WO2007122918A1 - Water treatment apparatus - Google Patents

Water treatment apparatus Download PDF

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Publication number
WO2007122918A1
WO2007122918A1 PCT/JP2007/055170 JP2007055170W WO2007122918A1 WO 2007122918 A1 WO2007122918 A1 WO 2007122918A1 JP 2007055170 W JP2007055170 W JP 2007055170W WO 2007122918 A1 WO2007122918 A1 WO 2007122918A1
Authority
WO
WIPO (PCT)
Prior art keywords
water
filter medium
water treatment
tubular
raw water
Prior art date
Application number
PCT/JP2007/055170
Other languages
French (fr)
Japanese (ja)
Inventor
Yuji Tanaka
Hiromitsu Kanamori
Original Assignee
Toray Industries, Inc.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Toray Industries, Inc. filed Critical Toray Industries, Inc.
Priority to JP2007513526A priority Critical patent/JPWO2007122918A1/en
Publication of WO2007122918A1 publication Critical patent/WO2007122918A1/en

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D29/00Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/11Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with bag, cage, hose, tube, sleeve or like filtering elements
    • B01D29/114Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with bag, cage, hose, tube, sleeve or like filtering elements arranged for inward flow filtration
    • B01D29/115Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with bag, cage, hose, tube, sleeve or like filtering elements arranged for inward flow filtration open-ended, the arrival of the mixture to be filtered and the discharge of the concentrated mixture are situated on both opposite sides of the filtering element
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D29/00Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/11Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with bag, cage, hose, tube, sleeve or like filtering elements
    • B01D29/13Supported filter elements
    • B01D29/15Supported filter elements arranged for inward flow filtration
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D29/00Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/50Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with multiple filtering elements, characterised by their mutual disposition
    • B01D29/52Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with multiple filtering elements, characterised by their mutual disposition in parallel connection
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2201/00Details relating to filtering apparatus
    • B01D2201/04Supports for the filtering elements
    • B01D2201/043Filter tubes connected to plates
    • B01D2201/0446Filter tubes connected to plates suspended from plates at the upper side of the filter elements

Definitions

  • the present invention is effective for stably removing and purifying suspended substances contained in water bodies such as lakes, moats, rivers, irrigation ponds, dam lakes, domestic wastewater, and factory wastewater for a long period of time. More specifically, the present invention relates to a small water treatment apparatus capable of filtering raw water with a high flux.
  • Patent Document 1 As a water treatment apparatus for removing suspended substances contained in water bodies such as lakes, moats, rivers, irrigation ponds, dam lakes, domestic effluents, factory effluents, etc., as shown in Patent Document 1, for example, Type water treatment equipment.
  • This device removes suspended solids with a filter cloth wound around the drum surface that allows water to pass through, and takes out the treated water from the intake pipe force disposed on the rotating shaft of the drum.
  • Patent Document 2 discloses a water treatment apparatus in which a filter cloth is attached around the drum and a solid-liquid separation apparatus in which the filter cloth is attached on a moving belt. This solid-liquid separator also has problems such as high equipment costs and large installation area due to its large size.
  • the filtration device described in Patent Document 4 has a configuration in which a plurality of bag-shaped filter medium elements are installed in a container for filtration.
  • the filtration device can be obtained in a short time. Suspended material accumulates on the surface of the filter element element, causing clogging, and filtering cannot be continued for a long time. There is a problem. Even if this filter element is washed by shower spraying or the like, it is difficult to continue stable filtration at a low differential pressure for a long period of time when the accumulated dirt is difficult to remove.
  • Patent Document 1 Japanese Patent Laid-Open No. 51-119168
  • Patent Document 2 International Publication No. 97Z45188 Pamphlet
  • Patent Document 3 Japanese Patent Laid-Open No. 61-222509
  • Patent Document 4 JP-A-5-245312
  • the present invention provides a water treatment device that is small in size and requires a small installation area, can increase the amount of treated water per unit area and unit time of a filter medium, and can operate stably for a long period of time. For the purpose.
  • the present invention has the following configuration.
  • a sealed container having a raw water supply port and a treated water outlet, and an opening for partitioning the inside of the container into a raw water chamber having a raw water supply port and a treated water chamber having a treated water outlet
  • a water treatment apparatus comprising: a partition plate having one end; a tubular filter medium having one end opened and the other end closed; and a tubular body having a surface force capable of passing water inserted into the tubular filter medium, An opening end of the cylindrical filter medium is disposed so as to be in a liquid-tight state with the opening of the partition plate, the cylindrical filter medium is composed of a napped knitted fabric having napped fibers, and has napped fibers.
  • a water treatment device characterized in that the surface is located on the raw water side.
  • the compressed fluid supply means provided with a flow path for supplying the compressed gas to the treated water chamber, or the flow path I for supplying the compressed gas to the treated water chamber and the compressed gas to the raw water chamber.
  • a ratio (AZB) of a cross-sectional area (A) of a cross-section of the tubular filter medium to a cross-sectional area (B) of a cross-section of the tubular body is 1.1 or more (1 ) Water treatment apparatus.
  • a water treatment method comprising: supplying treated water from an upstream water treatment device to a downstream water treatment device and sequentially passing the water.
  • a small-sized water treatment device which can stably remove suspended substances of a number; zm to several tens; Furthermore, the unit of filter media Since the amount of treated water per area and unit time can be increased, a large amount of water can be treated at a high flow rate by a small device.
  • FIG. 1 is a schematic longitudinal sectional view showing an embodiment of a water treatment apparatus according to the present invention.
  • FIG. 2 is a schematic longitudinal sectional view showing another embodiment of the water treatment apparatus according to the present invention.
  • FIG. 3 is a schematic longitudinal sectional view showing still another embodiment of the water treatment apparatus according to the present invention.
  • FIG. 4 is a schematic longitudinal sectional view showing still another embodiment of the water treatment apparatus according to the present invention.
  • FIG. 5 is an arrangement flow diagram illustrating a mode in which cleaning fluid supply means is arranged in the water treatment apparatus according to the present invention.
  • FIG. 1 and 2 are schematic longitudinal sectional views showing examples of the water treatment device according to the present invention.
  • the inside of the sealed container is divided into two upper and lower chambers by the partition plate 6, the upper chamber is the treated water chamber 19, and the lower chamber is the raw water chamber 20.
  • the container portion (container body 2) of the raw water chamber 20 is provided with a raw water supply port 8, and the container portion (lid portion 3) of the treated water chamber 19 is provided with a treated water outlet 9.
  • the partition plate 6 has a plurality of openings, and each of the openings 14 is provided with an opening end of the tubular filter medium 4 so as to be in a liquid-tight state.
  • the raw water supply port 8 and the treated water outlet 9 are respectively provided on the lower surface of the container body 2 and the upper surface of the lid part 3, but depending on the convenience of piping, etc. Even if it is provided on the side of the container body 2 and the side of the lid 3,
  • the tubular filter medium 4 has a tubular shape with one end opened and the other end closed, and is composed of a napped knitted fabric having napped fibers.
  • a tubular body 5 is inserted into the tubular filter medium 4. That is, the plurality of water-permeable cylindrical bodies 5 whose outer surfaces are covered with the filter medium by being covered with the cylindrical filter medium 4 are the opening end sides of the partition plate 6 having a plurality of openings. It is suspended from the opening 14 via the sealing material 12.
  • the opening end of the cylindrical filter medium 4 is fixed to the upper end of the cylindrical body 5 by, for example, an adhesive or a binding band (not shown), the opening of the partition plate 6 and the cylindrical The open ends of the filter media 4 are connected in a liquid-tight state.
  • the upper end portion of the cylindrical body 5 has a hook shape, and the hook portion 11 is hooked on the outer peripheral upper surface of the opening portion of the partition plate 6.
  • the flange portion 11 is fixed by overlapping a holding plate 7 having substantially the same shape as the partition plate 6 on the flange portion 11.
  • a cutting plate 6 and a holding plate 7 are sandwiched between the bolt (not shown) and the like.
  • the container body 2 and the lid part 3 are coupled and fixed using a fastening material, between the lid part 3 and the holding plate 7, between the holding plate 7 and the partition plate 6, and further to the partition plate 6 and
  • a sealing material 13 is disposed between the container body 2 and sealed.
  • the tubular filter medium 4 used in the present invention is constituted by a napped knitted fabric having napped fibers.
  • the tubular filter medium 4 is arranged so that the surface having napped fibers made of ultrafine fibers is located on the raw water side, and the napped portion exhibits the function of capturing suspended substances during filtration and immediately It functions as a filtration layer.
  • the raised knitted fabric having such a filtration function include a knitted fabric having a bundle of ultrafine fibers raised on one surface.
  • a fabric made of ultrafine fibers is used for the weft and the surface is extremely fine.
  • such a napped knitted fabric in which napped fabrics in which fibers are napped is used has, for example, one end or a part of an ultrafine fiber bundle as a root portion integrally fixed to the base layer as a base layer having a fabric strength.
  • the filter medium of the cloth that is present.
  • the method for fixing the microfiber bundle and the base layer integrally include adhesive bonding, heat fusion, ultrasonic bonding, entanglement of the base layer yarn and fiber bundle, and combinations thereof. It is not limited to.
  • an ultrafine fiber made of a polymer material having a fiber forming function may be used as the ultrafine fiber exhibiting a filtration function in this napped knitted fabric.
  • This high molecular weight material includes nylon 6, nylon 66, nylon 12, polyamide such as copolymer nylon, aromatic polyamide, polyethylene terephthalate, polyester such as copolymer polybutylene terephthalate, wholly aromatic polyester, polyethylene, polypropylene, etc.
  • Polyolefins Polyurethanes, polyacrylonitriles, polychlorinated burs, polybulal alcohols, bully polymers, polysulbivinylidene, polyhydrosulfite, polyfluorinated styrene, copolymerized polyfluorinated ethylene, polyoxymethylene, and the like.
  • combinations of fiber types such as core-sheath structures, multi-core-sheath structures, sea-island structures, bimetal structures, etc., in which a plurality of these polymer substances are combined may be used depending on the purpose.
  • the thickness (diameter) of the ultrafine fibers forming the napped fibers is preferably 10 m or less, which is relatively thin, but 0.1 to: LO / zm is more desirable to improve the capture performance of fine particles. In order to improve the capturing performance of the fine particles while maintaining high durability of the preferred fiber, 1.0 to 10; ⁇ ⁇ is further preferable.
  • the length of the raised fibers of the ultrafine fibers forming the raised fibers is preferably 2 to: LOmm. This is because if the nap of the ultrafine fibers is too short, the capture performance of the fine particles deteriorates. If it is too long, the ultrafine fibers are entangled with each other, and the capture performance of the fine particles and the separation performance after capture are reduced. is there.
  • the tubular body 5 is inserted into the tubular filter medium 4 so that the tubular filter medium 4 made of napped knitted fabric can maintain a predetermined shape of the tubular shape even when water pressure is applied during filtration. It is It is composed of a surface force that allows water to pass, such as a crushed or perforated plate. This water-permeable surface may be made of a material or shape that is not substantially deformed by the water pressure during filtration.
  • resin for example, polyolefin such as polyethylene, polypropylene, polybutene, or polytetrafluoroethylene.
  • PTFE tetrafluoroethylene 'perfluoroalkyl vinyl ether copolymer
  • PFA tetrafluoroethylene' hexafluoropropylene copolymer
  • FE P tetrafluoroethylene 'ethylene Fluorine resin
  • copolymer ETFE
  • PCTFE polychlorotrifluoroethylene
  • ECTFE black trifluoroethylene 'ethylene copolymer
  • PVDF polyvinylidene fluoride
  • Chlorinated resins such as bulls and polyvinyl chlorides, polysulfone resins, polyethersulfone resins, polyarylsulfone resins, and polyethers Resin, acrylonitrile-butadiene-styrene copolymer resin (ABS), acrylonitrile-styrene copolymer resin, polyphenylene sulfide resin, polyamide resin, polycarbonate resin, polyether ketone
  • the container body 2, the lid 3, the partition plate 6, the holding plate 7, and the cylindrical body 5 may all be made of the same material, or a combination of members having different material forces may be used. .
  • an O-ring or a sheet-like gasket is used as the sealing material 12 between the cylindrical body and the partition plate and the sealing material 13 between the container body, the partition plate, the holding plate, and the lid portion.
  • the cross-sectional shape may be a circle, an ellipse, a rectangle, a triangle, or the like.
  • the materials are ethylene propylene rubber, -tolyl rubber, acrylic rubber, silicone rubber, fluorosilicone rubber, fluorine rubber, urethane rubber, chloroprene rubber, 4-fluoroethylene rubber, polyamide resin, polyethylene terephthalate resin, stainless steel, aluminum, etc. Can be mentioned
  • raw water supplied from the raw water supply port 8 is a plurality of cylindrical bodies 5
  • the outside force of the tubular filter medium 4 attached to the inside also flows inward.
  • suspended substances in the raw water are captured by the raised portions on the surface of the tubular filter medium 4, and only the treated water flows into the tubular filter medium 4 and the tubular body 5.
  • the treated water that has flowed in flows upward through the inner part of the tubular filter medium 4, is collected inside the lid 3, and is taken out from the treated water outlet 9.
  • the outlet 10 since the outlet 10 is closed, the whole amount of raw water supplied from the raw water supply port 8 is filtered.
  • the cylindrical body 5 has a flow path inside the cylindrical filter medium 4 closed by water pressure or the like.
  • the cylindrical body 5 In order to prevent water from flowing into the inside of the tubular filter medium 4, it is formed with a surface that allows water to pass therethrough. Therefore, the cylindrical body 5 has a cylindrical peripheral surface formed from a porous material surface having openings, the bottom surface side is closed, and the upper surface side is open. If the above function is achieved, the higher the water flow performance, the smaller the pressure loss of the water treatment device 1 during raw water treatment. Preferably there is.
  • the compressed gas used in scrubbing for back pressure cleaning is a pressurized and compressed gas, and the type of the gas is not particularly limited, but air, nitrogen, or the like may be used.
  • the supply of compressed gas it is easy and preferable to send compressed air using a blower or a compressor.
  • the air piping from the blower 21 is branched halfway to form the air piping 22 of the flow channel I and the air piping 23 of the flow channel II, and the ends of the air pipings 22 and 23 are near the treated water outlet 9 To the treated water pipe 24 and the raw water pipe 25 near the raw water supply port 8 respectively.
  • the on-off valves 26 and 27 installed in the middle of the air pipes 22 and 23, they are directed toward the treatment water chamber 19 and the Z or raw water chamber 20, respectively. Compressed air can be supplied.
  • a flow meter and a pressure gauge may be installed, and the amount of compressed air supplied may be adjusted by adjusting the opening of the on-off valves 26 and 27.
  • the open / close valve of the treated water pipe 24 and the open / close valve of the raw water pipe 25 are in a closed state.
  • the blower 21 is used to send the compressed air as described above, and at the same time, for example, the pump 28 is used to form a tank (see FIG.
  • the treated water stored in may flow toward the treated water outlet 9.
  • the treated water and the compressed air merge in the treated water pipe 24 near the treated water outlet 9, and are sent into the treated water chamber 19 as a compressed gas mixed fluid.
  • the compressed gas is dispersed in the treated water and is uniformly sent by each cylindrical filter medium.
  • the same operation may be performed when the compressed gas mixed fluid is supplied into the raw water chamber 20. That is, the compressed air is sent using the blower 21, and at the same time, the raw water is flowed to the raw water supply port 8 by using the pump 29. Then, the raw water and the compressed air merge in the raw water pipe 25 near the raw water supply port 8 and are sent into the raw water chamber 20 as a compressed gas mixed fluid.
  • the compressed gas or the treated water mixed with the compressed gas flows from the inside of the tubular filter medium 4 to the outside, so that it adheres to the outer surface of the tubular filter medium 4 and is suspended.
  • the turbid material peels off the outer surface force of the filter medium or is easily peeled off.
  • the suspended substances float in water and are discharged together with water from the raw water supply port 8 in the drainage process.
  • back pressure cleaning and scrubbing can be performed simultaneously.
  • the treated water mixed with compressed gas is sent to the tubular filter medium 4 for back pressure cleaning, it adheres to the outer surface of the tubular filter medium 4, and the suspended substances are removed from the outer surface of the filter medium. Since it has the effect of floating in water at the same time as peeling, scrubbing is not necessarily required.
  • the pressure of the compressed gas supplied in the back pressure cleaning is determined according to the filter medium to be used.
  • the compressed gas in order for the compressed gas to penetrate through the internal force of the tubular filter medium 4 as well, the compressed gas must be supplied at a pressure higher than the bubble point of the filter cloth (puffed knitted fabric) used for the tubular filter medium. I must.
  • the flow rate of the treated water to be supplied per unit time is preferably about 1.5 to 3 times the flow rate of the treated water during filtration. If it is almost the same as the flow rate during filtration, On the contrary, the cleaning effect increases as the flow rate increases, but the amount of treated water finally obtained is reduced by the amount used for cleaning.
  • the amount of compressed gas supplied during scrubbing is (Q), and the cross-sectional area of the container body 2 (the inner wall cross-sectional area in the cross section perpendicular to the longitudinal direction of the tubular filter medium 2) is (S)
  • Q the amount of compressed gas supplied during scrubbing
  • S the cross-sectional area of the container body 2
  • (QZS) 0. 1LZ min ZCM 2 or more.
  • a gas outlet of the scrubbing pipe 15 is installed below each of the tubular filter media 4 as shown in FIG. 3, or as shown in FIG. It is also preferable to install a diffuser plate 17 having a diffuser port 16 below each tubular filter medium 4 below the tubular filter medium.
  • the compressed gas is intensively supplied in the vicinity of the cylindrical filter medium 4 in the container main body 2, so that effective cleaning, reduction of the flow rate of the compressed gas, and the like are possible.
  • the cylindrical filter medium 4 is constituted by a napped knitted fabric having naps of ultrafine fibers, so that suspended substances are trapped in the napped portions in the filtration step, and back pressure washing or scrubbing is performed. This is because the suspended matter trapped in the napping is easily peeled off by shaking the napping. Since the trapped suspended matter is peeled off and then discharged to the raw water side, the tubular filter medium 4 is arranged so that the surface having the napped fibers is located on the raw water side.
  • the ratio (AZB) is 1.1 or more.
  • the tubular filter medium 4 has a larger cross-sectional area than the cross-sectional area of the cylindrical body 5 and the suspended filter substance 4 is swayed or adhering to the outer surface immediately after scrubbing. This is because it is easy to peel off.
  • the upper limit of the ratio of AZB is practically about 2.
  • the raw water is continuously treated for a long time while repeating the above steps.
  • a plurality of tubular filter media 4 and tubular bodies 5 are arranged in the raw water chamber 20 of the water treatment apparatus. Compared to the cost of the cylindrical filter medium 4 and the cylindrical body 5, Because the cost is higher, it is possible to reduce the equipment cost by arranging as many cylindrical filter media 4 and cylindrical bodies 5 as possible in one container body 2 and increasing the filtration area. . At that time, it takes time to detach and attach the plurality of tubular filter media 4 and the tubular body 5 one by one in the container body 2 at the place where the water treatment device 1 is installed. It is preferable in terms of work efficiency that a plurality of cylindrical filter media 4 and a cylindrical body 5 are attached to the partition plate 6 so that the partition plate 6 and the plurality of cylindrical filter media 4 and the cylindrical body 5 can be attached and detached.
  • the water treatment apparatus of the present invention can be installed in a horizontal direction so that water flows in the horizontal direction in the apparatus.
  • the tubular filter medium 4 and the tubular body 5 may be installed in the container body 2 so that the longitudinal directions thereof are horizontal. In this way, when the longitudinal direction of the cylindrical filter medium 4 and the cylindrical body 5 is installed horizontally in the container body 2, the lid 3 is opened and the cylindrical filter medium 4 and the cylindrical body are installed. When exchanging the body 5 etc., there is an advantage that it can work from the side.
  • the tubular filter medium 4 and the tubular body 5 When detaching 5 to / from the container body 2, at least the space above the container body 2 is required for the height of the tubular filter medium 4 and the tubular body 5, so if installed in a building with a low ceiling, etc. There is a problem that it is difficult to remove the cylindrical filter medium 4 and the cylindrical body 5 in the installed state, and the lengths of the cylindrical filter medium 4 and the cylindrical body 5 are limited.
  • the water treatment can be performed by connecting a plurality of water treatment devices in a force when water treatment is performed by one water treatment device. For example, when performing filtration with higher filtration accuracy or stable operation over a longer period of time, multiple water treatment devices are placed in series, and the treated water outlet and the downstream water treatment device are connected in series. It is preferable to perform water treatment by connecting the raw water supply port of the water treatment device and sequentially passing water from the upstream water treatment device to the downstream water treatment device.
  • a plurality of water treatment devices each containing filter media with different filtration accuracy, are arranged in series, and they are directed from the upstream side to the downstream side so as to increase the filtration accuracy of the filter media and to make the water Even more preferred to do the processing.
  • the suspended matter in the raw water is trapped in stages depending on its size, so clogging of the filter medium can be reduced.
  • a water treatment device with the structure shown in Fig. 1 is used except that the number of cylinders and tubular filter media is two, and the water treatment device is placed vertically using a total filtration system that does not discharge raw water from the outlet. Installed at and treated raw water.
  • a napped woven fabric having a filtration accuracy of 18 m and having napped polyester fibers (length: 2 to 4 mm) having a thickness of about 7 ⁇ m was used as the filter medium constituting the cylindrical filter medium.
  • the napped fabric was sewn into a tubular shape having a diameter of about 30 mm and a length of about 500 mm, with one end open and the other closed.
  • This cylindrical filter medium was attached so as to cover the outer periphery of a cylindrical body having a diameter of about 25 mm, a length of about 500 mm, and a porosity of about 60%, which is also made of a resinous porous sheet.
  • the ratio of (AZB) when the cross-sectional area of the tubular filter medium is A and the cross-sectional area of the tubular body is B is 1.44.
  • a resin molded product made of polysalt cellulose was used for the container body, the lid, the partition plate, and the tubular body.
  • a water treatment apparatus having a structure in which two cylindrical filter media and a cylindrical body are housed in a sealed container. The cross-sectional area in the container body was 25 cm 2 .
  • Lake Biwa water with a turbidity of 3 to 5 degrees was used as raw water, and the raw water was supplied into the container for 10 minutes from the supply port with a pump at a flow rate of about 30 LZ, followed by filtration by the total filtration method.
  • about 6 OLZ of treated water and 50 LZ of compressed air are mixed and supplied from the treated water outlet 9 into the treated water chamber 19 for back pressure washing for 1 minute!
  • 15 LZ of air is fed into the raw water. Scrubbing was also performed by supplying the raw water chamber 20 from the supply port 8. Thereafter, all the raw water in the container was drained.
  • the water treatment apparatus of the present invention can perform stable water treatment at a high flow rate for a long time even with a small apparatus, the application requires a large amount of water treatment in a short time, for example, a lake, It can be used for removing suspended substances in outdoor water systems such as moats and rivers.

Abstract

A water treatment apparatus that is of compact size to thereby reduce the setting area therefor, increasing the amount of water treated per area of filter medium and per time, and that enables stable operation for a prolonged period of time. There is provided a water treatment apparatus including a hermetically closed vessel with a raw water supply port and a treated water outlet; divider plate (6) with aperture (14) for dividing of the interior of the vessel into raw water chamber (20) with raw water supply port (8) and treated water chamber (19) with treated water outlet (9); tubular filter medium (4) being open at its one end and closed at the other end; and tubular body (5) consisting of a water permeable plane, inserted within the tubular filter medium. The open end of the tubular filter medium (4) is arranged so as to become liquid-tight with the aperture (14) of the divider plate. The tubular filter medium (4) consists of a napped knitted or woven fabric with superfine fiber nap, and the napped surface is positioned on the side of raw water.

Description

明 細 書  Specification
水処理装置  Water treatment equipment
技術分野  Technical field
[0001] 本発明は、湖沼、堀、河川、用水池、ダム湖などの水域や生活排水、工場排水など に含まれる懸濁物質を長期間、安定して除去し、浄化するために有効な水処理装置 に関し、さらに詳しくは、原水を高流束でろ過することができる小型の水処理装置に 関する。  [0001] The present invention is effective for stably removing and purifying suspended substances contained in water bodies such as lakes, moats, rivers, irrigation ponds, dam lakes, domestic wastewater, and factory wastewater for a long period of time. More specifically, the present invention relates to a small water treatment apparatus capable of filtering raw water with a high flux.
背景技術  Background art
[0002] 湖沼、堀、河川、用水池、ダム湖などの水域や生活排水、工場排水などに含まれる 懸濁物質を除去するための水処理装置として、例えば特許文献 1に示すように、ドラ ム型の水処理装置がある。この装置は、通水可能なドラム胴面に巻き付けたろ過布 によって懸濁物質を除去し、ドラムの回転軸部に配設した取水管力 処理水を取出 すものであるが、装置が大型であるのため、設備費が高額になったり、装置の設置面 積が大きくなるなどの問題がある。また、ドラムの周囲にろ過布を取り付けた水処理装 置や、移動するベルト上にろ過布を取り付けた固液分離装置が、特許文献 2に記載 されている。この固液分離装置も、装置が大型であるため、設備費が高額、設置面積 が大きいなどの問題がある。  [0002] As a water treatment apparatus for removing suspended substances contained in water bodies such as lakes, moats, rivers, irrigation ponds, dam lakes, domestic effluents, factory effluents, etc., as shown in Patent Document 1, for example, Type water treatment equipment. This device removes suspended solids with a filter cloth wound around the drum surface that allows water to pass through, and takes out the treated water from the intake pipe force disposed on the rotating shaft of the drum. As a result, there are problems such as high equipment costs and large equipment installation area. Patent Document 2 discloses a water treatment apparatus in which a filter cloth is attached around the drum and a solid-liquid separation apparatus in which the filter cloth is attached on a moving belt. This solid-liquid separator also has problems such as high equipment costs and large installation area due to its large size.
[0003] 一方、ろ材の集積度を高め、装置の設置面積を小さくした水処理装置としては、例 えば、特許文献 3に示すような、多数本の中空糸膜を収納した中空糸膜モジュール の複数個を容器内に配設して原水を加圧ろ過するものが挙げられる。しかし、本装置 はろ材としてろ過表面の孔径が小さい中空糸膜を用いているため、例えば原水中の 1 μ m以下の微小な懸濁物質もろ過できる反面、ろ材の単位面積および単位時間当 たりの処理水量は高々数 m3Zm2Zday程度と小さぐ高流束で水処理できな!/ヽと 、 う問題がある。 [0003] On the other hand, as a water treatment device in which the degree of accumulation of filter media is increased and the installation area of the device is reduced, for example, as shown in Patent Document 3, a hollow fiber membrane module containing a large number of hollow fiber membranes is used. The thing which arrange | positions several in a container and pressurizes and filters raw | natural water is mentioned. However, since this device uses a hollow fiber membrane with a small pore size on the filtration surface as a filter medium, for example, even fine suspended substances of 1 μm or less in raw water can be filtered, but on the unit area and unit time of the filter medium. There is a problem that the amount of water treated cannot be treated with a high flux of a few m 3 Zm 2 Zday at most!
[0004] さらに、特許文献 4に記載されたろ過装置は、袋状ろ材エレメントの複数を容器内 に設置してろ過する構成をとつて 、るが、原水を高流束でろ過すると短時間でろ材ェ レメントの表面に懸濁物質が堆積して目詰まりを生じろ過を長時間継続できないとい う問題がある。このろ材エレメントをシャワー吹きつけ等で洗浄しても付着堆積した汚 れが除去され難ぐ長期間、低差圧で安定したろ過を継続することは困難である。 [0004] Further, the filtration device described in Patent Document 4 has a configuration in which a plurality of bag-shaped filter medium elements are installed in a container for filtration. However, when raw water is filtered with a high flux, the filtration device can be obtained in a short time. Suspended material accumulates on the surface of the filter element element, causing clogging, and filtering cannot be continued for a long time. There is a problem. Even if this filter element is washed by shower spraying or the like, it is difficult to continue stable filtration at a low differential pressure for a long period of time when the accumulated dirt is difficult to remove.
[0005] これら従来の水処理装置として、原水を高流束でろ過することができる水処理装置 も提案されているが、装置が大型で設置面積が広く設備費が高くなる問題があったり 、また、ろ過布に付着堆積した汚れの除去が難しく長期間安定した水処理ができな い問題がある。そこで、装置が小型で設置面積が小さくてすみ、ろ材の単位面積およ び単位時間当たりの処理水量を多くでき、かつ、長期間、安定運転が可能な水処理 装置が望まれていた。  [0005] As these conventional water treatment devices, water treatment devices capable of filtering raw water with a high flux have been proposed, but there is a problem that the device is large and has a large installation area and high equipment costs. In addition, it is difficult to remove dirt deposited on the filter cloth, and stable water treatment cannot be performed for a long time. Therefore, there has been a demand for a water treatment device that is small in size and requires a small installation area, can increase the amount of treated water per unit area and unit time of the filter medium, and can stably operate for a long period of time.
特許文献 1:特開昭 51— 119168号公報  Patent Document 1: Japanese Patent Laid-Open No. 51-119168
特許文献 2:国際公開 97Z45188号パンフレット  Patent Document 2: International Publication No. 97Z45188 Pamphlet
特許文献 3:特開昭 61 - 222509号公報  Patent Document 3: Japanese Patent Laid-Open No. 61-222509
特許文献 4:特開平 5 - 245312号公報  Patent Document 4: JP-A-5-245312
発明の開示  Disclosure of the invention
発明が解決しょうとする課題  Problems to be solved by the invention
[0006] 本発明は、装置が小型で設置面積が小さくてすみ、ろ材の単位面積および単位時 間当たりの処理水量を多くでき、さらに、長期間、安定運転が可能な水処理装置を提 供することを目的とする。 [0006] The present invention provides a water treatment device that is small in size and requires a small installation area, can increase the amount of treated water per unit area and unit time of a filter medium, and can operate stably for a long period of time. For the purpose.
課題を解決するための手段  Means for solving the problem
[0007] 本発明は、前記目的を達成するために、次のような構成をとる。 In order to achieve the above object, the present invention has the following configuration.
(1) 原水供給口と処理水出口とを有する密閉した容器と、該容器の内部を原水供 給口のある原水室と処理水出口のある処理水室とに仕切るための、開孔部を有する 仕切板と、一端が開口し他端が閉塞した筒状ろ材と、該筒状ろ材の内部に挿入され た通水可能面力 なる筒状体とを具備する水処理装置であって、前記仕切板の開孔 部と液密状態になるように前記筒状ろ材の開口端部が配設され、筒状ろ材が極細繊 維の立毛を有する立毛編織物から構成され、かつ、立毛を有する面が原水側に位置 することを特徴とする水処理装置。  (1) A sealed container having a raw water supply port and a treated water outlet, and an opening for partitioning the inside of the container into a raw water chamber having a raw water supply port and a treated water chamber having a treated water outlet A water treatment apparatus comprising: a partition plate having one end; a tubular filter medium having one end opened and the other end closed; and a tubular body having a surface force capable of passing water inserted into the tubular filter medium, An opening end of the cylindrical filter medium is disposed so as to be in a liquid-tight state with the opening of the partition plate, the cylindrical filter medium is composed of a napped knitted fabric having napped fibers, and has napped fibers. A water treatment device characterized in that the surface is located on the raw water side.
(2) さらに、処理水室内及び Z又は原水室内に圧縮気体もしくは圧縮気体混合流 体を供給するための洗浄流体供給手段が配設されている上記(1)に記載の水処理 装置。 (2) The water treatment according to (1) above, further comprising cleaning fluid supply means for supplying a compressed gas or a compressed gas mixed fluid into the treated water chamber and Z or the raw water chamber. apparatus.
(3) 前記洗浄流体供給手段が、圧縮気体を処理水室内へ供給する流路を備えた 圧縮気体供給装置、又は、圧縮気体を処理水室内へ供給する流路 Iと圧縮気体を原 水室内へ供給する流路 IIとを備えた圧縮気体供給装置力 なる上記(2)に記載の水 処理装置。  (3) The compressed fluid supply means provided with a flow path for supplying the compressed gas to the treated water chamber, or the flow path I for supplying the compressed gas to the treated water chamber and the compressed gas to the raw water chamber. The water treatment apparatus according to (2) above, wherein the compressed gas supply apparatus is provided with a flow path II to be supplied to
(4) 筒状ろ材を構成する立毛編織物における立毛の単糸直径が 1. 0〜: LO /z mで ある上記(1)に記載の水処理装置。  (4) The water treatment apparatus according to (1) above, wherein the single yarn diameter of the napped yarn in the napped knitted fabric constituting the cylindrical filter medium is 1.0 to LO / z m.
(5) 筒状ろ材を構成する立毛編織物における立毛の長さが 2〜: LOmmである上記( 1)に記載の水処理装置。  (5) The water treatment apparatus according to (1), wherein the length of the napped knitted fabric constituting the tubular filter medium is 2 to: LOmm.
[0008] (6) 前記筒状ろ材の横断面の断面積 (A)と、前記筒状体の横断面の断面積 (B) との比 (AZB)が 1. 1以上である上記(1)に記載の水処理装置。  [0008] (6) A ratio (AZB) of a cross-sectional area (A) of a cross-section of the tubular filter medium to a cross-sectional area (B) of a cross-section of the tubular body is 1.1 or more (1 ) Water treatment apparatus.
(7) 前記筒状ろ材の内部に挿入された筒状体の片端が前記仕切板の開孔部に連 接され、かつ、筒状体の通水可能面全体が筒状ろ材で覆われている上記(1)に記載 の水処理装置。  (7) One end of the tubular body inserted into the tubular filter medium is connected to the opening of the partition plate, and the entire water-permeable surface of the tubular body is covered with the tubular filter medium. The water treatment device according to (1) above.
(8) 前記筒状ろ材及び筒状体が、原水室内に複数配置されている上記(1)に記載 の水処理装置。  (8) The water treatment device according to (1), wherein a plurality of the tubular filter media and the tubular body are arranged in the raw water chamber.
(9) 前記筒状ろ材及び筒状体の長手方向が水平になるように前記容器内に設置さ れている上記(1)に記載の水処理装置。  (9) The water treatment device according to (1), wherein the water treatment device is installed in the container so that the longitudinal direction of the tubular filter medium and the tubular body is horizontal.
(10) 上記(1)に記載の水処理装置の複数台が直列に配置されるように、上流側の 水処理装置の処理水出口と下流側の水処理装置の原水供給口とを連接し、上流側 の水処理装置による処理水を下流側の水処理装置へと供給し、順次水を通過させる ことを特徴とする水処理方法。  (10) Connect the treated water outlet of the upstream water treatment device and the raw water supply port of the downstream water treatment device so that a plurality of the water treatment devices described in (1) above are arranged in series. A water treatment method comprising: supplying treated water from an upstream water treatment device to a downstream water treatment device and sequentially passing the water.
(11) 上記 (8)に記載の水処理装置において筒状ろ材を交換する際、複数の筒状 ろ材及び筒状体が仕切板に取り付けられ一体化された状態で容器から脱着し交換 することを特徴とする筒状ろ材の交換方法。  (11) When replacing the tubular filter medium in the water treatment device described in (8) above, the tubular filter medium and the tubular body must be attached to the partition plate and attached to and integrated with the partition plate for replacement. A method for replacing a tubular filter medium characterized by the above.
発明の効果  The invention's effect
[0009] 本発明の水処理装置を用いれば、小型の水処理装置であって、原水中に含まれる 数; z m〜数十; z m程度の懸濁物質を長期間、安定して除去でき、さらにろ材の単位 面積および単位時間当たりの処理水量を多くすることができるので、小型装置により 多量な水を高流速で処理することが可能となる。 [0009] By using the water treatment device of the present invention, a small-sized water treatment device, which can stably remove suspended substances of a number; zm to several tens; Furthermore, the unit of filter media Since the amount of treated water per area and unit time can be increased, a large amount of water can be treated at a high flow rate by a small device.
図面の簡単な説明  Brief Description of Drawings
[0010] [図 1]本発明に係る水処理装置の一実施形態を示す概略縦断面図である。  FIG. 1 is a schematic longitudinal sectional view showing an embodiment of a water treatment apparatus according to the present invention.
[図 2]本発明に係る水処理装置の他の一実施形態を示す概略縦断面図である。  FIG. 2 is a schematic longitudinal sectional view showing another embodiment of the water treatment apparatus according to the present invention.
[図 3]本発明に係る水処理装置のさらに他の一実施形態を示す概略縦断面図である  FIG. 3 is a schematic longitudinal sectional view showing still another embodiment of the water treatment apparatus according to the present invention.
[図 4]本発明に係る水処理装置のさらに他の一実施形態を示す概略縦断面図である FIG. 4 is a schematic longitudinal sectional view showing still another embodiment of the water treatment apparatus according to the present invention.
[図 5]本発明に係る水処理装置にお!ヽて洗浄流体供給手段を配設した態様を例示 する配置フロー図である。 FIG. 5 is an arrangement flow diagram illustrating a mode in which cleaning fluid supply means is arranged in the water treatment apparatus according to the present invention.
符号の説明  Explanation of symbols
[0011] 1:水処理装置、 2:密閉容器の下側部分 (容器本体)、 3:密閉容器の上側部分  [0011] 1: Water treatment device, 2: Lower part of sealed container (container body), 3: Upper part of sealed container
(蓋部)、 4:筒状ろ材、 5:筒状体、 6:仕切板、 7:抑え板、 8:原水供給口、 9 :処理水出口、 10:流出口、 11:鍔部、 12、 13:シール材、 14:開孔部、 15: スクラビング用配管、 16:散気口、 17:散気板、 18:締結材、 19:処理水室、 20:原水室、 21:ブロア、 22:空気配管(流路 1)、 23:空気配管(流路 11)、 24: 処理水配管、 25:原水配管、 26、 27:開閉弁、 28、 29:ポンプ  (Cover), 4: Tubular filter medium, 5: Tubular body, 6: Partition plate, 7: Suppressing plate, 8: Raw water supply port, 9: Outlet for treated water, 10: Outlet, 11: Saddle, 12 , 13: Sealing material, 14: Opening part, 15: Scrubbing pipe, 16: Air diffuser, 17: Air diffuser plate, 18: Fastening material, 19: Treated water chamber, 20: Raw water chamber, 21: Blower, 22: Air piping (channel 1), 23: Air piping (channel 11), 24: Treated water piping, 25: Raw water piping, 26, 27: On-off valve, 28, 29: Pump
発明を実施するための最良の形態  BEST MODE FOR CARRYING OUT THE INVENTION
[0012] 本発明の最良の実施形態を、湖沼水や河川水などを高流速でろ過して工業用水 などを取得するために適した水処理装置を例にとって、図面を参照しながら以下に 説明する。 The best embodiment of the present invention will be described below with reference to the drawings, taking as an example a water treatment apparatus suitable for obtaining industrial water and the like by filtering lake water and river water at a high flow rate. To do.
[0013] 図 1及び図 2は本発明に係る水処理装置の一例をそれぞれ示す概略縦断面図で ある。図中に示すように、密閉された容器の内部は、仕切板 6によって上下 2室に仕 切られていて、上側の室は処理水室 19、下側の室は原水室 20である。原水室 20の 容器部分 (容器本体 2)には原水供給口 8が設けられ、処理水室 19の容器部分 (蓋 部 3)には処理水出口 9が設けられている。仕切板 6には複数の開孔部があり、この開 孔部 14にはそれぞれ、液密状態になるように筒状ろ材 4の開口端部が配設されてい る。ここで、図 1及び図 2においては、原水供給口 8及び処理水出口 9はそれぞれ、 容器本体 2の下面と蓋部 3の上面に設けられているが、配管の都合などによりそれぞ れ、容器本体 2の側面と蓋部 3の側面に設けても力まわな 、。 1 and 2 are schematic longitudinal sectional views showing examples of the water treatment device according to the present invention. As shown in the figure, the inside of the sealed container is divided into two upper and lower chambers by the partition plate 6, the upper chamber is the treated water chamber 19, and the lower chamber is the raw water chamber 20. The container portion (container body 2) of the raw water chamber 20 is provided with a raw water supply port 8, and the container portion (lid portion 3) of the treated water chamber 19 is provided with a treated water outlet 9. The partition plate 6 has a plurality of openings, and each of the openings 14 is provided with an opening end of the tubular filter medium 4 so as to be in a liquid-tight state. The Here, in FIG. 1 and FIG. 2, the raw water supply port 8 and the treated water outlet 9 are respectively provided on the lower surface of the container body 2 and the upper surface of the lid part 3, but depending on the convenience of piping, etc. Even if it is provided on the side of the container body 2 and the side of the lid 3,
[0014] 筒状ろ材 4は、一端が開口し他端が閉塞した筒状であり、極細繊維の立毛を有する 立毛編織物から構成されている。図示した装置では、この筒状ろ材 4の中に筒状体 5 を挿入した構造をとつている。即ち、筒状ろ材 4が被せられたことにより外表面がろ材 で覆われた複数本の通水可能な筒状体 5は、その開口端側が、複数の開孔を有す る仕切板 6の開孔部 14に、シール材 12を介して吊持されている。ここで、筒状ろ材 4 の開口端部は、例えば接着剤や結束バンドなど(図示しない)によって筒状体 5の上 端部に固定されているので、仕切板 6の開孔部と筒状ろ材 4の開口端部は液密状態 で連結されている。 [0014] The tubular filter medium 4 has a tubular shape with one end opened and the other end closed, and is composed of a napped knitted fabric having napped fibers. In the illustrated apparatus, a tubular body 5 is inserted into the tubular filter medium 4. That is, the plurality of water-permeable cylindrical bodies 5 whose outer surfaces are covered with the filter medium by being covered with the cylindrical filter medium 4 are the opening end sides of the partition plate 6 having a plurality of openings. It is suspended from the opening 14 via the sealing material 12. Here, since the opening end of the cylindrical filter medium 4 is fixed to the upper end of the cylindrical body 5 by, for example, an adhesive or a binding band (not shown), the opening of the partition plate 6 and the cylindrical The open ends of the filter media 4 are connected in a liquid-tight state.
[0015] また、筒状体 5の上端部は鍔状となっていて、この鍔部 11が仕切板 6の開孔部の外 周上面に掛止されている。図 1では、鍔部 11の上に、仕切板 6と略同形状の抑え板 7 が重ねられていることによって鍔部 11は固定されている。このように、筒状体 5の上端 の鍔部 11が固定されているので、筒状ろ材 4と筒状体 5とは、水処理途中においても 、容器本体 2内に落下せず、かつ、水圧などによって蓋部 3内に押し上げられず、仕 切板に固定されている。  Further, the upper end portion of the cylindrical body 5 has a hook shape, and the hook portion 11 is hooked on the outer peripheral upper surface of the opening portion of the partition plate 6. In FIG. 1, the flange portion 11 is fixed by overlapping a holding plate 7 having substantially the same shape as the partition plate 6 on the flange portion 11. Thus, since the flange 11 at the upper end of the cylindrical body 5 is fixed, the cylindrical filter medium 4 and the cylindrical body 5 do not fall into the container body 2 even during water treatment, and It is not pushed up into the lid 3 by water pressure, etc., but is fixed to the cutting plate.
[0016] さらに、容器本体 2と、処理水出口 9を有する蓋部 3との連結部分では、その間に仕 切板 6と抑え板 7とを挟持した状態でボルト(図示しな 、)などの締結材を用いて、容 器本体 2と蓋部 3とが結合固定されていて、蓋部 3と抑え板 7との間、抑え板 7と仕切 板 6との間、さらに、仕切板 6と容器本体 2との間にはいずれもシール材 13が配され てシールされている。  [0016] Furthermore, at the connecting portion between the container body 2 and the lid portion 3 having the treated water outlet 9, a cutting plate 6 and a holding plate 7 are sandwiched between the bolt (not shown) and the like. The container body 2 and the lid part 3 are coupled and fixed using a fastening material, between the lid part 3 and the holding plate 7, between the holding plate 7 and the partition plate 6, and further to the partition plate 6 and A sealing material 13 is disposed between the container body 2 and sealed.
[0017] ここで、筒状体 5が容器本体 2内に落下したり、蓋部 2内に押し上がったりしないよう にするためには、例えば図 2に示すように、筒状体 5に設けた鍔部 11の部分をボルト などの締結材 18を用いて仕切板 6に固定しても力まわない。  [0017] Here, in order to prevent the cylindrical body 5 from falling into the container main body 2 or from being pushed up into the lid portion 2, for example, as shown in FIG. Even if the flange 11 is fixed to the partition plate 6 by using a fastening material 18 such as a bolt, it does not work.
[0018] 本発明において用いる筒状ろ材 4は、極細繊維の立毛を有する立毛編織物でもつ て構成される。ここで、極細繊維よりなる立毛を有する面が原水側に位置するように 筒状ろ材 4が配置され、立毛部分はろ過時に懸濁物質を捕捉する機能を発揮し、即 ちろ過層としての機能を発揮する。このようなろ過機能をもつ立毛編織物としては、片 表面に極細繊維の繊維束が立毛した編織物が挙げられ、例えば、緯糸に極細繊維 を用 、た織物を起毛加ェし、表面に極細繊維の立毛を形成した立毛織物が用いら れるこのような立毛編織物としては、例えば、織物力 なるベース層に極細繊維束の 一端もしくは一部が根元部としてベース層に一体ィ匕固定されている布帛のろ材が挙 げられる。極細繊維束とベース層との一体ィ匕固定の方法としては、接着剤による接着 、熱融着、超音波接着、ベース層の糸と繊維束との交絡およびこれらの組み合わせ などが挙げられるがこれらに限定されるものではない。 [0018] The tubular filter medium 4 used in the present invention is constituted by a napped knitted fabric having napped fibers. Here, the tubular filter medium 4 is arranged so that the surface having napped fibers made of ultrafine fibers is located on the raw water side, and the napped portion exhibits the function of capturing suspended substances during filtration and immediately It functions as a filtration layer. Examples of the raised knitted fabric having such a filtration function include a knitted fabric having a bundle of ultrafine fibers raised on one surface. For example, a fabric made of ultrafine fibers is used for the weft and the surface is extremely fine. For example, such a napped knitted fabric in which napped fabrics in which fibers are napped is used has, for example, one end or a part of an ultrafine fiber bundle as a root portion integrally fixed to the base layer as a base layer having a fabric strength. The filter medium of the cloth that is present. Examples of the method for fixing the microfiber bundle and the base layer integrally include adhesive bonding, heat fusion, ultrasonic bonding, entanglement of the base layer yarn and fiber bundle, and combinations thereof. It is not limited to.
[0019] また、この立毛編織物にお!、てろ過機能を発揮する極細繊維としては、繊維形成 能を有する高分子物質からなる極細繊維を使用すればよい。この高分子物質として は、ナイロン 6、ナイロン 66、ナイロン 12、共重合ナイロンなどのポリアミド、芳香族ポリ アミド、ポリエチレンテレフタレート、共重合ポリブチレンテレフタレートなどのポリエス テル、全芳香族ポリエステル、ポリエチレン、ポリプロピレンなどのポリオレフイン、ポリ ウレタン、ポリアクリロニトリル、ポリ塩化ビュル、ポリビュルアルコール、ビュル重合体 、ポリ塩ィ匕ビユリデン、ポリハイドロサルファイト、ポリフッ化工チレン、共重合ポリフッ化 エチレン、ポリオキシメチレンなどが挙げられる。また、これらの高分子物質を複数組 み合わせた芯鞘構造、多重芯鞘構造、海島構造、バイメタル構造などの複合繊維で もよぐその繊維の種類の組み合わせは目的に応じて用いられる。  [0019] Moreover, as the ultrafine fiber exhibiting a filtration function in this napped knitted fabric, an ultrafine fiber made of a polymer material having a fiber forming function may be used. This high molecular weight material includes nylon 6, nylon 66, nylon 12, polyamide such as copolymer nylon, aromatic polyamide, polyethylene terephthalate, polyester such as copolymer polybutylene terephthalate, wholly aromatic polyester, polyethylene, polypropylene, etc. Polyolefins, polyurethanes, polyacrylonitriles, polychlorinated burs, polybulal alcohols, bully polymers, polysulbivinylidene, polyhydrosulfite, polyfluorinated styrene, copolymerized polyfluorinated ethylene, polyoxymethylene, and the like. In addition, combinations of fiber types such as core-sheath structures, multi-core-sheath structures, sea-island structures, bimetal structures, etc., in which a plurality of these polymer substances are combined may be used depending on the purpose.
[0020] 立毛を形成する極細繊維の太さ(直径)としては、比較的細い 10 m以下が好まし いが、微細粒子の捕捉性能を向上させるには 0. 1〜: LO /z mがより好ましぐ繊維の 耐久性を高く維持しつつ微粒子の捕捉性能を向上させるには、 1. 0〜10 ;ζ ΐηがさら に好ましい。  [0020] The thickness (diameter) of the ultrafine fibers forming the napped fibers is preferably 10 m or less, which is relatively thin, but 0.1 to: LO / zm is more desirable to improve the capture performance of fine particles. In order to improve the capturing performance of the fine particles while maintaining high durability of the preferred fiber, 1.0 to 10; ζ ΐη is further preferable.
[0021] また、立毛を形成する極細繊維の立毛長さは、 2〜: LOmmが好ましい。これは、極 細繊維の立毛が短すぎると微細粒子の捕捉性能が低下し、逆に長すぎると極細繊 維が互いに絡み合って、微細粒子の捕捉性能および捕捉後の剥離性能が低下する ためである。  [0021] The length of the raised fibers of the ultrafine fibers forming the raised fibers is preferably 2 to: LOmm. This is because if the nap of the ultrafine fibers is too short, the capture performance of the fine particles deteriorates.If it is too long, the ultrafine fibers are entangled with each other, and the capture performance of the fine particles and the separation performance after capture are reduced. is there.
[0022] 筒状体 5は、立毛編織物からなる筒状ろ材 4が、ろ過時に水圧をかけた時でも筒形 の所定形状を保持することができるように、筒状ろ材 4の中に挿入されるものであり、メ ッシュ状や多孔板状のような通水可能面力 構成される。この通水可能面は、ろ過時 の水圧で実質的に変形しない材質や形状で構成されればよい。さらに、容器本体 2、 蓋部 3、仕切板 6、抑え板 7および筒状体 5を構成する材質としては、榭脂の場合、例 えば、ポリエチレン、ポリプロピレン、ポリブテン等のポリオレフインや、ポリテトラフルォ 口エチレン(PTFE)、テトラフルォロエチレン 'パーフルォロアルキルビニルエーテル 共重合体(PFA)、テトラフルォロエチレン'へキサフルォロプロピレン共重合体(FE P)、テトラフルォロエチレン 'エチレン共重合体(ETFE)、ポリクロ口トリフルォロェチ レン(PCTFE)、クロ口トリフルォエチレン 'エチレン共重合体(ECTFE)、ポリビ-リ デンフルオライド (PVDF)等のフッ素系榭脂、そしてポリ塩ィ匕ビュル、ポリ塩化ビ-リ デン等の塩素系榭脂、さらにポリスルホン樹脂、ポリエーテルスルホン榭脂、ポリアリ ルスルホン榭脂、ポリフエ-ルエーテル榭脂、アクリロニトリル-ブタジエン-スチレン共 重合体榭脂 (ABS)、アクリロニトリル-スチレン共重合体榭脂、ポリフエ-レンサルファ イド榭脂、ポリアミド榭脂、ポリカーボネート榭脂、ポリエーテルケトン樹脂、ポリエーテ ルエーテルケトン樹脂の単独及びこれらの混合物が用いられる。また、榭脂以外では[0022] The tubular body 5 is inserted into the tubular filter medium 4 so that the tubular filter medium 4 made of napped knitted fabric can maintain a predetermined shape of the tubular shape even when water pressure is applied during filtration. It is It is composed of a surface force that allows water to pass, such as a crushed or perforated plate. This water-permeable surface may be made of a material or shape that is not substantially deformed by the water pressure during filtration. In addition, as a material constituting the container body 2, the lid 3, the partition plate 6, the holding plate 7, and the cylindrical body 5, in the case of resin, for example, polyolefin such as polyethylene, polypropylene, polybutene, or polytetrafluoroethylene. (PTFE), tetrafluoroethylene 'perfluoroalkyl vinyl ether copolymer (PFA), tetrafluoroethylene' hexafluoropropylene copolymer (FE P), tetrafluoroethylene 'ethylene Fluorine resin such as copolymer (ETFE), polychlorotrifluoroethylene (PCTFE), black trifluoroethylene 'ethylene copolymer (ECTFE), polyvinylidene fluoride (PVDF), and polychlorinated resin Chlorinated resins such as bulls and polyvinyl chlorides, polysulfone resins, polyethersulfone resins, polyarylsulfone resins, and polyethers Resin, acrylonitrile-butadiene-styrene copolymer resin (ABS), acrylonitrile-styrene copolymer resin, polyphenylene sulfide resin, polyamide resin, polycarbonate resin, polyether ketone resin, polyether ether ketone resin Single and mixtures thereof are used. In addition, other than rosin
、アルミニウム、ステンレス鋼などが用いられ、さらに、榭脂と金属の複合体や、ガラス 繊維強化榭脂、炭素繊維強化榭脂などの複合材料を使用してもカゝまわない。また、 容器本体 2、蓋部 3、仕切板 6、抑え板 7および筒状体 5はすべてが同一の材質で構 成されていてもよいし、また、異なる材質力もなる部材の組合せでもかまわない。 Aluminum, stainless steel, and the like are used, and composite materials such as a resin-metal composite, glass fiber reinforced resin, and carbon fiber reinforced resin can be used. The container body 2, the lid 3, the partition plate 6, the holding plate 7, and the cylindrical body 5 may all be made of the same material, or a combination of members having different material forces may be used. .
[0023] また、筒状体と仕切板との間のシール材 12や、容器本体、仕切板、抑え板、蓋部 の相互の間のシール材 13としては、 Oリングやシート状物のガスケットなどが使用で き、その断面形状は円形、楕円形、四角形、三角形などであればよい。その材質は、 エチレンプロピレンゴム、 -トリルゴム、アクリルゴム、シリコーンゴム、フルォロシリコー ンゴム、フッ素ゴム、ウレタンゴム、クロロプレンゴム、四フツイ匕エチレン榭旨、ポリアミド 榭脂、ポリエチレンテレフタレート榭脂や、ステンレス、アルミニウムなどが挙げられる [0023] Further, as the sealing material 12 between the cylindrical body and the partition plate and the sealing material 13 between the container body, the partition plate, the holding plate, and the lid portion, an O-ring or a sheet-like gasket is used. The cross-sectional shape may be a circle, an ellipse, a rectangle, a triangle, or the like. The materials are ethylene propylene rubber, -tolyl rubber, acrylic rubber, silicone rubber, fluorosilicone rubber, fluorine rubber, urethane rubber, chloroprene rubber, 4-fluoroethylene rubber, polyamide resin, polyethylene terephthalate resin, stainless steel, aluminum, etc. Can be mentioned
[0024] 次に、図 1に示す水処理装置により、原水を全ろ過方式で処理する方法について 述べながら、本発明の効果について説明する。 Next, the effect of the present invention will be described while describing a method for treating raw water by a total filtration method using the water treatment apparatus shown in FIG.
[0025] まず、ろ過工程において、原水供給口 8から供給された原水は、複数本の筒状体 5 に取り付けられた筒状ろ材 4の外側力も内側に向力つて流れ込む。この際、筒状ろ材 4の表面の起毛部分等で原水中の懸濁物質が捕捉されて、処理水のみが筒状ろ材 4及び筒状体 5の内側に流入する。流入した処理水は筒状ろ材 4の内側部分を通つ て上方へと流れ、蓋部 3の内側に集められ、処理水出口 9から外部に取り出される。 このとき、流出口 10は閉塞されているので、原水供給口 8から供給された原水は全量 ろ過される。 [0025] First, in the filtration step, raw water supplied from the raw water supply port 8 is a plurality of cylindrical bodies 5 The outside force of the tubular filter medium 4 attached to the inside also flows inward. At this time, suspended substances in the raw water are captured by the raised portions on the surface of the tubular filter medium 4, and only the treated water flows into the tubular filter medium 4 and the tubular body 5. The treated water that has flowed in flows upward through the inner part of the tubular filter medium 4, is collected inside the lid 3, and is taken out from the treated water outlet 9. At this time, since the outlet 10 is closed, the whole amount of raw water supplied from the raw water supply port 8 is filtered.
[0026] ここで、筒状体 5は、仕切板 6の開孔部と筒状ろ材 4の開口部を連結する機能の他 に、水圧などにより筒状ろ材 4の内側の流路が閉塞されることを防止する機能を果た すものであり、筒状ろ材 4の内側へと水が流入することを妨げないように、通水可能な 面で形成されている。従って、筒状体 5は、筒周面が開孔を有する多孔材面から形 成されていて、底面側は閉塞し、上面側は開口しているものである。そして、前記機 能を達成するものであれば、通水性能が高いほど原水処理時の水処理装置 1の圧 力損失が小さくなるので好ましぐ筒周面の開孔率は 50%以上であることが好ましい 。例えば、榭脂製メッシュ状板で構成される筒状体や金属網で構成される筒状体、パ ンチングメタルで構成される筒状体等を用いることができる。  [0026] Here, in addition to the function of connecting the opening portion of the partition plate 6 and the opening portion of the cylindrical filter medium 4, the cylindrical body 5 has a flow path inside the cylindrical filter medium 4 closed by water pressure or the like. In order to prevent water from flowing into the inside of the tubular filter medium 4, it is formed with a surface that allows water to pass therethrough. Therefore, the cylindrical body 5 has a cylindrical peripheral surface formed from a porous material surface having openings, the bottom surface side is closed, and the upper surface side is open. If the above function is achieved, the higher the water flow performance, the smaller the pressure loss of the water treatment device 1 during raw water treatment. Preferably there is. For example, it is possible to use a cylindrical body made of a resin mesh-like plate, a cylindrical body made of a metal net, a cylindrical body made of a punching metal, or the like.
[0027] 次に、上記の一定時間のろ過工程が終了すると、筒状ろ材 4の外表面を洗浄する ために、圧縮気体または圧縮気体を混入させた処理水を処理水出口 9から原水側へ 流す逆圧洗浄や、圧縮気体または圧縮気体を混入させた原水を供給口 8から供給し 、容器本体 2内に蓄積した懸濁物質を排出するスクラビングを行う。このとき、流出口 10は開放する。ここで、逆圧洗浄ゃスクラビングにおいて使用する圧縮気体は、加圧 し圧縮した気体であり、その気体の種類は特に限定しないが、空気や窒素等を用い ればよい。圧縮気体の供給としては、ブロア一やコンプレッサーなどを用いて圧縮空 気を送ることが容易であり好まし 、。  [0027] Next, when the filtration process for a certain period of time is completed, in order to clean the outer surface of the tubular filter medium 4, compressed gas or treated water mixed with the compressed gas is supplied from the treated water outlet 9 to the raw water side. Rubbing is performed by flowing back-pressure washing or by supplying compressed gas or raw water mixed with compressed gas from the supply port 8 and discharging suspended substances accumulated in the container body 2. At this time, the outlet 10 is opened. Here, the compressed gas used in scrubbing for back pressure cleaning is a pressurized and compressed gas, and the type of the gas is not particularly limited, but air, nitrogen, or the like may be used. As the supply of compressed gas, it is easy and preferable to send compressed air using a blower or a compressor.
[0028] 図 5の配管フロー図を用いて具体的に説明する。例えば、ブロア 21からの空気配 管を途中で分岐させて、流路 Iの空気配管 22と、流路 IIの空気配管 23とし、それぞれ の空気配管 22、 23の先を、処理水出口 9付近の処理水配管 24および原水供給口 8 付近の原水配管 25に、それぞれ接続する。それぞれの空気配管 22、 23の途中に設 けた開閉弁 26、 27の開閉により、処理水室 19内及び Z又は原水室 20内に向けて 圧縮空気を供給することができる。このとき、流量計や圧力計 (図示しない)を設置す るとともに、開閉弁 26、 27の開度を調整することで供給する圧縮空気の量を調整す ればよい。なお、このとき、処理水配管 24の開閉弁や原水配管 25の開閉弁は、閉状 態となつている。 [0028] A specific description will be given using the piping flow diagram of FIG. For example, the air piping from the blower 21 is branched halfway to form the air piping 22 of the flow channel I and the air piping 23 of the flow channel II, and the ends of the air pipings 22 and 23 are near the treated water outlet 9 To the treated water pipe 24 and the raw water pipe 25 near the raw water supply port 8 respectively. By opening and closing the on-off valves 26 and 27 installed in the middle of the air pipes 22 and 23, they are directed toward the treatment water chamber 19 and the Z or raw water chamber 20, respectively. Compressed air can be supplied. At this time, a flow meter and a pressure gauge (not shown) may be installed, and the amount of compressed air supplied may be adjusted by adjusting the opening of the on-off valves 26 and 27. At this time, the open / close valve of the treated water pipe 24 and the open / close valve of the raw water pipe 25 are in a closed state.
[0029] 次に、処理水室 19内に圧縮気体混合流体を供給する場合は、前述のようにブロア 21を用 、て圧縮空気を送ると同時に、例えばポンプ 28を用 、てタンクなど(図示しな い)に貯めておいた処理水を処理水出口 9に向かって流せばよい。そうすれば、処理 水出口 9付近の処理水配管 24内において処理水と圧縮空気が合流し、圧縮気体混 合流体として処理水室 19内に送られる。この場合、圧縮気体が処理水中に分散して 各筒状ろ材により均等に送られるので好ましい。  [0029] Next, when the compressed gas mixed fluid is supplied into the treated water chamber 19, the blower 21 is used to send the compressed air as described above, and at the same time, for example, the pump 28 is used to form a tank (see FIG. The treated water stored in (not shown) may flow toward the treated water outlet 9. Then, the treated water and the compressed air merge in the treated water pipe 24 near the treated water outlet 9, and are sent into the treated water chamber 19 as a compressed gas mixed fluid. In this case, it is preferable because the compressed gas is dispersed in the treated water and is uniformly sent by each cylindrical filter medium.
[0030] また、原水室 20内に圧縮気体混合流体を供給する場合も同様に行えばよい。即ち 、ブロア 21を用いて圧縮空気を送ると同時に、ポンプ 29を用いて原水を原水供給口 8に向力つて流せばよい。そうすれば、原水供給口 8付近の原水配管 25内において 原水と圧縮空気が合流し、圧縮気体混合流体として原水室 20内に送られる。  [0030] The same operation may be performed when the compressed gas mixed fluid is supplied into the raw water chamber 20. That is, the compressed air is sent using the blower 21, and at the same time, the raw water is flowed to the raw water supply port 8 by using the pump 29. Then, the raw water and the compressed air merge in the raw water pipe 25 near the raw water supply port 8 and are sent into the raw water chamber 20 as a compressed gas mixed fluid.
[0031] まず、逆圧洗浄では、圧縮気体または圧縮気体を混入させた処理水が筒状ろ材 4 の内部から外部に向かって流れるため、筒状ろ材 4の外表面に付着して 、た懸濁物 質がそのろ材の外表面力も剥離しあるいは剥離し易 、状態となる。そして次のスクラ ビングで、その懸濁物質は水中に浮遊し、排水工程において原水供給口 8から水と 一緒に排出される。ここで、逆圧洗浄とスクラビングは同時に実施しても力まわない。 また、逆圧洗浄にお!ヽて圧縮気体を混入させた処理水を筒状ろ材 4に送る場合は、 筒状ろ材 4の外表面に付着して 、た懸濁物質をろ材の外表面から剥離すると同時に 水中に浮遊させる効果もあるので、必ずしもスクラビングを実施する必要はない。  [0031] First, in the back pressure cleaning, the compressed gas or the treated water mixed with the compressed gas flows from the inside of the tubular filter medium 4 to the outside, so that it adheres to the outer surface of the tubular filter medium 4 and is suspended. The turbid material peels off the outer surface force of the filter medium or is easily peeled off. In the next scrubbing, the suspended substances float in water and are discharged together with water from the raw water supply port 8 in the drainage process. Here, back pressure cleaning and scrubbing can be performed simultaneously. In addition, when the treated water mixed with compressed gas is sent to the tubular filter medium 4 for back pressure cleaning, it adheres to the outer surface of the tubular filter medium 4, and the suspended substances are removed from the outer surface of the filter medium. Since it has the effect of floating in water at the same time as peeling, scrubbing is not necessarily required.
[0032] 逆圧洗浄において供給する圧縮気体の圧力は、使用するろ材に応じて決定する。  [0032] The pressure of the compressed gas supplied in the back pressure cleaning is determined according to the filter medium to be used.
すなわち、圧縮気体が筒状ろ材 4の内部力も外部に向力つて貫通するためには、筒 状ろ材に使用するろ布(立毛編織物)のバブルポイント以上の圧力で圧縮気体を供 給しなければならない。  In other words, in order for the compressed gas to penetrate through the internal force of the tubular filter medium 4 as well, the compressed gas must be supplied at a pressure higher than the bubble point of the filter cloth (puffed knitted fabric) used for the tubular filter medium. I must.
[0033] 一方、供給する処理水の単位時間あたりの流量は、ろ過時の処理水の流量の 1. 5 倍以上 3倍以下程度であることが好ましい。ろ過時の流量と同程度であれば、洗浄効 果が小さぐ逆に、流量を増やすほど洗浄効果は大きくなるが、洗浄に使用した分だ け最終的に得られる処理水の量が減少するからである。 [0033] On the other hand, the flow rate of the treated water to be supplied per unit time is preferably about 1.5 to 3 times the flow rate of the treated water during filtration. If it is almost the same as the flow rate during filtration, On the contrary, the cleaning effect increases as the flow rate increases, but the amount of treated water finally obtained is reduced by the amount used for cleaning.
[0034] 次に、スクラビング時に供給する圧縮気体の量を (Q)、容器本体 2の横断面積 (筒 状ろ材 2の長手方向に対して垂直な方向の断面における内壁断面積)を (S)とすると 、(QZS)の値が 0. 1LZ分 Zcm2以上あれば好ましい。 [0034] Next, the amount of compressed gas supplied during scrubbing is (Q), and the cross-sectional area of the container body 2 (the inner wall cross-sectional area in the cross section perpendicular to the longitudinal direction of the tubular filter medium 2) is (S) When, preferable if the value of (QZS) 0. 1LZ min ZCM 2 or more.
[0035] また、スクラビングをより効果的に行うために、図 3に示すように筒状ろ材 4のそれぞ れの下方にスクラビング用配管 15の気体出口を設置したり、図 4に示すように各筒状 ろ材 4の下方に散気口 16を有する散気板 17を、筒状ろ材の下方に設置したりするこ とも好ましい。これらの場合、圧縮気体が容器本体 2内の筒状ろ材 4付近に集中的に 供給されるため、効果的な洗浄や圧縮気体流量の低減などが可能となる。  In addition, in order to perform scrubbing more effectively, a gas outlet of the scrubbing pipe 15 is installed below each of the tubular filter media 4 as shown in FIG. 3, or as shown in FIG. It is also preferable to install a diffuser plate 17 having a diffuser port 16 below each tubular filter medium 4 below the tubular filter medium. In these cases, the compressed gas is intensively supplied in the vicinity of the cylindrical filter medium 4 in the container main body 2, so that effective cleaning, reduction of the flow rate of the compressed gas, and the like are possible.
[0036] さらに、本発明では筒状ろ材 4を、極細繊維の立毛を有する立毛編織物でもって構 成するので、ろ過工程においては懸濁物質が立毛部分に捕捉され、逆圧洗浄また はスクラビングで立毛が揺れることで立毛に捕捉した懸濁物質を剥離し易いからであ る。そして、捕捉した懸濁物質は剥離させた後、原水側に排出するため、筒状ろ材 4 にお 、て極細繊維の立毛を有する面が原水側に位置するように配置して 、る。  [0036] Furthermore, in the present invention, the cylindrical filter medium 4 is constituted by a napped knitted fabric having naps of ultrafine fibers, so that suspended substances are trapped in the napped portions in the filtration step, and back pressure washing or scrubbing is performed. This is because the suspended matter trapped in the napping is easily peeled off by shaking the napping. Since the trapped suspended matter is peeled off and then discharged to the raw water side, the tubular filter medium 4 is arranged so that the surface having the napped fibers is located on the raw water side.
[0037] そしてまた、本発明によれば、筒状ろ材 4の横断面の面積を A、筒状体 5の横断面 の面積を Bとした場合、その比 (AZB)が 1. 1以上であることが好ましい。これは、筒 状ろ材 4の横断面積が筒状体 5の横断面積に対して大き 、ほど、逆圧洗浄時ゃスク ラビング時に筒状ろ材 4が揺れやすぐ外表面に付着した懸濁物質を剥離し易いか らである。なお、 AZBの比の上限は実用上 2程度である。  [0037] According to the present invention, when the area of the cross section of the tubular filter medium 4 is A and the area of the cross section of the tubular body 5 is B, the ratio (AZB) is 1.1 or more. Preferably there is. This is because the tubular filter medium 4 has a larger cross-sectional area than the cross-sectional area of the cylindrical body 5 and the suspended filter substance 4 is swayed or adhering to the outer surface immediately after scrubbing. This is because it is easy to peel off. The upper limit of the ratio of AZB is practically about 2.
[0038] 以上の工程を繰り返しながら長時間にわたり原水の処理が継続して行われる。  [0038] The raw water is continuously treated for a long time while repeating the above steps.
[0039] なお、上述の水処理は、原水をすべてろ過する、 V、わゆる全ろ過方式の場合につ いて説明したが、ろ過工程において、原水供給口 8から供給された原水の一部が容 器本体内を流れて流出口 10から排出され、残りの一部が、複数本の筒状体 5に取り 付けられた筒状ろ材 4の外側から内側に向力つて流れ込みろ過されるろ過方式、い わゆるクロスフローろ過方式で水処理を行ってもかまわない。  [0039] Although the water treatment described above has been described for the case of V, the so-called total filtration method, in which all of the raw water is filtered, in the filtration step, a part of the raw water supplied from the raw water supply port 8 is used. A filtration method in which the liquid flows through the container body and is discharged from the outlet 10, and the remaining part flows into the cylindrical filter medium 4 attached to multiple cylindrical bodies 5 from the outside to the inside and is filtered. So-called cross-flow filtration may be used for water treatment.
[0040] また、水処理装置の原水室 20内には筒状ろ材 4及び筒状体 5が複数配置されてい ることが好ましい。これは、筒状ろ材 4および筒状体 5のコストに比べて、容器本体 2の コストのほうが高いため、 1つの容器本体 2内に必要に応じて少しでも多くの筒状ろ材 4及び筒状体 5を配置し、ろ過面積を大きくする方が、装置コストを低減できるためで ある。その際、水処理装置 1を設置している場所において、容器本体 2内に複数の筒 状ろ材 4及び筒状体 5を 1本ずつ脱着するには手間が掛カるので、予め仕切板 6に 複数本の筒状ろ材 4及び筒状体 5を取り付けておき、仕切板 6と複数本の筒状ろ材 4 及び筒状体 5が一体化した状態で脱着できることが、作業効率上好ま 、。 [0040] Further, it is preferable that a plurality of tubular filter media 4 and tubular bodies 5 are arranged in the raw water chamber 20 of the water treatment apparatus. Compared to the cost of the cylindrical filter medium 4 and the cylindrical body 5, Because the cost is higher, it is possible to reduce the equipment cost by arranging as many cylindrical filter media 4 and cylindrical bodies 5 as possible in one container body 2 and increasing the filtration area. . At that time, it takes time to detach and attach the plurality of tubular filter media 4 and the tubular body 5 one by one in the container body 2 at the place where the water treatment device 1 is installed. It is preferable in terms of work efficiency that a plurality of cylindrical filter media 4 and a cylindrical body 5 are attached to the partition plate 6 so that the partition plate 6 and the plurality of cylindrical filter media 4 and the cylindrical body 5 can be attached and detached.
[0041] またさらに、本発明の水処理装置は、装置内を水が水平方向に流れるような横向き で設置することもできる。この場合、筒状ろ材 4及び筒状体 5の長手方向が水平にな るように容器本体 2内に設置されていればよい。このように横向きで設置し、筒状ろ材 4及び筒状体 5の長手方向が容器本体 2内で水平方向に設置されている場合には、 蓋部 3を開けて筒状ろ材 4及び筒状体 5等を交換する際に、横から作業することがで きるという利点がある。これに対し、水処理装置を縦向きに設置し、筒状ろ材 4及び筒 状体 5の長手方向が容器本体 2内に垂直方向に配置されている場合は、筒状ろ材 4 及び筒状体 5を容器本体 2に脱着する際に、少なくとも容器本体 2の上方に筒状ろ材 4及び筒状体 5の高さ分の空間が必要であるため、天井の低い建物内などに設置す ると設置したままでの筒状ろ材 4及び筒状体 5の脱着が困難という問題があり、筒状 ろ材 4及び筒状体 5の長さが制限される。  [0041] Furthermore, the water treatment apparatus of the present invention can be installed in a horizontal direction so that water flows in the horizontal direction in the apparatus. In this case, the tubular filter medium 4 and the tubular body 5 may be installed in the container body 2 so that the longitudinal directions thereof are horizontal. In this way, when the longitudinal direction of the cylindrical filter medium 4 and the cylindrical body 5 is installed horizontally in the container body 2, the lid 3 is opened and the cylindrical filter medium 4 and the cylindrical body are installed. When exchanging the body 5 etc., there is an advantage that it can work from the side. On the other hand, when the water treatment device is installed vertically and the longitudinal direction of the tubular filter medium 4 and the tubular body 5 is arranged vertically in the container body 2, the tubular filter medium 4 and the tubular body When detaching 5 to / from the container body 2, at least the space above the container body 2 is required for the height of the tubular filter medium 4 and the tubular body 5, so if installed in a building with a low ceiling, etc. There is a problem that it is difficult to remove the cylindrical filter medium 4 and the cylindrical body 5 in the installed state, and the lengths of the cylindrical filter medium 4 and the cylindrical body 5 are limited.
[0042] 上記の説明は、 1台の水処理装置で水処理する場合である力 複数台の水処理装 置を連接して水処理を行うこともできる。例えば、よりろ過精度の高いろ過を行うとき や、より長期間にわたって安定運転するときなどは、水処理装置の複数台を直列に 配置し、上流側の水処理装置の処理水出口と下流側の水処理装置の原水供給口と を連接し、上流側の水処理装置から下流側の水処理装置へと順次水を通過させる 方法により水処理することが好ましい。特に、それぞれろ過精度の異なるろ材を収納 した複数台の水処理装置を直列に配置し、上流側から下流側に向力つて、ろ材のろ 過精度を高くして 、く構成をとることによって水処理を行うことがさらに好まし 、。この 場合、原水中の懸濁物質がその大きさによって段階的に捕捉されるため、ろ材の目 詰まりが低減できる。  [0042] In the above description, the water treatment can be performed by connecting a plurality of water treatment devices in a force when water treatment is performed by one water treatment device. For example, when performing filtration with higher filtration accuracy or stable operation over a longer period of time, multiple water treatment devices are placed in series, and the treated water outlet and the downstream water treatment device are connected in series. It is preferable to perform water treatment by connecting the raw water supply port of the water treatment device and sequentially passing water from the upstream water treatment device to the downstream water treatment device. In particular, a plurality of water treatment devices, each containing filter media with different filtration accuracy, are arranged in series, and they are directed from the upstream side to the downstream side so as to increase the filtration accuracy of the filter media and to make the water Even more preferred to do the processing. In this case, the suspended matter in the raw water is trapped in stages depending on its size, so clogging of the filter medium can be reduced.
実施例 [0043] <実施例 1 > Example <Example 1>
筒状体及び筒状ろ材の収納本数を 2本にした以外は図 1に示す構造の水処理装 置を用い、流出口からの原水排出を行わない全ろ過方式で、水処理装置を縦置きで 設置して原水の処理を行った。  A water treatment device with the structure shown in Fig. 1 is used except that the number of cylinders and tubular filter media is two, and the water treatment device is placed vertically using a total filtration system that does not discharge raw water from the outlet. Installed at and treated raw water.
[0044] 筒状ろ材を構成するろ材としては、太さ約 7 μ mのポリエステル極細繊維の立毛 (長 さ 2〜4mm)を有するろ過精度 18 mの立毛織物を用いた。そして、この立毛織物 を、直径約 30mm、長さ約 500mmの大きさで、一端が開口し他端が閉塞した筒状に 縫製して筒状ろ材とした。この筒状ろ材を、直径約 25mm、長さ約 500mmで開孔率 が約 60%の榭脂製多孔板力もなる筒状体の外周を覆うように取り付けた。ここで、筒 状ろ材の横断面の面積を A、筒状体の横断面の面積を Bとしたときの (AZB)の比は 1. 44であった。また、容器本体、蓋部、仕切板および筒状体にはポリ塩ィ匕ビュル製 の榭脂成形品を用いた。密閉容器内に 2本の筒状ろ材及び筒状体を収納した構造 の水処理装置とした。また、容器本体内の横断面積は 25cm2であった。 [0044] As the filter medium constituting the cylindrical filter medium, a napped woven fabric having a filtration accuracy of 18 m and having napped polyester fibers (length: 2 to 4 mm) having a thickness of about 7 μm was used. The napped fabric was sewn into a tubular shape having a diameter of about 30 mm and a length of about 500 mm, with one end open and the other closed. This cylindrical filter medium was attached so as to cover the outer periphery of a cylindrical body having a diameter of about 25 mm, a length of about 500 mm, and a porosity of about 60%, which is also made of a resinous porous sheet. Here, the ratio of (AZB) when the cross-sectional area of the tubular filter medium is A and the cross-sectional area of the tubular body is B is 1.44. In addition, a resin molded product made of polysalt cellulose was used for the container body, the lid, the partition plate, and the tubular body. A water treatment apparatus having a structure in which two cylindrical filter media and a cylindrical body are housed in a sealed container. The cross-sectional area in the container body was 25 cm 2 .
[0045] 次に、原水として濁度が 3〜5度の琵琶湖湖水を用い、流量約 30LZ分で供給口 からポンプで 10分間、容器内に原水を供給し、全ろ過方式でろ過した。次いで、約 6 OLZ分の処理水と 50LZ分の圧縮空気を混合して処理水出口 9から処理水室 19内 に供給して 1分間逆圧洗浄を行!、、同時に 15LZ分の空気を原水供給口 8から原水 室 20内に供給してスクラビングも行った。その後、容器内の原水全部を排水した。  [0045] Next, Lake Biwa water with a turbidity of 3 to 5 degrees was used as raw water, and the raw water was supplied into the container for 10 minutes from the supply port with a pump at a flow rate of about 30 LZ, followed by filtration by the total filtration method. Next, about 6 OLZ of treated water and 50 LZ of compressed air are mixed and supplied from the treated water outlet 9 into the treated water chamber 19 for back pressure washing for 1 minute! At the same time, 15 LZ of air is fed into the raw water. Scrubbing was also performed by supplying the raw water chamber 20 from the supply port 8. Thereafter, all the raw water in the container was drained.
[0046] 上記の工程を繰り返しながら水処理を行ったところ、約 100時間以上連続で安定運 転を続け、処理水を得ることができた。  [0046] When water treatment was performed while repeating the above steps, stable operation was continued for about 100 hours or more, and treated water was obtained.
産業上の利用可能性  Industrial applicability
[0047] 本発明の水処理装置は、小型装置でも高流速で長時間安定した水処理を行うこと ができるので、短時間に大量の水処理を行うことが要求される用途、例えば、湖沼、 堀、河川等の屋外水系における懸濁物質除去用等に利用することができる。 [0047] Since the water treatment apparatus of the present invention can perform stable water treatment at a high flow rate for a long time even with a small apparatus, the application requires a large amount of water treatment in a short time, for example, a lake, It can be used for removing suspended substances in outdoor water systems such as moats and rivers.

Claims

請求の範囲 The scope of the claims
[1] 原水供給口と処理水出口とを有する密閉した容器と、該容器の内部を原水供給口の ある原水室と処理水出口のある処理水室とに仕切るための、開孔部を有する仕切板 と、一端が開口し他端が閉塞した筒状ろ材と、該筒状ろ材の内部に挿入された通水 可能面からなる筒状体とを具備する水処理装置であって、前記仕切板の開孔部と液 密状態になるように前記筒状ろ材の開口端部が配設され、筒状ろ材が極細繊維の立 毛を有する立毛編織物から構成され、かつ、立毛を有する面が原水側に位置するこ とを特徴とする水処理装置。  [1] A sealed container having a raw water supply port and a treated water outlet, and an opening for partitioning the inside of the container into a raw water chamber having a raw water supply port and a treated water chamber having a treated water outlet A water treatment apparatus comprising: a partition plate; a cylindrical filter medium having one end opened and the other end closed; and a cylindrical body including a water-permeable surface inserted into the cylindrical filter medium. An opening end portion of the cylindrical filter medium is disposed so as to be in a liquid-tight state with an opening portion of the plate, and the cylindrical filter medium is composed of a napped knitted fabric having napped fibers and has napped surfaces. Water treatment device characterized by being located on the raw water side.
[2] さらに、処理水室内及び Z又は原水室内に圧縮気体もしくは圧縮気体混合流体を 供給するための洗浄流体供給手段が配設されて!/ヽることを特徴とする請求項 1に記 載の水処理装置。  [2] The cleaning fluid supply means for supplying the compressed gas or the compressed gas mixed fluid to the treated water chamber and Z or the raw water chamber is further disposed! Water treatment equipment.
[3] 前記洗浄流体供給手段が、圧縮気体を処理水室内へ供給する流路を備えた圧縮気 体供給装置、又は、圧縮気体を処理水室内へ供給する流路 Iと圧縮気体を原水室内 へ供給する流路 Πとを備えた圧縮気体供給装置からなることを特徴とする請求項 2〖こ 記載の水処理装置。  [3] The compressed fluid supply device having a flow path for supplying the compressed gas to the treated water chamber, or the flow path I for supplying the compressed gas to the treated water chamber and the compressed gas to the raw water chamber. The water treatment apparatus according to claim 2, further comprising a compressed gas supply device provided with a flow path for supplying to the water.
[4] 筒状ろ材を構成する立毛編織物における立毛の単糸直径が 1. 0〜: LO /z mであるこ とを特徴とする請求項 1に記載の水処理装置。  [4] The water treatment device according to claim 1, wherein the single yarn diameter of the napped yarn in the napped knitted fabric constituting the tubular filter medium is 1.0 to LO / z m.
[5] 筒状ろ材を構成する立毛編織物における立毛の長さが 2〜: LOmmであることを特徴 とする請求項 1に記載の水処理装置。 [5] The water treatment device according to claim 1, wherein the length of the napped in the napped knitted fabric constituting the tubular filter medium is 2 to: LOmm.
[6] 前記筒状ろ材の横断面の断面積 (A)と、前記筒状体の横断面の断面積 (B)との比([6] Ratio of the cross-sectional area (A) of the cross-section of the tubular filter medium to the cross-sectional area (B) of the cross-section of the tubular body (
A/B)が 1. 1以上であることを特徴とする請求項 1に記載の水処理装置。 The water treatment apparatus according to claim 1, wherein A / B) is 1.1 or more.
[7] 前記筒状ろ材の内部に挿入された筒状体の片端が前記仕切板の開孔部に連接され[7] One end of the cylindrical body inserted into the cylindrical filter medium is connected to the opening of the partition plate.
、かつ、筒状体の通水可能面全体が筒状ろ材で覆われていることを特徴とする請求 項 1に記載の水処理装置。 2. The water treatment apparatus according to claim 1, wherein the entire surface of the tubular body through which water can pass is covered with a tubular filter medium.
[8] 前記筒状ろ材及び筒状体が、原水室内に複数配置されていることを特徴とする請求 項 1に記載の水処理装置。 8. The water treatment apparatus according to claim 1, wherein a plurality of the tubular filter media and the tubular body are arranged in the raw water chamber.
[9] 前記筒状ろ材及び筒状体の長手方向が水平になるように前記容器内に設置されて[9] It is installed in the container so that the longitudinal direction of the tubular filter medium and the tubular body is horizontal.
V、ることを特徴とする請求項 1に記載の水処理装置。 The water treatment device according to claim 1, wherein V is a water treatment device.
[10] 請求項 1に記載の水処理装置の複数台が直列に配置されるように、上流側の水処理 装置の処理水出口と下流側の水処理装置の原水供給口とを連接し、上流側の水処 理装置による処理水を下流側の水処理装置へと供給し、順次水を通過させることを 特徴とする水処理方法。 [10] The treated water outlet of the upstream water treatment device and the raw water supply port of the downstream water treatment device are connected so that a plurality of the water treatment devices according to claim 1 are arranged in series. A water treatment method characterized by supplying treated water from an upstream water treatment device to a downstream water treatment device and sequentially passing the water through.
[11] 請求項 8に記載の水処理装置において筒状ろ材を交換する際、複数の筒状ろ材及 び筒状体が仕切板に取り付けられ一体化された状態で容器から脱着し交換すること を特徴とする筒状ろ材の交換方法。  [11] When exchanging the cylindrical filter medium in the water treatment device according to claim 8, the cylindrical filter medium and the cylindrical body are attached to the partition plate and are detached and replaced from the container. A method for replacing a tubular filter medium characterized by the above.
PCT/JP2007/055170 2006-03-27 2007-03-15 Water treatment apparatus WO2007122918A1 (en)

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Publication number Priority date Publication date Assignee Title
JP2014147861A (en) * 2013-01-31 2014-08-21 Ryuki Engineering:Kk Filtration device

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS47766U (en) * 1971-01-11 1972-08-05
JPH01119317A (en) * 1987-10-30 1989-05-11 Mitaka Kogyosho:Kk Filter apparatus
JPH0414112U (en) * 1990-05-21 1992-02-05
JPH11319431A (en) * 1998-05-08 1999-11-24 Fuji Filter Kogyo Kk Filter device

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS47766U (en) * 1971-01-11 1972-08-05
JPH01119317A (en) * 1987-10-30 1989-05-11 Mitaka Kogyosho:Kk Filter apparatus
JPH0414112U (en) * 1990-05-21 1992-02-05
JPH11319431A (en) * 1998-05-08 1999-11-24 Fuji Filter Kogyo Kk Filter device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014147861A (en) * 2013-01-31 2014-08-21 Ryuki Engineering:Kk Filtration device

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