WO2022234738A1 - Cycle filtration system - Google Patents

Cycle filtration system Download PDF

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Publication number
WO2022234738A1
WO2022234738A1 PCT/JP2022/013351 JP2022013351W WO2022234738A1 WO 2022234738 A1 WO2022234738 A1 WO 2022234738A1 JP 2022013351 W JP2022013351 W JP 2022013351W WO 2022234738 A1 WO2022234738 A1 WO 2022234738A1
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WO
WIPO (PCT)
Prior art keywords
raw water
pump
pipe
flow pipe
water
Prior art date
Application number
PCT/JP2022/013351
Other languages
French (fr)
Japanese (ja)
Inventor
光雄 大嶺
秀樹 宮城
Original Assignee
ワイズグローバルビジョン株式会社
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Application filed by ワイズグローバルビジョン株式会社 filed Critical ワイズグローバルビジョン株式会社
Publication of WO2022234738A1 publication Critical patent/WO2022234738A1/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/02Reverse osmosis; Hyperfiltration ; Nanofiltration
    • B01D61/10Accessories; Auxiliary operations
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/28Treatment of water, waste water, or sewage by sorption
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/30Treatment of water, waste water, or sewage by irradiation
    • C02F1/32Treatment of water, waste water, or sewage by irradiation with ultraviolet light
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/42Treatment of water, waste water, or sewage by ion-exchange
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/44Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • C02F1/78Treatment of water, waste water, or sewage by oxidation with ozone
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00Multistage treatment of water, waste water or sewage

Definitions

  • the present invention relates to a circulation filtration system that uses the same water repeatedly.
  • a hand-washing place is required at a construction site deep in the mountains.
  • Such locations require a recirculating filtration system that uses the same water repeatedly. This is because it is sometimes difficult to secure clean water, or even water itself, in such places, and it is also difficult to release dirty water after washing hands into the environment. .
  • repeated use of the same water has the advantage of reducing the amount of water required and reducing the amount of dirty water released into the environment.
  • a circulation type filtration system is useful.
  • recirculating filtration systems are available and may be used where only one of these two advantages is desired.
  • the circulation filtration system is as follows. A case where a circulating filtration system is used in a hand-washing area will be described as an example.
  • the circulation filtration system has a raw water tank that stores raw water.
  • the raw water tank is connected to the base end of a flow channel pipe forming a flow channel for circulating raw water.
  • a pump is provided somewhere in the flow pipe, and the raw water in the raw water tank is sent from the base end side of the flow pipe toward the tip end side by the pump.
  • Purification equipment for purifying raw water is appropriately provided in the middle of the flow pipe.
  • the purification equipment is, for example, a filtration device for removing solids in the raw water, or an ozone generator or an ultraviolet sterilization device for removing chemical substances and microorganisms (bacteria, viruses, etc.) in the raw water.
  • Raw water becomes purified water by passing through purification equipment.
  • a faucet is provided at the tip of the flow pipe, and a saucer, for example a sink, is provided under the faucet.
  • purified water in the channel pipe flows out. Dirty water generated by washing hands with the purified water is received by the tray.
  • the sewage received by the tray reaches the raw water tank and returns to the raw water. For example, if the tray is provided directly above the raw water tank, the sewage received by the tray drops into the raw water tank directly below.
  • a tube of some kind connects the pan and the raw water tank, and the sewage is led from the pan to the raw water tank via the tube.
  • the circulation type filtration system as described above can be established at least in principle, it cannot be said that it is sufficiently popular for the demand. The reason for this is that it is difficult to obtain a sufficient quality of purified water from a circulation filtration system.
  • raw water is purified by passing it through purification equipment.
  • the circulating filtration system when used, for example, as a hand-washing place, the raw water may contain mud, oil, soap components, or the like.
  • raw water is repeatedly used, which is all the more so.
  • the object of the present invention is to provide a practical circulation filtration system that can obtain high-quality purified water even if the raw water is heavily contaminated to some extent.
  • a first invention comprises a raw water tank for storing raw water, which is water that is to be circulated and used repeatedly, and a pipe that constitutes a flow path for circulating the raw water and whose base end is connected to the raw water tank.
  • a conduit a facility for purifying the raw water into purified water provided in the middle of the conduit, the purification facility including at least one reverse osmosis membrane water purification unit, and in the conduit, provided in the front side portion of the reverse osmosis membrane water purification unit located on the most distal side with respect to the flow pipe, when it is driven, the raw water in the flow pipe is transferred into the flow pipe a sub-pump for flowing to the tip side of the flow pipe; and a portion of the flow pipe that is driven in conjunction with the sub-pump when the sub-pump is driven, and is provided at a portion of the flow pipe that contacts the raw water in the raw water tank.
  • a main pump that, when driven, causes the raw water in the raw water tank to flow to the tip side of the flow pipe, and a selection of permission or denial of discharge of the purified water from the flow pipe provided at the tip of the flow pipe. and a receptacle for receiving the purified water discharged from the faucet, and the purified water received by the receptacle reaches the raw water tank.
  • Filtration system In this circulation filtration system, a pipe branched from the flow pipe by connecting the base end of the flow pipe before the sub-pump to form a flow channel for circulating the raw water. and a second purification facility, which is provided in the middle of the branch pipe and is a facility for purifying the raw water.
  • the purified raw water coming out of the tip of the branch pipe reaches the raw water tank, and the main pump is driven independently of the sub-pump.
  • the sub-pump does not allow the raw water to pass through.
  • a circulation filtration system comprises a flow tube.
  • a base end of the flow pipe is connected to a raw water tank for storing raw water, and a tap is provided at a tip of the flow pipe.
  • purification equipment which is equipment for purifying raw water into purified water, is provided in the middle of the flow pipe.
  • the purification equipment may be equipment for purifying raw water, and the details thereof are not limited, but at least one reverse osmosis membrane water purification unit is included. Examples of what constitutes the purification equipment are filter media that are not reverse osmosis membrane water purification units, ozone generators, ultraviolet sterilizers, and aerators.
  • raw water is circulated in the flow pipe by the main pump and the sub-pump.
  • the main pump is positioned at the proximal end of the flow pipe and has a function of flowing the raw water in the raw water tank toward the distal end of the flow pipe.
  • the sub-pump is located in the middle of the flow pipe, more precisely, on the front side of the reverse osmosis membrane water purification unit located on the most distal side, and in the reverse osmosis membrane water purification unit located on the downstream side of the sub-pump. It has the function of applying the pressure necessary to force the water in the raw water to pass over the reverse osmosis membrane in the reverse osmosis membrane water purification unit.
  • the sub-pump is driven when the amount of raw water (or purified water) in the portion of the flow pipe on the tip side of the reverse osmosis membrane water purification unit is reduced, and is driven before the reverse osmosis membrane water purification unit.
  • Raw water is supplied to the part ahead of the reverse osmosis membrane water purification unit. Then, since the amount of raw water on the front side of the reverse osmosis membrane water purification unit in the flow channel decreases, the main pump supplies raw water from the raw water tank to that portion. To enable this, the main pump is driven in conjunction with the sub-pump when the sub-pump is driven.
  • the configuration described so far of the circulation filtration system according to the first invention may be substantially the same as the configuration of the conventional circulation filtration system, although it depends on the case.
  • the circulation filtration system of the first invention comprises a branch pipe.
  • a branch pipe is a pipe branched from a flow pipe by connecting its proximal end to the flow pipe before the sub-pump. The raw water coming out of the tip of the branch pipe is returned to the raw water tank.
  • a second purification facility is provided in the middle of the branch pipe.
  • the second purification equipment is equipment for purifying raw water.
  • the second purification equipment may be equipment for purifying raw water, and the details thereof are not limited.
  • the second purification equipment may include, for example, at least one of a filtering material that is not a reverse osmosis membrane water purification unit, an ozone generator, an ultraviolet sterilizer, and an aerator.
  • the ozone generator is a device that supplies ozone to the raw water passing through the branch pipe.
  • the ultraviolet sterilizer is a device that irradiates raw water passing through a branch pipe with ultraviolet rays.
  • An aerator is a device that supplies air bubbles to raw water passing through a branch pipe. The aerator supplies, for example, microbubbles or nanobubbles to the raw water. Ozone generators, ultraviolet sterilizers, and aerators improve the quality of raw water by different mechanisms.
  • raw water is circulated through the branch pipes by the main pump. As described above, the main pump is driven in conjunction with the sub-pump when the sub-pump is driven, but it can also be driven independently of the sub-pump.
  • the sub-pump acts like a closed valve and does not allow raw water to pass through.
  • the raw water flows from the raw water tank into the channel pipe, flows into the branch pipe branched before the sub-pump, flows through the branch pipe, and flows into the branch pipe. going back to the tank.
  • the raw water is purified by the second purification equipment in the middle of the branch pipe.
  • the series of circulation paths of the raw water created by the flow pipe from the raw water tank to the faucet are necessary for purification because the raw water flows only when the faucet is opened.
  • the time during which such a flow occurs in the raw water is very limited, and therefore it is difficult to sufficiently purify the raw water.
  • a circulation path different from the above-mentioned circulation path formed by the flow pipe is created and the raw water is purified there, it becomes possible to purify the raw water regardless of whether the faucet is open. Since the raw water can be purified as much as necessary, it is possible to obtain sufficiently purified raw water.
  • the inventor of the present application adopted a branch pipe as a raw water circulation path different from the flow pipe, and adopted the second purification equipment as equipment for purifying the raw water flowing through the branch pipe. I did. Moreover, even if the branch pipe as described above is adopted in the first invention, only the originally existing main pump and sub-pump are required to flow the raw water through the branch pipe, and there is no need to adopt a new pump. Therefore, it is advantageous in terms of cost.
  • the main pump in the circulation filtration system of the first invention may be driven for eight hours or more a day independently of the sub-pump.
  • the main pump may be driven for a predetermined length of time every predetermined time.
  • the "predetermined time" at which the main pump is driven at intervals may or may not be the same.
  • the "predetermined time” during which the main pump is driven at one time may or may not be the same.
  • the circulation type filtration system according to the second invention is as follows.
  • the circulation filtration system according to the second invention comprises a raw water tank for storing raw water, which is water to be circulated and used repeatedly, and a flow path for circulating the raw water, the base end of which is connected to the raw water tank.
  • a flow pipe which is a pipe that is a flat pipe
  • a purification equipment which is a facility for purifying the raw water into purified water and which is provided in the middle of the flow pipe, and which includes at least one reverse osmosis membrane water purification unit; a portion of the flow pipe provided on the front side of the reverse osmosis membrane water purification unit located on the most distal side with respect to the flow pipe, and when it is driven, the raw water in the flow pipe is a sub-pump for flowing to the tip end side of the flow pipe in the flow pipe; a main pump that, when driven, causes the raw water in the raw water tank to flow to the tip side of the flow pipe;
  • the apparatus comprises a faucet capable of selecting permission or denial of discharge, and a tray for receiving the purified water discharged from the faucet, and the purified water received by the tray reaches the raw water tank.
  • a second flow different from the flow pipe is a pipe having a base end connected to the raw water tank, which constitutes the flow channel for circulating the raw water. and a passage pipe provided at a portion of the second passage pipe in contact with the raw water in the raw water tank, and when the pipe is driven, the raw water in the raw water tank flows to the tip side of the second passage pipe.
  • a second pump for flowing the raw water and a second purification equipment for purifying the raw water provided in the middle of the second flow pipe are provided. Further, in the circulation filtration system of the second invention, the purified raw water discharged from the tip of the second flow pipe reaches the raw water tank, and the second pump is the main pump. and driven independently of the sub-pump.
  • the circulation filtration system of the second invention employs substantially the same configuration as the circulation filtration system of the first invention.
  • the circulation-type filtration system of the second invention also has flow pipes, like the circulation-type filtration system of the first invention.
  • the base end of the channel pipe is connected to a raw water tank for storing raw water, as in the case of the circulation filtration system of the first invention, and the tip of the channel pipe is provided with a faucet.
  • the circulation filtration system of the second invention is equipped with purification equipment, which is equipment for purifying raw water into purified water, in the middle of the flow pipe, as in the circulation filtration system of the first invention.
  • the purification equipment in the circulation filtration system of the second invention is the same as the purification equipment in the circulation filtration system of the first invention.
  • raw water is circulated in the flow pipe by a main pump and a sub-pump, as in the circulation filtration system of the first invention.
  • Both the main pump and the sub-pump in the circulation filtration system of the second invention are the same as those in the first invention.
  • the main pump in the second invention is not driven independently of the sub-pump.
  • the circulation filtration system of the second invention does not have branch pipes. Instead, the circulation filtration system of the second invention comprises a second flow pipe.
  • the second flow pipe is a pipe that forms a flow channel for circulating raw water and has a base end connected to the raw water tank.
  • the purified raw water coming out of the tip of the second flow pipe reaches the raw water tank.
  • a second purification facility which is a facility for purifying the raw water, is provided in the middle of the second flow pipe.
  • the second purification equipment in the circulation filtration system of the second invention can be the same as the second purification equipment in the circulation filtration system of the first invention.
  • the raw water in the second flow pipe is provided in a portion of the second flow pipe in contact with the raw water in the raw water tank. Circulation is carried out using a second pump that flows to the tip side of the tube.
  • the second pump is driven independently of the main pump and sub-pump. That is, in the circulation filtration system of the second invention, the second flow forming the flow path that exits from the raw water tank and returns to the raw water tank is different from the flow path pipe that forms the flow path that exits from the raw water tank and returns to the raw water tank.
  • the circulation filtration system of the second invention requires a second pump.
  • the second pump causes the second flow pipe to be filled. can circulate the raw water.
  • the second pump in the circulation filtration system of the second invention may be driven for eight hours or more a day. If the second pump is driven to this degree, the raw water is well purified by the second purification equipment, so it is possible to keep the quality of purified water coming out of the faucet high. Of course, it is also possible to make the second pump independent of the sub-pump for a period longer than 8 hours, and by doing so, it is possible to improve the quality of the purified water coming out of the faucet of the circulation filtration system. becomes.
  • the second pump may be driven for a predetermined length of time at predetermined time intervals. The "predetermined time" that the second pump is driven at intervals may or may not be the same. The "predetermined time" for which the second pump is driven at one time may or may not be the same. By doing so, it becomes possible to determine the ratio of the time that the second pump drives independently of the main pump and the sub-pump to a desired ratio.
  • the circulation filtration system of the first invention and the second invention may be provided with a filter medium for filtering the purified water for passing the purified water from the receiving tray to the raw water tank.
  • Purified water returning from the receiving tray to the raw water tank is already in a dirty state, such as containing mud and soap components, for example, when a circulation filtration system is applied to a hand-washing area. Instead of returning dirty purified water to the raw water tank as it is, it is easier to keep the raw water clean by returning it to the raw water tank after passing it through a filter medium.
  • the filter medium for passing purified water returning from the receiving tray to the raw water tank may include at least one of an oil adsorption sheet, an ion exchange resin, and activated carbon, for example.
  • the oil adsorption sheet is useful for removing oil contained in water passing through it
  • the ion exchange resin is useful for removing surfactant contained in water passing through it.
  • activated carbon is useful in removing heavy metals and odor causing substances contained in water passing through it.
  • the filter medium may contain two or more of oil adsorption sheet, ion exchange resin and activated carbon, or all of them.
  • the filter medium for passing purified water returning from the receiving tray to the raw water tank may be incorporated in a bag filter. As a result, the filter medium can be replaced together with the bag filter, so that the labor and cost of replacing the filter medium can be reduced.
  • FIG. 2 is a cross-sectional view conceptually showing the configuration of a reverse osmosis membrane water purification unit included in the circulation filtration system shown in FIG. 1 ;
  • FIG. 2 is a cross-sectional view conceptually showing the configuration of a filtering member included in the circulation filtering system shown in FIG. 1;
  • FIG. 1 shows an overall configuration diagram of a circulation filtration system 1 according to the first embodiment.
  • the circulating filtration system 1 in this embodiment is used for a wash basin.
  • the circulation filtration system 1 of the first embodiment includes a raw water tank 10 .
  • the raw water tank 10 is a tank for storing raw water 11, which is water before being purified by a first purification facility, which is a purification facility to be described later.
  • the raw water tank 10 only needs to store the raw water 11 without leakage, and is made of metal or resin, for example.
  • the raw water tank 10 may be a well-known or well-known tank, and may be a commercially available one.
  • the capacity of the raw water tank 10 in this embodiment is, but not limited to, about 100 liters.
  • a main pump 21 is arranged in an appropriate portion of the raw water tank 10 in contact with the raw water 11 .
  • the main pump 21 is a pump that can send water, and any pump that can do so may be used.
  • the main pump 21 can be configured by a known or well-known pump, and may be a commercially available one.
  • the main pump 21 is connected to the proximal end of the flow pipe 31 .
  • the main pump 21 guides the raw water 11 in the raw water tank 10 into the channel pipe 31 and causes it to flow toward the tip side of the channel pipe 31 .
  • the main pump 21 is connected to a computer 40 by a connection line 21A, and under the control of the computer 40, control of driving and stopping is performed. It is sufficient for the computer 40 to be able to perform such control, and it may be a known or well-known one, or a commercially available one. How the computer 40 controls the main pump 21 will be described later.
  • the flow pipe 31 is a pipe for circulating the raw water 11 in the raw water tank 10 as described later.
  • the flow pipe 31 is sufficient as long as it can flow raw water (the raw water becomes the purified water 12 in the middle of the flow pipe 31 as will be described later).
  • the flow pipe 31 is made of metal or resin, for example.
  • the flow pipe 31 is provided with purification equipment for purifying the raw water 11 carried from the raw water tank 10 into purified water.
  • the purification equipment may be any equipment for purifying the raw water 11, and includes at least one reverse osmosis membrane water purification unit 51, although the details thereof are not limited.
  • the purification equipment may also include filter media other than reverse osmosis membranes, an ozone generator, an ultraviolet sterilizer, and an aerator, but in this embodiment, they are not included in the purification equipment.
  • An example of the filter medium is a well-known sediment filter provided upstream of the flow pipe 31 from the reverse osmosis membrane water purification unit 51, for example, upstream of the sub-pump 22.
  • the raw water 11 that has passed through the most downstream purification facility of the flow pipe 31 is the purified water 12 .
  • the raw water 11 becomes purified water 12 after passing through the reverse osmosis membrane water purification unit 51 .
  • the sediment filter as a type of filter medium, other facilities such as the reverse osmosis membrane water purification unit 51 belonging to the purification facility, the filter medium including the sediment filter, the ozone generator, etc.
  • the tube 31 need not be continuous.
  • another device such as an ozone generator can be provided further downstream of the accumulator tank described later in the flow pipe 31. It does not matter if it is provided.
  • the reverse osmosis membrane water purification unit 51 will be described.
  • the reverse osmosis membrane water purification unit 51 is known or well-known, and may be commercially available. Therefore, only a brief description of the principle will be given.
  • a principle diagram of the reverse osmosis membrane water purification unit 51 is shown in FIG.
  • the reverse osmosis membrane water purification unit 51 has a case 51A.
  • the case 51A is, for example, a cylindrical pressure-resistant container.
  • the inside of the case 51A is divided into two spaces by a reverse osmosis membrane 51B.
  • reverse osmosis membrane 51B is parallel to the axis of case 51A.
  • the reverse osmosis membrane 51B may be cylindrical, and the space inside the case 51A may be divided into two spaces, one outside and one inside the reverse osmosis membrane 51B.
  • the reverse osmosis membrane 51B does not need to be exclusively used for seawater because of the characteristics of the circulating hand washing unit.
  • an Extra Low Energy RO Membrane series reverse osmosis membrane from FilmTecTM can be used as reverse osmosis membrane 51B.
  • An inlet 51C into which the raw water 11 flows is provided in one end face (lower side in FIG. 2) of the case 51A.
  • a drain port 51D through which waste water, which is the concentrated raw water 11, flows out is provided on the other end face of the case 51A.
  • the inlet 51C and the outlet 51D communicate with the same space of the two spaces inside the case 51A divided by the reverse osmosis membrane 51B.
  • a purified water port 51E for discharging the purified water 12 produced from the raw water 11 by the reverse osmosis membrane water purification unit 51 is provided on the other end surface of the case 51A.
  • the purified water port 51E communicates with the space on the side where the inflow port 51C and the water discharge port 51D do not communicate among the two spaces inside the case 51A divided by the reverse osmosis membrane 51B.
  • the raw water 11 flows into the case 51A from an inlet 51C to which the flow pipe 31 is connected.
  • a high pressure is applied to the raw water 11 entering the case 51A from the inlet 51C by maintaining an appropriate relationship between the inflow of the raw water 11 from the inlet 51C and the outflow of waste water from the drain 51D.
  • water that is close to pure water is in communication between the inlet 51C and the outlet 51D of two spaces inside the case 51A divided by the reverse osmosis membrane 51B. From the space, it passes through the reverse osmosis membrane 51B and oozes out into the space communicating with the purified water port 51E. That is, the raw water 11 is separated into the purified water 12 and the concentrated raw water 11 in the case 51A by the reverse osmosis membrane 51B.
  • the raw water 11 and the purified water 12 are discharged from the case 51A through the drain port 51D and the purified water port 51E, respectively.
  • the water purification port 51 ⁇ /b>E is connected to the flow pipe 31 on the downstream side of the reverse osmosis membrane water purification unit 51 .
  • the drain port 51D is connected to a drain pipe, which will be described later.
  • a sub-pump 22 is provided upstream of the reverse osmosis membrane water purification unit 51 of the flow pipe 31 (raw water tank 10 side).
  • the sub-pump 22 is a pump for supplying the raw water 11 at high pressure to the reverse osmosis membrane water purification unit 51 .
  • the sub-pump 22 is a pump that can send water, and as long as it can do that, it may be of any type, like the main pump 21 .
  • the sub-pump 22 is connected to a computer 40 by a connection line 22A, and is controlled to be driven and stopped under the control of the computer 40. As shown in FIG. How the computer 40 controls the sub-pump 22 will be described later.
  • An accumulator tank 60 is provided downstream of the reverse osmosis membrane water purification unit 51 in the flow pipe 31 .
  • the accumulator tank 60 is for keeping the water pressure of purified water 12 coming out of a faucet, which will be described later, within a predetermined range.
  • the accumulator tank 60 is made of a watertight tank and an elastic film material called Prada arranged in the tank, and a constant It is equipped with something like an airtight balloon filled with gas at a pressure higher than the pressure.
  • Purified water 12 fills the gap between the prada and the tank. By setting the amount of the purified water 12 in the accumulator tank 60 within an appropriate range, an appropriate pressure is applied to the purified water 12 in the accumulator tank 60 from the prada.
  • the accumulator tank 60 is normally located above the faucet, and is so in this embodiment. Since the accumulator tank 60 is positioned above the faucet and an appropriate pressure is applied to the purified water 12 in the accumulator tank 60 from the prada, the purified water 12 coming out of the faucet, which will be described later, is applied with an appropriate water pressure. will come out from The accumulator tank 60 need not be located above the faucet 71 if sufficient pressure can be applied to the purified water 12 from the bladder within the accumulator tank 60 . The water pressure of the purified water 12 in the accumulator tank 60 is detected by a sensor (not shown). , is sent to the computer 40 .
  • a faucet 71 is attached to the tip of the flow pipe 31 .
  • the faucet 71 is a publicly known one or a well-known one, and allows selection of permission or denial of outflow of the purified water 12 .
  • the faucet 71 is open, purified water 12 comes out of the faucet 71, and when the faucet 71 is closed, the purified water 12 does not come out of the faucet 71.
  • a saucer 72 for receiving purified water 12 discharged from the faucet 71 is provided below the faucet 71.
  • the saucer 72 is a sink with a drain. In the circulation filtration system 1 according to this embodiment, only the faucet 71 and the saucer 72 are required to be exposed to the outside, and all other parts need not be exposed to the outside.
  • a drain pipe 83 is connected to the drain port of the tray 72 .
  • the drain pipe 83 is for guiding the purified water 12 received by the tray 72 to the raw water tank 10, and is vertical in this embodiment, although not limited to this.
  • Purified water 12 discharged from the faucet 71 and received by the receiving tray 72 flows down through the drain pipe 83 by gravity and reaches the raw water tank 10 .
  • a filter member 84 is attached in the middle of the drain pipe 83 .
  • the filter member 84 passes the purified water 12 from the tray 72 to the raw water tank 10 through the drain pipe 83 to filter and remove mud and soap components contained in the purified water 12 .
  • Filtration member 84 in this embodiment provides filtration of dirty purified water 12 flowing down by gravity.
  • the filtering member 84 is as shown in FIG.
  • the filtering member 84 has a bag filter 84A.
  • the bag filter 84A is a bag made of a mesh fabric, and has an open top, although not limited to this. Since many bag filters that can be used as the bag filter 84A are commercially available, a suitable one can be selected and used.
  • An oil adsorption sheet 84B is incorporated in the upper portion of the bag filter 84A.
  • the oil adsorption sheet 84B is a sheet that removes oil contained in the purified water 12. As shown in FIG. A plurality of oil adsorption sheets 84B are stacked and housed in the bag filter 84A.
  • oil adsorption sheet 84B for example, an oil adsorption sheet (trade name Grease Screen (trademark) series) manufactured and sold by Asahi Kasei Home Products Corporation can be used.
  • a mixture 84C of ion exchange resin and activated carbon is incorporated in the lower portion of the bag filter 84A. Both the ion exchange resin and the activated carbon are in the form of powder, and are contained in the bag filter 84A in a mixed state.
  • the ion exchange resin in the mixture 84C is useful for removing surfactants contained in the dirty water 12 passing through it, and the activated carbon in the mixture 84C is useful for removing the surfactant contained in the dirty water 12 passing through it.
  • the filtering member 84 contains at least one of the oil adsorption sheet 84B, ion exchange resin, and activated carbon.
  • the bag filter 84A included in the filter member 84 is for facilitating replacement of the filter member 84. If the effect is not required, the oil adsorption sheet 84B, the ion exchange resin, and the activated carbon may be used. need not be housed in the bag filter 84A.
  • the circulation filtration system 1 in the first embodiment is equipped with a branch pipe 32 .
  • the branch pipe 32 is a pipe that constitutes a flow path for circulating the raw water 11 in the raw water tank 10 through a path different from the above-described circulation path formed by the flow path pipe 31 .
  • the branch pipe 32 is a pipe whose base end is connected to the flow pipe 31 upstream of the sub-pump 22 , that is, to the base end side of the flow pipe 31 , and is branched from the flow pipe 31 . .
  • the specifications of the pipes forming the branch pipe 32 may or may not be the same as those of the pipes forming the flow channel pipe 31 .
  • the raw water 11 coming out of the tip of the branch pipe 32 reaches the raw water tank 10. - ⁇ For example, the tip of the branch pipe 32 is located right above the raw water tank 10, and the raw water 11 coming out of the tip of the branch pipe 32 falls into the raw water tank 10 by gravity.
  • a second purification facility is provided in the middle of the branch pipe 32 .
  • the second purification equipment is equipment for purifying the raw water 11 flowing through the branch pipe 32 .
  • the details are not limited as long as it includes at least one of an ozone generator, an ultraviolet sterilizer, and an aerator.
  • the ozone generator has a function of supplying the raw water 11 with generated ozone. By supplying ozone to the raw water 11 , organic substances in the raw water 11 are decomposed by the oxidizing action of ozone, and the raw water 11 is purified.
  • the decomposition of organic matter can also include the effect of killing or inactivating plankton, bacteria and viruses, for example.
  • the ozone generator may be a known or well-known one, or may be a commercially available one.
  • As the ozone generator for example, a compact one that generates a relatively small amount of ozone of about 1000 mg/h that does not adversely affect the human body even if inhaled by a person can be used.
  • the ultraviolet sterilizer has a function of irradiating the raw water 11 with the generated ultraviolet rays. By irradiating the raw water 11 with ultraviolet rays, the effect of killing or inactivating bacteria and viruses can be obtained.
  • the ultraviolet sterilizer may be a publicly known or well-known one, or may be a commercially available one.
  • an ultraviolet sterilizer for purification of running water equipped with a deep ultraviolet LED lamp manufactured and sold by Nikkiso Co., Ltd. can be used.
  • the aeration device aerates the raw water 11 by supplying microbubbles or nanobubbles, for example. By aerating the raw water 11, aerobic bacteria in the raw water 11 become active, thereby improving the water quality of the raw water 11.
  • the aerator may be a publicly known or well-known one, or may be a commercially available one. It is preferable to use an aeration device that generates 100 million or more nanobubbles per 1 ml, for example.
  • an ozone generator 91 and an ultraviolet sterilizer 92 are provided in the middle of the branch pipe 32 as the second purification equipment.
  • the raw water 11 passing through the branch pipe 32 is purified by the above-described principle by the ozone generator 91 and the ultraviolet sterilizer 92, and the quality of the water is improved.
  • the second purification facility may also include other facilities, such as sediment filters.
  • the sediment filter is generally provided, for example, at the most upstream part of the second purification equipment.
  • the concentrated raw water 11 is discharged from the drain port 51D.
  • the drain port 51D is connected to the proximal end of the drain pipe 33 .
  • the tip of the discharge pipe 33 is connected to the upstream side (flow pipe 31 side) of the portion of the branch pipe 32 where the second purification equipment is provided.
  • This circulation type filtration system 1 is applied to a hand-washing place as described above.
  • the user wants to wash his/her hands, the user operates the faucet 71 to open the closed faucet 71 .
  • the purified water 12 stored in the accumulator tank 60 has potential energy due to being in a relatively high position with respect to the faucet 71, and from the prada (not shown) arranged in the accumulator tank 60 Due to the pressure, the fluid flows from the accumulator tank 60 through the flow pipe 31 toward the faucet 71 and out of the faucet 71 . If the accumulator tank 60 is positioned lower than the faucet 71, then gravity will not contribute to the pressure exerted on the purified water 12 exiting the faucet 71, only the pressure from the prada.
  • the clean water 12 will contain soap components, and if the user's hands are dirty, the clean water 12 will contain oil and mud. Purified water 12 soiled in this manner is received by a saucer 72 .
  • the filter member 84 is composed of the bag filter 84A, the oil adsorption sheet 84B housed inside the bag filter 84A, and the mixture 84C of ion exchange resin and activated carbon.
  • those larger than the mesh of the bag filter 84A are filtered and captured by the bag filter 84A. Oil contained in the dirty purified water 12 is captured by the oil adsorption sheet 84B.
  • the sensor detects the water pressure of the purified water 12 in the accumulator tank 60 .
  • Data about the water pressure are sent to the computer 40 at all times.
  • the computer 40 sends drive signals to the main pump 21 and the sub-pump 22 via the connection lines 21A and 22A, respectively, when the water pressure of the purified water 12 becomes low (for example, when it falls below a certain value).
  • the main pump 21 and the sub-pump 22 are driven. That is, at this time, the main pump 21 and the sub-pump 22 are driven in conjunction with each other.
  • the main pump 21 When the main pump 21 is driven, the raw water 11 in the raw water tank 10 sucked by the main pump 21 is sent from the proximal end of the flow pipe 31 to the distal end of the flow pipe 31 .
  • the sub-pump 22 pumps the raw water 11 sent from the main pump 21 to the reverse osmosis membrane water purification unit 51 at a pressure that allows the water contained in the raw water 11 to overcome the reverse osmosis membrane 51B in the reverse osmosis membrane water purification unit 51. Send to 51.
  • the amount of raw water 11 sent from the main pump 21 to the flow pipe 31 per unit time is approximately the same as the amount of raw water 11 sent from the sub-pump 22 to the reverse osmosis membrane water purification unit 51 per unit time.
  • the main pump 21 and the sub-pump 22 are controlled by the computer 40 .
  • the raw water 11 sent from the raw water tank 10 into the channel pipe 31 by the main pump 21 is sent to the reverse osmosis membrane water purification unit 51 by the sub pump 22 without going to the branch pipe 32 .
  • the raw water 11 sent by the sub-pump 22 enters into the case 51A of the reverse osmosis membrane water purification unit 51 through an inlet 51C provided in the case 51A.
  • a high pressure is applied to the raw water 11 entering the case 51A from the inlet 51 .
  • water that is close to pure water contained in the raw water 11 flows out of the two spaces inside the case 51A divided by the reverse osmosis membrane 51B, where the inlet 51C and the outlet 51D communicate with each other. , passes through the reverse osmosis membrane 51B and oozes out into the space communicating with the purified water port 51E.
  • the raw water 11 is separated into the purified water 12 and the concentrated raw water 11 by the reverse osmosis membrane 51B in the case 51A. Then, the purified water 12 reaches the flow pipe 31 through the water purification port 51E, passes through the flow pipe 31, and reaches the accumulator tank 60. As shown in FIG. Although the purified water 12 in the accumulator tank 60 is reduced by opening the faucet 71, the reduced purified water in the accumulator tank 60 is replenished by supplying the purified water 12 from the reverse osmosis membrane water purification unit 51.
  • the water pressure of the purified water 12 in the accumulator tank 60 is constantly detected by the sensor, and water pressure data is constantly sent to the computer 40 .
  • the computer 40 sends the main pump 21 and the sub pump 22 via the connection line 21A or the connection line 22A. send a stop signal to stop their driving. Thereby, the main pump 21 and the sub-pump 22 stop driving.
  • the concentrated raw water 11 reaches the discharge pipe 33 through the discharge port 51D and reaches the branch pipe 32 from the discharge pipe 33 .
  • the concentrated raw water 11 proceeds downstream through the branch pipe 32 and reaches the second purification equipment.
  • the second purification equipment in this embodiment includes the ozone generator 91 and the ultraviolet sterilizer 92 .
  • the concentrated raw water 11 is supplied with ozone from an ozone generator 91 and irradiated with ultraviolet rays from an ultraviolet sterilization device 92 to be purified and improved in water quality.
  • the raw water 11 whose water quality has been improved advances downstream through the branch pipe 32 , exits from the tip of the branch pipe 32 , and drops into the raw water tank 10 .
  • the computer 40 drives only the main pump 21 for a predetermined length of time at predetermined intervals.
  • the computer 40 incorporates a timer, and when a predetermined time comes, it drives only the main pump 21 by sending a drive signal to the main pump 21 via the connection line 21A.
  • the main pump 21 tries to flow the raw water 11 stored in the raw water tank 10 from the base end of the flow pipe 31 toward the tip side of the flow pipe 31 .
  • the sub-pump 22 that is not driven at this time functions like a closed valve in the flow pipe 31 and does not allow the raw water 11 to pass through. Therefore, the raw water 11 flows into the branch pipe 32 branched from the flow pipe 31 .
  • the raw water 11 that has flowed into the branch pipe 32 proceeds downstream through the branch pipe 32 in the same manner as the concentrated raw water 11 described above, and reaches the second purification equipment.
  • the raw water 11 is supplied with ozone from an ozone generator 91 and is irradiated with ultraviolet rays from an ultraviolet sterilizer 92 to be purified and improved in water quality.
  • the raw water 11 whose water quality has been improved advances downstream through the branch pipe 32 , exits from the tip of the branch pipe 32 , and drops into the raw water tank 10 .
  • This process is performed, for example, every 30 minutes for 15 minutes. However, the time interval at which this process is started and the length of time each time this process is executed need not always be the same. Assuming that only the main pump 21 is driven for 15 minutes every 30 minutes, the raw water 11 stored in the raw water tank 10 is kept open for 12 hours out of 24 hours a day. It will be purified in the second purification facility regardless of whether or not it has been cleaned. By repeatedly performing purification in the second purification equipment, the raw water 11 in the raw water tank 10 is maintained in a purified state to some extent. , the purified water 12 purified by the purification equipment in the flow pipe 31 maintains good water quality. The process of driving only the main pump 21 is preferably performed for eight hours or more a day.
  • the quality of the raw water 11 in the raw water tank 10 can be kept high to some extent.
  • the process of driving only the main pump 21 can be prevented from being executed when the faucet 71 is in the open state. Even with this, for example, if the computer 40 is set to execute the process of driving only the main pump 21 even at night, the process of driving only the main pump 21 can be executed for eight hours or more a day. It is easy.
  • the driving and stopping of the main pump 21 and the sub-pump 22 are controlled using the computer 40, but if similar control is possible, a simpler mechanism, such as an accumulator It is also possible to replace the computer 40 with a sensor provided on the tank 60, a switch associated with the sensor, a timer for driving the main pump 21, and the like.
  • FIG. 4 shows an overall configuration diagram of the circulation filtration system 2 in the second embodiment.
  • the circulating filtration system 2 in this embodiment is used for a wash basin.
  • the circulation filtration system 2 of the second embodiment has a considerable portion in common with the circulation filtration system 1 of the first embodiment.
  • the circulation filtration system 2 of the second embodiment is configured in the same manner as the circulation filtration system 1 of the first embodiment, except for the portions described as differences below.
  • a circulation filtration system 2 of the second embodiment includes a raw water tank 10 .
  • the raw water tank 10 provided in the circulation filtration system 2 may be the same as the raw water tank 10 provided in the circulation filtration system 1 of the first embodiment, which is the case in this embodiment.
  • the main pump 21 and the sub-pump 22, which are similar to those provided in the circulation filtration system 1 of the first embodiment, are interlocked to drive the raw water tank 10.
  • a series of facilities are provided for circulating raw water 11 to the raw water tank 10 . That is, the circulation filtration system 2 of the second embodiment includes a main pump 21, a flow pipe 31, a sub-pump 22, purification equipment, an accumulator tank 60, and a faucet 71.
  • the main pump 21, the flow pipe 31, the sub-pump 22, the purification equipment, the accumulator tank 60, and the faucet 71 included in the circulation filtration system 2 of the second embodiment are the same as those of the circulation filtration system 1 of the first embodiment. They may be the same as those provided, but not limited to this, in this embodiment except for the parts described below.
  • the main pump 21, flow pipe 31, sub-pump 22, purification equipment, accumulator tank 60, and faucet 71 provided in the circulation filtration system 2 of the second embodiment differ from the first embodiment in the configuration of the purification equipment. Further, the position of the sub-pump 22 in the circulation filtration system 2 of the second embodiment is different from that of the first embodiment due to the configuration of the purification equipment.
  • the branch pipe 32 is not connected to the flow pipe 31 in the circulation filtration system 2 of the second embodiment. This is because the branch pipe 32 does not exist in the circulation filtration system 2 of the second embodiment, as will be described later.
  • the purification facility in the second embodiment is the same as in the first embodiment in that it is a facility for purifying the raw water 11 carried from the raw water tank 10 into purified water, as in the case of the first embodiment. .
  • the purification installation of the second embodiment includes at least one reverse osmosis membrane water purification unit.
  • the purification equipment includes a filter medium (for example, a sediment filter) that is not a reverse osmosis membrane, an ozone generator, an ultraviolet sterilizer, It may contain an aerator.
  • the reverse osmosis membrane water purification unit was only one reverse osmosis membrane water purification unit 51 provided in the flow path pipe 31, but the flow in the circulation filtration system 2 of the second embodiment
  • the pipeline 31 is provided with two reverse osmosis membrane water purification units, a reverse osmosis membrane water purification unit 51 and a reverse osmosis membrane water purification unit 52 .
  • the reverse osmosis membrane water purification unit 51 and the reverse osmosis membrane water purification unit 52 may or may not be the same. However, the principle by which they purify the raw water 11 is the one explained using FIG. 2 and is common.
  • the reverse osmosis membrane water purification unit 51 and the reverse osmosis membrane water purification unit 52 may differ only in the reverse osmosis membrane 51B in FIG.
  • the reverse osmosis membrane water purification unit 51 and the reverse osmosis membrane water purification unit 52 are the same.
  • the sub-pump 22 is provided upstream of the only one reverse osmosis membrane water purification unit 51 in the flow pipe 31 .
  • the sub-pump 22 is positioned between the two reverse osmosis membrane water purification units 51 and 52 in the flow pipe 31 .
  • the sub-pump 22 may be arranged upstream of the most downstream unit. Therefore, the sub-pump 22 may be arranged upstream of the reverse osmosis membrane water purification unit 51 .
  • This situation is the same even if there are two reverse osmosis membrane water purification units in the circulation filtration system 1 of the first embodiment.
  • the raw water 11 that has passed through the most downstream purification facility of the flow pipe 31 becomes the purified water 12 .
  • the raw water 11 becomes the purified water 12 by passing through the reverse osmosis membrane water purification unit 52 .
  • the circulation filtration system 2 of the second embodiment does not have the branch pipe 32 provided in the circulation filtration system 1 of the first embodiment.
  • the circulation filtration system 2 of the second embodiment includes the second flow pipe 34 and the second pump 23, which were not present in the circulation filtration system 1 of the first embodiment.
  • the second pump 23 is arranged in a suitable portion of the raw water tank 10 within the range of contact with the raw water 11 .
  • the second pump 23 may be equivalent to the main pump 21, and may be any pump capable of sending water.
  • the second pump 23 is connected to the proximal end of the second flow pipe 34 .
  • the second pump 23 guides the raw water 11 in the raw water tank 10 into the second flow pipe 34 and causes it to flow toward the tip side of the second flow pipe 34 .
  • the second pump 23 is connected to the computer 40 by a connecting line 23A, and includes a main pump 21 connected to the computer 40 via a connecting line 21A and a sub-pump 22 connected to the computer 40 via a connecting line 22A. Similarly, under the control of the computer 40, control of driving and stopping is performed. Note that the computer 40 in the second embodiment may be equivalent to the computer 40 in the first embodiment.
  • the second flow pipe 34 is a pipe for circulating the raw water 11 in the raw water tank 10 as described later.
  • the specifications of the second flow pipe 34 may be the same as those of the flow pipe 31, and are used in this embodiment, although not limited to this.
  • the raw water 11 coming out of the tip of the second flow pipe 34 drops into the raw water tank 10 in the same way as the raw water 11 coming out of the tip of the branch pipe 32 of the first embodiment.
  • the second purification equipment which was present in the branch pipe 32 in the first embodiment, is provided in the second flow pipe 34 in the circulation filtration system 2 of the second embodiment. Also in the case of the second embodiment, as in the first embodiment, the second purification equipment is equipment for purifying the raw water 11 flowing through the second flow pipe 34 .
  • the second purification equipment in the second embodiment only needs to be able to purify the raw water 11.
  • the ozone generator, the ultraviolet sterilizer, and the aerator. contains at least one of In this embodiment, although not limited to this, an ultraviolet sterilizer 92 and an aerator 93 are provided in the middle of the second flow pipe 34 as the second purification equipment.
  • the raw water 11 passing through the second flow pipe 34 is purified by the above-described principle by the ultraviolet sterilization device 92 and the aeration device 93, and the quality of the water is improved.
  • the second purification facility may also include other facilities, such as sediment filters.
  • the sediment filter is generally provided, for example, at the most upstream part of the second purification equipment.
  • the concentrated raw water 11 discharged from the reverse osmosis membrane water purification unit 51 is allowed to join the raw water 11 in the branch pipe 32 via the discharge pipe 33 .
  • the concentrated raw water 11 generated from the reverse osmosis membrane water purification unit 51 and the reverse osmosis membrane water purification unit 52 respectively flows through the discharge pipe 33 to the raw water 11 of the second flow pipe 34. It is designed to be merged.
  • the connection portion of the tip of the discharge pipe 33 to the second flow pipe 34 in the second embodiment is the same as the connection portion of the tip of the discharge pipe 33 to the branch pipe 32 in the first embodiment. It is on the upstream side of the part where the equipment is provided.
  • the raw water 11 concentrated in the reverse osmosis membrane water purification unit 51 and the reverse osmosis membrane water purification unit 52 reaches the second flow pipe 34 via the discharge pipe 33, and reaches the second flow pipe 34.
  • the water is purified by the provided second purification equipment, the water quality is improved, and then the raw water tank 10 is reached.
  • the circulation filtration system 2 of the second embodiment is applied to a hand-washing area as in the case of the first embodiment.
  • the user wants to wash his/her hands, the user operates the faucet 71 to open the closed faucet 71 .
  • the purified water 12 stored in the accumulator tank 60 flows out from the faucet 71 as in the case of the first embodiment.
  • the user washes his/her hands with the purified water 12 coming out of the faucet 71 .
  • the clean water 12 will contain soap components, and if the user's hands are dirty, the clean water 12 will contain oil and mud. Purified water 12 soiled in this manner is received by a saucer 72 .
  • Dirty purified water 12 received by the receiving tray 72 flows down through the drain pipe 83 by gravity from the drainage port of the receiving tray 72 toward the raw water tank 10 .
  • the purified water 12 that has become dirty on the way passes through a filter member 84 in the middle of the drain pipe 83 and is purified.
  • Purified water 12 that has been cleaned to some extent comes out of the tip of drain pipe 83 and drops into raw water tank 10. ⁇ So far, it is the same as the first embodiment.
  • the sensor detects the water pressure of the purified water 12 in the accumulator tank 60, as in the first embodiment.
  • Data about the water pressure are sent to the computer 40 at all times.
  • the computer 40 sends drive signals to the main pump 21 and the sub-pump 22 via the connection lines 21A and 22A, respectively, when the water pressure of the purified water 12 becomes low (for example, when it falls below a certain value).
  • the stopped main pump 21 and sub-pump 22 are driven. That is, at this time, the main pump 21 and the sub-pump 22 are driven in conjunction with each other.
  • the main pump 21 When the main pump 21 is driven, the raw water 11 in the raw water tank 10 sucked by the main pump 21 is sent from the proximal end of the flow pipe 31 to the distal end of the flow pipe 31 .
  • the main pump 21 feeds the raw water 11 to the reverse osmosis membrane water purification unit 51 while applying pressure enough to overcome the reverse osmosis membrane 51B in the reverse osmosis membrane water purification unit 51.
  • the sub-pump 22 feeds the raw water 11 to the reverse osmosis membrane water purification unit 52 while applying a pressure enough to push the water contained in the raw water 11 over the reverse osmosis membrane in the reverse osmosis membrane water purification unit 52 .
  • the main pump 21 and the sub-pump 22 are controlled by the computer 40 so that the flow rate per unit time of the raw water 11 flowed by the main pump 21 and the flow rate per unit time of the raw water 11 flowed by the sub-pump 22 are approximately the same. controlled.
  • the raw water 11 sent to the reverse osmosis membrane water purification unit 51 by the main pump 21 is separated into the concentrated raw water 11 and the purified raw water 11 close to the purified water 12 as described in the first embodiment. .
  • the purified raw water 11 is directed to the sub-pump 22 via the flow pipe 31 and sent to the reverse osmosis membrane water purification unit 52 by the sub-pump 22 .
  • the raw water 11 sent to the reverse osmosis membrane water purification unit 52 by the sub-pump 22 is separated into the concentrated raw water 11 and the purified water 12 by the same principle as the raw water 11 is purified by the reverse osmosis membrane water purification unit 51. be.
  • the purified water 12 generated from the reverse osmosis membrane water purification unit 52 reaches the flow pipe 31 and reaches the accumulator tank 60 through the flow pipe 31 .
  • the purified water 12 in the accumulator tank 60 which is reduced by opening the faucet 71, is replenished.
  • computer 40 stops main pump 21 and sub-pump 22 .
  • the concentrated raw water 11 generated from the reverse osmosis membrane water purification unit 51 and the reverse osmosis membrane water purification unit 52 reaches the second flow pipe 34 via the discharge pipe 33 .
  • the concentrated raw water 11 proceeds downstream through the second flow pipe 34 and reaches the second purification equipment.
  • the second purification equipment in the second embodiment includes the ultraviolet sterilization device 92 and the aeration device 93 .
  • the concentrated raw water 11 is irradiated with ultraviolet rays from an ultraviolet sterilizer 92 and aerated by an aeration device 93 to be purified and improved in water quality.
  • the raw water 11 whose water quality has been improved advances downstream through the second flow pipe 34 , exits from the tip of the second flow pipe 34 , and drops into the raw water tank 10 .
  • the computer 40 drives the second pump 23 for a predetermined length of time every predetermined time.
  • the computer 40 incorporates a timer, and drives the second pump 23 by sending a drive signal to the second pump 23 via the connection line 23A when a predetermined time comes.
  • the second pump 23 causes the raw water 11 accumulated in the raw water tank 10 to flow from the base end of the second flow pipe 34 toward the tip side of the second flow pipe 34. .
  • the raw water 11 flowing through the second flow pipe 34 advances downstream through the second flow pipe 34 and reaches the second purification facility in the same manner as the concentrated raw water 11 described above.
  • the raw water 11 is purified and improved in quality, as is the case with the concentrated raw water 11 .
  • the raw water 11 whose water quality has been improved advances downstream through the second flow pipe 34 , exits from the tip of the second flow pipe 34 , and drops into the raw water tank 10 .
  • the timing of execution of this process and the length of one time when this process is executed are determined by the process in which only the main pump 21 is driven in the circulation filtration system 1 of the first embodiment. and the length of each time when the process is executed.
  • the raw water in the raw water tank 10 is 11 will be repeatedly purified in the second purification facility.
  • the raw water 11 in the raw water tank 10 is kept purified to some extent. Therefore, even in the case of the second embodiment, the purified water 12, which is once stored in the accumulator tank 60 coming out of the faucet 71 and purified by the purification equipment in the flow pipe 31, maintains good water quality.
  • the main pump 21, the sub-pump 22, and further the second pump 23 can be driven simultaneously.
  • the computer 40 can be omitted and replaced with another simpler mechanism.

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Abstract

Provided is a practical cycle filtration system. Raw water 11 stored in a raw water tank 10 circulates by passing from the raw water tank 10 through a flow channel pipe 31 to be purified by a reverse osmosis membrane water purification unit 51 located in the middle of the flow channel pipe 31, then flowing toward a tap 71 and out of the tap 71 to be received by a bowl 72, and thereafter returning to the raw water tank 10. On the other hand, the raw water 11 stored in the raw water tank 10 circulates through a second flow channel pipe 34, regardless of whether the tap 71 is opened or closed, by means of a second pump 23 that is periodically driven, and is repeatedly purified by an ultraviolet sterilization device 92 and an aeration device 93 located in the middle of the second flow channel pipe 34.

Description

循環式濾過システムCirculating filtration system
 本発明は、同じ水を繰返し使用する循環式濾過システムに関する。 The present invention relates to a circulation filtration system that uses the same water repeatedly.
 例えば、山奥の工事現場において手洗い場が必要となる。そのような場所では、同じ水を繰返し使用する循環式濾過システムが必要とされる。
 なぜなら、そのような場所では、綺麗な水、もっと言えば水自体を確保することが難しいことがあるためであり、また、手洗い後の汚れた水を環境中に放出することが難しいためである。
 したがって、そのような場所では、同じ水を繰返し使用することによって、必要な水の量を減らすことができ、且つ環境中に放出される汚れた水の量を減らすことができるという利点を持つ、循環式濾過システムが重宝される。
 もちろんこの2つの利点の一方のみが要求されるような場合においても、循環式濾過システムは利用可能であるし、利用される場合がある。
For example, a hand-washing place is required at a construction site deep in the mountains. Such locations require a recirculating filtration system that uses the same water repeatedly.
This is because it is sometimes difficult to secure clean water, or even water itself, in such places, and it is also difficult to release dirty water after washing hands into the environment. .
Thus, in such locations, repeated use of the same water has the advantage of reducing the amount of water required and reducing the amount of dirty water released into the environment. A circulation type filtration system is useful.
Of course, recirculating filtration systems are available and may be used where only one of these two advantages is desired.
 大雑把にいえば、循環式濾過システムは、次のようなものである。手洗い場に循環式濾過システムが用いられる場合を例にとって説明する。
 循環式濾過システムは、原水を貯める原水タンクを備えている。原水タンクには、原水を循環させるための流路を構成する流路管の基端が接続されている。流路管のどこかにポンプが設けられており、ポンプによって、原水タンク中の原水は、流路管の基端側から先端側に向けて送られる。
 流路管の途中には、原水を浄化するための浄化設備が適宜設けられている。浄化設備は、例えば、原水中の固形物を除去するための濾過装置であり、或いは原水中の化学物質や微生物(細菌、ウイルス等)を除去するためのオゾン発生装置や紫外線殺菌装置である。原水は、浄化設備を通過することにより、浄水となる。
 流路管の先端には、蛇口が設けられており、蛇口の下には例えばシンクである、受皿が設けられている。蛇口を操作すると、流路管内の浄水が流れ出る。その浄水で手洗いをすることによって生じた汚水が、受皿によって受けられる。
 受皿で受けられた汚水は、原水タンクに至って原水に戻るようになっている。例えば、受皿が原水タンクの真上に設けられているのであれば、受皿が受けた汚水は、その真下の原水タンクに落下する。何らかの管によって受皿と原水タンクを接続し、その管を介して、受皿から原水タンクに汚水を導くようになっている場合もある。
Roughly speaking, the circulation filtration system is as follows. A case where a circulating filtration system is used in a hand-washing area will be described as an example.
The circulation filtration system has a raw water tank that stores raw water. The raw water tank is connected to the base end of a flow channel pipe forming a flow channel for circulating raw water. A pump is provided somewhere in the flow pipe, and the raw water in the raw water tank is sent from the base end side of the flow pipe toward the tip end side by the pump.
Purification equipment for purifying raw water is appropriately provided in the middle of the flow pipe. The purification equipment is, for example, a filtration device for removing solids in the raw water, or an ozone generator or an ultraviolet sterilization device for removing chemical substances and microorganisms (bacteria, viruses, etc.) in the raw water. Raw water becomes purified water by passing through purification equipment.
A faucet is provided at the tip of the flow pipe, and a saucer, for example a sink, is provided under the faucet. When the faucet is operated, purified water in the channel pipe flows out. Dirty water generated by washing hands with the purified water is received by the tray.
The sewage received by the tray reaches the raw water tank and returns to the raw water. For example, if the tray is provided directly above the raw water tank, the sewage received by the tray drops into the raw water tank directly below. In some cases, a tube of some kind connects the pan and the raw water tank, and the sewage is led from the pan to the raw water tank via the tube.
 上述の如き循環式濾過システムは、少なくとも原理上は成立し得るものの、需要の割には十分に普及しているとは言えない。
 その理由は、循環式濾過システムで得られる浄水の質を十分なものとするのが難しいことにある。上述したように、循環式濾過システムでは、浄化設備を通過させることによって、原水を浄水にする。ここで、循環式濾過システムが、例えば、手洗い場を用途とする場合においては、原水には泥や油、或いは石鹸の成分等が含まれることがある。そのような原水を質の高い浄水にするための浄化設備を準備するのは、技術的になかなか難しい。しかも、循環式濾過システムでは、原水が繰返し利用されるから尚更である。
Although the circulation type filtration system as described above can be established at least in principle, it cannot be said that it is sufficiently popular for the demand.
The reason for this is that it is difficult to obtain a sufficient quality of purified water from a circulation filtration system. As described above, in the circulation filtration system, raw water is purified by passing it through purification equipment. Here, when the circulating filtration system is used, for example, as a hand-washing place, the raw water may contain mud, oil, soap components, or the like. Technically, it is quite difficult to prepare purification equipment for converting such raw water into high-quality purified water. Moreover, in the circulation type filtration system, raw water is repeatedly used, which is all the more so.
 本願発明は、汚れがある程度酷い原水であっても質の高い浄水を得ることのできるような、実用に足る循環式濾過システムを提供することをその課題とする。 The object of the present invention is to provide a practical circulation filtration system that can obtain high-quality purified water even if the raw water is heavily contaminated to some extent.
 本願発明は以下のようなものである。本願発明は2つに大分することができるので、それらを便宜的に第1発明、第2発明と呼ぶこととする。
 第1発明は、以下のようなものである。
 第1発明は、循環させて繰返し使用される水である原水を貯める原水タンクと、前記原水を循環させるための流路を構成する、その基端が前記原水タンクに接続された管である流路管と、前記流路管の途中に設けられた、前記原水を浄化して浄水にするための設備であり、少なくとも1つの逆浸透膜浄水ユニットを含む浄化設備と、前記流路管における、前記流路管に対して最も先端側に位置する前記逆浸透膜浄水ユニットの手前側の部分に設けられた、それが駆動した場合に、前記流路管内の前記原水を、前記流路管内において前記流路管の先端側に流すサブポンプと、前記サブポンプが駆動したときに前記サブポンプと連動して駆動する、前記流路管の前記原水タンク内の前記原水と接する部分に設けられた、それが駆動した場合に、前記原水タンク内の原水を前記流路管の先端側に流すメインポンプと、前記流路管の先端に設けられた、前記浄水の前記流路管からの排出の許否を選択することのできるようにされた蛇口と、前記蛇口から排出された前記浄水を受ける受皿と、を備えており、前記受皿で受けた前記浄水が前記原水タンクに至るようにされている、循環式濾過システムである。
 そしてこの循環式濾過システムは、前記原水を循環させるための流路を構成する、その基端が前記流路管における前記サブポンプの手前に接続されることで前記流路管から分岐させられた管である分岐管と、前記分岐管の途中に設けられた、前記原水を浄化するための設備である第2浄化設備と、を備えている。また、前記分岐管の先端から出た浄化された原水が、前記原水タンクに至るようにされているとともに、前記メインポンプは、前記サブポンプと独立して駆動させられるようになっているとともに、前記メインポンプが駆動し、且つ前記サブポンプが停止しているときには、前記サブポンプは前記原水を通過させないようになっている。
The present invention is as follows. Since the present invention can be roughly divided into two, they will be called the first invention and the second invention for convenience.
The first invention is as follows.
A first invention comprises a raw water tank for storing raw water, which is water that is to be circulated and used repeatedly, and a pipe that constitutes a flow path for circulating the raw water and whose base end is connected to the raw water tank. a conduit, a facility for purifying the raw water into purified water provided in the middle of the conduit, the purification facility including at least one reverse osmosis membrane water purification unit, and in the conduit, provided in the front side portion of the reverse osmosis membrane water purification unit located on the most distal side with respect to the flow pipe, when it is driven, the raw water in the flow pipe is transferred into the flow pipe a sub-pump for flowing to the tip side of the flow pipe; and a portion of the flow pipe that is driven in conjunction with the sub-pump when the sub-pump is driven, and is provided at a portion of the flow pipe that contacts the raw water in the raw water tank. A main pump that, when driven, causes the raw water in the raw water tank to flow to the tip side of the flow pipe, and a selection of permission or denial of discharge of the purified water from the flow pipe provided at the tip of the flow pipe. and a receptacle for receiving the purified water discharged from the faucet, and the purified water received by the receptacle reaches the raw water tank. Filtration system.
In this circulation filtration system, a pipe branched from the flow pipe by connecting the base end of the flow pipe before the sub-pump to form a flow channel for circulating the raw water. and a second purification facility, which is provided in the middle of the branch pipe and is a facility for purifying the raw water. Further, the purified raw water coming out of the tip of the branch pipe reaches the raw water tank, and the main pump is driven independently of the sub-pump. When the main pump is driven and the sub-pump is stopped, the sub-pump does not allow the raw water to pass through.
 第1発明による循環式濾過システムは、流路管を備えている。流路管の基端は原水を貯める原水タンクに接続されており、流路管の先端には、蛇口が設けられている。蛇口の下には受皿があり、受皿で受けられた浄水は、原水タンクに戻るようになっている。この循環式濾過システムは、基本的に、このような構成によって、原水を循環させるから、原水の量が少なくて済み、また、汚水を環境中に放出することもない。
 もっとも、原水を単に循環させるだけでは、蛇口から出る水が綺麗なものとはならない。そのようなことを防止するために、流路管の途中には、原水を浄化して浄水にするための設備である浄化設備を備えている。浄化設備は、原水を浄化するための設備であれば良く、その詳細は問わないが、逆浸透膜浄水ユニットを少なくとも1つ含んでいる。浄化設備を構成するものの例は、逆浸透膜浄水ユニットではない濾材、オゾン発生装置、紫外線殺菌装置、曝気装置である。
 第1発明の循環式濾過システムでは、原水は、メインポンプとサブポンプによって、流路管内を循環する。メインポンプは、流路管の基端に位置しており、原水タンク内の原水を流路管の先端側に向けて流す機能を有している。他方、サブポンプは、流路管の途中、より正確には最も先端側に位置する逆浸透膜浄水ユニットの手前側に位置しており、サブポンプよりも下流側に位置する逆浸透膜浄水ユニット内の原水中の水に、逆浸透膜浄水ユニット内の逆浸透膜を乗り越えさせるために必要な圧力を与える機能を有している。
 サブポンプは、蛇口が開放されることにより、流路管の逆浸透膜浄水ユニットよりも先端側の部分の原水(又は浄水)の量が減ったときに駆動され、逆浸透膜浄水ユニットの手前の原水を、逆浸透膜浄水ユニットよりも先の部分に供給するようになっている。そうすると、今度は、流路管の逆浸透膜浄水ユニットよりも手前側の原水の量が減るので、メインポンプがその部分に、原水タンクから原水を供給するようになっている。それが可能なように、メインポンプは、サブポンプが駆動するときには、サブポンプと連動して駆動するようになっている。
 第1発明による循環式濾過システムのここまでに説明した構成は、場合にもよるが、従来の循環式濾過システムの構成と概ね変わらないものとすることができる。
A circulation filtration system according to the first invention comprises a flow tube. A base end of the flow pipe is connected to a raw water tank for storing raw water, and a tap is provided at a tip of the flow pipe. There is a tray under the faucet, and the purified water received by the tray is returned to the raw water tank. Since the circulation type filtration system basically circulates the raw water with such a configuration, the amount of raw water can be reduced and no polluted water is discharged into the environment.
However, simply circulating the raw water does not make the water coming out of the faucet clean. In order to prevent such a problem, purification equipment, which is equipment for purifying raw water into purified water, is provided in the middle of the flow pipe. The purification equipment may be equipment for purifying raw water, and the details thereof are not limited, but at least one reverse osmosis membrane water purification unit is included. Examples of what constitutes the purification equipment are filter media that are not reverse osmosis membrane water purification units, ozone generators, ultraviolet sterilizers, and aerators.
In the circulation filtration system of the first invention, raw water is circulated in the flow pipe by the main pump and the sub-pump. The main pump is positioned at the proximal end of the flow pipe and has a function of flowing the raw water in the raw water tank toward the distal end of the flow pipe. On the other hand, the sub-pump is located in the middle of the flow pipe, more precisely, on the front side of the reverse osmosis membrane water purification unit located on the most distal side, and in the reverse osmosis membrane water purification unit located on the downstream side of the sub-pump. It has the function of applying the pressure necessary to force the water in the raw water to pass over the reverse osmosis membrane in the reverse osmosis membrane water purification unit.
By opening the faucet, the sub-pump is driven when the amount of raw water (or purified water) in the portion of the flow pipe on the tip side of the reverse osmosis membrane water purification unit is reduced, and is driven before the reverse osmosis membrane water purification unit. Raw water is supplied to the part ahead of the reverse osmosis membrane water purification unit. Then, since the amount of raw water on the front side of the reverse osmosis membrane water purification unit in the flow channel decreases, the main pump supplies raw water from the raw water tank to that portion. To enable this, the main pump is driven in conjunction with the sub-pump when the sub-pump is driven.
The configuration described so far of the circulation filtration system according to the first invention may be substantially the same as the configuration of the conventional circulation filtration system, although it depends on the case.
 第1発明の循環式濾過システムは、分岐管を備えている。分岐管は、その基端が流路管におけるサブポンプの手前に接続されることで流路管から分岐させられた管である。分岐管の先端から出た原水は、原水タンクに戻るようになっている。
 分岐管の途中には、第2浄化設備が設けられている。第2浄化設備は、原水を浄化するための設備である。第2浄化設備は、原水を浄化するための設備であれば良く、その詳細は問わない。第2浄化設備は、例えば、逆浸透膜浄水ユニットではない濾材、オゾン発生装置、紫外線殺菌装置、曝気装置のうちの少なくとも1つを含んでいても良い。オゾン発生装置は、分岐管を通過する原水に対してオゾンを供給する装置である。紫外線殺菌装置は、分岐管を通過する原水に対して紫外線を照射する装置である。曝気装置は、分岐管を通過する原水に対して空気の泡を供給する装置である。曝気装置は例えば、マイクロバブルやナノバブルを原水に対して供給する。オゾン発生装置、紫外線殺菌装置、曝気装置は、それぞれ異なる機序ではあるが、原水の水質を改善する。
 第1発明による循環式濾過システムでは、メインポンプによって、原水が分岐管内を循環する。上述したように、メインポンプは、サブポンプが駆動したときにサブポンプに連動して駆動するようになっているが、他方、サブポンプと独立して駆動することも可能とされている。サブポンプが駆動していない、つまり停止しているときにメインポンプが駆動すると、サブポンプは閉まった弁のように機能して原水を通過させない。
 そのような構成により、サブポンプを停止した状態でメインポンプを駆動させると、原水は、原水タンクから流路管内に至り、サブポンプの手前で分岐させられた分岐管に流れ込んで分岐管内を流れ、原水タンクに戻ることになる。このとき、原水は、分岐管の途中にある第2浄化設備によって浄化される。
 本願発明者の考えによれば、従来の循環式濾過システムにおいて原水を綺麗に保つことが難しかったのは、以下の理由による。即ち、従来の循環式濾過システムにおける原水タンクから蛇口に至る、流路管によって作られる原水の一連の循環経路は、蛇口が開放されたときにしか原水が流れないから、浄化を行うときに必要となる流れが原水に生じる時間が極めて限られており、それ故原水の浄化を十分に行うのが難しいのである。他方、流路管によって形成される上述の循環経路とは異なる循環経路を作り、そこで原水の浄化を行うこととすれば、蛇口の開放とは無関係に、原水の浄化を行うことが可能となり、必要なだけ原水を浄化することができるから、原水を十分に浄化した浄水を得ることができるのである。
 そのような考えから、本願発明者は、流路管とは異なる原水の循環経路として分岐管を採用し、且つ分岐管を流れる原水を浄化するための設備として第2浄化設備を採用することにしたのである。しかも、第1発明において上述の如き分岐管を採用したとしても、分岐管に原水を流す場合に必要なのは、元々存在していたメインポンプとサブポンプのみであり、新たなポンプを採用する必要がないから、コスト面でも有利である。
The circulation filtration system of the first invention comprises a branch pipe. A branch pipe is a pipe branched from a flow pipe by connecting its proximal end to the flow pipe before the sub-pump. The raw water coming out of the tip of the branch pipe is returned to the raw water tank.
A second purification facility is provided in the middle of the branch pipe. The second purification equipment is equipment for purifying raw water. The second purification equipment may be equipment for purifying raw water, and the details thereof are not limited. The second purification equipment may include, for example, at least one of a filtering material that is not a reverse osmosis membrane water purification unit, an ozone generator, an ultraviolet sterilizer, and an aerator. The ozone generator is a device that supplies ozone to the raw water passing through the branch pipe. The ultraviolet sterilizer is a device that irradiates raw water passing through a branch pipe with ultraviolet rays. An aerator is a device that supplies air bubbles to raw water passing through a branch pipe. The aerator supplies, for example, microbubbles or nanobubbles to the raw water. Ozone generators, ultraviolet sterilizers, and aerators improve the quality of raw water by different mechanisms.
In the circulation filtration system according to the first invention, raw water is circulated through the branch pipes by the main pump. As described above, the main pump is driven in conjunction with the sub-pump when the sub-pump is driven, but it can also be driven independently of the sub-pump. If the main pump is activated while the sub-pump is not activated, i.e. stopped, the sub-pump acts like a closed valve and does not allow raw water to pass through.
With such a configuration, when the main pump is driven while the sub-pump is stopped, the raw water flows from the raw water tank into the channel pipe, flows into the branch pipe branched before the sub-pump, flows through the branch pipe, and flows into the branch pipe. going back to the tank. At this time, the raw water is purified by the second purification equipment in the middle of the branch pipe.
According to the idea of the inventor of the present application, the reason why it was difficult to keep the raw water clean in the conventional circulation filtration system is as follows. That is, in the conventional circulation filtration system, the series of circulation paths of the raw water created by the flow pipe from the raw water tank to the faucet are necessary for purification because the raw water flows only when the faucet is opened. The time during which such a flow occurs in the raw water is very limited, and therefore it is difficult to sufficiently purify the raw water. On the other hand, if a circulation path different from the above-mentioned circulation path formed by the flow pipe is created and the raw water is purified there, it becomes possible to purify the raw water regardless of whether the faucet is open. Since the raw water can be purified as much as necessary, it is possible to obtain sufficiently purified raw water.
Based on this idea, the inventor of the present application adopted a branch pipe as a raw water circulation path different from the flow pipe, and adopted the second purification equipment as equipment for purifying the raw water flowing through the branch pipe. I did. Moreover, even if the branch pipe as described above is adopted in the first invention, only the originally existing main pump and sub-pump are required to flow the raw water through the branch pipe, and there is no need to adopt a new pump. Therefore, it is advantageous in terms of cost.
 第1発明の循環式濾過システムにおける前記メインポンプは、前記サブポンプとは独立して、一日に8時間以上駆動するようになっていても構わない。
 この程度メインポンプを駆動させることとすれば、原水が第2浄化設備によって良く浄化されるので、蛇口から出る浄水の質を高く保つことが可能となる。もちろん、メインポンプをサブポンプから独立させて駆動させる時間を、8時間より長くすることも可能であり、そうすることにより、循環式濾過システムの蛇口から出る浄水の質をより高くすることが可能となる。
 前記メインポンプは、所定の時間毎に、所定の時間長さだけ駆動するようになっていても構わない。メインポンプが間隔をおいて駆動する「所定の時間」は同じでもそうでなくても良い。メインポンプが一回に駆動する「所定の時間」は同じでもそうでなくても良い。このようにすることにより、メインポンプがサブポンプと独立して駆動する時間の割合を、所望の割合に決定することが可能となる。
The main pump in the circulation filtration system of the first invention may be driven for eight hours or more a day independently of the sub-pump.
By driving the main pump to this extent, the raw water is well purified by the second purification equipment, so that the quality of purified water coming out of the faucet can be maintained at a high level. Of course, it is also possible to make the main pump independent of the sub-pump for longer than 8 hours, and by doing so, it is possible to improve the quality of the purified water that comes out of the faucet of the circulation filtration system. Become.
The main pump may be driven for a predetermined length of time every predetermined time. The "predetermined time" at which the main pump is driven at intervals may or may not be the same. The "predetermined time" during which the main pump is driven at one time may or may not be the same. By doing so, it is possible to determine the ratio of time for which the main pump is driven independently of the sub-pump to a desired ratio.
 第2発明による循環式濾過システムは以下のようなものである。
 第2発明による循環式濾過システムは、循環させて繰返し使用される水である原水を貯める原水タンクと、前記原水を循環させるための流路を構成する、その基端が前記原水タンクに接続された管である流路管と、前記流路管の途中に設けられた、前記原水を浄化して浄水にするための設備であり、少なくとも1つの逆浸透膜浄水ユニットを含む浄化設備と、前記流路管における、前記流路管に対して最も先端側に位置する前記逆浸透膜浄水ユニットの手前側の部分に設けられた、それが駆動した場合に、前記流路管内の前記原水を、前記流路管内において前記流路管の先端側に流すサブポンプと、前記サブポンプが駆動したときに前記サブポンプと連動して駆動する、前記流路管の前記原水タンク内の前記原水と接する部分に設けられた、それが駆動した場合に、前記原水タンク内の原水を前記流路管の先端側に流すメインポンプと、前記流路管の先端に設けられた、前記浄水の前記流路管からの排出の許否を選択することのできるようにされた蛇口と、前記蛇口から排出された前記浄水を受ける受皿と、を備えており、前記受皿で受けた前記浄水が前記原水タンクに至るようにされている。
 そして、第2発明の循環式濾過システムは、前記原水を循環させるための流路を構成する、その基端が前記原水タンクに接続された管である、前記流路管とは異なる第2流路管と、前記第2流路管の前記原水タンク内の前記原水と接する部分に設けられた、それが駆動した場合に、前記原水タンク内の原水を前記第2流路管の先端側に流す第2ポンプと、前記第2流路管の途中に設けられた、前記原水を浄化するための設備である第2浄化設備と、を備えている。また、第2発明の循環式濾過システムでは、前記第2流路管の先端から出た浄化された原水が、前記原水タンクに至るようにされているとともに、前記第2ポンプは、前記メインポンプ及び前記サブポンプと独立して駆動させられるようになっている。
The circulation type filtration system according to the second invention is as follows.
The circulation filtration system according to the second invention comprises a raw water tank for storing raw water, which is water to be circulated and used repeatedly, and a flow path for circulating the raw water, the base end of which is connected to the raw water tank. a flow pipe, which is a pipe that is a flat pipe; a purification equipment, which is a facility for purifying the raw water into purified water and which is provided in the middle of the flow pipe, and which includes at least one reverse osmosis membrane water purification unit; a portion of the flow pipe provided on the front side of the reverse osmosis membrane water purification unit located on the most distal side with respect to the flow pipe, and when it is driven, the raw water in the flow pipe is a sub-pump for flowing to the tip end side of the flow pipe in the flow pipe; a main pump that, when driven, causes the raw water in the raw water tank to flow to the tip side of the flow pipe; The apparatus comprises a faucet capable of selecting permission or denial of discharge, and a tray for receiving the purified water discharged from the faucet, and the purified water received by the tray reaches the raw water tank. ing.
In the circulation filtration system of the second invention, a second flow different from the flow pipe is a pipe having a base end connected to the raw water tank, which constitutes the flow channel for circulating the raw water. and a passage pipe provided at a portion of the second passage pipe in contact with the raw water in the raw water tank, and when the pipe is driven, the raw water in the raw water tank flows to the tip side of the second passage pipe. A second pump for flowing the raw water and a second purification equipment for purifying the raw water provided in the middle of the second flow pipe are provided. Further, in the circulation filtration system of the second invention, the purified raw water discharged from the tip of the second flow pipe reaches the raw water tank, and the second pump is the main pump. and driven independently of the sub-pump.
 第2発明の循環式濾過システムは、概ね第1発明の循環式濾過システムと同様の構成を採用している。
 第2発明の循環式濾過システムも、第1発明による循環式濾過システムと同様に、流路管を備えている。流路管の基端は、第1発明の循環式濾過システムの場合と同様に、原水を貯める原水タンクに接続されており、流路管の先端には、蛇口が設けられている。蛇口の下には受皿があり、受皿で受けられた浄水は、原水タンクに戻るようになっている。したがって、第2発明の循環式濾過システムは、第1発明の場合と同様に原水を循環させるから、原水の量が少なくて済み、また、汚水を環境中に放出することもない。
 また、第2発明の循環式濾過システムは、第1発明の循環式濾過システムと同様に、流路管の途中に、原水を浄化して浄水にするための設備である浄化設備を備えている。第2発明の循環式濾過システムにおける浄化設備は、第1発明の循環式濾過システムにおける浄化設備と同様である。
 第2発明の循環式濾過システムは、第1発明の循環式濾過システムと同様に、原水は、メインポンプとサブポンプによって、流路管内を循環する。メインポンプ、サブポンプともに、第2発明の循環式濾過システムにおけるそれらは、第1発明におけるそれらと同様である。ただし、第2発明におけるメインポンプは、第1発明における循環式濾過システムの場合とは異なり、サブポンプから独立して駆動することはない。
The circulation filtration system of the second invention employs substantially the same configuration as the circulation filtration system of the first invention.
The circulation-type filtration system of the second invention also has flow pipes, like the circulation-type filtration system of the first invention. The base end of the channel pipe is connected to a raw water tank for storing raw water, as in the case of the circulation filtration system of the first invention, and the tip of the channel pipe is provided with a faucet. There is a tray under the faucet, and the purified water received by the tray is returned to the raw water tank. Therefore, since the circulation type filtration system of the second invention circulates the raw water in the same manner as in the first invention, the amount of raw water can be reduced, and polluted water is not discharged into the environment.
In addition, the circulation filtration system of the second invention is equipped with purification equipment, which is equipment for purifying raw water into purified water, in the middle of the flow pipe, as in the circulation filtration system of the first invention. . The purification equipment in the circulation filtration system of the second invention is the same as the purification equipment in the circulation filtration system of the first invention.
In the circulation filtration system of the second invention, raw water is circulated in the flow pipe by a main pump and a sub-pump, as in the circulation filtration system of the first invention. Both the main pump and the sub-pump in the circulation filtration system of the second invention are the same as those in the first invention. However, unlike the circulation filtration system of the first invention, the main pump in the second invention is not driven independently of the sub-pump.
 第2発明の循環式濾過システムは、第1発明の循環式濾過システムの場合と異なり、分岐管を備えていない。その代わりに、第2発明の循環式濾過システムは、第2流路管を備えている。
 第2流路管は、原水を循環させるための流路を構成する、その基端が原水タンクに接続された管である。第2発明の循環式濾過システムでは、第2流路管の先端から出た浄化された原水が、原水タンクに至るようにされている。そして、第2流路管の途中には、原水を浄化するための設備である第2浄化設備が設けられている。第2発明の循環式濾過システムにおける第2浄化設備は、第1発明の循環式濾過システムにおける第2浄化設備と同様のものとすることができる。
 第2発明では、第2流路管内の原水を、第2流路管の原水タンク内の原水と接する部分に設けられた、それが駆動した場合に、原水タンク内の原水を第2流路管の先端側に流す第2ポンプを用いて循環させることとしている。そして、第2ポンプは、メインポンプ及びサブポンプと独立して駆動させられるようになっている。
 つまり、第2発明の循環式濾過システムでは、原水タンクから出て原水タンクに戻る流路を形成する流路管とは異なる、原水タンクから出て原水タンクに戻る流路を形成する第2流路管を設けることにより、第2流路管の途中にある第2浄化設備によって、蛇口が開放されるか否か、つまり、流路管内の原水或いは浄水が動くか否かとは無関係に、原水タンク内の原水を浄化できるようにしているのである。
 第2発明の循環式濾過システムでは、第1発明の循環式濾過システムとは異なり、第2ポンプが必要となる。他方、第2発明の循環式濾過システムでは、第1発明の循環式濾過システムとは異なり、サブポンプ及びサブポンプと連動するメインポンプが駆動しているときにも、第2ポンプにより第2流路管内で原水を循環させることができる。
Unlike the circulation filtration system of the first invention, the circulation filtration system of the second invention does not have branch pipes. Instead, the circulation filtration system of the second invention comprises a second flow pipe.
The second flow pipe is a pipe that forms a flow channel for circulating raw water and has a base end connected to the raw water tank. In the circulation filtration system of the second invention, the purified raw water coming out of the tip of the second flow pipe reaches the raw water tank. A second purification facility, which is a facility for purifying the raw water, is provided in the middle of the second flow pipe. The second purification equipment in the circulation filtration system of the second invention can be the same as the second purification equipment in the circulation filtration system of the first invention.
In the second invention, the raw water in the second flow pipe is provided in a portion of the second flow pipe in contact with the raw water in the raw water tank. Circulation is carried out using a second pump that flows to the tip side of the tube. The second pump is driven independently of the main pump and sub-pump.
That is, in the circulation filtration system of the second invention, the second flow forming the flow path that exits from the raw water tank and returns to the raw water tank is different from the flow path pipe that forms the flow path that exits from the raw water tank and returns to the raw water tank. By providing the channel pipe, the raw water can be discharged regardless of whether the faucet is opened by the second purification equipment in the middle of the second channel pipe, that is, regardless of whether the raw water or purified water in the channel pipe moves. This allows the raw water in the tank to be purified.
Unlike the circulation filtration system of the first invention, the circulation filtration system of the second invention requires a second pump. On the other hand, in the circulation filtration system of the second invention, unlike the circulation filtration system of the first invention, even when the sub-pump and the main pump interlocking with the sub-pump are driven, the second pump causes the second flow pipe to be filled. can circulate the raw water.
 第2発明の循環式濾過システムにおける第2ポンプは、一日に8時間以上駆動するようになっていても構わない。
 この程度第2ポンプを駆動させることとすれば、原水が第2浄化設備によって良く浄化されるので、蛇口から出る浄水の質を高く保つことが可能となる。もちろん、第2ポンプをサブポンプから独立させて駆動させる時間を、8時間より長くすることも可能であり、そうすることにより、循環式濾過システムの蛇口から出る浄水の質をより高くすることが可能となる。
 前記第2ポンプは、所定の時間毎に、所定の時間長さだけ駆動するようになっていても構わない。第2ポンプが間隔をおいて駆動する「所定の時間」は同じでもそうでなくても良い。第2ポンプが一回に駆動する「所定の時間」は同じでもそうでなくても良い。このようにすることにより、第2ポンプが、メインポンプ及びサブポンプと独立して駆動する時間の割合を、所望の割合に決定することが可能となる。
The second pump in the circulation filtration system of the second invention may be driven for eight hours or more a day.
If the second pump is driven to this degree, the raw water is well purified by the second purification equipment, so it is possible to keep the quality of purified water coming out of the faucet high. Of course, it is also possible to make the second pump independent of the sub-pump for a period longer than 8 hours, and by doing so, it is possible to improve the quality of the purified water coming out of the faucet of the circulation filtration system. becomes.
The second pump may be driven for a predetermined length of time at predetermined time intervals. The "predetermined time" that the second pump is driven at intervals may or may not be the same. The "predetermined time" for which the second pump is driven at one time may or may not be the same. By doing so, it becomes possible to determine the ratio of the time that the second pump drives independently of the main pump and the sub-pump to a desired ratio.
 この段落の記載は、第1発明、第2発明の循環式濾過システムに共通する。
 第1発明、第2発明の循環式濾過システムは、前記受皿から前記原水タンクへ至る浄水を通過させるための、浄水を濾過するための濾材を備えていてもよい。受皿から原水タンクに戻る浄水は、例えば循環式濾過システムが手洗い場に応用されている場合等では、泥や石鹸の成分を含む等して既に汚れた状態となっている。汚れた浄水をそのまま原水タンクに戻すのではなく、濾材を通過させてから原水タンクに戻すようにすることで、原水を綺麗に保ちやすくなる。
 ここで、受皿から原水タンクへ戻る浄水を通過させるための濾材は、例えば、オイル吸着シート、イオン交換樹脂、活性炭のうちの少なくとも一つを含んでいてもよい。オイル吸着シートは、それを通過する水に含まれている油を除去するのに有用であり、イオン交換樹脂は、それを通過する水に含まれている界面活性剤を除去するのに有用であり、活性炭は、それを通過する水に含まれている重金属類及び悪臭の原因物質を除去するのに有用である。濾材は、オイル吸着シート、イオン交換樹脂、活性炭のうちの2つ以上、或いはすべてを含んでいても良い。
 受皿から原水タンクへ戻る浄水を通過させるための前記濾材は、バッグフィルターに内蔵されていてもよい。これにより、バッグフィルターごと濾材を交換できるようになるので、濾材の交換の手間、コストを下げることが可能となる。
The description in this paragraph is common to the circulation filtration systems of the first and second inventions.
The circulation filtration system of the first invention and the second invention may be provided with a filter medium for filtering the purified water for passing the purified water from the receiving tray to the raw water tank. Purified water returning from the receiving tray to the raw water tank is already in a dirty state, such as containing mud and soap components, for example, when a circulation filtration system is applied to a hand-washing area. Instead of returning dirty purified water to the raw water tank as it is, it is easier to keep the raw water clean by returning it to the raw water tank after passing it through a filter medium.
Here, the filter medium for passing purified water returning from the receiving tray to the raw water tank may include at least one of an oil adsorption sheet, an ion exchange resin, and activated carbon, for example. The oil adsorption sheet is useful for removing oil contained in water passing through it, and the ion exchange resin is useful for removing surfactant contained in water passing through it. Yes, activated carbon is useful in removing heavy metals and odor causing substances contained in water passing through it. The filter medium may contain two or more of oil adsorption sheet, ion exchange resin and activated carbon, or all of them.
The filter medium for passing purified water returning from the receiving tray to the raw water tank may be incorporated in a bag filter. As a result, the filter medium can be replaced together with the bag filter, so that the labor and cost of replacing the filter medium can be reduced.
第1実施形態による循環式濾過システムの全体構成を概略的に示す図。The figure which shows roughly the whole structure of the circulation-type filtration system by 1st Embodiment. 図1に示した循環式濾過システムに含まれる逆浸透膜浄水ユニットの構成を概念的に示す断面図。FIG. 2 is a cross-sectional view conceptually showing the configuration of a reverse osmosis membrane water purification unit included in the circulation filtration system shown in FIG. 1 ; 図1に示した循環式濾過システムに含まれる濾過部材の構成を概念的に示す断面図。FIG. 2 is a cross-sectional view conceptually showing the configuration of a filtering member included in the circulation filtering system shown in FIG. 1; 第2実施形態による循環式濾過システムの全体構成を概略的に示す図。The figure which shows roughly the whole structure of the circulation-type filtration system by 2nd Embodiment.
 以下、本発明の好ましい第1実施形態と第2実施形態を、図面を参照しながら詳細に説明する。
 両実施形態の説明において、共通する対象には共通する符号を付すものとする。また、重複する説明は場合により省略するものとする。
Preferred first and second embodiments of the present invention will now be described in detail with reference to the drawings.
In the description of both embodiments, common reference numerals are given to common objects. In addition, overlapping explanations will be omitted in some cases.
≪第1実施形態≫
 第1実施形態における循環式濾過システム1の全体構成図を図1に示す。これには限られないが、この実施形態における循環式濾過システム1は、手洗い場の用途に用いられる。
<<First embodiment>>
FIG. 1 shows an overall configuration diagram of a circulation filtration system 1 according to the first embodiment. Although not limited to this, the circulating filtration system 1 in this embodiment is used for a wash basin.
 第1実施形態の循環式濾過システム1は、原水タンク10を備えている。原水タンク10は、後述する浄化設備である第1浄化設備で浄化される前の水である原水11を貯めるためのタンクである。
 原水タンク10は、原水11を漏れなく貯めることができれば良く、例えば金属や樹脂によって構成されている。原水タンク10は、公知或いは周知のタンクで十分であり、市販のものでも良い。この実施形態における原水タンク10の容量は、これには限られないが、100l程度とされている。
The circulation filtration system 1 of the first embodiment includes a raw water tank 10 . The raw water tank 10 is a tank for storing raw water 11, which is water before being purified by a first purification facility, which is a purification facility to be described later.
The raw water tank 10 only needs to store the raw water 11 without leakage, and is made of metal or resin, for example. The raw water tank 10 may be a well-known or well-known tank, and may be a commercially available one. The capacity of the raw water tank 10 in this embodiment is, but not limited to, about 100 liters.
 原水タンク10の原水11と触れる範囲の適当な部分に、メインポンプ21が配置されている。メインポンプ21は、水を送ることのできるポンプであり、それができるのであれば、どのようなものであっても構わない。メインポンプ21は、公知或いは周知のポンプによって構成することができ、市販のものでも良い。
 メインポンプ21は、流路管31の基端に接続されている。メインポンプ21は、原水タンク10内の原水11を、流路管31内に導き、流路管31の先端側に向けて流すようになっている。
 メインポンプ21は、接続線21Aによってコンピュータ40に接続されており、コンピュータ40の制御下で、駆動と停止の制御が行われるようになっている。コンピュータ40は、そのような制御を行えれば十分であり、公知或いは周知のもので良く、市販のものでも良い。コンピュータ40がどのようにメインポンプ21を制御するかについては後述する。
A main pump 21 is arranged in an appropriate portion of the raw water tank 10 in contact with the raw water 11 . The main pump 21 is a pump that can send water, and any pump that can do so may be used. The main pump 21 can be configured by a known or well-known pump, and may be a commercially available one.
The main pump 21 is connected to the proximal end of the flow pipe 31 . The main pump 21 guides the raw water 11 in the raw water tank 10 into the channel pipe 31 and causes it to flow toward the tip side of the channel pipe 31 .
The main pump 21 is connected to a computer 40 by a connection line 21A, and under the control of the computer 40, control of driving and stopping is performed. It is sufficient for the computer 40 to be able to perform such control, and it may be a known or well-known one, or a commercially available one. How the computer 40 controls the main pump 21 will be described later.
 流路管31は、後述するようにして、原水タンク10内の原水11を循環させるための管である。流路管31は、原水(原水は、流路管31の途中で後述するように浄水12となる。)を流すことができる管であれば十分であり、公知或いは周知のもので良く、市販のものでも良い。流路管31は、例えば、金属製、或いは樹脂製である。 The flow pipe 31 is a pipe for circulating the raw water 11 in the raw water tank 10 as described later. The flow pipe 31 is sufficient as long as it can flow raw water (the raw water becomes the purified water 12 in the middle of the flow pipe 31 as will be described later). . The flow pipe 31 is made of metal or resin, for example.
 流路管31には、原水タンク10から運ばれてきた原水11を浄化して浄水とするための設備である浄化設備が設けられている。浄化設備は、原水11を浄化するための設備であれば良く、その詳細は問わないが、少なくとも1つの逆浸透膜浄水ユニット51を含んでいる。
 浄化設備は他にも、逆浸透膜ではない濾材、オゾン発生装置、紫外線殺菌装置、曝気装置を含んでいても構わないが、この実施形態では、浄化設備にそれらは含まれていない。濾材の例としては、逆浸透膜浄水ユニット51よりも流路管31の上流側に、例えば、サブポンプ22よりも上流側に設けられた、公知或いは周知のセディメントフィルタを挙げることができる。
 浄化設備のうち、流路管31の最も下流側にあるものを通過した原水11が浄水12である。この実施形態であれば、逆浸透膜浄水ユニット51を通過すると、原水11は浄水12となる。
 濾材の一種としてのセディメントフィルタについての上述の説明から明らかなように、浄化設備に属する逆浸透膜浄水ユニット51や、セディメントフィルタを含む濾材、オゾン発生装置等の他の設備は、流路管31において、連続して設けられている必要はない。セディメントフィルタを、流路管31におけるサブポンプ22の上流側に設けることができるのと同様に、流路管31の、後述するアキュムレータタンクの更に下流側に、オゾン発生装置等の他の装置が設けられていても構わない。
The flow pipe 31 is provided with purification equipment for purifying the raw water 11 carried from the raw water tank 10 into purified water. The purification equipment may be any equipment for purifying the raw water 11, and includes at least one reverse osmosis membrane water purification unit 51, although the details thereof are not limited.
The purification equipment may also include filter media other than reverse osmosis membranes, an ozone generator, an ultraviolet sterilizer, and an aerator, but in this embodiment, they are not included in the purification equipment. An example of the filter medium is a well-known sediment filter provided upstream of the flow pipe 31 from the reverse osmosis membrane water purification unit 51, for example, upstream of the sub-pump 22.
The raw water 11 that has passed through the most downstream purification facility of the flow pipe 31 is the purified water 12 . In this embodiment, the raw water 11 becomes purified water 12 after passing through the reverse osmosis membrane water purification unit 51 .
As is clear from the above description of the sediment filter as a type of filter medium, other facilities such as the reverse osmosis membrane water purification unit 51 belonging to the purification facility, the filter medium including the sediment filter, the ozone generator, etc. The tube 31 need not be continuous. In the same way that the sediment filter can be provided on the upstream side of the sub-pump 22 in the flow pipe 31, another device such as an ozone generator can be provided further downstream of the accumulator tank described later in the flow pipe 31. It does not matter if it is provided.
 逆浸透膜浄水ユニット51について説明する。逆浸透膜浄水ユニット51は公知或いは周知であり、市販のものでも良い。したがって、その原理を、簡単に説明するにとどめる。
 逆浸透膜浄水ユニット51の原理図を、図2に示す。逆浸透膜浄水ユニット51は、ケース51Aを有している。ケース51Aは、例えば、円筒形の耐圧容器である。
 ケース51Aの内部は、逆浸透膜51Bによって2つの空間に分けられている。例えば、この実施形態では、逆浸透膜51Bは、ケース51Aの軸に平行とされている。或いは、逆浸透膜51Bは筒状であり、逆浸透膜51Bの外と内の2つの空間に、ケース51Aの内部の空間を分割していても良い。逆浸透膜51Bは、循環式手洗いユニットの特性から、海水専用である必要はなく、むしろ淡水用の低圧力で造水量が多いRO膜が望ましい。例としては、FilmTec(商標)製のExtra Low Energy RO Membraneシリーズの逆浸透膜を、逆浸透膜51Bとして用いることができる。
 ケース51Aの一方側の端面(図2の下側)には、原水11が流入する流入口51Cが設けられている。また、ケース51Aの他方側の端面には、濃縮された原水11である排水が流出する排水口51Dが設けられている。流入口51Cと、排水口51Dは、逆浸透膜51Bによって分割されたケース51A内部の2つの空間のうちの同じ空間に連通している。また、ケース51Aの他方側の端面には、逆浸透膜浄水ユニット51で原水11から作られた浄水12を排出するための浄水口51Eが設けられている。浄水口51Eは、逆浸透膜51Bによって分割されたケース51A内部の2つの空間のうち、流入口51Cと、排水口51Dとが連通しない側の空間に連通させられている。
 ケース51Aの内部には、流路管31が接続された流入口51Cから原水11が流れ込んで来る。流入口51Cからケース51Aの中に入った原水11には、流入口51Cからの原水11の流入量と、排水口51Dからの排水の流出量を適切な関係に保つことにより、高い圧力がかかるようになっている。
 高い圧力のかけられた原水11のうち純水に近い水分は、逆浸透膜51Bによって分割されたケース51A内部の2つの空間のうちの、流入口51Cと、排水口51Dとが連通している空間から、逆浸透膜51Bを通過して、浄水口51Eが連通している空間に滲み出る。
 つまり、原水11は、ケース51A内において、逆浸透膜51Bによって、浄水12と、濃縮状態とされた原水11とに分離されることになる。そして、原水11は排水口51Dを介することにより、浄水12は浄水口51Eを介することにより、それぞれケース51Aから出るようになっている。浄水口51Eは、逆浸透膜浄水ユニット51の下流側における流路管31と接続されている。排水口51Dは、後述する排出管に接続されている。
The reverse osmosis membrane water purification unit 51 will be described. The reverse osmosis membrane water purification unit 51 is known or well-known, and may be commercially available. Therefore, only a brief description of the principle will be given.
A principle diagram of the reverse osmosis membrane water purification unit 51 is shown in FIG. The reverse osmosis membrane water purification unit 51 has a case 51A. The case 51A is, for example, a cylindrical pressure-resistant container.
The inside of the case 51A is divided into two spaces by a reverse osmosis membrane 51B. For example, in this embodiment, reverse osmosis membrane 51B is parallel to the axis of case 51A. Alternatively, the reverse osmosis membrane 51B may be cylindrical, and the space inside the case 51A may be divided into two spaces, one outside and one inside the reverse osmosis membrane 51B. The reverse osmosis membrane 51B does not need to be exclusively used for seawater because of the characteristics of the circulating hand washing unit. As an example, an Extra Low Energy RO Membrane series reverse osmosis membrane from FilmTec™ can be used as reverse osmosis membrane 51B.
An inlet 51C into which the raw water 11 flows is provided in one end face (lower side in FIG. 2) of the case 51A. A drain port 51D through which waste water, which is the concentrated raw water 11, flows out is provided on the other end face of the case 51A. The inlet 51C and the outlet 51D communicate with the same space of the two spaces inside the case 51A divided by the reverse osmosis membrane 51B. A purified water port 51E for discharging the purified water 12 produced from the raw water 11 by the reverse osmosis membrane water purification unit 51 is provided on the other end surface of the case 51A. The purified water port 51E communicates with the space on the side where the inflow port 51C and the water discharge port 51D do not communicate among the two spaces inside the case 51A divided by the reverse osmosis membrane 51B.
The raw water 11 flows into the case 51A from an inlet 51C to which the flow pipe 31 is connected. A high pressure is applied to the raw water 11 entering the case 51A from the inlet 51C by maintaining an appropriate relationship between the inflow of the raw water 11 from the inlet 51C and the outflow of waste water from the drain 51D. It's like
Among the highly pressurized raw water 11, water that is close to pure water is in communication between the inlet 51C and the outlet 51D of two spaces inside the case 51A divided by the reverse osmosis membrane 51B. From the space, it passes through the reverse osmosis membrane 51B and oozes out into the space communicating with the purified water port 51E.
That is, the raw water 11 is separated into the purified water 12 and the concentrated raw water 11 in the case 51A by the reverse osmosis membrane 51B. The raw water 11 and the purified water 12 are discharged from the case 51A through the drain port 51D and the purified water port 51E, respectively. The water purification port 51</b>E is connected to the flow pipe 31 on the downstream side of the reverse osmosis membrane water purification unit 51 . The drain port 51D is connected to a drain pipe, which will be described later.
 流路管31の逆浸透膜浄水ユニット51の上流側(原水タンク10側)には、サブポンプ22が設けられている。サブポンプ22は、逆浸透膜浄水ユニット51に対して、高い圧力で原水11を供給するためのポンプである。サブポンプ22は、水を送ることのできるポンプであり、それができるのであれば、メインポンプ21と同様にどのようなものであっても構わない。
 サブポンプ22は、接続線22Aによってコンピュータ40に接続されており、コンピュータ40の制御下で、駆動と停止の制御が行われるようになっている。コンピュータ40がどのようにサブポンプ22を制御するかについては後述する。
A sub-pump 22 is provided upstream of the reverse osmosis membrane water purification unit 51 of the flow pipe 31 (raw water tank 10 side). The sub-pump 22 is a pump for supplying the raw water 11 at high pressure to the reverse osmosis membrane water purification unit 51 . The sub-pump 22 is a pump that can send water, and as long as it can do that, it may be of any type, like the main pump 21 .
The sub-pump 22 is connected to a computer 40 by a connection line 22A, and is controlled to be driven and stopped under the control of the computer 40. As shown in FIG. How the computer 40 controls the sub-pump 22 will be described later.
 流路管31における、逆浸透膜浄水ユニット51の下流側には、アキュムレータタンク60が設けられている。
 アキュムレータタンク60は、後述する蛇口から出る浄水12の水圧を所定の範囲に保つためのものである。公知或いは周知であるから詳細な説明は省略するが、アキュムレータタンク60は、水密なタンクと、タンクの中に配された、プラダと呼ばれる、伸縮性のある膜材によって作られ、その内部に常圧よりも高い圧力で気体が充填された気密な風船のようなものとを備えている。プラダと、タンクの間の隙間に浄水12が満たされる。アキュムレータタンク60内の浄水12には、アキュムレータタンク60内の浄水12の量を適宜の範囲とすることにより、プラダから適宜の圧力がかかるようになっている。
 アキュムレータタンク60は通常蛇口の上方に配されるが、この実施形態でもそうなっている。アキュムレータタンク60が蛇口の上方に位置することと、プラダからアキュムレータタンク60内の浄水12に適宜の圧力がかかることにより、後述する蛇口から出る浄水12は、適宜の水圧がかかった状態で、蛇口から出ることになる。アキュムレータタンク60内で、浄水12にプラダから十分な圧力を加えることができるのであれば、アキュムレータタンク60は蛇口71の上方に位置させる必要はない。
 なお、アキュムレータタンク60内の浄水12の水圧は、図示せぬセンサによって検出されており、その水圧のデータは、例えば常時(数秒置き等、適宜の時間が経過する毎でも構わない。)センサから、コンピュータ40に送られるようになっている。
An accumulator tank 60 is provided downstream of the reverse osmosis membrane water purification unit 51 in the flow pipe 31 .
The accumulator tank 60 is for keeping the water pressure of purified water 12 coming out of a faucet, which will be described later, within a predetermined range. The accumulator tank 60 is made of a watertight tank and an elastic film material called Prada arranged in the tank, and a constant It is equipped with something like an airtight balloon filled with gas at a pressure higher than the pressure. Purified water 12 fills the gap between the prada and the tank. By setting the amount of the purified water 12 in the accumulator tank 60 within an appropriate range, an appropriate pressure is applied to the purified water 12 in the accumulator tank 60 from the prada.
The accumulator tank 60 is normally located above the faucet, and is so in this embodiment. Since the accumulator tank 60 is positioned above the faucet and an appropriate pressure is applied to the purified water 12 in the accumulator tank 60 from the prada, the purified water 12 coming out of the faucet, which will be described later, is applied with an appropriate water pressure. will come out from The accumulator tank 60 need not be located above the faucet 71 if sufficient pressure can be applied to the purified water 12 from the bladder within the accumulator tank 60 .
The water pressure of the purified water 12 in the accumulator tank 60 is detected by a sensor (not shown). , is sent to the computer 40 .
 流路管31の先端には、蛇口71が取付けられている。蛇口71は、公知或いは周知のものであり、浄水12の流出の許否を選択できるようになっている。
 周知なように、蛇口71を開状態とすれば蛇口71から浄水12が出て、蛇口71を閉状態とすれば蛇口71から浄水12が出ない。
 蛇口71の下方には、蛇口71から出た浄水12を受ける受皿72が設けられている。受皿72は、排水口を備えた流し台である。なお、この実施形態による循環式濾過システム1において、外部に露出させることが必須なものは、蛇口71と受皿72のみであり、それ以外のすべての部品は、外部に露出させる必要はない。
A faucet 71 is attached to the tip of the flow pipe 31 . The faucet 71 is a publicly known one or a well-known one, and allows selection of permission or denial of outflow of the purified water 12 .
As is well known, when the faucet 71 is open, purified water 12 comes out of the faucet 71, and when the faucet 71 is closed, the purified water 12 does not come out of the faucet 71.
Below the faucet 71, a saucer 72 for receiving purified water 12 discharged from the faucet 71 is provided. The saucer 72 is a sink with a drain. In the circulation filtration system 1 according to this embodiment, only the faucet 71 and the saucer 72 are required to be exposed to the outside, and all other parts need not be exposed to the outside.
 受皿72の排水口には、排水管83が接続されている。排水管83は、受皿72で受けられた浄水12を原水タンク10に導くためのものであり、これには限られないがこの実施形態では、鉛直とされる。受皿72で受けられた、蛇口71から出た浄水12は、重力によって排水管83内を流下して、原水タンク10へと至るようになっている。
 排水管83の途中には、濾過部材84が取付けられている。濾過部材84は、排水管83を介して受皿72から原水タンク10へと向かう浄水12を通過させて、浄水12に含まれる泥や石鹸の成分を濾過して除去するためのものである。この実施形態における濾過部材84は、重力によって流下する汚れた浄水12の濾過を行う。
 これには限られないがこの実施形態では、濾過部材84は、図3に示したようなものとされている。
 濾過部材84は、バッグフィルター84Aを備えている。バッグフィルター84Aは、メッシュ状の生地で構成された袋であって、これには限られないが、上面が開放されている。バッグフィルター84Aとして用いることのできるバッグフィルターは数多く市販されているので、適当なものを選択して利用可能である。
 バッグフィルター84Aの上部には、オイル吸着シート84Bが内蔵されている。オイル吸着シート84Bは、浄水12に含まれた油を除去するシートである。オイル吸着シート84Bは複数枚重ねて、バッグフィルター84Aの中に収納されている。オイル吸着シート84Bとしては、例えば、旭化成ホームプロダクツ株式会社が製造販売する油吸着シート(商品名グリースクリーン(商標)シリーズ)を用いることができる。
 バッグフィルター84Aの下部には、イオン交換樹脂と、活性炭との混合物84Cが内蔵されている。イオン交換樹脂と活性炭はともに粉状であって、混合した状態で、バッグフィルター84A内に収納されている。
 混合物84C中のイオン交換樹脂は、それを通過する汚れた浄水12に含まれている界面活性剤を除去するのに有用であり、混合物84C中の活性炭は、それを通過する汚れた浄水12に含まれている重金属類や悪臭の原因物質を除去するのに有用である。
 なお、濾過部材84は、オイル吸着シート84B、イオン交換樹脂、活性炭のうちの少なくとも1つを含んでいれば足りる。
 また、濾過部材84に含まれるバッグフィルター84Aは、濾過部材84の交換を容易にするためのものであり、その効果を必要としないのであれば、オイル吸着シート84B、イオン交換樹脂、活性炭のうちの少なくとも1つは、バッグフィルター84Aに収納されている必要はない。
A drain pipe 83 is connected to the drain port of the tray 72 . The drain pipe 83 is for guiding the purified water 12 received by the tray 72 to the raw water tank 10, and is vertical in this embodiment, although not limited to this. Purified water 12 discharged from the faucet 71 and received by the receiving tray 72 flows down through the drain pipe 83 by gravity and reaches the raw water tank 10 .
A filter member 84 is attached in the middle of the drain pipe 83 . The filter member 84 passes the purified water 12 from the tray 72 to the raw water tank 10 through the drain pipe 83 to filter and remove mud and soap components contained in the purified water 12 . Filtration member 84 in this embodiment provides filtration of dirty purified water 12 flowing down by gravity.
In this embodiment, although not limited to this, the filtering member 84 is as shown in FIG.
The filtering member 84 has a bag filter 84A. The bag filter 84A is a bag made of a mesh fabric, and has an open top, although not limited to this. Since many bag filters that can be used as the bag filter 84A are commercially available, a suitable one can be selected and used.
An oil adsorption sheet 84B is incorporated in the upper portion of the bag filter 84A. The oil adsorption sheet 84B is a sheet that removes oil contained in the purified water 12. As shown in FIG. A plurality of oil adsorption sheets 84B are stacked and housed in the bag filter 84A. As the oil adsorption sheet 84B, for example, an oil adsorption sheet (trade name Grease Screen (trademark) series) manufactured and sold by Asahi Kasei Home Products Corporation can be used.
A mixture 84C of ion exchange resin and activated carbon is incorporated in the lower portion of the bag filter 84A. Both the ion exchange resin and the activated carbon are in the form of powder, and are contained in the bag filter 84A in a mixed state.
The ion exchange resin in the mixture 84C is useful for removing surfactants contained in the dirty water 12 passing through it, and the activated carbon in the mixture 84C is useful for removing the surfactant contained in the dirty water 12 passing through it. It is useful for removing contained heavy metals and odor-causing substances.
It is sufficient that the filtering member 84 contains at least one of the oil adsorption sheet 84B, ion exchange resin, and activated carbon.
In addition, the bag filter 84A included in the filter member 84 is for facilitating replacement of the filter member 84. If the effect is not required, the oil adsorption sheet 84B, the ion exchange resin, and the activated carbon may be used. need not be housed in the bag filter 84A.
 第1実施形態における循環式濾過システム1は、分岐管32を備えている。分岐管32は、原水タンク10内の原水11を、流路管31が作る上述の循環経路とは異なる経路で、循環させるための流路を構成する管である。
 分岐管32は、その基端が、流路管31のサブポンプ22よりも上流側、つまりは、流路管31の基端側に接続された管であり、流路管31から分岐している。分岐管32を構成する管の仕様は、流路管31を構成する管と同じでも良いし、そうでなくても良い。
 分岐管32の先端から出た原水11は、原水タンク10へと至るようになっている。例えば、分岐管32の先端は、原水タンク10の真上に位置しており、分岐管32の先端から出た原水11は重力によって原水タンク10に落ちるようになっている。
The circulation filtration system 1 in the first embodiment is equipped with a branch pipe 32 . The branch pipe 32 is a pipe that constitutes a flow path for circulating the raw water 11 in the raw water tank 10 through a path different from the above-described circulation path formed by the flow path pipe 31 .
The branch pipe 32 is a pipe whose base end is connected to the flow pipe 31 upstream of the sub-pump 22 , that is, to the base end side of the flow pipe 31 , and is branched from the flow pipe 31 . . The specifications of the pipes forming the branch pipe 32 may or may not be the same as those of the pipes forming the flow channel pipe 31 .
The raw water 11 coming out of the tip of the branch pipe 32 reaches the raw water tank 10. - 特許庁For example, the tip of the branch pipe 32 is located right above the raw water tank 10, and the raw water 11 coming out of the tip of the branch pipe 32 falls into the raw water tank 10 by gravity.
 分岐管32の途中には、第2浄化設備が設けられている。第2浄化設備は、分岐管32の中を流れる原水11を浄化するための設備である。第2浄化設備は、原水11を浄化することができれば良く、その限りにおいて詳細は問わないが、オゾン発生装置、紫外線殺菌装置、曝気装置のうちの少なくとも1つを含んでいる。
 オゾン発生装置は、発生させたオゾンを原水11に供給する機能を有している。原水11にオゾンを供給することにより、オゾンの持つ酸化作用によって、原水11中の有機物が分解され、原水11が浄化されることになる。有機物の分解には、例えば、プランクトンや、細菌、ウィルスの死滅又は不活化の効果も含まれ得る。オゾン発生装置は、公知或いは周知のもので良く、市販のものでも良い。オゾン発生装置としては、例えば、人が吸引しても人体への悪影響が出ない、1000mg/h程度の比較的少量のオゾンを発生させる小型のものを用いることができる。
 紫外線殺菌装置は、発生させた紫外線を原水11に照射する機能を有している。原水11に紫外線を照射することにより、細菌、ウィルスの死滅又は不活化の効果を得られることになる。紫外線殺菌装置は、公知或いは周知のもので良く、市販のものでも良い。紫外線殺菌装置としては、例えば、日機装株式会社が製造、販売する深紫外線LEDランプ搭載の流水浄化用の紫外線殺菌装置を用いることができる。
 曝気装置は、原水11に対して、例えば、マイクロバブル又はナノバブルを供給することにより曝気を行うものとなっている。原水11に対して曝気を行うことにより原水11中の好気性菌が活発に活動するようになり、それにより、原水11の水質が改善する。曝気装置は、公知或いは周知のもので良く、市販のものでも良い。曝気装置は、曝気装置としては、例えば、ナノバブル発生量が1mlあたり1億個以上のナノバブルが発生するものを用いるのが好ましい。
 この実施形態では、これには限られないが、第2浄化設備として、オゾン発生装置91と、紫外線殺菌装置92とが、分岐管32の途中に設けられている。分岐管32を通過する原水11は、オゾン発生装置91と、紫外線殺菌装置92により、上述した原理によって浄化され、その水質が改善される。
 第2浄化設備には、他の設備、例えばセディメントフィルタが含まれていても良い。セディメントフィルタは、例えば、第2浄化設備の最上流部に設けられるのが一般的である。
A second purification facility is provided in the middle of the branch pipe 32 . The second purification equipment is equipment for purifying the raw water 11 flowing through the branch pipe 32 . As long as the second purification equipment can purify the raw water 11, the details are not limited as long as it includes at least one of an ozone generator, an ultraviolet sterilizer, and an aerator.
The ozone generator has a function of supplying the raw water 11 with generated ozone. By supplying ozone to the raw water 11 , organic substances in the raw water 11 are decomposed by the oxidizing action of ozone, and the raw water 11 is purified. The decomposition of organic matter can also include the effect of killing or inactivating plankton, bacteria and viruses, for example. The ozone generator may be a known or well-known one, or may be a commercially available one. As the ozone generator, for example, a compact one that generates a relatively small amount of ozone of about 1000 mg/h that does not adversely affect the human body even if inhaled by a person can be used.
The ultraviolet sterilizer has a function of irradiating the raw water 11 with the generated ultraviolet rays. By irradiating the raw water 11 with ultraviolet rays, the effect of killing or inactivating bacteria and viruses can be obtained. The ultraviolet sterilizer may be a publicly known or well-known one, or may be a commercially available one. As the ultraviolet sterilizer, for example, an ultraviolet sterilizer for purification of running water equipped with a deep ultraviolet LED lamp manufactured and sold by Nikkiso Co., Ltd. can be used.
The aeration device aerates the raw water 11 by supplying microbubbles or nanobubbles, for example. By aerating the raw water 11, aerobic bacteria in the raw water 11 become active, thereby improving the water quality of the raw water 11. - 特許庁The aerator may be a publicly known or well-known one, or may be a commercially available one. It is preferable to use an aeration device that generates 100 million or more nanobubbles per 1 ml, for example.
In this embodiment, although not limited to this, an ozone generator 91 and an ultraviolet sterilizer 92 are provided in the middle of the branch pipe 32 as the second purification equipment. The raw water 11 passing through the branch pipe 32 is purified by the above-described principle by the ozone generator 91 and the ultraviolet sterilizer 92, and the quality of the water is improved.
The second purification facility may also include other facilities, such as sediment filters. The sediment filter is generally provided, for example, at the most upstream part of the second purification equipment.
 上述したように、逆浸透膜浄水ユニット51では、濃縮状態とされた原水11が排水口51Dから出るようになっている。排水口51Dは排出管33の基端と接続されている。排出管33の先端は、分岐管32の、第2浄化設備が設けられた部分よりも上流側(流路管31側)に接続されている。
 それにより、逆浸透膜浄水ユニット51で濃縮状態とされた原水11は、排出管33を介して分岐管32に至り、分岐管32の途中に設けられた第2浄化設備によって浄化され、水質を改善された上で原水タンク10へと至るようになっている。
As described above, in the reverse osmosis membrane water purification unit 51, the concentrated raw water 11 is discharged from the drain port 51D. The drain port 51D is connected to the proximal end of the drain pipe 33 . The tip of the discharge pipe 33 is connected to the upstream side (flow pipe 31 side) of the portion of the branch pipe 32 where the second purification equipment is provided.
As a result, the raw water 11 concentrated in the reverse osmosis membrane water purification unit 51 reaches the branch pipe 32 through the discharge pipe 33 and is purified by the second purification equipment provided in the middle of the branch pipe 32, thereby improving the water quality. After being improved, it reaches the raw water tank 10 .
 次に、以上のように構成された循環式濾過システム1の使用方法、及び動作について説明する。 Next, the usage and operation of the circulation filtration system 1 configured as described above will be described.
 この循環式濾過システム1は、上述したように手洗い場に応用される。
 ユーザが手を洗おうとしたとき、ユーザは、蛇口71を操作して、閉状態であった蛇口71を開状態にする。
 そうすると、アキュムレータタンク60内に貯まっていた浄水12は、蛇口71に対して相対的に高い位置にあることによって持っている位置エネルギーと、アキュムレータタンク60内に配された図示を省略のプラダからの圧力とにより、アキュムレータタンク60から流路管31を通って蛇口71に向かい、蛇口71から流れ出る。アキュムレータタンク60が蛇口71よりも低い位置にあるなら、蛇口71から出る浄水12にはたらく圧力には、重力は寄与せず、プラダからの圧力のみが寄与することになる。
 ユーザは、蛇口71から出た浄水12で手を洗う。ここで、例えばユーザが石鹸を使用すれば、浄水12には石鹸の成分が混ざることになり、また、ユーザの手が汚れていれば浄水12には、油や泥が混ざることになる。そのようにして汚れた浄水12は、受皿72によって受けられる。
This circulation type filtration system 1 is applied to a hand-washing place as described above.
When the user wants to wash his/her hands, the user operates the faucet 71 to open the closed faucet 71 .
Then, the purified water 12 stored in the accumulator tank 60 has potential energy due to being in a relatively high position with respect to the faucet 71, and from the prada (not shown) arranged in the accumulator tank 60 Due to the pressure, the fluid flows from the accumulator tank 60 through the flow pipe 31 toward the faucet 71 and out of the faucet 71 . If the accumulator tank 60 is positioned lower than the faucet 71, then gravity will not contribute to the pressure exerted on the purified water 12 exiting the faucet 71, only the pressure from the prada.
The user washes his/her hands with the purified water 12 coming out of the faucet 71 . Here, for example, if the user uses soap, the clean water 12 will contain soap components, and if the user's hands are dirty, the clean water 12 will contain oil and mud. Purified water 12 soiled in this manner is received by a saucer 72 .
 受皿72によって受けられた汚れた浄水12は、受皿72の排水口から排水管83内を重力によって流下して原水タンク10へと向かう。
 その途中で汚れた浄水12は、排水管83の途中にある濾過部材84を通過する。上述したように濾過部材84は、バッグフィルター84Aと、バッグフィルター84Aの内部に収納されたオイル吸着シート84B、及びイオン交換樹脂及び活性炭の混合物84Cとから構成されている。
 汚れた浄水12に含まれる固形物のうち、バッグフィルター84Aの目よりも大きいものはバッグフィルター84Aによって濾過され捉えられる。汚れた浄水12に含まれる油は、オイル吸着シート84Bによって捉えられる。汚れた浄水12に含まれる金属イオンや、石鹸の成分の一部は、イオン交換樹脂によって捉えられる。また、汚れた浄水12に含まれる臭気物質やトリハロメタンの一部は、活性炭によって捉えられる。
 したがって、濾過部材84を通過することにより、汚れた浄水12はある程度綺麗になる。ある程度綺麗になった浄水12は、排水管83の先端から出て、原水タンク10に落下する。
Dirty purified water 12 received by the receiving tray 72 flows down through the drain pipe 83 by gravity from the drainage port of the receiving tray 72 toward the raw water tank 10 .
The purified water 12 that has become dirty on the way passes through a filtering member 84 on the way of the drain pipe 83 . As described above, the filter member 84 is composed of the bag filter 84A, the oil adsorption sheet 84B housed inside the bag filter 84A, and the mixture 84C of ion exchange resin and activated carbon.
Of the solids contained in the dirty purified water 12, those larger than the mesh of the bag filter 84A are filtered and captured by the bag filter 84A. Oil contained in the dirty purified water 12 is captured by the oil adsorption sheet 84B. Some of the metal ions contained in the dirty water 12 and soap components are captured by the ion exchange resin. Also, some of the odorants and trihalomethanes contained in the dirty purified water 12 are captured by the activated carbon.
Therefore, by passing through the filtering member 84, the dirty purified water 12 becomes clean to some extent. Purified water 12 that has been cleaned to some extent comes out of the tip of drain pipe 83 and drops into raw water tank 10.例文帳に追加
 他方、上述したように、アキュムレータタンク60では、アキュムレータタンク60内の浄水12の水圧をセンサが検知している。
 その水圧についてのデータは、常時コンピュータ40に送られている。コンピュータ40は、浄水12の水圧が小さくなったとき(例えば、ある値を下回ったとき)、メインポンプ21とサブポンプ22のそれぞれに、接続線21A、接続線22Aを介して駆動信号を送る。それにより、メインポンプ21とサブポンプ22は駆動する。つまり、このとき、メインポンプ21とサブポンプ22とは、連動して駆動する。
 メインポンプ21が駆動すると、メインポンプ21が吸い込んだ原水タンク10内の原水11が流路管31の基端から、流路管31の先端側に送られる。他方、サブポンプ22は、メインポンプ21から送られてきた原水11を、原水11に含まれた水が逆浸透膜浄水ユニット51内の逆浸透膜51Bを乗り越えるだけの圧力で、逆浸透膜浄水ユニット51に送り込む。このとき、メインポンプ21から流路管31に送られる原水11の単位時間あたりの量は、サブポンプ22から逆浸透膜浄水ユニット51に送られる原水11の単位時間あたりの量と概ね同じになるように、メインポンプ21とサブポンプ22とはコンピュータ40によって制御される。
 それにより、原水タンク10から流路管31内にメインポンプ21によって送られた原水11は、分岐管32に向かうことなく、サブポンプ22によって逆浸透膜浄水ユニット51に送られることになる。
On the other hand, as described above, in the accumulator tank 60 , the sensor detects the water pressure of the purified water 12 in the accumulator tank 60 .
Data about the water pressure are sent to the computer 40 at all times. The computer 40 sends drive signals to the main pump 21 and the sub-pump 22 via the connection lines 21A and 22A, respectively, when the water pressure of the purified water 12 becomes low (for example, when it falls below a certain value). Thereby, the main pump 21 and the sub-pump 22 are driven. That is, at this time, the main pump 21 and the sub-pump 22 are driven in conjunction with each other.
When the main pump 21 is driven, the raw water 11 in the raw water tank 10 sucked by the main pump 21 is sent from the proximal end of the flow pipe 31 to the distal end of the flow pipe 31 . On the other hand, the sub-pump 22 pumps the raw water 11 sent from the main pump 21 to the reverse osmosis membrane water purification unit 51 at a pressure that allows the water contained in the raw water 11 to overcome the reverse osmosis membrane 51B in the reverse osmosis membrane water purification unit 51. Send to 51. At this time, the amount of raw water 11 sent from the main pump 21 to the flow pipe 31 per unit time is approximately the same as the amount of raw water 11 sent from the sub-pump 22 to the reverse osmosis membrane water purification unit 51 per unit time. Also, the main pump 21 and the sub-pump 22 are controlled by the computer 40 .
As a result, the raw water 11 sent from the raw water tank 10 into the channel pipe 31 by the main pump 21 is sent to the reverse osmosis membrane water purification unit 51 by the sub pump 22 without going to the branch pipe 32 .
 サブポンプ22により送られた原水11は、逆浸透膜浄水ユニット51のケース51Aに設けられた流入口51Cからケース51A内に入る。
 流入口51からケース51A内に入った原水11には高い圧力がかけられている。それにより、原水11に含まれる純水に近い水分は、逆浸透膜51Bによって分割されたケース51A内部の2つの空間のうちの、流入口51Cと、排水口51Dとが連通している空間から、逆浸透膜51Bを通過して、浄水口51Eが連通している空間に滲み出る。つまり、原水11は、ケース51A内において、逆浸透膜51Bによって、浄水12と、濃縮状態とされた原水11とに分離される。
 そして、浄水12は浄水口51Eを介して流路管31に至り、流路管31を通ってアキュムレータタンク60に至る。蛇口71を開状態とすることによってアキュムレータタンク60内の浄水12は減ったが、逆浸透膜浄水ユニット51から浄水12が供給されることにより、減った分のアキュムレータタンク60内の浄水が補充されることになる。上述したように、アキュムレータタンク60内の浄水12の水圧はセンサによって常に検知されており、水圧のデータはコンピュータ40に常時送られている。水圧のデータが所定の範囲に達したら、例えば、蛇口71が開状態とされる前の値に戻ったら、コンピュータ40は、接続線21A又は接続線22Aを介して、メインポンプ21とサブポンプ22に対して、それらの駆動を停止するための停止信号を送る。それにより、メインポンプ21とサブポンプ22とは、駆動を停止する。
 他方、濃縮された原水11は、排出口51Dを介して排出管33に至り、排出管33から、分岐管32に至る。濃縮された原水11は、分岐管32を下流側に進み、第2浄化設備に至る。上述したように、この実施形態における第2浄化設備には、オゾン発生装置91と、紫外線殺菌装置92とが含まれている。濃縮された原水11は、オゾン発生装置91からオゾンの供給を受け、また、紫外線殺菌装置92から紫外線を照射されることによって、浄化され水質が改善させられる。
 水質が改善させられた原水11は、分岐管32を下流側に進み、分岐管32の先端から出て、原水タンク10に落下する。
The raw water 11 sent by the sub-pump 22 enters into the case 51A of the reverse osmosis membrane water purification unit 51 through an inlet 51C provided in the case 51A.
A high pressure is applied to the raw water 11 entering the case 51A from the inlet 51 . As a result, water that is close to pure water contained in the raw water 11 flows out of the two spaces inside the case 51A divided by the reverse osmosis membrane 51B, where the inlet 51C and the outlet 51D communicate with each other. , passes through the reverse osmosis membrane 51B and oozes out into the space communicating with the purified water port 51E. That is, the raw water 11 is separated into the purified water 12 and the concentrated raw water 11 by the reverse osmosis membrane 51B in the case 51A.
Then, the purified water 12 reaches the flow pipe 31 through the water purification port 51E, passes through the flow pipe 31, and reaches the accumulator tank 60. As shown in FIG. Although the purified water 12 in the accumulator tank 60 is reduced by opening the faucet 71, the reduced purified water in the accumulator tank 60 is replenished by supplying the purified water 12 from the reverse osmosis membrane water purification unit 51. will be As described above, the water pressure of the purified water 12 in the accumulator tank 60 is constantly detected by the sensor, and water pressure data is constantly sent to the computer 40 . When the water pressure data reaches a predetermined range, for example, returns to the value before the faucet 71 was opened, the computer 40 sends the main pump 21 and the sub pump 22 via the connection line 21A or the connection line 22A. send a stop signal to stop their driving. Thereby, the main pump 21 and the sub-pump 22 stop driving.
On the other hand, the concentrated raw water 11 reaches the discharge pipe 33 through the discharge port 51D and reaches the branch pipe 32 from the discharge pipe 33 . The concentrated raw water 11 proceeds downstream through the branch pipe 32 and reaches the second purification equipment. As described above, the second purification equipment in this embodiment includes the ozone generator 91 and the ultraviolet sterilizer 92 . The concentrated raw water 11 is supplied with ozone from an ozone generator 91 and irradiated with ultraviolet rays from an ultraviolet sterilization device 92 to be purified and improved in water quality.
The raw water 11 whose water quality has been improved advances downstream through the branch pipe 32 , exits from the tip of the branch pipe 32 , and drops into the raw water tank 10 .
 以上の処理は、蛇口71が閉状態から開状態にさせられたときに、その度に実行される。
 他方、この循環式濾過システム1では、蛇口71が開状態であるか閉状態であるかを問わず、以下の処理を実行する。
 この循環式濾過システム1では、コンピュータ40が、所定の時間毎に、所定の時間長さだけ、メインポンプ21のみを駆動させる。コンピュータ40は、タイマーを内蔵しており、予め定められた定刻が来ると、接続線21Aを介してメインポンプ21に対して駆動信号を送ることにより、メインポンプ21のみを駆動させる。
 メインポンプ21のみが駆動した場合、メインポンプ21は、流路管31の基端から流路管31の先端側に向けて、原水タンク10内に貯まっていた原水11を流そうとする。しかしながら、このとき駆動していないサブポンプ22は流路管31において、閉まった弁のように機能し、原水11の通過を許さない。したがって、原水11は、流路管31から分岐した分岐管32に流れ込む。
 分岐管32に流れ込んだ原水11は、上述した濃縮された原水11の場合と同様に分岐管32を下流側に進み、第2浄化設備に至る。原水11は、オゾン発生装置91からオゾンの供給を受け、また、紫外線殺菌装置92から紫外線を照射されることによって、浄化され水質が改善させられる。
 水質が改善させられた原水11は、分岐管32を下流側に進み、分岐管32の先端から出て、原水タンク10に落下する。
 この処理は、例えば、30分毎に15分間の間実行される。もっとも、この処理が開始される時間間隔と、この処理が実行される1回あたりの時間長さは、常に同じである必要はない。仮に、30分毎に15分間の間だけメインポンプ21のみが駆動させられるとすると、1日24時間のうち、12時間は、原水タンク10に貯められた原水11は、蛇口71が開状態にされたか否かと無関係に、第2浄化設備で浄化されることになる。繰返し第2浄化設備での浄化が行われることにより、原水タンク10内の原水11はある程度浄化された状態が保たれることになるので、蛇口71から出ることになるアキュムレータタンク60に一旦貯められる、流路管31にある浄化設備で浄化された浄水12は、良い水質を保ったものとなる。
 メインポンプ21のみを駆動させる処理は、1日に8時間以上実施されるのが好ましい。それにより、原水タンク10内の原水11の水質をある程度高く保つことが可能となる。
 なお、メインポンプ21のみを駆動させる処理は、蛇口71が開状態とされている場合には、実行されないようにすることができる。それをもってしても、例えば、夜間においてもメインポンプ21のみを駆動させる処理を実行させるようにコンピュータ40を設定しておけば、メインポンプ21のみを駆動させる処理を1日に8時間以上実施させることは容易である。
 なお、以上の説明では、メインポンプ21とサブポンプ22との駆動と停止は、コンピュータ40を用いて制御されることとしていたが、同様の制御が可能なのであれば、より簡単な仕組み、例えば、アキュムレータタンク60に設けられたセンサ、そのセンサと組合されたスイッチ、及びメインポンプ21を駆動するためのタイマー等によって、コンピュータ40を置換することも可能である。
The above processing is executed each time the faucet 71 is changed from the closed state to the open state.
On the other hand, in this circulation filtration system 1, the following processing is executed regardless of whether the faucet 71 is open or closed.
In this circulation filtration system 1, the computer 40 drives only the main pump 21 for a predetermined length of time at predetermined intervals. The computer 40 incorporates a timer, and when a predetermined time comes, it drives only the main pump 21 by sending a drive signal to the main pump 21 via the connection line 21A.
When only the main pump 21 is driven, the main pump 21 tries to flow the raw water 11 stored in the raw water tank 10 from the base end of the flow pipe 31 toward the tip side of the flow pipe 31 . However, the sub-pump 22 that is not driven at this time functions like a closed valve in the flow pipe 31 and does not allow the raw water 11 to pass through. Therefore, the raw water 11 flows into the branch pipe 32 branched from the flow pipe 31 .
The raw water 11 that has flowed into the branch pipe 32 proceeds downstream through the branch pipe 32 in the same manner as the concentrated raw water 11 described above, and reaches the second purification equipment. The raw water 11 is supplied with ozone from an ozone generator 91 and is irradiated with ultraviolet rays from an ultraviolet sterilizer 92 to be purified and improved in water quality.
The raw water 11 whose water quality has been improved advances downstream through the branch pipe 32 , exits from the tip of the branch pipe 32 , and drops into the raw water tank 10 .
This process is performed, for example, every 30 minutes for 15 minutes. However, the time interval at which this process is started and the length of time each time this process is executed need not always be the same. Assuming that only the main pump 21 is driven for 15 minutes every 30 minutes, the raw water 11 stored in the raw water tank 10 is kept open for 12 hours out of 24 hours a day. It will be purified in the second purification facility regardless of whether or not it has been cleaned. By repeatedly performing purification in the second purification equipment, the raw water 11 in the raw water tank 10 is maintained in a purified state to some extent. , the purified water 12 purified by the purification equipment in the flow pipe 31 maintains good water quality.
The process of driving only the main pump 21 is preferably performed for eight hours or more a day. As a result, the quality of the raw water 11 in the raw water tank 10 can be kept high to some extent.
It should be noted that the process of driving only the main pump 21 can be prevented from being executed when the faucet 71 is in the open state. Even with this, for example, if the computer 40 is set to execute the process of driving only the main pump 21 even at night, the process of driving only the main pump 21 can be executed for eight hours or more a day. It is easy.
In the above description, the driving and stopping of the main pump 21 and the sub-pump 22 are controlled using the computer 40, but if similar control is possible, a simpler mechanism, such as an accumulator It is also possible to replace the computer 40 with a sensor provided on the tank 60, a switch associated with the sensor, a timer for driving the main pump 21, and the like.
≪第2実施形態≫
 第2実施形態における循環式濾過システム2の全体構成図を図4に示す。これには限られないが、この実施形態における循環式濾過システム2は、手洗い場の用途に用いられる。
 第2実施形態の循環式濾過システム2は、第1実施形態の循環式濾過システム1とかなりの部分で共通している。以下に相違点として説明する部分を除けば、第2実施形態の循環式濾過システム2は、第1実施形態の循環式濾過システム1と同様に構成されている。
<<Second embodiment>>
FIG. 4 shows an overall configuration diagram of the circulation filtration system 2 in the second embodiment. Although not limited to this, the circulating filtration system 2 in this embodiment is used for a wash basin.
The circulation filtration system 2 of the second embodiment has a considerable portion in common with the circulation filtration system 1 of the first embodiment. The circulation filtration system 2 of the second embodiment is configured in the same manner as the circulation filtration system 1 of the first embodiment, except for the portions described as differences below.
 第2実施形態の循環式濾過システム2は、原水タンク10を備えている。循環式濾過システム2が備える原水タンク10は、第1実施形態の循環式濾過システム1が備える原水タンク10と同じで良く、この実施形態ではそうされている。
 第2実施形態の循環式濾過システム2は、第1実施形態の循環式濾過システム1が備えていたのと同様の、メインポンプ21及びサブポンプ22を連動して駆動させることにより、原水タンク10から原水タンク10へと原水11を循環させるための一連の設備を備えている。
 つまり、第2実施形態の循環式濾過システム2は、メインポンプ21、流路管31、サブポンプ22、浄化設備、アキュムレータタンク60、蛇口71を備えている。
A circulation filtration system 2 of the second embodiment includes a raw water tank 10 . The raw water tank 10 provided in the circulation filtration system 2 may be the same as the raw water tank 10 provided in the circulation filtration system 1 of the first embodiment, which is the case in this embodiment.
In the circulation filtration system 2 of the second embodiment, the main pump 21 and the sub-pump 22, which are similar to those provided in the circulation filtration system 1 of the first embodiment, are interlocked to drive the raw water tank 10. A series of facilities are provided for circulating raw water 11 to the raw water tank 10 .
That is, the circulation filtration system 2 of the second embodiment includes a main pump 21, a flow pipe 31, a sub-pump 22, purification equipment, an accumulator tank 60, and a faucet 71.
 基本的に、第2実施形態の循環式濾過システム2が備えるメインポンプ21、流路管31、サブポンプ22、浄化設備、アキュムレータタンク60、蛇口71は、第1実施形態の循環式濾過システム1が備えるそれらと同じで良く、これには限られないがこの実施形態では、以下に説明する部分を除いてそうされている。
 第2実施形態の循環式濾過システム2が備えるメインポンプ21、流路管31、サブポンプ22、浄化設備、アキュムレータタンク60、蛇口71における第1実施形態との違いは、浄化設備の構成である。また、浄化設備の構成に伴い、第2実施形態の循環式濾過システム2におけるサブポンプ22の位置が、第1実施形態の場合と異なるものとなっている。加えて、第2実施形態の循環式濾過システム2における流路管31には、分岐管32が接続されていない。これは、後述するように、第2実施形態の循環式濾過システム2には分岐管32が存在していないからである。
Basically, the main pump 21, the flow pipe 31, the sub-pump 22, the purification equipment, the accumulator tank 60, and the faucet 71 included in the circulation filtration system 2 of the second embodiment are the same as those of the circulation filtration system 1 of the first embodiment. They may be the same as those provided, but not limited to this, in this embodiment except for the parts described below.
The main pump 21, flow pipe 31, sub-pump 22, purification equipment, accumulator tank 60, and faucet 71 provided in the circulation filtration system 2 of the second embodiment differ from the first embodiment in the configuration of the purification equipment. Further, the position of the sub-pump 22 in the circulation filtration system 2 of the second embodiment is different from that of the first embodiment due to the configuration of the purification equipment. In addition, the branch pipe 32 is not connected to the flow pipe 31 in the circulation filtration system 2 of the second embodiment. This is because the branch pipe 32 does not exist in the circulation filtration system 2 of the second embodiment, as will be described later.
 第2実施形態における浄化設備は、第1実施形態の場合と同様に、原水タンク10から運ばれてきた原水11を浄化して浄水とするための設備である点では第1実施形態と変わりない。第1実施形態の場合と同様に、第2実施形態の浄化設備は、少なくとも1つの逆浸透膜浄水ユニットを含んでいる。また、第1実施形態の場合と同様に、第2実施形態の循環式濾過システム2でも、浄化設備は、逆浸透膜ではない濾材(例えば、セディメントフィルタ)、オゾン発生装置、紫外線殺菌装置、曝気装置を含んでいても構わない。
 ただし、第1実施形態では、逆浸透膜浄水ユニットは、流路管31に1つだけ設けられた逆浸透膜浄水ユニット51のみであったが、第2実施形態の循環式濾過システム2における流路管31には、逆浸透膜浄水ユニット51と、逆浸透膜浄水ユニット52という2つの逆浸透膜浄水ユニットが設けられている。
 逆浸透膜浄水ユニット51と逆浸透膜浄水ユニット52とは同じものでも良いし、同じものでなくても良い。ただし、それらが原水11を浄化する原理は、図2を用いて説明したものであり、共通である。例えば、逆浸透膜浄水ユニット51と逆浸透膜浄水ユニット52とでは、図2における逆浸透膜51Bのみが異なるものとなっていても構わない。この実施形態ではこれには限られないが、逆浸透膜浄水ユニット51と逆浸透膜浄水ユニット52とは同じものとされている。
 第1実施形態では、サブポンプ22は、流路管31における、1つのみとされた逆浸透膜浄水ユニット51の上流側の位置に設けられていた。それに対して、第2実施形態では、サブポンプ22は、流路管31における、2つとされた逆浸透膜浄水ユニット51及び逆浸透膜浄水ユニット52の間に位置するようになっている。もっとも、サブポンプ22は、逆浸透膜浄水ユニットが複数存在している場合には、その最も下流側に位置するものよりも上流側に配置すれば良い。したがって、サブポンプ22は、逆浸透膜浄水ユニット51よりも上流側に配置されていても構わない。この事情は、仮に第1実施形態の循環式濾過システム1に逆浸透膜浄水ユニットが2つ存在する場合でも同様である。
 第2実施形態でも、第1実施形態の場合と同様に、浄化設備のうち、流路管31の最も下流側にあるものを通過した原水11が浄水12となる。第2実施形態では、逆浸透膜浄水ユニット52を通過することにより、原水11が浄水12となる。
The purification facility in the second embodiment is the same as in the first embodiment in that it is a facility for purifying the raw water 11 carried from the raw water tank 10 into purified water, as in the case of the first embodiment. . As in the first embodiment, the purification installation of the second embodiment includes at least one reverse osmosis membrane water purification unit. Further, as in the case of the first embodiment, in the circulation filtration system 2 of the second embodiment, the purification equipment includes a filter medium (for example, a sediment filter) that is not a reverse osmosis membrane, an ozone generator, an ultraviolet sterilizer, It may contain an aerator.
However, in the first embodiment, the reverse osmosis membrane water purification unit was only one reverse osmosis membrane water purification unit 51 provided in the flow path pipe 31, but the flow in the circulation filtration system 2 of the second embodiment The pipeline 31 is provided with two reverse osmosis membrane water purification units, a reverse osmosis membrane water purification unit 51 and a reverse osmosis membrane water purification unit 52 .
The reverse osmosis membrane water purification unit 51 and the reverse osmosis membrane water purification unit 52 may or may not be the same. However, the principle by which they purify the raw water 11 is the one explained using FIG. 2 and is common. For example, the reverse osmosis membrane water purification unit 51 and the reverse osmosis membrane water purification unit 52 may differ only in the reverse osmosis membrane 51B in FIG. Although not limited to this in this embodiment, the reverse osmosis membrane water purification unit 51 and the reverse osmosis membrane water purification unit 52 are the same.
In the first embodiment, the sub-pump 22 is provided upstream of the only one reverse osmosis membrane water purification unit 51 in the flow pipe 31 . On the other hand, in the second embodiment, the sub-pump 22 is positioned between the two reverse osmosis membrane water purification units 51 and 52 in the flow pipe 31 . However, if there are a plurality of reverse osmosis membrane water purification units, the sub-pump 22 may be arranged upstream of the most downstream unit. Therefore, the sub-pump 22 may be arranged upstream of the reverse osmosis membrane water purification unit 51 . This situation is the same even if there are two reverse osmosis membrane water purification units in the circulation filtration system 1 of the first embodiment.
In the second embodiment, as in the first embodiment, the raw water 11 that has passed through the most downstream purification facility of the flow pipe 31 becomes the purified water 12 . In the second embodiment, the raw water 11 becomes the purified water 12 by passing through the reverse osmosis membrane water purification unit 52 .
 また、既に述べたように、第2実施形態の循環式濾過システム2には、第1実施形態の循環式濾過システム1が備えていた分岐管32が存在しない。
 その代わりに、第2実施形態の循環式濾過システム2には、第1実施形態の循環式濾過システム1には存在しなかった第2流路管34と、第2ポンプ23とが存在している。
 第2ポンプ23は、原水タンク10の原水11と触れる範囲の適当な部分に配置されている。第2ポンプ23は、メインポンプ21と同等のものとすることができ、水を送ることのできるポンプであれば良い。
 第2ポンプ23は、第2流路管34の基端に接続されている。第2ポンプ23は、原水タンク10内の原水11を、第2流路管34内に導き、第2流路管34の先端側に向けて流すようになっている。
 第2ポンプ23は、接続線23Aによってコンピュータ40に接続されており、接続線21Aを介してコンピュータ40に接続されたメインポンプ21と、接続線22Aを介してコンピュータ40に接続されたサブポンプ22と同様に、コンピュータ40の制御下で、駆動と停止の制御が行われるようになっている。なお、第2実施形態におけるコンピュータ40は、第1実施形態におけるコンピュータ40と同等のもので良い。
Further, as already described, the circulation filtration system 2 of the second embodiment does not have the branch pipe 32 provided in the circulation filtration system 1 of the first embodiment.
Instead, the circulation filtration system 2 of the second embodiment includes the second flow pipe 34 and the second pump 23, which were not present in the circulation filtration system 1 of the first embodiment. there is
The second pump 23 is arranged in a suitable portion of the raw water tank 10 within the range of contact with the raw water 11 . The second pump 23 may be equivalent to the main pump 21, and may be any pump capable of sending water.
The second pump 23 is connected to the proximal end of the second flow pipe 34 . The second pump 23 guides the raw water 11 in the raw water tank 10 into the second flow pipe 34 and causes it to flow toward the tip side of the second flow pipe 34 .
The second pump 23 is connected to the computer 40 by a connecting line 23A, and includes a main pump 21 connected to the computer 40 via a connecting line 21A and a sub-pump 22 connected to the computer 40 via a connecting line 22A. Similarly, under the control of the computer 40, control of driving and stopping is performed. Note that the computer 40 in the second embodiment may be equivalent to the computer 40 in the first embodiment.
 第2流路管34は、後述するようにして、原水タンク10内の原水11を循環させるための管である。第2流路管34の仕様は、流路管31と同等で良く、この実施形態ではこの限りではないがそうされている。第2流路管34の先端から出た原水11は、第1実施形態の分岐管32の先端から出た原水11と同じように、原水タンク10へと落下するようになっている。
 第1実施形態では分岐管32に存在した第2浄化設備が、第2実施形態の循環式濾過システム2では、第2流路管34に設けられている。
 第2実施形態の場合でも、第1実施形態の場合と同様に、第2浄化設備は、第2流路管34内を流れる原水11を浄化するための設備である。第2実施形態における第2浄化設備は、第1実施形態の場合と同様に、原水11を浄化することができれば良く、その限りにおいて詳細は問わないが、オゾン発生装置、紫外線殺菌装置、曝気装置のうちの少なくとも1つを含んでいる。
 この実施形態では、これには限られないが、第2浄化設備として、紫外線殺菌装置92と、曝気装置93とが、第2流路管34の途中に設けられている。第2流路管34を通過する原水11は、紫外線殺菌装置92と、曝気装置93とにより、上述した原理によって浄化され、その水質が改善される。
 第2浄化設備には、他の設備、例えばセディメントフィルタが含まれていても良い。セディメントフィルタは、例えば、第2浄化設備の最上流部に設けられるのが一般的である。
The second flow pipe 34 is a pipe for circulating the raw water 11 in the raw water tank 10 as described later. The specifications of the second flow pipe 34 may be the same as those of the flow pipe 31, and are used in this embodiment, although not limited to this. The raw water 11 coming out of the tip of the second flow pipe 34 drops into the raw water tank 10 in the same way as the raw water 11 coming out of the tip of the branch pipe 32 of the first embodiment.
The second purification equipment, which was present in the branch pipe 32 in the first embodiment, is provided in the second flow pipe 34 in the circulation filtration system 2 of the second embodiment.
Also in the case of the second embodiment, as in the first embodiment, the second purification equipment is equipment for purifying the raw water 11 flowing through the second flow pipe 34 . As in the case of the first embodiment, the second purification equipment in the second embodiment only needs to be able to purify the raw water 11. As long as the details are not limited, the ozone generator, the ultraviolet sterilizer, and the aerator. contains at least one of
In this embodiment, although not limited to this, an ultraviolet sterilizer 92 and an aerator 93 are provided in the middle of the second flow pipe 34 as the second purification equipment. The raw water 11 passing through the second flow pipe 34 is purified by the above-described principle by the ultraviolet sterilization device 92 and the aeration device 93, and the quality of the water is improved.
The second purification facility may also include other facilities, such as sediment filters. The sediment filter is generally provided, for example, at the most upstream part of the second purification equipment.
 第1実施形態では、逆浸透膜浄水ユニット51から出た濃縮状態とされた原水11は、排出管33を介して分岐管32内の原水11に合流させられるようになっていた。
 第2実施形態では、逆浸透膜浄水ユニット51と、逆浸透膜浄水ユニット52とからそれぞれ生じた濃縮状態とされた原水11が、排出管33を介して第2流路管34の原水11に合流させられるようになっている。第2実施形態における排出管33の先端の第2流路管34に対する接続部分は、第1実施形態における排出管33の先端の分岐管32に対する接続部分がそうであったように、第2浄化設備が設けられた部分よりも上流側となっている。
 それにより、逆浸透膜浄水ユニット51、逆浸透膜浄水ユニット52で濃縮状態とされた原水11は、排出管33を介して第2流路管34に至り、第2流路管34の途中に設けられた第2浄化設備によって浄化され、水質を改善された上で原水タンク10へと至るようになっている。
In the first embodiment, the concentrated raw water 11 discharged from the reverse osmosis membrane water purification unit 51 is allowed to join the raw water 11 in the branch pipe 32 via the discharge pipe 33 .
In the second embodiment, the concentrated raw water 11 generated from the reverse osmosis membrane water purification unit 51 and the reverse osmosis membrane water purification unit 52 respectively flows through the discharge pipe 33 to the raw water 11 of the second flow pipe 34. It is designed to be merged. The connection portion of the tip of the discharge pipe 33 to the second flow pipe 34 in the second embodiment is the same as the connection portion of the tip of the discharge pipe 33 to the branch pipe 32 in the first embodiment. It is on the upstream side of the part where the equipment is provided.
As a result, the raw water 11 concentrated in the reverse osmosis membrane water purification unit 51 and the reverse osmosis membrane water purification unit 52 reaches the second flow pipe 34 via the discharge pipe 33, and reaches the second flow pipe 34. The water is purified by the provided second purification equipment, the water quality is improved, and then the raw water tank 10 is reached.
 次に、以上のように構成された第2実施形態における循環式濾過システム2の使用方法、及び動作について説明する。 Next, the usage method and operation of the circulation filtration system 2 in the second embodiment configured as described above will be described.
 第2実施形態の循環式濾過システム2は、第1実施形態の場合と同様に、手洗い場に応用される。
 ユーザが手を洗おうとしたとき、ユーザは、蛇口71を操作して、閉状態であった蛇口71を開状態にする。
 そうすると、アキュムレータタンク60内に貯まっていた浄水12は、第1実施形態の場合と同様に、蛇口71から流れ出る。ユーザは、蛇口71から出た浄水12で手を洗う。ここで、例えばユーザが石鹸を使用すれば、浄水12には石鹸の成分が混ざることになり、また、ユーザの手が汚れていれば浄水12には、油や泥が混ざることになる。そのようにして汚れた浄水12は、受皿72によって受けられる。
 受皿72によって受けられた汚れた浄水12は、受皿72の排水口から排水管83内を重力によって流下して原水タンク10へと向かう。
 その途中で汚れた浄水12は、排水管83の途中にある濾過部材84を通過して浄化される。ある程度綺麗になった浄水12は、排水管83の先端から出て、原水タンク10に落下する。
 ここまでは第1実施形態と変わらない。
The circulation filtration system 2 of the second embodiment is applied to a hand-washing area as in the case of the first embodiment.
When the user wants to wash his/her hands, the user operates the faucet 71 to open the closed faucet 71 .
Then, the purified water 12 stored in the accumulator tank 60 flows out from the faucet 71 as in the case of the first embodiment. The user washes his/her hands with the purified water 12 coming out of the faucet 71 . Here, for example, if the user uses soap, the clean water 12 will contain soap components, and if the user's hands are dirty, the clean water 12 will contain oil and mud. Purified water 12 soiled in this manner is received by a saucer 72 .
Dirty purified water 12 received by the receiving tray 72 flows down through the drain pipe 83 by gravity from the drainage port of the receiving tray 72 toward the raw water tank 10 .
The purified water 12 that has become dirty on the way passes through a filter member 84 in the middle of the drain pipe 83 and is purified. Purified water 12 that has been cleaned to some extent comes out of the tip of drain pipe 83 and drops into raw water tank 10.例文帳に追加
So far, it is the same as the first embodiment.
 他方、アキュムレータタンク60では、第1実施形態のときと同様に、アキュムレータタンク60内の浄水12の水圧をセンサが検知している。
 その水圧についてのデータは、常時コンピュータ40に送られている。コンピュータ40は、浄水12の水圧が小さくなったとき(例えば、ある値を下回ったとき)、メインポンプ21とサブポンプ22のそれぞれに、接続線21A、接続線22Aを介して駆動信号を送る。それにより、停止していたメインポンプ21とサブポンプ22は駆動する。つまり、このとき、メインポンプ21とサブポンプ22とは、連動して駆動する。
 メインポンプ21が駆動すると、メインポンプ21が吸い込んだ原水タンク10内の原水11が流路管31の基端から、流路管31の先端側に送られる。メインポンプ21は、原水11に含まれた水が逆浸透膜浄水ユニット51内の逆浸透膜51Bを乗り越えるだけの圧力をかけつつ、原水11を逆浸透膜浄水ユニット51に送り込む。同様に、サブポンプ22は、原水11に含まれた水が逆浸透膜浄水ユニット52内の逆浸透膜を乗り越えるだけの圧力をかけつつ、原水11を逆浸透膜浄水ユニット52に送り込む。
 このとき、メインポンプ21が流す原水11の単位時間あたりの流量と、サブポンプ22が流す原水11の単位時間あたりの流量とが概ね同じになるように、メインポンプ21とサブポンプ22とはコンピュータ40によって制御される。
On the other hand, in the accumulator tank 60, the sensor detects the water pressure of the purified water 12 in the accumulator tank 60, as in the first embodiment.
Data about the water pressure are sent to the computer 40 at all times. The computer 40 sends drive signals to the main pump 21 and the sub-pump 22 via the connection lines 21A and 22A, respectively, when the water pressure of the purified water 12 becomes low (for example, when it falls below a certain value). As a result, the stopped main pump 21 and sub-pump 22 are driven. That is, at this time, the main pump 21 and the sub-pump 22 are driven in conjunction with each other.
When the main pump 21 is driven, the raw water 11 in the raw water tank 10 sucked by the main pump 21 is sent from the proximal end of the flow pipe 31 to the distal end of the flow pipe 31 . The main pump 21 feeds the raw water 11 to the reverse osmosis membrane water purification unit 51 while applying pressure enough to overcome the reverse osmosis membrane 51B in the reverse osmosis membrane water purification unit 51. - 特許庁Similarly, the sub-pump 22 feeds the raw water 11 to the reverse osmosis membrane water purification unit 52 while applying a pressure enough to push the water contained in the raw water 11 over the reverse osmosis membrane in the reverse osmosis membrane water purification unit 52 .
At this time, the main pump 21 and the sub-pump 22 are controlled by the computer 40 so that the flow rate per unit time of the raw water 11 flowed by the main pump 21 and the flow rate per unit time of the raw water 11 flowed by the sub-pump 22 are approximately the same. controlled.
 メインポンプ21によって逆浸透膜浄水ユニット51に送られた原水11は、第1実施形態で説明したようにして、濃縮された原水11と、浄水12に近い浄化された原水11とに分離される。浄化された原水11は、流路管31を介してサブポンプ22に向かい、サブポンプ22によって逆浸透膜浄水ユニット52に送られる。サブポンプ22によって逆浸透膜浄水ユニット52に送られた原水11は、逆浸透膜浄水ユニット51で原水11が浄化されるのと同様の原理で、濃縮された原水11と、浄水12とに分離される。
 逆浸透膜浄水ユニット52から生じた浄水12は、流路管31に至り、流路管31を通ってアキュムレータタンク60に至る。これによって、蛇口71を開状態とすることによって減ったアキュムレータタンク60内の浄水12が補充される。そして、アキュムレータタンク60内の浄水12の水圧が適当な範囲に達したら、コンピュータ40は、メインポンプ21とサブポンプ22とを停止させる。
 他方、逆浸透膜浄水ユニット51と逆浸透膜浄水ユニット52から生じた濃縮された原水11は、排出管33を介して第2流路管34に至る。濃縮された原水11は、第2流路管34を下流側に進み、第2浄化設備に至る。上述したように、第2実施形態における第2浄化設備には、紫外線殺菌装置92と、曝気装置93が含まれている。濃縮された原水11は、紫外線殺菌装置92から紫外線を照射され、また、曝気装置93によって曝気されることによって、浄化され水質が改善させられる。
 水質が改善させられた原水11は、第2流路管34を下流側に進み、第2流路管34の先端から出て、原水タンク10に落下する。
The raw water 11 sent to the reverse osmosis membrane water purification unit 51 by the main pump 21 is separated into the concentrated raw water 11 and the purified raw water 11 close to the purified water 12 as described in the first embodiment. . The purified raw water 11 is directed to the sub-pump 22 via the flow pipe 31 and sent to the reverse osmosis membrane water purification unit 52 by the sub-pump 22 . The raw water 11 sent to the reverse osmosis membrane water purification unit 52 by the sub-pump 22 is separated into the concentrated raw water 11 and the purified water 12 by the same principle as the raw water 11 is purified by the reverse osmosis membrane water purification unit 51. be.
The purified water 12 generated from the reverse osmosis membrane water purification unit 52 reaches the flow pipe 31 and reaches the accumulator tank 60 through the flow pipe 31 . As a result, the purified water 12 in the accumulator tank 60, which is reduced by opening the faucet 71, is replenished. When the water pressure of purified water 12 in accumulator tank 60 reaches an appropriate range, computer 40 stops main pump 21 and sub-pump 22 .
On the other hand, the concentrated raw water 11 generated from the reverse osmosis membrane water purification unit 51 and the reverse osmosis membrane water purification unit 52 reaches the second flow pipe 34 via the discharge pipe 33 . The concentrated raw water 11 proceeds downstream through the second flow pipe 34 and reaches the second purification equipment. As described above, the second purification equipment in the second embodiment includes the ultraviolet sterilization device 92 and the aeration device 93 . The concentrated raw water 11 is irradiated with ultraviolet rays from an ultraviolet sterilizer 92 and aerated by an aeration device 93 to be purified and improved in water quality.
The raw water 11 whose water quality has been improved advances downstream through the second flow pipe 34 , exits from the tip of the second flow pipe 34 , and drops into the raw water tank 10 .
 以上の処理は、蛇口71が閉状態から開状態にさせられたときに、その度に実行される。
 他方、この循環式濾過システム2では、蛇口71が開状態であるか閉状態であるかを問わず、以下の処理を実行する。
 この循環式濾過システム2では、コンピュータ40が、所定の時間毎に、所定の時間長さだけ、第2ポンプ23を駆動させる。コンピュータ40は、タイマーを内蔵しており、予め定められた定刻が来ると、接続線23Aを介して第2ポンプ23に対して駆動信号を送ることにより、第2ポンプ23を駆動させる。
 第2ポンプ23が駆動した場合、第2ポンプ23は、第2流路管34の基端から第2流路管34の先端側に向けて、原水タンク10内に貯まっていた原水11を流す。
 第2流路管34内を流れる原水11は、上述した濃縮された原水11の場合と同様に第2流路管34を下流側に進み、第2浄化設備に至る。原水11は、濃縮された原水11の場合と同様に、浄化され水質が改善させられる。
 水質が改善させられた原水11は、第2流路管34を下流側に進み、第2流路管34の先端から出て、原水タンク10に落下する。
 この処理が実行されるタイミングと、この処理が実行されるときの1回あたりの長さは、第1実施形態の循環式濾過システム1において、メインポンプ21のみが駆動される処理が実行されるときのタイミングと、その処理が実行されるときの1回あたりの長さに準じることができる。
 それにより、第2実施形態の循環式濾過システム2でも、第1実施形態の循環式濾過システム1の場合と同様に、蛇口71が開状態にされたか否かと無関係に、原水タンク10内の原水11が、第2浄化設備で繰返し浄化されることになる。それにより、原水タンク10内の原水11はある程度浄化された状態が保たれる。したがって、第2実施形態の場合でも、蛇口71から出ることになるアキュムレータタンク60に一旦貯められる、流路管31にある浄化設備で浄化された浄水12は、良い水質を保ったものとなる。
 なお、第2実施形態では、メインポンプ21とサブポンプ22と更には第2ポンプ23とを同時に駆動させることも可能である。
 第2実施形態でも、第1実施形態の場合と同様に、コンピュータ40を省略し、他のより簡単な仕組みに置換することが可能である。
The above processing is executed each time the faucet 71 is changed from the closed state to the open state.
On the other hand, in this circulation filtration system 2, the following processing is executed regardless of whether the faucet 71 is open or closed.
In this circulation filtration system 2, the computer 40 drives the second pump 23 for a predetermined length of time every predetermined time. The computer 40 incorporates a timer, and drives the second pump 23 by sending a drive signal to the second pump 23 via the connection line 23A when a predetermined time comes.
When the second pump 23 is driven, the second pump 23 causes the raw water 11 accumulated in the raw water tank 10 to flow from the base end of the second flow pipe 34 toward the tip side of the second flow pipe 34. .
The raw water 11 flowing through the second flow pipe 34 advances downstream through the second flow pipe 34 and reaches the second purification facility in the same manner as the concentrated raw water 11 described above. The raw water 11 is purified and improved in quality, as is the case with the concentrated raw water 11 .
The raw water 11 whose water quality has been improved advances downstream through the second flow pipe 34 , exits from the tip of the second flow pipe 34 , and drops into the raw water tank 10 .
The timing of execution of this process and the length of one time when this process is executed are determined by the process in which only the main pump 21 is driven in the circulation filtration system 1 of the first embodiment. and the length of each time when the process is executed.
As a result, in the circulation filtration system 2 of the second embodiment, as in the circulation filtration system 1 of the first embodiment, regardless of whether the faucet 71 is open or not, the raw water in the raw water tank 10 is 11 will be repeatedly purified in the second purification facility. As a result, the raw water 11 in the raw water tank 10 is kept purified to some extent. Therefore, even in the case of the second embodiment, the purified water 12, which is once stored in the accumulator tank 60 coming out of the faucet 71 and purified by the purification equipment in the flow pipe 31, maintains good water quality.
In addition, in the second embodiment, the main pump 21, the sub-pump 22, and further the second pump 23 can be driven simultaneously.
In the second embodiment, as in the first embodiment, the computer 40 can be omitted and replaced with another simpler mechanism.

Claims (10)

  1.  循環させて繰返し使用される水である原水を貯める原水タンクと、
     前記原水を循環させるための流路を構成する、その基端が前記原水タンクに接続された管である流路管と、
     前記流路管の途中に設けられた、前記原水を浄化して浄水にするための設備であり、少なくとも1つの逆浸透膜浄水ユニットを含む浄化設備と、
     前記流路管における、前記流路管に対して最も先端側に位置する前記逆浸透膜浄水ユニットの手前側の部分に設けられた、それが駆動した場合に、前記流路管内の前記原水を、前記流路管内において前記流路管の先端側に流すサブポンプと、前記サブポンプが駆動したときに前記サブポンプと連動して駆動する、前記流路管の前記原水タンク内の前記原水と接する部分に設けられた、それが駆動した場合に、前記原水タンク内の原水を前記流路管の先端側に流すメインポンプと、
     前記流路管の先端に設けられた、前記浄水の前記流路管からの排出の許否を選択することのできるようにされた蛇口と、
     前記蛇口から排出された前記浄水を受ける受皿と、
     を備えており、
     前記受皿で受けた前記浄水が前記原水タンクに至るようにされている、
     循環式濾過システムであって、
     前記原水を循環させるための流路を構成する、その基端が前記流路管における前記サブポンプの手前に接続されることで前記流路管から分岐させられた管である分岐管と、
     前記分岐管の途中に設けられた、前記原水を浄化するための設備である第2浄化設備と、
     を備えており、
     前記分岐管の先端から出た浄化された原水が、前記原水タンクに至るようにされているとともに、
     前記メインポンプは、前記サブポンプと独立して駆動させられるようになっているとともに、前記メインポンプが駆動し、且つ前記サブポンプが停止しているときには、前記サブポンプは前記原水を通過させないようになっている、
     循環式濾過システム。
    a raw water tank for storing raw water that is circulated and used repeatedly;
    a flow path pipe having a proximal end connected to the raw water tank, which constitutes a flow path for circulating the raw water;
    A purification facility, which is provided in the middle of the flow pipe and which is for purifying the raw water into purified water, and which includes at least one reverse osmosis membrane water purification unit;
    provided in a portion of the flow pipe on the front side of the reverse osmosis membrane water purification unit that is positioned on the most distal side with respect to the flow pipe, and when it is driven, the raw water in the flow pipe is a sub-pump for flowing the fluid to the tip end side of the flow pipe in the flow pipe; a main pump that, when driven, causes the raw water in the raw water tank to flow to the tip side of the flow pipe;
    a faucet that is provided at the tip of the flow pipe and that allows selection of whether or not to allow the purified water to be discharged from the flow pipe;
    a saucer for receiving the purified water discharged from the faucet;
    and
    The purified water received by the saucer reaches the raw water tank,
    A circulation filtration system,
    a branch pipe, which is a pipe branched from the flow channel pipe by connecting the proximal end thereof to the flow channel pipe before the sub-pump, which constitutes the flow channel for circulating the raw water;
    a second purification equipment, which is equipment for purifying the raw water, provided in the middle of the branch pipe;
    and
    Purified raw water coming out of the tip of the branch pipe reaches the raw water tank,
    The main pump is driven independently of the sub-pump, and when the main pump is driven and the sub-pump is stopped, the sub-pump does not allow the raw water to pass through. there is
    Circulating filtration system.
  2.  前記メインポンプは、前記サブポンプとは独立して、一日に8時間以上駆動するようになっている、
     請求項1記載の循環式濾過システム。
    The main pump is driven independently of the sub-pump for 8 hours or more per day.
    The circulation filtration system according to claim 1.
  3.  前記メインポンプは、所定の時間毎に、所定の時間長さだけ駆動するようになっている、
     請求項1記載の循環式濾過システム。
    The main pump is driven for a predetermined length of time every predetermined time.
    The circulation filtration system according to claim 1.
  4.  循環させて繰返し使用される水である原水を貯める原水タンクと、
     前記原水を循環させるための流路を構成する、その基端が前記原水タンクに接続された管である流路管と、
     前記流路管の途中に設けられた、前記原水を浄化して浄水にするための設備であり、少なくとも1つの逆浸透膜浄水ユニットを含む浄化設備と、
     前記流路管における、前記流路管に対して最も先端側に位置する前記逆浸透膜浄水ユニットの手前側の部分に設けられた、それが駆動した場合に、前記流路管内の前記原水を、前記流路管内において前記流路管の先端側に流すサブポンプと、前記サブポンプが駆動したときに前記サブポンプと連動して駆動する、前記流路管の前記原水タンク内の前記原水と接する部分に設けられた、それが駆動した場合に、前記原水タンク内の原水を前記流路管の先端側に流すメインポンプと、
     前記流路管の先端に設けられた、前記浄水の前記流路管からの排出の許否を選択することのできるようにされた蛇口と、
     前記蛇口から排出された前記浄水を受ける受皿と、
     を備えており、
     前記受皿で受けた前記浄水が前記原水タンクに至るようにされている、
     循環式濾過システムであって、
     前記原水を循環させるための流路を構成する、その基端が前記原水タンクに接続された管である、前記流路管とは異なる第2流路管と、
     前記第2流路管の前記原水タンク内の前記原水と接する部分に設けられた、それが駆動した場合に、前記原水タンク内の原水を前記第2流路管の先端側に流す第2ポンプと、
     前記第2流路管の途中に設けられた、前記原水を浄化するための設備である第2浄化設備と、
     を備えており、
     前記第2流路管の先端から出た浄化された原水が、前記原水タンクに至るようにされているとともに、
     前記第2ポンプは、前記メインポンプ及び前記サブポンプと独立して駆動させられるようになっている、
     循環式濾過システム。
    a raw water tank for storing raw water that is circulated and used repeatedly;
    a flow path pipe having a proximal end connected to the raw water tank, which constitutes a flow path for circulating the raw water;
    A purification facility, which is provided in the middle of the flow pipe and which is for purifying the raw water into purified water, and which includes at least one reverse osmosis membrane water purification unit;
    provided in a portion of the flow pipe on the front side of the reverse osmosis membrane water purification unit that is positioned on the most distal side with respect to the flow pipe, and when it is driven, the raw water in the flow pipe is a sub-pump for flowing the fluid to the tip end side of the flow pipe in the flow pipe; a main pump that, when driven, causes the raw water in the raw water tank to flow to the tip side of the flow pipe;
    a faucet that is provided at the tip of the flow pipe and that allows selection of whether or not to allow the purified water to be discharged from the flow pipe;
    a saucer for receiving the purified water discharged from the faucet;
    and
    The purified water received by the saucer reaches the raw water tank,
    A circulation filtration system,
    a second flow pipe different from the flow pipe, which constitutes a flow channel for circulating the raw water and is a pipe whose base end is connected to the raw water tank;
    A second pump provided at a portion of the second channel pipe in contact with the raw water in the raw water tank, and when driven, causes the raw water in the raw water tank to flow to the tip side of the second channel pipe. When,
    a second purification equipment, which is equipment for purifying the raw water, provided in the middle of the second flow pipe;
    and
    Purified raw water coming out of the tip of the second flow pipe reaches the raw water tank,
    The second pump is driven independently of the main pump and the sub-pump,
    Circulating filtration system.
  5.  前記第2ポンプは、一日に8時間以上駆動するようになっている、
     請求項4記載の循環式濾過システム。
    said second pump is adapted to operate for 8 hours or more per day;
    The circulation filtration system according to claim 4.
  6.  前記第2ポンプは、所定の時間毎に、所定の時間長さだけ駆動するようになっている、
     請求項4記載の循環式濾過システム。
    the second pump is adapted to run for a predetermined length of time at each predetermined time;
    The circulation filtration system according to claim 4.
  7.  前記第2浄化設備は、オゾン発生装置、紫外線殺菌装置、曝気装置の少なくとも一つを含む、
     請求項1又は4記載の循環式濾過システム。
    The second purification equipment includes at least one of an ozone generator, an ultraviolet sterilizer, and an aerator.
    The circulation filtration system according to claim 1 or 4.
  8.  前記受皿から前記原水タンクへ至る浄水を通過させるための、浄水を濾過するための濾材を備えている、
     請求項1又は4記載の循環式濾過システム。
    A filter medium for filtering purified water for passing purified water from the saucer to the raw water tank,
    The circulation filtration system according to claim 1 or 4.
  9.  前記濾材は、オイル吸着シート、イオン交換樹脂、活性炭のうちの少なくとも一つを含んでいる、
     請求項8記載の循環式濾過システム。
    The filter medium contains at least one of an oil adsorption sheet, an ion exchange resin, and activated carbon.
    The circulation filtration system according to claim 8.
  10.  前記濾材は、バッグフィルターに内蔵されている、
     請求項8又は9記載の循環式濾過システム。
    The filter medium is built into a bag filter,
    The circulation filtration system according to claim 8 or 9.
PCT/JP2022/013351 2021-05-06 2022-03-23 Cycle filtration system WO2022234738A1 (en)

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JPH03218758A (en) * 1990-01-24 1991-09-26 Matsushita Electric Ind Co Ltd Bubble bath circulating device
JPH07108142A (en) * 1993-10-15 1995-04-25 Hitachi Ltd Device for treating antifreeze for cooling automobile engine
JP2001314862A (en) * 2000-05-08 2001-11-13 Kurita Water Ind Ltd Slime preventing method
JP2003039071A (en) * 2001-07-31 2003-02-12 Sanyo Electric Co Ltd Water treatment apparatus and water treatment method
JP2017148793A (en) * 2016-02-19 2017-08-31 株式会社テックコーポレーション Hydrogen water supply apparatus, and hydrogen water production method

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