WO2017168861A1 - Dispositif à cyclone magnétique et son procédé de traitement - Google Patents

Dispositif à cyclone magnétique et son procédé de traitement Download PDF

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Publication number
WO2017168861A1
WO2017168861A1 PCT/JP2016/087113 JP2016087113W WO2017168861A1 WO 2017168861 A1 WO2017168861 A1 WO 2017168861A1 JP 2016087113 W JP2016087113 W JP 2016087113W WO 2017168861 A1 WO2017168861 A1 WO 2017168861A1
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Prior art keywords
magnetic
cyclone
cylindrical base
cylindrical
liquid
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PCT/JP2016/087113
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English (en)
Japanese (ja)
Inventor
望月 明
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株式会社日立製作所
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D21/00Separation of suspended solid particles from liquids by sedimentation
    • B01D21/28Mechanical auxiliary equipment for acceleration of sedimentation, e.g. by vibrators or the like
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C1/00Magnetic separation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04CAPPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C11/00Accessories, e.g. safety or control devices, not otherwise provided for, e.g. regulators, valves in inlet or overflow ducting
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04CAPPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00Apparatus in which the axial direction of the vortex is reversed
    • B04C5/24Multiple arrangement thereof
    • B04C5/28Multiple arrangement thereof for parallel flow

Definitions

  • the present invention relates to a magnetic cyclone device and a processing method thereof.
  • Patent Document 1 discloses a solid-liquid separation device that improves the ability to separate impurities from raw water and prevents re-mixing of separated impurities into treated water.
  • Patent Document 2 discloses a magnetic fluid recovery device for efficiently separating and removing magnetic particles contained in a fluid.
  • Patent Document 3 discloses a magnetic separation apparatus that can separate a magnetic floc with little use of washing water to generate high-density sludge.
  • a fluid containing magnetic floc is allowed to flow into the inside from near the bottom of the conical container with the apex directed downward. Then, the inflowing fluid is rotated inside the conical container, and heavy impurities are slid down the conical wall surface using the difference in specific gravity to remove downward from the vicinity of the apex of the conical container. And it is the system which collect
  • the magnetic separation method is a method for obtaining treated water from which magnetic flocs in the fluid are attracted by the magnetic force of the magnets to remove the magnetic flocs from the fluid.
  • centrifugal force is used to separate magnetic flocs.
  • it is necessary to increase the fluid velocity for the purpose of increasing the centrifugal force.
  • the magnetic floc is broken by centrifugal force or the like.
  • Patent Document 2 in order to separate the magnetic floc from the fluid, the magnetic fine particles discharged from the cyclone are attracted to the wall surface by the magnetic force of the magnet, and the magnetic fine particles are separated from the fluid. Thereafter, the magnetic force applied to the magnetic fine particles is reduced or eliminated by physically separating the magnet from the wall surface. As a result, the magnetic particles are separated from the wall surface and dropped by gravity to collect the magnetic floc. In this case, since the centrifugal force and magnetic force of the fluid work separately, it is not necessary to dare to use one device.
  • the magnetic force works in both directions of the N pole and the S pole, but there is a problem that only one direction is utilized.
  • the centrifugal force there is a problem that the centrifugal force for separating the magnetic substance from the fluid does not work satisfactorily due to the small mass of the particles having a small particle size and the separation performance is poor.
  • an operation of opening / closing a valve near the outlet or reducing magnetic force by moving the magnetic field applying means is used for final separation. Therefore, there is a problem that it is not suitable for continuous operation.
  • Patent Document 3 magnetic force is used to separate magnetic flocs.
  • the magnetic floc is separated by the film.
  • the magnetic floc is separated by the magnetic force.
  • the flow rate cannot be increased because the magnetic flocs are separated without being destroyed.
  • the present invention has been devised in view of the above circumstances, and an object thereof is to provide a magnetic cyclone apparatus capable of reliably separating magnetic particles and magnetic floc from a fluid, and a treatment method thereof.
  • a magnetic cyclone device has a truncated cone shape with a vertex facing downward, a cylindrical cylindrical base portion having an inflow port on a side, and a lower portion of the cylindrical base portion.
  • the processing method of the magnetic cyclone device according to the second aspect of the present invention is a method for realizing the first aspect of the present invention.
  • the present invention it is possible to provide a magnetic cyclone apparatus that can reliably separate magnetic particles and magnetic flocs from a fluid and a processing method thereof.
  • FIG. 1 The figure which shows the structural example of the purification system of the magnetic cyclone apparatus of Embodiment 1.
  • FIG. The figure which shows the structure which looked at the magnetic cyclone apparatus which concerns on Embodiment 1 from the side.
  • the figure which shows the example of the control pattern of a magnetic cyclone apparatus The figure which shows the structural example which looked at the magnetic cyclone apparatus which concerns on the modification 1 from upper direction.
  • the magnetic cyclone apparatus 1S of the present invention (see FIG. 1) is a polluted water that enables high speed, high reliability, and high performance to treat polluted water by fusing the agglomeration magnetic separation and cyclone separation in the high speed water treatment apparatus. It is a processing device.
  • the magnetic cyclone device 1S uses a magnetic force in addition to a fluid force in order to separate the magnetic floc at a low speed (for example, 0.2 m / s or less) that does not destroy the magnetic floc. Make magnetic frock in polluted water. Then, by applying an attractive force by magnetic force to the magnetic floc, the magnetic floc is attracted to the vicinity of the side surface of the cyclone 1 where the flow velocity of the turning motion in the cyclone 1 becomes substantially zero. Thereby, since the specific gravity is heavier than water, a magnetic particle and a magnetic floc descend
  • the magnetic force of the electromagnet 5 is large at the N-pole and S-pole magnetic poles 5a and 5b. Therefore, by disposing any one of the magnetic poles 5a and 5b of the electromagnet 5 near the cyclone 1, the magnetic force of the electromagnet 5 can be effectively used, and the magnetic floc can be separated efficiently with a small current.
  • embodiments of the present invention will be described in detail with reference to the drawings as appropriate.
  • Embodiment 1 In FIG. 1, the structural example of the purification system of the magnetic cyclone apparatus of Embodiment 1 is shown.
  • the purification system S of Embodiment 1 includes a magnetic substance supply device 30, a flocculant supply device 31, a rapid stirring device 32, a polymer supply device 36, a slow stirring device 34, and a magnetic cyclone device 1S.
  • the magnetic substance supply device 30, the flocculant supply device 31, the rapid stirring device 32, the slow stirring device 34, and the magnetic cyclone device 1S are connected via a pipe k (k1, k2, k3).
  • the polluted water of the fluid that is the liquid to be treated flows through the pipe k.
  • the polluted water is, for example, sewage, ballast water, oil, accompanying water containing heavy metals, water, water containing SS (Suspended Solid), and the like.
  • the magnetic body supply device 30 applies a magnetic body to the liquid to be processed flowing through the pipe k1 in order to create a magnetic floc.
  • the flocculant supply device 31 supplies the flocculant to the liquid to be processed flowing through the pipe k1 in order to collect the floating substances and foreign matters in the liquid to be processed to make micro flocs.
  • the micro floc is a mass having a diameter of 100 ⁇ m or less.
  • the rapid stirring device 32 rapidly stirs the contaminated water supplied with the magnetic substance and the flocculant to create micro flocs.
  • the polymer supply device 36 collects the micro flocs including the magnetic material and the micro flocs not including the magnetic material to supply the polymer 36s which is an inorganic flocculant in order to make the floc including the magnetic material.
  • a floc is a lump with a diameter of 1 mm or more.
  • the slow stirring device 34 collects the micro flocs containing the magnetic substance and the micro flocs not containing the magnetic substance with the polymer 36s of the inorganic flocculant to make the floc containing the magnetic substance, and the liquid to be treated flowing through the pipe k2 Is stirred at a slow speed.
  • the magnetic cyclone apparatus 1S is an apparatus that attracts a floc containing a magnetic material from a liquid to be processed by an electromagnet 5 and separates the floc into a processing liquid other than the floc. Processing liquids other than floc are acquired.
  • Magnetic material 30s and coagulant 31s are added to the fluid 100 in the pipe k1 from the magnetic material supply device 30 and the coagulant supply device 31, respectively, at arbitrary concentrations. The order of adding the magnetic body 30s and the flocculant 31s may be reversed.
  • the fluid 100 to which the magnetic body 30 s and the flocculant 31 s are added is stirred by the stirrer 33 of the rapid stirrer 32, and a micro floc having a particle size of about several tens of ⁇ m is formed.
  • the polymer 36s of the inorganic flocculant is added from the polymer supply device 36 to the fluid 100 flowing through the pipe k2.
  • the fluid 100 to which the polymer 36s has been added is stirred by the stirrer 35 of the slow stirring device 34, and a large magnetic floc having a particle size of 100 ⁇ m or more is created by the aggregation action of the polymer 36s.
  • a fluid 7 containing magnetic floc flows into the cyclone 1. Near the outer periphery of the cyclone 1, any one of the magnetic poles 5a and 5b of the electromagnet 5 is disposed.
  • the electromagnet 5 is controlled to be turned on / off by the controller 1C (see FIG. 2).
  • the magnetic floc in the fluid 7 flowing into the cyclone 1 is attracted to the magnetic pole 5 a of the electromagnet 5, separated from the fluid 7, falls downward by gravity, and is discharged from the downstream outlet 4.
  • the fluid from which the magnetic floc has been removed flows out from the upstream outlet 3 of the upper cylindrical portion 1e and is acquired.
  • the magnetic substance 30s is contained in all the micro flocs of about several tens of ⁇ m after being stirred by the stirrer 33 of the rapid stirring device 32, the polymer 36s as an inorganic flocculant is added and the stirring is performed slowly. There is no need to provide a step of stirring with the stirrer 35 of the apparatus 34 to produce a large magnetic floc having a particle size of 100 ⁇ m or more.
  • FIG. 2 is a diagram illustrating a configuration of the magnetic cyclone device according to the first embodiment when viewed from the side.
  • a magnetic cyclone device 1S according to the first embodiment includes a cyclone 1 and an electromagnet 5.
  • the cyclone 1 is made of a nonmagnetic material such as plastic or aluminum.
  • the cyclone 1 includes an inlet 2, an upstream outlet 3, and a downstream outlet 4.
  • the cyclone 1 has an inlet portion 1a, a cylindrical base portion 1b, an inverted conical portion 1c, a lower cylindrical portion 1d, and an upper cylindrical portion 1e.
  • the inlet portion 1a has a cylindrical shape whose inner surface is a horizontal axis.
  • One of the inlet portions 1a is the inflow port 2, and the other inner surface is communicated with a cylindrical base portion 1b having the following cylindrical shape.
  • the cylindrical base portion 1b and the reverse cone portion 1c form an inverted truncated cone portion whose apex is directed downward.
  • the inverted truncated cone part has an upper inner surface (side wall surface 1b1) having a cylindrical cylindrical part 1b, and a lower inner surface (conical sidewall 9) having an inverted conical inverted cone part 1c.
  • the inverted conical portion 1c has a shape in which the inner surface thereof is an inverted cone, and the bottom surface located above has a shape corresponding to the lower surface of the cylindrical base portion 1b, and is continuously formed below the cylindrical base portion 1b. .
  • the inner surface of the lower cylindrical portion 1d has a cylindrical shape.
  • the upper portion of the lower cylindrical portion 1d communicates with the inverted conical portion 1c, and the lower portion thereof is opened as the downstream outlet 4.
  • the upper cylindrical portion 1e has a cylindrical inner surface.
  • the upper cylindrical part 1e is provided in the center of the cylindrical base part 1b.
  • the upper cylindrical part 1e is opened at the lower part to the inside of the inverted conical part 1c or the cylindrical base part 1b, and the upper part is communicated with the treated water recovery part (not shown) as the upstream outlet 3.
  • one of the S poles and N poles 5a and 5b of the electromagnet 5 is disposed.
  • the S pole or N pole of the electromagnet 5 is provided on the other side (opposite side) with respect to the inlet 2 on one side of the cyclone 1.
  • the fluid 7 to be treated containing magnetic particles and magnetic flocs flows from the inlet 2 through the inlet 1a into the cyclone 1 (arrow ⁇ 0 in FIG. 2) by a pump (not shown).
  • the fluid 7 of the liquid to be treated which flows in is guided by the side wall surface 1b1 of the cylindrical base portion 1b and flows around (solid line arrow ⁇ 1 in FIG. 2).
  • the fluid 7a such as water other than the magnetic particles and the magnetic floc is a non-magnetic material, and is not affected by the magnetic force, that is, the magnetic stopping force does not work, and the specific gravity is lighter than that of the fluid 7. Therefore, it receives a centrifugal force and is guided by the side wall surface 1b1 of the cylindrical base portion 1b to rotate upward (arrow ⁇ 3 in FIG. 2). And it flows into the upper cylindrical part 1e of the cylindrical shape, flows up, and is discharged from the upstream outlet 3 (arrow ⁇ 4 in FIG. 2). Thereby, the fluid 7 containing the magnetic particles and the magnetic floc is separated into the magnetic particles and the magnetic floc and the fluid 7a other than the magnetic particles and the magnetic floc.
  • FIG. 3 shows a configuration example of the magnetic cyclone device according to the first embodiment viewed from above.
  • Magnetic particles or magnetic flocs 10, 11, 12 in the fluid 7 entering from the inlet 2 of the cyclone 1 are pulled by the fluid force and the magnetic force generated by the electromagnet 5 and travel in the direction of the thin solid arrow ⁇ 0,
  • the cyclone 1 moves near the side wall surface 1b1 of the inner peripheral surface. Since the flow velocity around the side wall surface 1b1 is close to zero due to friction, the magnetic particles or the magnetic flocs 20, 21, and 22 cannot get on the flow of other fluids 7 due to the magnetic stopping force. It adheres to 1b1 or exists in the vicinity thereof. Since the magnetic particles or the magnetic flocs 20, 21, 22 have a specific gravity larger than 1, they naturally fall from the fluid 7 along the conical side wall 9 of the inverted conical portion 1 c and are discharged from the downstream outlet 4.
  • the flow rate of the fluid 7 flowing in from the inflow port 2 is Q1
  • the flow rate of magnetic particles discharged from the downstream outlet 4 (see FIG. 2) and the magnetic floc containing magnetic particles is Q2
  • the product In the production of liquid substances using water such as petroleum, the product is produced in a mixed state with water, that is, in the form of accompanying water.
  • separation methods using specific gravity differences or centrifugal force such as when the product is a liquid, or when separating substances with small specific gravity differences from water, such as sewage treatment plants and algae culture plants, are effective separations. It is difficult.
  • high-performance separation is possible by aggregating magnetic particles and magnetic powder with petroleum and algae to form and separate flocs.
  • the magnetic poles 5a of the electromagnet 5 are arranged in the same direction as, or perpendicular to, the moving direction of the magnetic particles and the magnetic floc entering the cyclone 1.
  • the magnetic particles and the magnetic floc are attracted to the vicinity of the side wall surface 1b1 of the cyclone 1 by pulling with any one of the magnetic forces 5b.
  • the magnetic particles and the magnetic flocs are further reduced to zero by the magnetic force, so that the magnetic particles and the magnetic flocs become conical side walls 9 of the inverted conical portion 1c. Fall into. Since the conical side wall 9 has an oblique inclination with respect to the direction of gravity, the magnetic particles and the magnetic flocs descend along the conical side wall 9 due to gravity. As a result, the magnetic particles and the magnetic floc descend along the side surface of the cyclone 1 and are discharged from the downstream outlet 4.
  • FIG. 4 shows an internal configuration example of the magnetic cyclone device according to the second embodiment viewed from the side.
  • a first cyclone 21A and a second cyclone 21B are arranged with an electromagnet 25 interposed therebetween.
  • the first and second cyclones 21A and 21B are made of a nonmagnetic material such as plastic or aluminum.
  • the electromagnet 25 has S poles and N poles 25a and 25b. Therefore, one of the magnetic poles 25a and 25b of the electromagnet 25 is disposed to face the first cyclone 21A, and the other magnetic pole is disposed to face the second cyclone 21B.
  • the other configuration is the same as that of the first embodiment, and therefore, the same components are denoted by reference numerals in the 20th order, and detailed description thereof is omitted.
  • the first cyclone 21A includes a first inlet portion 21a1, a first cylindrical base portion 21b1, a first inverted conical portion 21c1, a first lower cylindrical portion 21d1, and a first upper cylindrical portion 21e1.
  • a first downstream outlet 24a is provided in the first lower cylindrical portion 21d1.
  • the inner surface of the first upper cylindrical portion 21e1 has a cylindrical shape.
  • the first upper cylindrical portion 21e1 is formed at the center of the first cylindrical base portion 21b1.
  • the lower part of the first upper cylindrical part 21e1 is opened inside the first inverted conical part 21c1 or the first cylindrical base part 21b1, and the upper part is communicated with a treated water recovery part (not shown) as a first upstream outlet 23a. Yes.
  • the second cyclone 21B includes a second inlet portion 21a2, a second cylindrical base portion 21b3, a second inverted conical portion 21c2, a second lower cylindrical portion 21d2, and a second upper cylindrical portion 21e2.
  • a second downstream outlet 24b is provided in the second lower cylindrical portion 21d2.
  • the inner surface of the second upper cylindrical portion 21e2 has a cylindrical shape.
  • the second upper cylindrical portion 21e2 is formed at the center of the second cylindrical base portion 21b3.
  • the lower part of the second upper cylindrical part 21e2 is opened inside the second inverted conical part 21c2 or the second cylindrical base part 21b3, and the upper part is communicated with a treated water recovery part (not shown) as a second upstream outlet 23b. Yes.
  • the fluids 103 and 104 containing magnetic particles and magnetic flocs are respectively supplied from the first inlet 22a of the first cyclone 21A and the first inlet 22b of the second cyclone 21B from the first cylindrical base 21b1 and the second cylindrical base. 21b3 from the opposite direction.
  • the direction in which the fluid 103 flowing into the first cyclone 21A and the fluid 104 flowing into the second cyclone 21B travel is the direction toward the magnetic poles 25a and 25b of the electromagnet 25.
  • the electromagnet 25 is controlled in current by the control unit 2C.
  • the magnetic particles and magnetic floc of the fluid 103 in the first cyclone 21A are attracted to the first side wall surface 21b2 of the first cylindrical base portion 21b1 by the magnetic force generated in one magnetic pole 25a of the electromagnet 25, and the flow velocity is greatly increased. descend.
  • the first reverse cone portion 21c1 is rotated while rotating as indicated by an arrow ⁇ 22a. To do. Finally, the magnetic particles and the magnetic floc are discharged from the downstream outlet 24a of the first cyclone 21A (arrow ⁇ 25a in FIG. 4).
  • the fluid 103a from which magnetic particles and magnetic flocs have been removed has a specific gravity lighter than that of the fluid 103, so that it is pushed by the inflowing fluid 103 and rises in a spiral flow as indicated by the arrow ⁇ 23a.
  • the gas is discharged from the first upstream outlet 23a of the portion 21e1 (arrow ⁇ 24a in FIG. 4).
  • the magnetic particles and magnetic floc of the fluid 104 in the second cyclone 21B are attracted to the second side wall surface 21b4 of the second cyclone 21B by the magnetic force generated in the other magnetic pole 25b of the electromagnet 25, and the flow velocity is greatly increased. To drop. A speed difference occurs between the magnetic particles and magnetic floc and the fluid 104a.
  • the inverted cone portion 21c2 falls while rotating as indicated by an arrow ⁇ 22b. Finally, the magnetic particles and the magnetic floc are discharged from the second downstream outlet 24b of the second cyclone 21B (arrow ⁇ 25b in FIG. 4).
  • the fluid 104a from which the magnetic particles and magnetic flocs have been removed has a specific gravity lighter than that of the fluid 104, so that it is pushed by the inflowing fluid 104 and rises in a spiral flow as indicated by the arrow ⁇ 23b.
  • the gas is discharged from the second upstream outlet 23b of the portion 21e2 (arrow ⁇ 24b in FIG. 4).
  • FIG. 5 shows an example of a control pattern of the magnetic cyclone device.
  • the horizontal axis of FIG. 5 shows (elapsed) time (T), and the vertical axis shows the magnitude of current (I).
  • T time
  • I magnitude of current
  • the current pattern 200 for applying a constant current value is easy to control, but the magnetic particles in the fluid and the like on the first side wall surface 21b2 of the first cyclone 21A and the second side wall surface 21b4 of the second cyclone 21B shown in FIG. There is a risk that magnetic flocs will continue to adhere. Therefore, the pulse current pattern 201 is optimal as the control pattern.
  • the heating times 202, 203, 204, 205, 206, and 207 for applying the current are basically the same time, but can be changed to different times.
  • the non-heating times 210, 211, 212, 213, and 214 in which no current is applied are basically the same time, but can be changed. Assuming that the concentration of magnetic flocs and the like in the liquid to be processed is the same, the magnetic particles in the fluids 103 and 104 flowing into the first cyclone 21A and the second cyclone 21B when the flow rates of the fluids 103 and 104 of the liquid to be processed are low While the magnetic flocs (amount to be processed) are reduced, the magnetic particles and magnetic flocs in the fluids 103 and 104 flowing into the first cyclone 21A and the second cyclone 21B when the flow rates of the fluids 103 and 104 of the liquid to be processed are low. (Amount to be processed) increases.
  • the charging times 202, 203, 204, 205, 206, and 207 are changed depending on the flow velocity of the flowing fluid. It is desirable that the time is substantially the same as the time for making a round in the first cyclone 21A and the second cyclone 21B depending on the flow velocity.
  • control pattern intermittently applies current to the electromagnet 25, the magnetic particles and the magnetic floc continue to adhere to the first side wall surface 21b2 of the first cyclone 21A and the second side wall surface 21b4 of the second cyclone 21B. There is no. Therefore, the magnetic particles and magnetic floc in the fluids 103 and 104 can be effectively and reliably removed from the fluids 103 and 104.
  • the control pattern described above may be applied to the magnetic cyclone device 1S of the first embodiment.
  • the electromagnet 25 is provided with the magnetic poles 25a and 25b facing between the first cylindrical base portion 21b1 of the first cyclone 21A and the second cylindrical base portion 21b3 of the second cyclone 21B. Therefore, only one electromagnet 25 is required. Since one electromagnet 25 is sufficient for the two first cyclones 21A and the second cyclone 21B, the configuration is simple, and the cost of the magnetic cyclone device 2S can be reduced.
  • the magnetic cyclone device 2S can be made compact because it can be constituted by the two first cyclones 21A, the second cyclone 21B, and one electromagnet 25.
  • the magnetic particles and the magnetic floc that flowed in are first and second sides of the first and second cylindrical base portions 21b1 and 21b3 of the first and second cyclones 21A.
  • the adhesion to the wall surfaces 21b2 and 21b4 is suppressed. Therefore, it is possible to realize a magnetic cyclone device 2S that is low in cost, small in size, and highly reliable.
  • FIG. 6 shows a configuration example of the magnetic cyclone device according to the first modification viewed from above.
  • the magnetic cyclone device 3S of Modification 1 is arranged with an electromagnet 35 sandwiched between a first cyclone 31A and a second cyclone 31B.
  • the inflow direction of the inlet portion 31a1 of the first cyclone 31A and the inflow direction of the inlet portion 31a2 of the second cyclone 31B are arranged in opposite directions.
  • the first and second cyclones 31A and 31B are made of a nonmagnetic material such as plastic or aluminum.
  • the electromagnet 35 is sandwiched between the inflow direction of the first inlet portion 31a1 of each first cyclone 31A (arrow ⁇ 31 in FIG. 6) and the inflow direction of the inlet portion 31a2 of the second cyclone 31B (arrow ⁇ 32 in FIG. 6). Placed in.
  • one magnetic pole 35a of the electromagnet 35 is disposed in the vicinity of the outer periphery of the first cylindrical base portion 31b1 so as to face the inflow direction of the first inlet portion 31a1 of the first cyclone 31A. Further, the other magnetic pole 35b of the electromagnet 35 is disposed in the vicinity of the outer periphery of the second cylindrical base portion 31b3 so as to face the inflow direction of the inlet portion 31a2 of the second cyclone 31B. Since other configurations are the same as those of the second embodiment, detailed description thereof is omitted.
  • the magnetic particles and the magnetic floc in the fluid of the liquid to be processed flowing into the first inlet portion 31a1 of the first cyclone 31A are added to the fluid flow force (arrow ⁇ 31 in FIG. 6), and the magnetic pole 35a of the electromagnet 35. It is attracted by the magnetic force.
  • the magnetic particles and the magnetic floc in the fluid of the liquid to be processed flowing into the second inlet 31a2 of the second cyclone 31B are added to the magnetic force 35b of the electromagnet 35 in addition to the fluid flow force (arrow ⁇ 32 in FIG. 6). Attracted by magnetic force.
  • the magnetic particles and magnetic floc in the fluid flowing in from the first inlet portion 31a1 of the first cyclone 31A are moved toward the first side wall surface 31b2 of the first cylindrical base portion 31b1 by the magnetic force of the magnetic pole 35a of the electromagnet 35.
  • the magnetic particles and magnetic floc in the fluid flowing from the second inlet portion 31a2 of the second cyclone 31B are moved to the second side wall surface 31b4 side of the second cylindrical base portion 31b3 by the magnetic force of the magnetic pole 35b of the electromagnet 35. And attached to the second side wall surface 31b4 or in the vicinity of the second side wall surface 31b4.
  • the magnetic particles and the magnetic flocs adhering to the first side wall surface 31b2 of the first cyclone 31A or existing in the vicinity of the first side wall surface 31b2 slide down on the conical side wall of the first inverted conical portion (not shown) due to gravity. 1 is discharged from the downstream outlet 34a.
  • the fluid from which the magnetic particles and the magnetic floc have been removed is taken from the first upstream outlet 33a.
  • magnetic particles and magnetic flocks attached to the second side wall surface 31b4 of the second cyclone 31B or present in the vicinity of the second side wall surface 31b4 slide down the conical side wall of the second inverted conical portion (not shown) due to gravity, It is discharged from the second downstream outlet 34b.
  • the fluid from which the magnetic particles and magnetic floc have been removed is taken from the second upstream outlet 33b.
  • the inflow direction of the first inlet portion 31a1 of the first cyclone 31A is opposite to the inflow direction of the second inlet portion 31a2 of the second cyclone 31B.
  • the magnetic pole 35a and the magnetic pole 35b of the electromagnet 35 are arrange
  • the magnetic poles 35 and 35b of the electromagnet 35 are attracted to each other. Therefore, magnetic particles and magnetic flocs in the fluid can be effectively separated from the fluid.
  • FIG. 7 shows a configuration example of the magnetic cyclone device according to the second modification viewed from above.
  • the first cyclone 41 ⁇ / b> A and the second cyclone 41 ⁇ / b> B of the magnetic cyclone device 4 ⁇ / b> S of Modification 2 are arranged symmetrically with the electromagnet 45 interposed therebetween.
  • the first and second cyclones 41A and 41B are made of a nonmagnetic material such as plastic or aluminum.
  • the electromagnet 45 is disposed at a position orthogonal to each inflow direction (arrows ⁇ 41 and ⁇ 42 in FIG. 7) of the first inlet 41a1 and the second inlet 41a2 of the first cyclone 41A and the second cyclone 41B.
  • the magnetic force is perpendicular to the fluid flow, and attracts the magnetic particles and magnetic flocs toward the channels on the outermost surfaces of the first inlet portion 41a1 and the second inlet portion 41a2.
  • the electromagnet 45 may be a permanent magnet because there is a low possibility that the magnetic particles and the magnetic floc in the flow path are fixed to the first side wall surface 41b2 and the second side wall surface 41b4 by magnetic force. Since other configurations are the same as those of the second embodiment, detailed description thereof is omitted.
  • the electromagnet 45 is disposed between the first cylindrical base part 41b1 of the first cyclone 41A and the second cylindrical base part 41b3 of the second cyclone 41B.
  • the first cylindrical base is substantially perpendicular to the direction in which one of the N and S poles of the electromagnet 45 intersects the inflow direction from the first inlet 41a1 of the first cyclone 41A. It arrange
  • the second cylindrical base is substantially perpendicular to the direction in which the other magnetic pole 45b of the N pole and S pole of the electromagnet 45 intersects with the inflow direction from the second inlet portion 41a2 of the second cyclone 41B. It arrange
  • the fluid containing the magnetic floc of the liquid to be processed flows into the first cylindrical base 41b1 from the first inlet 41a1 (arrow ⁇ 41 in FIG. 7).
  • Either one of the N pole and the S pole of the electromagnet 45 is arranged in a substantially vertical direction intersecting the inflow direction of the fluid containing the magnetic floc of the liquid to be processed from the first inlet portion 41a1, and is in the fluid.
  • the magnetic floc is attracted toward the first side wall surface 41b2 of the first cylindrical base portion 41b1.
  • the magnetic floc in the fluid adheres to the first side wall surface 41b2 or exists in the vicinity of the first side wall surface 41b2.
  • the magnetic flock slides down on the conical side wall of the first inverted conical portion (not shown) due to gravity and is discharged downward from the first downstream outlet 44a.
  • the fluid from which the magnetic particles and magnetic floc have been removed is taken from the first upstream outlet 43a.
  • the fluid containing the magnetic floc of the liquid to be processed flows into the second cylindrical base 41b3 from the second inlet 41a2 (arrow ⁇ 42 in FIG. 7).
  • the other magnetic pole 45b of the N pole and the S pole of the electromagnet 45 is disposed in a direction substantially perpendicular to the inflow direction of the fluid containing the magnetic floc of the liquid to be processed from the second inlet portion 41a2, and the fluid The inside magnetic floc is attracted toward the second side wall surface 41b4 of the second cylindrical base portion 41b3.
  • the magnetic floc in the fluid adheres to the second side wall surface 41b4 or exists in the vicinity of the second side wall surface 41b4.
  • the magnetic flock slides down the conical side wall of the second reverse conical portion (not shown) due to gravity and is discharged downward from the second downstream outlet 44b.
  • the fluid from which the magnetic particles and magnetic floc have been removed is taken from the second upstream outlet 43b.
  • Polar poles 45a and 45b are arranged. Therefore, the magnetic particles and the magnetic floc in the fluid are effectively attracted by the magnetic force to the first side wall surface 41b2 of the first cylindrical base part 41b1 and the second side wall surface 41b4 of the second cylindrical base part 41b3, respectively. Therefore, magnetic particles and magnetic flocs in the fluid can be effectively separated from the fluid.
  • the magnetic poles 45a and 45b of the electromagnet 45 are substantially perpendicular to the inflow direction from the first inlet portion 41a1 of the first cyclone 41A and the inflow direction from the second inlet portion 41a2 of the second cyclone 41B. However, as long as they are arranged so as to cross each other, they are not necessarily vertical.
  • the electromagnets 5, 25, 35, and 45 are described as examples. However, permanent magnets may be used instead of the electromagnets 5, 25, 35, and 45. .
  • Embodiments 1 and 2 and Modifications 1 and 2 may be combined as appropriate.
  • the first and second embodiments and the first and second modified examples 1 and 2 show examples of the present invention, and the present invention can have various specific forms and modified forms within the scope of the claims.
  • high-performance separation is possible by agglomerating the magnetic particles and magnetic powder with the petroleum and algae to form and separate flocs.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Cyclones (AREA)

Abstract

La présente invention concerne un dispositif à cyclone magnétique (1S) comprenant : un cyclone (1) qui est un cône tronqué dont le sommet est tourné vers le bas et qui a une base cylindrique (1b) ayant une entrée (2) sur un côté et une section conique (1c) formée en continuité avec le fond de la base cylindrique (1b) et pourvue d'une sortie inférieure (4) à proximité du sommet ; une section cylindrique (1e) qui est disposée au centre de la base cylindrique (1b) et qui est pourvue d'une sortie supérieure (3) ; et un aimant (5) qui est disposé à proximité de la circonférence externe de la base cylindrique (1b). Un floculat magnétique contenu dans un liquide à traiter (7) s'écoulant dans la base cylindrique (1b) à partir de l'entrée (2) est évacué de la sortie inférieure (4) après avoir été attiré par l'aimant (5) à proximité d'une face interne (1b1) de la base cylindrique (1b), et le liquide à traiter à partir duquel le floculat magnétique a été retiré s'écoule hors de la sortie supérieure (3) de la section cylindrique (1e).
PCT/JP2016/087113 2016-03-28 2016-12-13 Dispositif à cyclone magnétique et son procédé de traitement WO2017168861A1 (fr)

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CN110577316B (zh) * 2019-10-17 2024-08-02 辽阳博仕流体设备有限公司 黑臭水体处理用磁粉投加及混凝的超磁分离系统
JP7569606B2 (ja) 2020-06-12 2024-10-18 リファインホールディングス株式会社 炭素材料分散体の製造方法および炭素材料分散体並びにこれに用いる装置
JP6948742B1 (ja) 2021-05-13 2021-10-13 株式会社Ambitious Technologies 凝集サイクロン装置、それを用いた海洋プラスチック除去システム及びそのシステムを搭載した船舶並びにその船舶の運航方法

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JPS3419994Y1 (fr) * 1957-10-19 1959-12-05
US4343707A (en) * 1980-03-10 1982-08-10 Electric Power Research Institute, Inc. Method and apparatus for separating out solids suspended in flowing, pure water systems
JPH1147632A (ja) * 1997-07-30 1999-02-23 Toshiba Corp 懸濁液磁気分離装置
US20010013491A1 (en) * 2000-02-12 2001-08-16 Egon Kaske Magnetic separator
JP2005021835A (ja) * 2003-07-04 2005-01-27 Takahashi:Kk 磁性粒体回収装置
JP2009056426A (ja) * 2007-09-03 2009-03-19 Toshiba Corp 固液分離装置
JP2011083696A (ja) * 2009-10-15 2011-04-28 Toshiba Corp 固液分離装置

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS3419994Y1 (fr) * 1957-10-19 1959-12-05
US4343707A (en) * 1980-03-10 1982-08-10 Electric Power Research Institute, Inc. Method and apparatus for separating out solids suspended in flowing, pure water systems
JPH1147632A (ja) * 1997-07-30 1999-02-23 Toshiba Corp 懸濁液磁気分離装置
US20010013491A1 (en) * 2000-02-12 2001-08-16 Egon Kaske Magnetic separator
JP2005021835A (ja) * 2003-07-04 2005-01-27 Takahashi:Kk 磁性粒体回収装置
JP2009056426A (ja) * 2007-09-03 2009-03-19 Toshiba Corp 固液分離装置
JP2011083696A (ja) * 2009-10-15 2011-04-28 Toshiba Corp 固液分離装置

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