Abstract
In a conventional flocculation and magnetic separation device, it was not possible to make the device downsized because the flocs are easily broken. In addition, there was no system for the ballast water treatment that is capable of simultaneous removal of plastics and microplastics drifting in the ocean. Furthermore, there were no ships and their navigation method capable of solving the pollution problem caused by plastics and microplastics floating in the ocean. By arranging a magnetic drum that rotates in a direction opposite to the flow of a fluid containing flocs and by changing the flow path by about 180 degrees or so immediately before contacting the magnetic drum, the flocs can be removed without breaking. This method can downsize the size of the magnetic drum with the required area reduced. By combining small-sized flocculation and magnetic separation device and a device that breaks and recovers floating plastics, it is possible to remove plastics and microplastics floating in the ocean at the same time. By taking into account the status of marine plastics in the ship's planned route information, it becomes possible to remove plastics and microplastics floating on the ocean by the ship.
Claims
1.-6. (canceled)
7. A flocculation and magnetic separation device, comprising: a stirrer for stirring a fluid that contains plastics and plankton putting flocculant, magnetic material, and polymer into said fluid to produce flocs; a first magnetic drum having magnets on the surface thereof to attract said flocs thereon and rotating in the direction opposite to the flow direction of said floc-contained fluid to create eddies for attracting said flocs thereto; a second magnetic drum having magnets on the surface thereof to attract said flocs, and rotating in the same direction as a fluid of which flow direction being changed at a bump-like protrusion arranged at the rear of said first magnetic drum so as not to cause peeling off of said flocs attracted to said second magnetic drum; and a floc recovering section for recovering by grouping said flocs attracted to said first magnetic drum and to said second magnetic drum into one.
8. The flocculation and magnetic separation device according to claim 7, comprising a pipe into which a fluid containing plastic broken by a slit mechanism flows; wherein said slit mechanism has first slit section provided on said pipe at a predetermined angle and second slit section provided at the rear stage of said first slit section at an angel different from said predetermined angle; wherein the cross section of both a slit plate of said first slit section and a slit plate of said second slit section is acute with respect to the flow-in direction.
9. A marine plastic, microplastic, and ballast water purifying system having the flocculation and magnetic separation device according to claim 7.
10. A method of operation of a ship equipped with a flocculation and magnetic separation device, wherein, based on a request from a ship equipped with the flocculation and magnetic separation device according to claim 9, a planned course information center collects information on the pollution situation caused by marine plastics from a satellite, creates data on a planned course information based on said pollution status information, and transmits said planned course information to said ship having said device on-board.
Description
BRIEF DESCRIPTION OF DRAWINGS
[0035] FIG. 1 This figure is a side view of an example of a configuration diagram of the magnetic separating section of the flocculation and magnetic separation device of the present invention.
[0036] FIG. 2 This figure is a side view of an example of a configuration diagram of a separating section in a flocculation magnetic device of the present invention which device employs one fluid acceleration drum and one magnetic drum of the present invention.
[0037] FIG. 3 This figure is a side view of an example of a configuration diagram of the magnetic separating section of the flocculation magnetic device of the present invention which device employs two magnetic drums.
[0038] FIG. 4 This figure shows an example of a floc recovery section in the flocculation and magnetic separation device of the present invention.
[0039] FIG. 5 This figure shows an example of the configuration diagram of the flocculation and magnetic separation device of the present invention.
[0040] FIG. 6 This figure shows an example of the slit mechanism of the present invention for breaking plastics floating in the sea.
[0041] FIG. 7 This figure shows an example of the slit in a slitting mechanism of the present invention for breaking plastics floating in the sea.
[0042] FIG. 8 This figure shows an example of the marine plastic recovery system of the present invention.
[0043] FIG. 9 This figure shows an example of the marine plastic, microplastic, and ballast water purification system of the present invention.
[0044] FIG. 10 The figure shows an embodiment example of the operation of a ship equipped with the system for purifying marine plastic, microplastic, and ballast water.
[0045] FIG. 11 This figure is a side view of an example of a configuration diagram of the magnetic separating section of the flocculation and magnetic separation device of the present invention.
DESCRIPTION OF EMBODIMENTS
[0046] Hereinafter, embodiments of the present invention will be described with reference to the accompanying drawings.
EXAMPLES
[0047] FIG. 1 shows an embodiment example of a magnetic separating section of the flocculation and magnetic separation device of the present invention. A magnetic drum 1 having magnets near the surface thereof and flocs 4, containing a magnetic substance such as magnetite, on the flow 8a from the flocculation section, which is not shown in the figure, flow toward the drum 1 in the ascending direction opposite direction to the gravity direction 99. A flow velocity distribution 3a in a flow 8a has the highest flow velocity about or at the center and the slowest flow velocity on the wall of the flow channel. Therefore, the flocs collect in the portion of the flow where its velocity is high and its pressure is low in accordance with Bernoulli's equation. In order to prevent the fluid in front of the magnetic drum 1 from separating off from a bump-like protrusion 5a, the direction of the flow is changed by about 180 degrees or so at the bump-like protrusion 5a having a predetermined curvature. At that time, the flow in the vicinity of the bump-like protrusion 5a flows along a curved wall 6b, because the height of the bump-like protrusion 5a is lower than the maximum height of a wall 6a that forms one wall of the flow channel. The flock 4 rises and becomes a flock 4a carried on a flow close to the surface of the liquid of the flow of the bump-like protrusion 5a, and flows toward the magnetic drum 1. Since the direction of rotation of the magnetic drum 1 is opposite to that of a fluid flow 3b, fine eddies 10 are created, and the eddies 10 cancels out the velocity of the fluid, causing the floc 4a to float on the surface of the water with almost zero velocity. The flocs 4a on the surface of the water is attracted by the magnetic force of the magnet of the magnetic drum 1, and move closer to the magnetic drum 1, and sticks on the magnetic drum 1 by magnetic force. When the flocs 4a on the water surface are attracted to the magnetic drum 1 by magnetic force and pulled up from the water surface, the forces acting on the flocs are surface tension and magnetic force. Since the surface tension is a weak force, the flocs 4a are not broken. The magnetic drum 1 rotates in an opposite direction 2 to the flow direction of the flow 3b, the flocs 4b on the drum are, therefore, separated immediately from the fluid. Therefore, the area of the magnetic drum 1 required for the magnetic drum 1 to separate magnetically the flocs 4a is small.
[0048] Therefore, the magnetic drum 1 can be downsized because there is no need to take into account the travel time until the floc 4a defies the fluid resistance and adheres to the magnetic drum 1 by magnetic force. The floc 4b moves with the rotation of the magnetic drum 1 and collides with a scraper 9. Flocs 4c on the magnetic drum 1 are peeled off from the magnetic drum 1 by the scraper 9 pressed against the magnetic drum 1, and a brush roller 7 rotating in a direction 7b opposite to a rotating direction 2. The scraper 9 is supported in slant from a higher position to a lower position. Therefore, flocs 4d that have moved from the magnetic drum 1 onto the scraper 9 move on the scraper 9 by gravity and are recovered in the free-falling as flocs 4e. As shown with the flow 3b, the treated water, from which flocs have been removed from the fluid, flow through the flow channel formed by the magnetic drum 1 and a wall 6b, and then the direction of the flow is changed by 180 degrees or so at a bump-like protrusion 5b. The treated water falls freely with a velocity distribution 3c and is discharged as a flow 8b. Further, the flocs 4e are discharged as a flow 8c. The flow velocity in the area between the bump-like protrusion 5b and the magnetic drum 1 is slow and close to zero. Therefore, even if flocs 4 that were not removed in the vicinity of the bump-like protrusion 5a are present, they are attracted to the magnetic drum 1 in the vicinity of the bump-like protrusion 5b and are removed from the treated water.
[0049] FIG. 2 shows an embodiment example of the separating section of a flocculation and magnetic separation device using a rotating drum 11a that gives a flow velocity to the fluid and one magnetic drum 11b. The non-magnetic rotating drum 11a rotates in a direction 12a same as a flow 18a which includes flocs 14 and rotates at the rotation speed such that the peripheral speed thereof is at least equal to or higher than the average speed of a flow velocity. By forcibly increasing the flow velocity on the surface as in the Couette Flow, there is an effect that the portion of the flow having the highest flow velocity is brought closer to the vicinity of the rotating drum 11a. The purpose of this is to increase the probability that the flocs will collect in a place where the flow velocity is high, that is, where the pressure is low, and that the flocs will be carried by a flow flowing to a magnetic drum 12b that is located at the subsequent stage and rotates in the opposite direction. From the flocculation area, which is not shown in the figure, the fluid including flocs flows toward the rotating drum 11a rotating in the direction 18a, which is opposite to the direction of gravity 99. As shown in a velocity distribution 13a in the fluid, the velocity is fastest about in the center of the flow channel. The flocs 14, therefore, collect in the center of the flow. The direction of the flow is changed by 180 degrees or so at a bump-like projection 15a having a predetermined curvature. In a vicinity 13b of the bump-like protrusion 15a, the rotational force of the rotating drum 11a increases the speed of the flow. Therefore, the flow containing the flocs does not stay in the vicinity of the rotating drum 11a but flows toward a wall 16a. The high-velocity part of the flow 13b in the flow channel formed by the rotating drum 11a and the wall 16a is closer to the rotating drum 11a than when the drum 11a is not rotating. This is attributable to the peripheral velocity of the rotating drum 11a. Therefore, in a flow 13d in the vicinity of a bump-like protrusion 15b with curvature, the flow velocity is the highest at the part near the periphery. Flocs 14c collects in such a high flow velocity part and heads toward the magnetic drum 11b. In the vicinity of the magnetic drum 11b, there is a stagnant basin where the flow velocity is slowed down to almost zero by eddies 20b. Due to this almost-zero velocity, flocs 14b are attracted to the magnetic drum 11a rotating in the rotational direction 12a and are moved then released from the magnetic drum 11b by a slant-installed scraper 19 and a brush roller 17a which rotates in a rotational direction 17b opposite to a rotational direction 12b. The scraper 19 is supported in slant from a higher position to a lower position. Therefore, the flocs that have moved from the magnetic drum 11b onto the scraper 19 move on the scraper 19 by gravity and are recovered by free-falling as flocs 14e. The treated water from which the flocs have been removed flows around the magnetic drum 11b, and the direction of flow is changed by about 180 degrees or so at a bump-like protrusion 15c and is discharged by the gravity as a flow 18b with a velocity distribution 13e. Flocs 14e is also discharged as a flow 18c.
[0050] FIG. 3 shows an embodiment example of the present invention, which example is the magnetic separating section of the flocculation and magnetic separation device using two magnetic drums. The device of the present invention comprises a first magnetic drum 21a and a second magnetic drum 21b arranged front and back each other. The first magnetic drum 21a rotates in a direction 22a opposite to the direction of the flow that includes flocs and the second magnetic drum 21b rotates in a direction 22b the same as the flow that includes flocs. The flocculating section, though not shown in the figure, produces a flock-contained fluid by flocculating floating matters in a fluid together with magnetic substances such as magnetite. A flock-contained fluid flows out from the flocculation section, carried on a flow 28a, of which flow direction is opposite to the gravity direction 99, and heads toward the first magnetic drum 21a beyond a bump-like protrusion 25a. The flow 28a has the highest flow velocity about or at its center and the slow flow velocity in the vicinity of the wall 26c of the flow channel. Therefore, the flocs collect in the portion of the flow where its velocity is high and its pressure is low according to Bernoulli's equation and the distribution of velocity forms as shown with a velocity distribution 23a. In order to prevent the fluid from separating at a bump-like protrusion 5a provided at the front of the magnetic drum 1, the direction of the flow is changed by about 180 degrees or so at that bump-like protrusion 5a having a predetermined curvature. Like the velocity distribution 23a, the velocity in the fluid is fastest in the center of the flow channel; the flocks 24, therefore, collect in the center of the flow. At the time when the direction of the flow is changed largely by 180 degrees or so at the bump-like projection 25a having a predetermined curvature, the flow velocity in the outer circumference reaches the fastest, therefore, the flocks 24 move to the flocs 24a carried on a flow in the vicinity of the fluid surface, and the flocks 24a head the magnetic drum 21a, carried on a flow flowing toward the magnetic drum 21a. And further are attracted to the magnetic drum 21a by the magnetic force of the magnet on the surface thereof. Flocs 24b, which are attracted to the surface of the magnetic drum 21a by magnetic force, attach on the magnetic drum 21a rotating in the rotation direction 22a. Flocs 24b, which are attracted to the surface of the magnetic drum 21a by magnetic force, attach on the magnetic drum 21a rotating in the rotation direction 22a. Then the flocs 24b so attached to the magnetic drum 21a are separated therefrom by a scraper 29a, which is pressure-contacted to the magnetic drum 21a, and by a brush 27a. Being separated, the flocs 24c move on the scraper 29a and recovered into a floc recovering section 30. Since the direction of rotation of the magnetic drum 21a and the fluid flowing in the flow channel between the magnetic drum 21a and a curved wall 26a of the flow channel are opposite in velocity direction, eddies are generated in the fluid. The eddies cause the flocs to adhere to the magnetic drum. In this instance, however, the rotation speed of the magnetic drum 21a needs to be low enough that the eddies do not break the flocs, and the rotation speed is controlled considering the flocculation state. The flow direction of the fluid is greatly changed by a bump-like protrusion 25b, resulting in the movement of flogs toward the magnetic drum 21b, and the magnetic force causes the flocs 24d to attach to the magnetic drum 21b. Since the flow direction of the fluid and the rotation direction of the magnetic drum 21b is the same, there imposed no shearing or other force from the fluid, therefore the floc 24d on the surface of the magnetic drum 21b will not be separated by the fluid. The magnetic drum 21b rotates in the direction of rotation 22b, and the floc 24d on the magnetic drum 21b is scraped off by a scraper 29b which is in pressure-contact and by a brush 27b. The scraped flocs are then collected in the floc collection section 30, as shown with the flocs 24c. In the present invention, the floc collection section 30 can be integrated into one, so that the cost can be reduced. Instead of using the magnetic drum 21b, a filter separation method, as shown in FIG. 8, may be used. In the filter separation method, the same effect can be achieved by using a filter mesh of 47 microns or less so as to meet the removal standards for ballast water purification systems.
[0051] FIG. 4 shows an embodiment example of the floc recovery section in the flocculation and magnetic separation device of the present invention. A recovery section 34 consists mainly of a magnetic drum 31, a scraper 37 pressed against thereto, and a brush roller 36 used to peel off the flocs attracted by magnetic force on the surface of a magnetic drum 31. The flocs moved from the magnetic drum 31 by the brush roller 36 onto the scraper 37 are moved further by gravity and collected in the floc recovery section 34. Since the floc recovery section 34 is arranged in slant, the flocs move by gravity and are discharged from the end of the floc recovery section 34. The floc recovery section 34 has a semi-cylindrical shape to collect the flocs, but a concave or inverted triangular cross-section is also acceptable.
[0052] FIG. 5 shows an example of the embodiment configuration of the flocculation and magnetic separation device. In this configuration, a fluid 59 flows into a flocculation and magnetic separation device 55, and the appropriate amount of flocculant from a flocculant storage tank 40 and the appropriate amount of magnetite from a magnetite solution storage tank 41 are fed into the device, which is then agitated by a stirrer 43 in a quick stirrer unit 42 to produce micro-flocs. Inorganic flocculant and magnetite can be fed in any order and may be fed at the same time. Then, an organic flocculant 46 such as a polymer is added and agitated by a stirrer 45 in a slow-speed stirrer 44 to produce flocs in a size of several hundred microns to several millimeters. The flocs enter the separating section, and the fluid including flocs, of which speed has been increased by the rotational force of a non-magnetic rotating drum 49, head to a magnetic drum 50. The floc attaching to the surface of the magnetic drum is scraped from the surface thereof by a scraper 52 and a brush roller 51 that are in press-contact with the surface of the magnetic drum. Plankton and micro-flocs in the fluid 59 are flocculated and become flocs, which are removed from the fluid by the magnetic drum 50 described above. A separation section may be the separation section shown in above-stated FIG. 3.
[0053] FIG. 6 shows an example of the slitting mechanism for breaking plastics floating in the ocean. When plastics drifting in the sea is taken in by a ballast pump together with ballast water, seawater 63 is sucked also into a pipe 60 by the ballast pump, which is not shown in the figure. A first slit section 61 is arranged at a predetermined angle 611 with respect to the fluid to be sucked. A second slit section 62 is arranged at the rear stage of the first slit section 61 at a predetermined angle 622, which is different from the angle 611, with respect to the fluid to be sucked. The reason that the angle 611 is an acute angle and the complementary angle of the angle 622 is an obtuse angle in relation to the sucking direction of seawater 63 is to prevent clogging between the slit 61 and the slit 62 caused by drifting plastics. The slits are placed at a predetermined angle with respect to the inflow direction so that the shearing force can work.
[0054] FIG. 7 shows an embodiment example of the slit section of a slitting mechanism that breaks plastics floating in the ocean. A slit section 61 of a pipe 60 comprises plates 61a, 61b, and 61c each for forming slits thereon, as shown in FIG. 6. A slit section 62 shown in FIG. 6 comprises plates 62a, 62b, and 62c each for forming slits thereon. The cross-section of the plates 61a, 61b, 61c, 62a, 62b, and 62c are acute angles 61x and 65x with respect to the inflow direction. The reason for being the acute angle is to break the inflowing plastic. The plates 61a, 61b, 61c, 62a, 62b, 62c are arranged at equal intervals of 65a. 65b, 65c, and 65d. However, considering that the flow rate of the middle part is the maximum, spacings wider than the intervals 65b and 65c can be given to the plates 65a and 65d. With this, the effect for reducing the probability that the plastic waste may clog the slits will be produced.
[0055] FIG. 8 shows an embodiment example of the broken plastic recovery mechanism of the present invention. A fluid 73 such as seawater that includes a plastic 77 broken by the slit mechanism mentioned before flows in through a pipe 72. An endless belt filter 70, consisting of a filter of predetermined mesh size, rotates continuously between the rollers 71a and 71b, and the fluid 73 containing the broken plastics 77 passes between the rollers 71a and 71b. While passing, the endless belt filter 70 holds and conveys the broken plastics 77, which is then separated by a scraper 75 press-contacted on the endless belt filter 70, and the separated broken plastics 77 are put in a floe recovery tank 76. Further, the fluid 73 from which the broken plastics 77 has been removed flows into a pipe 74. The fluid 73 contains fine floating matter such as microplastics and plankton. The fluid 73 is sent to the flocculation and magnetic separation device 55 described above and undergoes flocculation and magnetic separation to become the fluid 59. In some cases, this recovery mechanism is installed at the rear stage of the magnetic separation mechanism to filter the objects that cannot be magnetically separated.
[0056] FIG. 9 shows an embodiment example of the marine plastic, microplastic, and ballast water purification system of the present invention. The marine plastic, microplastic, and ballast water purification system 100 is a system that is equipped on a ship.
[0057] The system comprises: [0058] a slitting mechanism 101 for breaking plastics, [0059] a pump 102 for supplying and draining seawater or freshwater, [0060] a recovering mechanism 103 for recovering large floating matters of tens of mm or more such as broken plastics, [0061] a recovery tank 104 for temporarily storing the recovered floating matters, [0062] a flocculation and magnetic separation mechanism 105 for recovering small floating matters of less than tens of mm, such as microplastics and plankton, [0063] a recovery tank 106 for temporally storing removed flocs that include microplastics or the like, and [0064] a control mechanism 108.
[0065] The flocculation and magnetic separation device 105 can be a composite mechanism that is a combination of a filter such as a ceramic filter and ozone or ultraviolet light. The treated water is temporarily stored in a ballast tank 107.
[0066] FIG. 10 shows an embodiment example of the operation method of the marine plastics, microplastics, and ballast water purification system.
[0067] A course plan information center 210 is configured with: [0068] a means for acquiring marine traffic information 202, [0069] a means for collecting marine plastic information 203, [0070] a means for collecting geographic information 204, [0071] a means for creating planned course 295. [0072] a means for receiving planned course request 201, and [0073] a means for providing planned course 206.
[0074] The means for acquiring marine traffic information 202 gathers the information of the automatic vessel identification system and other similar information collected from the base stations not illustrated in the figure. The means for collecting marine plastic information 203 collects information on the pollution caused by marine plastics in the sea area of which state is gathered by a satellite 200. The means for acquiring geographic information 202 acquires the location of own ship, the port of destination, and the geographic information on the sea area between these two places included in the planned course request signal. A means for creating planned course 205 produces a planned course based on the information collected by the means for acquiring regional traffic information 202 mentioned above, the means for collecting marine plastics and other marine pollution information 203, and the means for collecting geographic information 204. When creating this planned course, the plan will take into account whether the ballast water is loaded, how much are the quantity of loaded ballast water when loaded, whether the removal work of ocean plastics and other marine pollution matters can be performed, and the urgency of the ocean plastics removal work. A ship 220 is equipped with a means for transmitting the planned course request 221, a means for receiving the planned course 222, and a steering means 223 that operates reflecting the received results. The results of the removal work for marine plastics and other marine pollution matters (removed marine area, amount of removed marine plastics, and other marine pollution matters) are transmitted to the course plan information center 210. The course plan information center transmits this information to the International Maritime Organization (IMO) and other public organizations, and environmental protection groups. International organizations, such as the International Maritime Organization, and environmental protection groups will make this information available to the public and formulate strategies against marine pollution. As a result, if further removal of pollution is necessary, cooperation will be asked ships that are scheduled to sail near the area in question for taking measures against marine pollution. The collected marine plastics and other marine pollutants will be purchased by the government or municipality of the port of call as industrial waste. This means that the ships equipped with marine plastics, microplastics, and ballast water purification systems will take the charge of cleaning the ocean in addition to transporting oil and other valuable materials.
[0075] FIG. 11 shows an embodiment example of the magnetic separating section of the flocculation and magnetic separation device of the present invention. A magnetic drum 301 having magnets near the surface thereof, and flocs 304 on a flow 308a from a flocculation section, which is not shown in the figure, containing magnetite and other magnetic substances flow in the direction opposite to the direction of gravity 99 toward the magnetic drum 301. The velocity distribution 303a in the flow 308a has the highest velocity almost at the middle and the low velocity at the wall of the flow channel. Therefore, the flocs gather in the center of the flow where the velocity is faster according to Bernoulli's law (Bernoulli's equation). In order to move the flocs 304 flowing in the middle of the fluid in the immediate front of the magnetic drum 301 to the fluid surface, the direction of flow is changed by about 180 degrees or so at a bump-like projection 305a having a predetermined curvature, and the fluid flows along a concave 305a having a predetermined curvature placed at the subsequent stage. This concave 305b and a bump-like protrusion 305c configure a waterfall-basin-like structure, which produces eddies 310a. Since the particle size of a floc 304b is larger compared to that of a fluid molecule, this size difference produces fluid resistance, which causes the eddies 310a. The eddies 310a make the flocs 304b float on the fluid surface. The flocs flow towards the magnetic drum 301. Since the direction of rotation of the magnetic drum 301 is opposite to that of a fluid flow 303b, this direction difference creates eddies 310b, and the velocity of the fluid in the eddies 310b cancels each other, resulting in a lower velocity of flocs 4a. Flocs 304a on the flow of low-velocity approach a magnetic drum 1 by the magnetic force and attracted thereon. Since the resistance acting on the flocs 304a is mainly surface tension, the flocs 304a are not easily broken. The magnetic drum 301 rotates in a direction 302 opposite to the flow 303b, so that the floc 304b on the drum is immediately separated from the water. Therefore, the contact area of the magnetic drum 301 required for separating magnetically the flocs 304a can be reduced to an extent several mm above and below the fluid surface. The reason for this is that when the flocs 304 are attracted to the magnetic drum 301, a new surface with no flocs attracted appears since the magnetic drum 301 is rotating. Therefore, the actual contact area on a magnetic drum 301 required for attracting flocs thereto by the magnetic force of the magnetic drum 301 is small. The magnetic drum 1 is not damaged by the fluid resistance. Furthermore, it is not necessary to consider the travel time of the flocks to adhere, by the magnetic force, to the magnetic drum 1 against the fluid resistance, as described in {Patent Literature 1}. Therefore, the magnetic drum 301 can be miniaturized. Flocs 304c on the magnetic drum 301 is separated therefrom by a scraper 309 pressed against the magnetic drum 301 and the brush roller 307 rotating in a rotation direction 307a opposite to the rotation direction 302, and the flocs 304b move onto the scraper 309. The flocs 304b are recovered by free fall due to gravity like flocs 304d. Further, the treated water from which the flocs have been removed flows along the magnetic drum 301 as shown in the flow 303b, and the direction of the flow is changed by about 180 degrees or so at the bump-like protrusion 305c. The treated water flows with a flow velocity distribution 303c and is discharged as a flow Sb. Further, the flocs 4c are discharged as a flow 308c.
INDUSTRIAL APPLICABILITY
[0076] The International Maritime Organization (IMO) established the Convention for the Control and Management of Ships' Ballast Water and Sediments (hereinafter referred to as the Convention) in order to prevent the destruction of ecosystems caused by seawater substitution by ships' ballast water which includes species that did not originally exist in the sea area. However, the problem of ocean pollution by plastics and microplastics has arisen. The mainstream of ballast water treatment method is a sterilization method using ultraviolet rays, ozone, hypochlorous acid, or the like. This method can kill aquatic organisms in ballast water. However, the problem of marine pollution caused by the above-stated plastics and microplastics cannot be solved. Even a ship that collects marine plastics is built, it is still difficult to recover microplastics, though such a ship can recover large plastics. The present invention provides a method for simultaneous solving the problem of ecosystem destruction caused by ballast water and the problem of marine pollution caused by plastics and microplastics.
TABLE-US-00001 {Reference Signs List} 1, 11b, 22a, 22b, Magnetic drum 31, 50, 301 2, 12a, 12b, 22a, Direction of rotation 22b, 78, 302 3a, 3c, 13a, 13b, Flow velocity distribution 23a, 23b, 303a, 303b 3b Direction of flow 4, 14, 304 Flocs 4a, 14a, 14c, Flocs flowing toward magnetic drum 24a, 304a 4b, 14d, 24b, Flocs attracted on magnetic drum 24d, 304c 4c, 14e, 14f, 24c Recovered flocs 5a, 5b, 15a, 15b, Bump-like protrusion 15c, 25a, 25b, 25c 6a, 6b, 16a, 16b Wall surface 7, 17a, 17d, 27a, Brush roller 27b, 51, 307 7a, 17b, 17c Brash roller rotation direction 7a, 17b, 17c Flow direction of fluid including flocs 8b, 18b, 28b Flow direction of treated fluid 8c, 18c, 18d Flow direction of recovered flocs 9, 19a, 19b, 29a, Scraper 29b, 37, 52 11a, 49 Rotating drum 34 Flocs recovery section 40 Flocculant storage tank 41 Magnetite storage tank 42 Slow stirring device 44 Quick stirrer 43, 44 Stirrer 46 Polymer storage tank 59, 63, 73 Fluid 60, 72, 74 Pipe 61, 61a, 61b, 61c, Plate for forming slit 62, 62a, 62b, 62c 61x, 65x Cross section of plate 65a, 65b, 65c, 65d Plate spacing 70 Endless belt filter 71a, 71b Roller 76 Flocs recovery tank 100 Marine plastics, microplastics and ballast water purification systems 101 Filtering mechanism 102 Pump 103 Recovering mechanism 104, 106 Recovery tank 105 Flocculation and magnetic separation mechanism 107 Ballast tank 108 Control console 200 Satellite 210 Course plan information center 201 Means for receiving planned course request 202 Means for collecting marine traffic information 203 Means for collecting information on marine pollution such as marine plastics 204 Means for collecting geographical information 205 Means for creating planned course 206 Means for providing planned course 210 Ships 221 Means for transmitting planned course request 222 Means for receiving planned course 223 Steering means 305a Concave
