of a through water treatment chemical, organic, oil a number but triggers, purifying processing to perform completely biological treatment step in which. may be added. In addition, when the biological processing supplying formed by laser and the gas is blown into the are constructed onshore and reduce the amount of waste is by-products can be. Energy source to the organic microorganism in biological treatment since extinguishing can be thereby decreasing the amount of waste. The present in the embodiment an auxiliary which treats biological treatment in (40) or main which treats (90) can be in. I.e., includes microorganism which treats assist are a (40) or main which treats (90) a silicon oxide layer caused by the organic matter can be authored in the first client by a number. In particular, the present in the embodiment (not shown) in tank liquid microorganism without a space column circuit are installed separately, ship (800) can be the last which will conceive tank and is of. I.e., seawater be immersed in tank the last which will conceive micro-organisms on the liquid can be blending and supplying. The present in the embodiment relates to a biologically treatment process. 1 table of Figure 13 the one in the embodiment of the present invention liquid microorganism use in. foil distribution of microorganisms in the culture bottle. In the present invention from a treatment solution microorganism using efficacy as an anti-microbes indigenous, photosynthetic bacteria, yeast, lactic acid, filamentous bacteria and filamentous fungus is included, approximately 130 made of a species of the bacteria and yeast. The present soil sample (bamboo the leaf mold, cargo micro rumination, bleached hardwood the leaf mold) to a 80 - 120 mesh crushed to a medium (rice bran, rice hull, sawdust, egg shells, shell, peat moss) to 40 - 60% is moisture concentration after mixing the controlled such that, liver 90 penumbra cultured on a soil state. Culture sample to and the contents stored in the database 30 weight % rice bran, rice hull 20 weight %, 30 weight % sawdust by mixing 60% moisture concentration in a medium in which the medium after adjusted to 0%, by weight of the water. 01% 80-90 °C in temperature to be inoculated with a time from twisting during fermentation to 4. After this 3 daytime later of 7:3 by mixing on powder 8% hereinafter moisture concentration after the separation of the microorganisms number dope under trillion was received. Microorganism on liquid at from each respective separated, pH, and organic solvent and is assumed to be a yeast through microscope observing since the microorganisms sympathy crossroad the selected automatic identifying and biochemical Canadian boidini 99% homology to the light passed through the test result, been identified to Saccharomyces cerevisiae. The present microorganism onto a treatment object surface of microorganisms in biochemical response of the positive reaction Nitrate assimilation a few weeks, ammonium, nitrate, nitrite, organic hope fulfillment, element, in the form of amino acid as one that might employ both and a nitrogen source, and is shown to, nutrient salts for producing a sedated number of very favorably to protect user's private life.. In addition, nor generating an protease of a phenol compound which been irradiated to the temperature sensor of a proliferation. A variety of bacteria is identified the symbiotic coexistence one another RCM rhdwjddptj number of contamination material is at least one selected from the group while well! ratio and further to improve, in composite is extended in that contribute. The present applicant and marine antifouling using microbial liquid deposit water treatment experiment is performed for all the. fish market cavity by-product in as blocks, restrict device of timer and marine antifouling, the third to eo only 223a 10 μm hereinafter. The nature of the fed ventilation a few weeks shown in the following table 1, table 2 showed to the operating conditions. Organic well! in efficiency number for a experiments showed listed in tables so that individual asset of Figure 14. COD concentration is 550 - 650 mg/L of raw water inlet. Then, the apparatus doesn't demand water a [...] Seeding COD concentration 61. 2 mg. Is/L, operation is operated by a global word 18 mg/L until been is, stable number been showed a trend for for producing a sedated, of it has been discovered that the of that is unlikely to be affected. In addition nitrogen number of Figure 15 result is the experiments to see well! efficiency showed listed in tables so that individual asset. Total nitrogen concentration raw water inlet 6 - 8. Is 5 mg/L. Then, the apparatus doesn't demand water a [...] Seeding for T-n concentration 1. 166 mg/L is operated by a global word operated in a 0. 067 mg/L until stable been is have been shown to tendency for producing a sedated number. For experiments well! in efficiency a total and a number have been shown listed in tables so that individual asset of Figure 16. Total raw water inlet 8-10mg/L is a density of the additive. A [...] Seeding then, the apparatus doesn't demand water T-P concentration 0. 505 mg/L is operated by a global word operated in a 0. 0242 mg/L until been is, stable number showed tendency for producing a sedated. As said, the present in the embodiment microorganisms in water of pollutants in sea water by the liquid, nitrogen, phosphorus effectively identifying improving can be authored in the first client by a number. Other than processing biological said well as a magnetic force to separation, divided, fall off oil, settling separation, Flotaion through the process of heavy metals in earth and marine antifouling, oil environment appears much lower than permitted limit between the gas pipes under a fault signal by sensing the processing directly, in the sense it is found out that the torsion bar is used for. As taught or more, the present invention refers to the marine system water treatment to a water craft river or instantaneous dredging stratified clay contaminants out of the exhaust gas and water treatment in situ again wastewater treatment process of rotating in a first direction and wherein the load of logistics the speech signal can be reconstructed, mirror signal controller unit is off member and the spraying member are number. Heavy contaminants deposition of marine or river in addition, organic, composite by oil unknown to the device but polluted, the present system for purifying various psi or more terminal unit and to be vertically movable.. In addition using microorganism and a multistage cyclone device the waste compares contour line values to progressing directions waste can be due to buried land of 2 difference pollution can be connected a contact point is turned off. 10.. 3 on drum screen 20.. Number 1 magnetic force separator 30.. (Multistage) cyclone device 40.. Auxiliary which treats 50.. Number 2 magnetic force separator 60.. settling separation trillion 70.. Dehydrator centrifugal separator 80.. Main dehydrator (multistage cyclone to) 90.. Main which treats 100.. Levitation increasing dissolved 110.. Sand filter 800.. Ship 700.. System for purifying 900.. For line having joint groove in joint earth contamination The present invention relates to a vessel for in-situ treatment of oil-contaminated soil capable of dredging contaminated soil, deposited in an ocean or a river, and purifying the contaminated soil inside the vessel. The vessel for in-situ treatment of contaminated soil, according to the present invention, is prepared with: an accommodation tub, formed on the deck to accommodate dredged water, sucked in with soil dredged from the ocean or a river; a vessel formed with an outlet for discharging the dredged water; and a purification system which purifies the dredged soil and water, and discharges the purified dredged water through the outlet. Sea (lake, reservoir) (Yan ') or river with dredged in dredging in the case and stores water dredging, the suction is formed received on deck to the reservoir, said unit and an outlet for supplying air water dredging vessel which is intended is formed; and said non-thrombogenic heparin derivatives dredged and water treatment water, treated dredging water is exhausted to the outlet of said ship purge processing system; is provided with, the, is connected to non-thrombogenic heparin derivatives dredged dredger flows in water, said status a dredged screening unit and extractor extracts plurality of groups, said sorting unit is safe to skin without any side at a group of dredged is non-thrombogenic heparin derivatives while the water flows into the water, a dredged said status plurality of groups so that the screening device and a cyclone, said cyclone device during groups at relatively small particle size flows in water dredging and dredged having, said soil of dredged sediment is attached particles and oil to generate microbubbles for that desorbs number 2 oil of dredged sediment said bubble generator is connected to an auxiliary performing detachmentcontrol trillion and, said auxiliary which treats coming from receives temporarily water dredging dredged, during said dredged the heavier particles to precipitate 7S, said ship of a of pairing a predefined settling separation trillion and, said settling separation trillion water dredging and fine particles not precipitated in flows in said aggregation number number aggregation is connected to tank through a main for agglomerating particles fine said control trillion and, and bubble generator number 1 to generate microbubbles, which treats main said agglomerated said microparticles and dredging the case and stores water which, said number 1 receive a supply of bubble generator bubbles from said fine particles floating separates the inoculating activated microorganisms injury, said recessed in said floating increasing dissolved injuries in settling separation trillionwith fall-out providing a of injury is the main exhaust stream, such as internal dehydration to thereby said dryer and receives water dredging reparing over-number is levitation filters the outlet of said ship having buffer layer containing metal oxide stabilized filter conductive metal for blocking electromagnetic wave characterized in that for line oil-polluted earth having joint groove in joint. According to Claim 1, cyclone unit and sorting said device is disposed between, said sorting unit at a group of is safe to skin without any side the magnet while the water flows into the water non-thrombogenic heparin derivatives dredged using magnetic material contained within the dredged said passage and for separating a magnetic force number 1, and further comprising a separator oil-polluted earth having joint groove in joint characterized in that for line. According to Claim 2, non-thrombogenic heparin derivatives dredged said cyclone said transfer track in order to water is disposed between which treats and an auxiliary device, said cyclone device at during groups having relatively small particle size flows in water dredging and dredged, said number 1 separated from separator magnetic force-free magnetic material is deposited on the magnetic force, and further comprising a separator separating number 2 characterized in that for line oil-polluted earth having joint groove in joint. According to Claim 3, said number 2 number magnetization improved effectiveness of heat exchange and magnetic force the magnetic is charged into the number, and further comprising a tank characterized in that for line oil-polluted earth having joint groove in joint. According to Claim 1, said sorting unit 3 a dredged said status selectable groups, and is 3 on drum screen, during passage therethrough of granules of sand and said dredged having the smallest particle size included in characterized in that screening oil-polluted earth having joint groove in joint for line. According to Claim 1, the device said cyclone, said sequentially dredged separated particle size into the upper is a section for the shape of a cylinder, a conical lower cyclone, a plurality of formed, said plurality of cyclone is located size of the particles of hereinafter is separated by a the passes exceeds particles by vibrating and vibration screen for dehydrating, said vibration passes through the screen and several particles a is flowed to flux of cyclone gas and lower ends of the which in the anodizing, a dredged said plurality of said sequentially group cyclone particle size constant final through only particles of said conveyed in settling separation trillion hereinafter characterized in that for line oil-polluted earth having joint groove in joint. According to Claim 6, the optical through cyclone plurality of said auxiliary said 0 for discharging conveyed particles. 075 mm hereinafter with sizes down fine toe-in characterized in that for line oil-polluted earth having joint groove in joint. According to Claim 1, said between dehydrator main settling separation trillion and is line the pipe, at the bottom the membrane settling separation mourning said reciprocating is mounted so as to be movable is flowed to said recessed in settling separation trillionfall-out for pallet for said pipeline, and further comprising a characterized in that for line oil-polluted earth having joint groove in joint. According to Claim 1, said recessed in a dehydrator main said settling separation trillionfall-out sequentially separated particle size into the upper is a section for the shape of a cylinder, a conical lower cyclone, a plurality of formed, said plurality of cyclone is located of the particles of a size no less than constant is separated by a the passes exceeds particles by vibrating and vibration screen for dehydrating, said vibration passes through the screen and several particles a is flowed to flux of cyclone gas and lower ends of the which in the anodizing, fall-out said sequentially through said plurality of cyclone group final constant only particles of particle size hereinafter said main for discharging conveyed characterized in that for line oil-polluted earth having joint groove in joint. According to Claim 9, the cyclone plurality of said dog 3, which forms a unit which, is first disposed cyclone particle size 0. 074 mm hereinafter mounted on an upper portion of particles after being discharged, the defrosted with moving air from the cyclone disposed second 0. 03 mm hereinafter mounted on an upper portion of particles after being discharged, final arranged 0 the defrosted with moving air from the cyclone. 01 mm hereinafter is protruded from a required side of the of particles, each cyclone from particles are defrosted with moving air from the cyclone with post-arranged or via a bypass line inner characterized in that from being discharged for line oil-polluted earth having joint groove in joint. According to Claim 1, said floating crisis mourning upper suspended in injury to triggers number product said floating crisis mourning on top volume of the reformed ski from being installed to be reciprocally moved, said ski Metamers of injury by the hopper, is inspected is characterized in that having oil-polluted earth having joint groove in joint for line. According to Claim 11, said waste hopper from the circuit and to dispose of a centrifugal separator for dehydration to thereby, and further comprising a dehydrator characterized in that for line oil-polluted earth having joint groove in joint. According to Claim 1, said number 1 number 2 and bubble generator 0 bubbles hole, which is communicated with the bubble. 0003 - 0. Fine bubbles with a diameter 001 mm characterized in that the line for a oil-polluted earth having joint groove in joint. According to Claim 1, for processing biological purifying a liquid containing microorganism capable of said auxiliary in control trillion microorganisms for supplying liquid, and further comprising a tank characterized in that for line oil-polluted earth having joint groove in joint. According to Claim 14, said the last which will conceive tank of ship a microorganism and containing microorganism capable of mixed liquid, said auxiliary said microbial connected control trillion andthe last which will conceive tank liquid tank a characterised in that it consists in using oil-polluted earth having joint groove in joint for line.
