WO2011099578A1 - Water purification device - Google Patents

Water purification device Download PDF

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Publication number
WO2011099578A1
WO2011099578A1 PCT/JP2011/052929 JP2011052929W WO2011099578A1 WO 2011099578 A1 WO2011099578 A1 WO 2011099578A1 JP 2011052929 W JP2011052929 W JP 2011052929W WO 2011099578 A1 WO2011099578 A1 WO 2011099578A1
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WO
WIPO (PCT)
Prior art keywords
water
filtrate
filtration
line
raw water
Prior art date
Application number
PCT/JP2011/052929
Other languages
French (fr)
Japanese (ja)
Inventor
邦彦 山中
精一 石川
Original Assignee
Yamanaka Kunihiko
Ishikawa Seiichi
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Yamanaka Kunihiko, Ishikawa Seiichi filed Critical Yamanaka Kunihiko
Priority to JP2011553899A priority Critical patent/JP5563604B2/en
Publication of WO2011099578A1 publication Critical patent/WO2011099578A1/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D69/00Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/08Hollow fibre membranes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D65/00Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
    • B01D65/02Membrane cleaning or sterilisation ; Membrane regeneration
    • 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2313/00Details relating to membrane modules or apparatus
    • B01D2313/26Specific gas distributors or gas intakes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2321/00Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2321/00Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
    • B01D2321/02Forward flushing
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2321/00Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
    • B01D2321/10Use of feed
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2321/00Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
    • B01D2321/18Use of gases
    • B01D2321/185Aeration
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2321/00Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
    • B01D2321/44Specific cleaning apparatus
    • 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
    • C02F1/441Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by 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
    • C02F1/74Treatment of water, waste water, or sewage by oxidation with air
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/05Conductivity or salinity
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/16Regeneration of sorbents, filters
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124Water desalination
    • Y02A20/131Reverse-osmosis

Definitions

  • the present invention relates to a circulation type water purifier that performs partial filtration with a filtration membrane, can suppress the growth of bacteria, eliminates the need for cleaning with a chemical solution, or can greatly reduce the frequency thereof, maintainability, environmental conservation It is related with the water purifier excellent in property and energy saving.
  • Patent Document 1 includes a desalination apparatus for seawater (or brine)
  • Patent Document 2 includes a system for producing a sterile aqueous solution
  • Patent Document 3 includes a water treatment apparatus for processing sewage such as sewage. It is disclosed.
  • water shortages are becoming a serious problem on a global scale, and there is a growing demand for technologies for recycling organic wastewater including industrial wastewater and domestic wastewater.
  • membrane filtration methods such as reverse osmosis membranes and ultrafiltration membranes to produce reclaimed water with extremely good water quality that can be used as industrial, agricultural, or household water. Yes.
  • JP-A-6-23356 JP 7-8996 A Japanese Patent Application Laid-Open No. 2007-244979
  • the present invention solves the above-mentioned conventional problems, with a simple configuration, without using a chemical solution, or significantly reducing the frequency, and reliably and efficiently removing solid particles and bacteria attached to the filtration membrane.
  • Bacteria growth can be suppressed, filtration membrane cleaning efficiency and environmental protection are excellent, and the durability, long life and maintenance of the filtration membrane can be greatly improved.
  • Prevention, stability of operation, filtration efficiency, energy saving, and control of electrolyte components contained in filtered water which can easily adjust the conductivity and dissolved oxygen concentration of filtered water.
  • the purpose is to provide a water purifier with excellent versatility that can be used for a wide range of purposes such as drinking water, washing water for foods, tableware and the like.
  • the water purification apparatus is a circulation type water purification apparatus that performs partial filtration with a filtration membrane disposed in a filtration unit, the raw water tank storing raw water, the raw water tank, and the A raw water supply line having a raw water supply pump and a raw water supply valve for connecting the filtration unit and supplying the raw water from the raw water tank to the filtration unit, and an upstream side of the raw water supply pump and the filtration unit connected to the raw water supply line
  • a concentrated water circulation line that circulates the concentrated water in which the solid particles are concentrated in the filtration unit, and a filtered water discharge line that has a filtered water discharge valve that is connected to the filtration unit and discharges the filtered water filtered by the filtration unit;
  • a concentrated water drain having a filtrate water tank for storing filtrate discharged from the filtrate drain line, and a concentrated water discharge valve for branching from the concentrate circulation line and discharging the concentrated
  • a raw water-side bubble generating part that is disposed downstream of the concentrated water discharge valve of the concentrated water discharge line and bubbles in the raw water tank, and from the upstream side of the filtered water discharge valve of the filtered water discharge line
  • a filtered filtrate supply line for washing having a filtrate supply valve that branches and is connected to the concentrated water circulation line downstream from the branch position of the concentrated water circulation line with the concentrated water discharge line and supplies the filtrate as washing water.
  • Concentrated between the raw water supply line and the filtration unit by continuously operating the raw water supply pump because it has a concentrated water circulation line that connects the upstream side of the pump and the filtration unit and circulates the concentrated water in which the solid particles are concentrated in the filtration unit. Filtration can be performed while circulating water, the load of the raw water supply pump can be reduced, and the durability and operational stability are excellent.
  • a concentrated water discharge line having a concentrated water discharge valve that branches off from the concentrated water circulation line and discharges the concentrated water to the raw water tank is provided. Therefore, the concentrated water can be prevented from being excessively concentrated, clogging of the filtration membrane can be reduced, and the filtration efficiency is excellent.
  • the raw water supply pump is not limited as long as it can suck the raw water from the raw water tank and supply it to the filtration unit and circulate the concentrated water concentrated in the filtration unit, but a centrifugal pump or the like is preferably used.
  • a centrifugal pump or the like is preferably used.
  • electromagnetic valves are preferably used.
  • the raw water side bubble generating unit may be any unit that can generate bubbles, but sucks ambient air into the drainage pipe using the negative pressure generated when the concentrated water is discharged from the concentrated water discharge line. Those that generate bubbles are preferably used. This is because drainage energy can be used effectively, no special power is required, and energy saving is excellent.
  • Invention of Claim 2 is a water purifier of Claim 1, Comprising: The switching valve arrange
  • a switching valve disposed downstream from the filtrate water supply valve of the filtrate water supply line for washing and a branch from the filtrate water supply line for washing between the filtrate water supply valve and the selector valve are connected to the raw water tank.
  • the filtration water supply valve of the washing filtrate supply line is closed during filtration, and the switching valve is opened, so that a part of the washing filtrate supply line is used to remove the raw water tank from the drainage line.
  • Concentrated water can be discharged, the piping can be simplified and the apparatus can be miniaturized, and space saving and mass productivity are excellent.
  • the drainage line is arranged in parallel with the concentrated water discharge line, it is possible to circulate by selecting the opening and closing of the switching valve of the washing filtrate supply line and the opening and closing of the concentrated water discharge valve of the concentrated water discharge line.
  • the amount of concentrated water discharged and the amount of bubbling in the raw water tank can be adjusted, and the concentration of the concentrated water can be kept at a moderate level to prevent clogging of the filtration membrane. Excellent.
  • the switching valve only needs to be able to adjust the opening / closing amount in the washing filtrate supply line, but a solenoid valve is preferably used.
  • the switching valve can adjust the supply amount of filtrate when supplying filtrate from the washing filtrate supply line, and also adjust the drainage of concentrated water and the drainage of concentrated water from the concentrate circulation line. be able to.
  • Invention of Claim 3 is a water purifier of Claim 1 or 2, Comprising: The said filtered water tank is connected upstream and the said filtrate water tank of the said filtrate drain valve of the said filtrate drain line, and the said filtrate water is used. It has the structure provided with the filtrate circulating line which has the filtrate circulating pump to circulate. With this configuration, in addition to the operation of the first or second aspect, the following operation is provided. (1) Connect the filtrate water tank upstream with the filtrate drain valve of the filtrate drain line and have a filtrate circulating pump to circulate the filtrate, so circulate the filtrate and filter it on the inner wall of the filtrate drain line. It can prevent the adhesion of minerals in the water and is excellent in maintainability.
  • the filtrate circulating pump may be any pump that can suck and circulate filtrate from the filtrate tank.
  • the required amount of filtered water can be taken out using the power of the filtered water circulation pump. It can be supplied to and has excellent energy savings.
  • Invention of Claim 4 is a water purification apparatus of Claim 3, Comprising: It branches from the said filtrate water supply valve of the said filtrate water supply line for washing
  • a filtration water bubbling line having a filtrate water bubble generating section that branches from the filtrate water supply valve downstream from the filtrate water supply valve and is connected to the filtrate water tank and bubbles in the filtrate water tank.
  • the filtered water-side bubble generating unit may be anything that can generate bubbles, but the negative pressure generated when the filtered water is discharged from the filtered water bubbling line, Those that suck air into a drain pipe to generate bubbles are preferably used. This is because drainage energy can be used effectively, no special power is required, and energy saving is excellent.
  • the Invention of Claim 5 is a water purifier of Claim 4, Comprising:
  • natural water side bubble generation part and the said filtrate water side bubble generation part are a cylindrical liquid inflow pipe, and the said liquid inflow pipe
  • a cylindrical liquid outflow pipe that is provided on the downstream side and has an inner diameter larger than the inner diameter of the liquid inflow pipe, and a plurality of air introduction pipes that are formed in the peripheral wall on the upstream side of the liquid outflow pipe and communicate with the liquid outflow pipe. And a hole.
  • Bubbling can be performed using the drainage energy of the concentrated water and filtered water that passes through the concentrated water discharge line and the filtered water bubbling line. The device can be simplified and the size can be reduced, and the space is saved.
  • the diameters of the liquid inflow pipe, the liquid outflow pipe, and the air introduction microhole can be appropriately selected according to the flow rate (flow velocity) of the fluid passing through the inside, but the inner diameter of the liquid outflow pipe is that of the liquid inflow pipe.
  • the inner diameter of the air introduction micropore is preferably 0.05 to 0.2 times the inner diameter of the liquid outflow pipe. As the inner diameter of the liquid outflow pipe becomes smaller than twice the diameter of the liquid inflow pipe, the gap formed between the fluid passing through the liquid outflow pipe and the inner wall surface of the liquid outflow pipe becomes smaller (the air layer becomes smaller).
  • the amount of air sucked from the air introduction micropores decreases, and bubbles tend to be less likely to be generated, and passes through the liquid outflow pipe as it becomes larger than 5 times the diameter of the liquid inflow pipe.
  • the fluid velocity drops below the pipe resistance, making it difficult for negative pressure to occur, reducing the amount of air sucked in, and the gap formed between the fluid passing through the liquid outlet pipe and the inner wall surface of the liquid outlet pipe Is large (the air layer is thick), the fluid passing through the liquid outflow pipe and the air sucked from the air introduction micropores are difficult to mix and stir, and the amount of bubbles generated tends to decrease, both of which are preferable. Absent.
  • the inner diameter of the air introduction microhole becomes smaller than 0.05 times the inner diameter of the liquid outflow pipe, the workability is lowered and clogging is likely to occur, and the stability of bubble generation tends to be reduced.
  • the pressure difference between the inside and outside of the liquid outflow pipe becomes smaller, and the fluid passing through the liquid outflow pipe And air are less likely to be mixed and stirred, and the amount of bubbles generated tends to decrease, which is not preferable.
  • the cross-sectional shapes of the liquid inflow pipe and the liquid outflow pipe may be uniform in the longitudinal direction, but various combinations can be selected as necessary.
  • the cross-sectional area may be gradually reduced toward the bottom, or the cross-sectional area may be gradually increased from the upstream end side of the liquid inflow pipe toward the downstream end side of the liquid outflow pipe.
  • the cross-sectional area of the liquid outflow pipe is gradually enlarged from the upstream end side toward the downstream end side, turbulent flow is generated inside the liquid outflow pipe, and the suction force of the air introduction micropore is increased. Bubbling (aeration) performance can be improved.
  • the Invention of Claim 6 is a water purifier of any one of Claims 1 thru
  • the said filtration part is two or more filtration membranes from which the performance arrange
  • the filtration unit is arranged in two or more filtration membranes arranged in parallel, a merging pipe connecting the filtration side of each filtration membrane and the filtrate discharge line, and each merging pipe And an electric conductivity meter on the filtrate discharge line, so that the conductivity of the filtrate discharged from the filtration unit can be measured with the conductivity meter.
  • an ultrafiltration membrane As a kind of filtration membrane arrange
  • a reverse osmosis membrane When a reverse osmosis membrane is used as one of the filtration membranes in the filtration section, RO water obtained by filtration through the reverse osmosis membrane can be used as washing filtered water, such as bacteria adhering to the raw water side of the filtration membrane It is possible to remove the deposits reliably and efficiently, and the cleaning efficiency is excellent.
  • Invention of Claim 7 is a water purifier of Claim 6, Comprising: The raw
  • the filtration unit has a raw water side connection pipe connecting the raw water sides of two filtration membranes arranged in parallel and having different performances, and an on-off valve arranged in the raw water side connection pipe, By closing the filtrate discharge valve of the filtrate drain line, the filtered water filtered through the high-performance filtration membrane out of the two filtration membranes has low performance through the confluence pipe by the pressure of the filtrate circulating pump It can be sent to the filtration side of the filtration membrane for cleaning, and is excellent in cleaning efficiency and long life of the filtration membrane.
  • the raw water supply valve of the raw water supply line, the filtrate discharge valve of the filtrate discharge line, and the concentrate discharge valve of the concentrate discharge line are closed, and the filtrate supply line for washing
  • the filtrate water stored in the filtrate water tank is led from the filtrate water circulation line to the filtrate water discharge line and washing filtrate water supply line to the concentrated water circulation line, and then the raw water It can be supplied to the raw water side of the filtration section through the supply line.
  • the raw water supply pump can be opened by opening an on-off valve arranged in the raw water side connecting pipe that connects the raw water sides of the two filtration membranes.
  • the raw water side of the two filtration membranes can be circulated and washed with filtered water, and the filtration membrane is excellent in durability and long life. Then, by selecting the opening and closing of the concentrated water discharge valve as appropriate, a portion of the filtered water used for cleaning is discharged to the raw water tank, and cleaning is performed while exchanging the circulating filtered water with new filtered water. The cleaning efficiency and reliability are excellent.
  • the water purifier of the present invention has the following effects.
  • (1) By generating bubbles in the raw water side bubble generation unit and oxidizing and precipitating organic matter, iron, magnesium, manganese, calcium, etc., the supernatant liquid in the raw water tank is supplied to the filtration unit and efficient in a short time
  • the filter membrane can be filtered and the raw water side of the filtration membrane can be washed using the filtered water filtered in the filtration section, greatly reducing or eliminating the use of chemicals. It is possible to provide a water purifier that is excellent in maintainability and environmental protection, that does not chemically deteriorate the filtration membrane, and that is excellent in durability and long life of the filtration membrane.
  • FIG. 1 is a schematic diagram showing a configuration of a water purifier according to Embodiment 1.
  • 1 is the water purifier of the first embodiment
  • 2 is the raw water tank of the water purifier 1 where raw water collected from rivers, lakes, seas, etc.
  • a discharge section for discharging the sediment precipitated in the raw water tank 2 and the concentrated raw water, 3 is a filtration of the water purification apparatus 1 provided with a filtration membrane such as an ultrafiltration membrane or a reverse osmosis membrane 4, 4 is a raw water supply line connecting the raw water tank 2 and the filtration unit 3, 4a and 4b are pipelines of the raw water supply line 4 from the raw water tank 2 to the filtration unit 3, and 5 is a raw water supply line 4 (pipe 4a).
  • a raw water supply valve that uses an electromagnetic valve or the like that opens and closes the raw water supply line 4, and 6 is a raw water supply that is provided in the raw water supply line 4 (pipe 4 b) to supply raw water from the raw water tank 2 to the filtration unit 3.
  • the pump 7 is disposed in the raw water supply line 4 (pipe 4b).
  • a pressure meter 8 that measures the supply pressure of water, 8 is a concentrated water circulation line of the water purification apparatus 1 that connects the upstream side of the raw water supply pump 6 of the raw water supply line 4 and the filtration unit 3 and circulates the concentrated water concentrated in the filtration unit 3.
  • Pipe line of the discharge line 9, 10 is a filtrate water tank of the water purification device 1 that stores filtrate water discharged from the filtrate water discharge line 9, and 11 is provided in the filtrate water discharge line 9 (between the pipe lines 9 a and 9 b).
  • An air chamber for preventing air from entering the filtration membrane when washing the filtration unit 3 by backflowing filtered water (during backwashing), 12 is disposed in the filtrate discharge line 9 (pipe 9b).
  • Reference numerals a and 13b are arranged in parallel with the filtrate drain line 9, and one or both of them are opened to adjust the filtrate discharge pressure.
  • Concentrated water discharge line 15 of the water purifier 1 for branching out from the concentrated water discharge line 14 for discharging the concentrated water to the raw water tank 2.
  • Reference numeral 16 denotes a check valve disposed downstream of the concentrated water discharge valve 15 of the concentrated water discharge line 14 to prevent the backflow of the concentrated water
  • reference numeral 17 denotes the concentrated water discharge valve 15 and the check of the concentrated water discharge line 14.
  • a raw water-side bubble generating section disposed downstream of the valve 16 and bubbling in the raw water tank 2, 18 is branched from the filtered water discharge valves 13 a and 13 b of the filtered water discharge line 9 from the upstream side (pipe 9 c), and concentrated water is circulated.
  • Concentrated water in line 8 The filtered filtrate supply line 18a, 18b, 18c of the water purifier 1 is connected to the concentrated water circulation line 8 downstream of the branch line with the discharge line 14 and supplies filtered water as washing water.
  • a pipe 19 of the washing filtrate supply line 18 that branches and reaches the concentrated water circulation line 8 is an electromagnetic valve 19 that is disposed in the washing filtrate supply line 18 (pipe 18a) and opens and closes the washing filtrate supply line 18.
  • the filtered water supply valve 20 and the like are disposed downstream of the filtered water supply valve 19 (pipe 18 c) of the washing filtrate supply line 18 and switch between discharging concentrated water and supplying washing filtrate.
  • a switching valve 21 using a solenoid valve or the like is branched from the washing filtrate supply line 18 (between the pipes 18b and 18c) between the filtrate supply valve 19 and the switch valve 20 and connected to the raw water tank 2.
  • Drainage line of the water purifier 1, 1a is a drainage adjusting unit using a pressure regulating valve such as a spring check valve that adjusts the pressure of drainage and is disposed in the drainage line 21, and 21b is disposed in a pipe line 18b of the filtered water supply line 18 for washing.
  • a check valve 22 for preventing the concentrated water discharged from the passage 18 c from flowing into the filtrate water tank 10 through the pipe 18 b is provided downstream of the filtrate water supply valve 19 of the washing filtrate water supply line 18.
  • the filtered water bubbling line 23 of the water purification apparatus 1 branched from the side (between the pipes 18a and 18b) and connected to the filtered water tank 10 is provided in the filtered water bubbling line 22 and passes through the filtered water tank 10.
  • the filtered water side bubble generating unit 24 to be bubbled, 24 is the filtered water circulation of the purified water device 1 that connects the filtered water discharge valve 13a, 13b upstream of the filtered water discharge line 9 (between the pipe lines 9b and 9c) and the filtered water tank 10.
  • a filtered water intake line 26a for supplying water, 26a is a filtered water intake switching valve disposed at a branch position between the conduit 9d of the filtered water discharge line 9 and the filtered water intake line 26, and 27 is a concentrated water discharge line 14.
  • the waste water line 27a is disposed at a branch position between the concentrated water discharge line 14 and the waste water line 27 to prevent the concentrated water from being drained out of the system and concentrated in the raw water tank 2 if necessary.
  • FIG. 1 A wastewater switching valve for switching between discharge of concentrated water to the raw water tank 2 and wastewater to the outside of the system.
  • the filtered water discharge line 9 is provided with two filtered water discharge valves 13a and 13b, and one or both are opened to adjust the pressure.
  • the opening degree (pressure) is arbitrary. In the case of using an arbitrary valve that can be set to 1, one is sufficient.
  • the concentrated water concentrated without being filtered by the filtration unit 3 returns to the raw water supply line 4 (pipe 4b) through the concentrated water circulation line 8 and is circulated. At this time, a part of the circulated concentrated water is discharged to the raw water tank 2 by opening the concentrated water discharge valve 15 of the concentrated water discharge line 14 and the switching valve 20 of the washing filtrate supply line 18 as necessary. To prevent excessive concentration of concentrated water.
  • FIG. 2 is a schematic cross-sectional view of an essential part of a raw water side bubble generating part of the water purifier according to the first embodiment.
  • 30 is a straight liquid inflow pipe of the raw water side bubble generating unit 17
  • 30 a is a liquid inflow hole drilled in the liquid inflow pipe 30, and 31 is connected to the downstream side of the liquid inflow pipe 30 and has an inner diameter.
  • the inner diameters of the liquid inflow pipe 30, the liquid outflow pipe 31, and the air introduction microhole 32 can be appropriately selected depending on the flow rate (flow velocity) of the concentrated water passing through the inside and the number of the air introduction microholes 32.
  • the concentrated water passing through the liquid outflow hole 31a and the liquid outflow pipe 31 There is a tendency that the gap formed between the inner wall surface is small (the air layer is thin), the amount of air sucked from the air introduction microhole 32 is reduced, and bubbles are less likely to be generated.
  • the inner diameter becomes larger than 5 times the speed of the concentrated water passing through the liquid outflow hole 31a decreases, it becomes difficult to generate negative pressure, the amount of air sucked in decreases, and the liquid outflow hole 31a passes through.
  • the gap formed between the concentrated water and the inner wall surface of the liquid outflow pipe 31 is large (the air layer is thick), and the concentrated water passing through the liquid outflow hole 31a and the air sucked from the air introduction microhole 32 are mixed. Become difficult to stir This is because the bubble generation amount is found to have a tendency to become liable to lower.
  • the inner diameter of the air introduction microholes 32 becomes smaller than 0.05 times the inner diameter of the liquid outflow pipe 31, workability deteriorates and clogging occurs.
  • the number of air introduction microholes 32 is preferably 2 to 8, although it varies depending on the inner diameter of the liquid outflow pipe 31.
  • the number of air introduction micropores 32 is less than two, the amount of air sucked from the air introduction micropores 32 is reduced, and it becomes difficult for the concentrated water and air to be mixed and stirred, and the amount of generated bubbles is likely to decrease.
  • the number of air introduction micro-holes 32 is more than 8, the pressure difference between the inside and outside of the liquid outflow pipe 31 becomes small, and the concentrated water and air passing through the liquid outflow hole 31a are mixed and stirred. This is because it has been found that there is a tendency that the bubble generation amount tends to decrease and the durability of the liquid outflow pipe 31 tends to decrease.
  • the cross-sectional shapes of the liquid inflow pipe 30 and the liquid outflow pipe 31 are uniformly formed in the longitudinal direction, but the present invention is not limited to this, and various combinations can be selected as necessary. can do.
  • the cross-sectional area is gradually reduced from the upstream end side to the downstream end side of the liquid outflow pipe 31, or the cross-sectional area is gradually increased from the upstream end side of the liquid inflow pipe 30 toward the downstream end side of the liquid outflow pipe 31. May be enlarged.
  • the cross-sectional area of the liquid outflow pipe 31 is gradually enlarged from the upstream end side toward the downstream end side, turbulent flow is generated inside the liquid outflow pipe 31 and the suction force of the air introduction microhole 32 is increased.
  • the bubbling (aeration) performance can be improved.
  • the filtrate water stored in the filtrate water tank 10 can be removed from the filtrate water discharge line 9 by driving the filtrate circulation pump 25 during filtration. It can be made to circulate between 9d and the filtrate water tank 10, and it can prevent that the mineral content etc. in filtrate water adhere to the pipe inner wall of the filtrate water discharge line 9.
  • the raw water supply valve 5 of the raw water supply line 4 the filtrate water discharge valves 13 a and 13 b of the filtrate discharge line 9 and the concentrated water discharge valve 15 of the concentrated water discharge line 14 are closed while the raw water supply pump 6 and the filtrate circulating pump 25 are driven.
  • the filtrate water stored in the filtrate water tank 10 is opened from the filtrate water circulation line 24 to the pipeline 9c of the filtrate discharge line 9 by opening the filtrate water supply valve 19 and the switching valve 20 of the filtrate water supply line 18 for washing.
  • the bubbled filtered water can be used as the washing water, the substance adhering to the filtration membrane can be peeled off by an oxidizing action, and the washing efficiency by chemical reaction can be improved.
  • the concentrated water discharge valve 15 of the concentrated water discharge line 14 as necessary, a part of the filtered water used for washing can be discharged to the raw water tank 2, and the circulating filtered water can be removed. Washing can be performed efficiently while replacing with new filtered water.
  • the filtrate water side bubble generation part 23 has the same structure as the raw
  • the raw water supply pump 6 and the filtrate circulating pump 25 are continuously driven throughout the filtration and washing, the raw water supply pump is compared with the case where the raw water supply pump 6 and the filtrate circulating pump 25 are intermittently operated. 6 and when the filtrate circulating pump 25 is stopped or re-driven, the load generated can be reduced, and the operation stability and the durability of the apparatus are excellent.
  • the air chamber 11 may be provided as necessary, and may be omitted.
  • the water purifier according to Embodiment 1 has the following action. (1) A raw water tank 2 in which raw water is stored, a raw water supply line 4 having a raw water supply pump 6 and a raw water supply valve 5 that connect the raw water tank 2 and the filtration unit 3 and supply the raw water from the raw water tank 2 to the filtration unit 3. Then, the upstream side of the raw water supply line 6 of the raw water supply line 6 is connected to the filtration unit 3, and the concentrated water in which the solid particles are concentrated in the filtration unit 3 is circulated from the filtration unit 3 to the pipe 4 b of the raw water supply line 4.
  • the water circulation line 8 Since the water circulation line 8 is provided, it is possible to perform filtration while continuously operating the raw water supply pump 6 to circulate the concentrated water, and it is possible to reduce the load caused by stopping or restarting the raw water supply pump 6. Excellent operational stability.
  • the concentrated water discharge line 14 having the concentrated water discharge valve 15 that branches from the concentrated water circulation line 8 and discharges the concentrated water to the raw water tank 2 is provided, the concentrated water that circulates through the concentrated water circulation line 8 as necessary. A part is discharged to the raw water tank 2 to prevent the concentrated water from being excessively concentrated, clogging of the filtration membrane can be reduced, and the filtration efficiency is excellent.
  • the washing filtrate supply line 18 having the filtrate supply valve 19 for supplying water as washing water
  • the raw water side of the filtration membrane can be washed with filtered water, so that no chemical solution is required or the chemical solution
  • the amount used can be greatly reduced, it is excellent in environmental protection, the filtration membrane is not chemically deteriorated, and the filtration membrane is excellent in durability and long life.
  • the switching valve 20 disposed on the downstream side of the filtrate water supply valve 19 of the washing filtrate supply line 18, and the washing filtrate supply line 18 branches between the filtrate water supply valve 19 and the switching valve 20.
  • the filtration filtrate supply line 19 of the washing filtrate supply line 18 is closed during filtration, and the switching valve 20 is opened to open the filtration filtrate supply line 18 for washing.
  • Concentrated water can be discharged from the drainage line 21 to the raw water tank 2 using a part (the pipe line 18c), so that the piping can be simplified and the apparatus can be miniaturized. Excellent.
  • a part (pipe line 18 c) of the washing filtrate supply line 18 and the drainage line 21 are arranged in parallel with the concentrated water discharge line 14, they are arranged in the pipe line 18 c of the washing filtrate supply line 18.
  • the filtrate water discharge line 13 is connected upstream of the filtrate water discharge valves 13a and 13b (the pipe line 9c) and the filtrate water tank 10 and has a filtrate water circulation pump 25 for circulating the filtrate water.
  • Filtrated water bubbling having a filtered water side bubble generating unit 23 that branches from the filtered water supply valve 19 of the washing filtered water supply line 18 from the downstream side and is connected to the filtered water tank 10 to bubble inside the filtered water tank 10.
  • the filtered water bubbled in the filtered water tank 10 can be used as washing water, so that substances such as colloids and hardly soluble salts adhering to the filtration membrane are peeled off by an oxidizing action. It is possible to improve the cleaning efficiency by chemical reaction, suppress the deterioration of the filtration membrane, and have excellent long life.
  • the raw water side bubble generating part 17 and the filtered water side bubble generating part 23 are connected to the liquid inflow part 30 having the liquid inflow hole 30a and the downstream side of the liquid inflow part 30 and have a larger diameter than the liquid inflow hole 30a. Since the liquid outflow part 31 having the liquid outflow hole 31a and the plurality of air introduction micro holes 32 which are formed in the peripheral wall on the upper end side of the liquid outflow part 31 and communicate with the liquid outflow hole 31a are provided, the liquid inflow of the liquid inflow part 30 Concentrated water or filtered water flowing in from the hole 30a passes through the liquid outflow hole 31a of the liquid outflow part 31, so that the pressure inside the liquid outflow part 31 becomes lower than the outside, and the external air becomes the air introduction microhole 32.
  • Bubbling can be performed by using the drainage energy of the concentrated water and filtered water passing through the concentrated water discharge line 14 and the filtered water bubbling line 22, and no power is required separately.
  • the structure can be simplified and the apparatus can be miniaturized, and the space is saved.
  • FIG. 3 is a schematic diagram showing the configuration of the water purifier according to the second embodiment.
  • symbol is attached
  • the water purifier 1a of the second embodiment is different from the first embodiment in that the filtration unit 3A has two filtration membranes 3a and 3b having different performances arranged in parallel, and the filtration membranes 3a and 3b.
  • the raw water side connecting pipe 3c that connects the raw water sides of each other, the merging pipes 28a, 28b that connect the filtration side of each filtration membrane 3a, 3b and the conduit 9a of the filtered water discharge line 9, and each merging pipe 28a, It is the point provided with the electrical conductivity meter 35 arrange
  • the two filtration membranes 3a and 3b having different performances are arranged in parallel in the filtration unit 3A. While measuring and confirming the conductivity (purity) of the filtrate with the conductivity meter 35, the degree of opening of each of the filtrate adjustment valves 29a and 29b is adjusted to obtain filtrate with a desired conductivity (purity). be able to.
  • the filtration membranes 3a and 3b an ultrafiltration membrane, a reverse osmosis membrane, a nano membrane and the like can be used in combination.
  • RO water obtained by filtration through the reverse osmosis membrane can be used as the filtration water for washing, and the filtration membranes 3a and 3b Deposits such as bacteria attached to the raw water side can be reliably and efficiently peeled off, resulting in excellent cleaning efficiency.
  • the pressure is increased on the raw water side of the filtration membrane (for example, reverse osmosis membrane) having the higher performance among the filtration membranes 3a and 3b.
  • the pressure can be released to the raw water side of the lower performance filtration membrane (for example, ultrafiltration membrane) to prevent the filtration membrane from being damaged, and the filtration membrane is excellent in protection.
  • the filtered water amount adjusting valves 29a and 29b may be opened and closed with a time difference by a delay timer or the like to adjust the filtered water amount in each of the filtration membranes 3a and 3b.
  • the filtration unit 3A includes two or more filtration membranes 3a and 3b having different performances arranged in parallel, and filtration water amount adjusting valves 29a and 29b arranged on the filtration side of the respective filtration membranes 3a and 3b.
  • the conductivity meter 35 is disposed in the conduit 9d of the filtrate discharge line 9, so that the conductivity (purity) of the filtrate discharged from the filtration unit 3A is measured with the conductivity meter.
  • each filtered water volume adjustment valve 29a, 29b can be adjusted, and the conductivity (purity) of filtered water can be kept optimal according to the purpose, application, etc., preventing excessive or insufficient filtration. It is excellent in filtration efficiency and energy saving.
  • FIG. 4 is a schematic diagram illustrating the configuration of the water purifier according to the third embodiment.
  • symbol is attached
  • the water purifier 1b of the third embodiment is different from the second embodiment in that the filtration unit 3B is opened and closed disposed on the raw water side connecting pipe 3c that connects the raw water sides of the filtration membranes 3a and 3b.
  • the point provided with the valve 3d and the point provided with the separation tank 4c connected to the tip of the pipe line 4a of the raw water supply line 4 and sunk in the raw water tank 2. Since the operation
  • the filtration membrane 3a is a high performance filtration membrane such as a reverse osmosis membrane
  • the filtration membrane 3b is a medium performance filtration membrane such as an ultrafiltration membrane having a lower performance than the filtration membrane 3a.
  • the on-off valve 3d, the raw water supply valve 5, the filtrate discharge valves 13a and 13b and the filtrate supply valve 19 of the filtrate discharge line 9 are By closing, the filtrate filtered through the high-performance filtration membrane 3a out of the two filtration membranes 3a and 3b is sent to the filtration side of the low-performance filtration membrane 3b by the pressure of the filtrate circulating pump 25, Washing (back washing) can be performed.
  • the filtrate water supply valve 19 is opened, filtration with low performance is performed with a large amount of mixed water obtained by mixing the filtrate filtered through the high-performance filtration membrane 3a and the filtrate stored in the filtrate tank 10.
  • the membrane 3b can be washed (backwashed) from the filtration side.
  • the filtrate shut-off valve is closed, the filtrate filtered through the filtration membrane 3a is sent directly to the filtration side of the filtration membrane 3b through the merge pipes 28a and 28b (filtrate adjustment valves 29a and 29b). Washing (back washing) can be performed, and cleaning reliability and reliability are excellent.
  • the cleaning method for the filtration membranes 3a and 3b can be appropriately selected by opening and closing the on-off valve 3d, and the versatility is excellent.
  • natural water side of the filtration membranes 3a and 3b) in the water purifier 1b of Embodiment 3 is the same as that of Embodiment 1, filtered water is the filtration part 3B.
  • the raw water side is supplied, by opening the on-off valve 3d disposed in the raw water side connecting pipe 3c, the raw water side of the two filtration membranes 3a and 3b is circulated and washed with filtered water by the raw water supply pump 6. be able to.
  • the separation tank 4c is formed in a cylindrical shape with a bottom, and a plurality of through holes are formed in the peripheral wall surface.
  • SS floating matter
  • the separation tank 4c is formed in a cylindrical shape with a bottom, and a plurality of through holes are formed in the peripheral wall surface.
  • Embodiment 3 in addition to the action obtained in Embodiment 1 or 2, it has the following action.
  • the raw water side connection pipe 3c that connects the raw water sides of the two filtration membranes 3a and 3b having different performances arranged in parallel with the filtration unit 3B, and the on-off valve provided in the raw water side connection pipe 3c 3d, the open / close valve 3d, the raw water supply valve 5, and the filtered water discharge line 9 are filtered while the concentrated water discharge valve 15, the switching valve 20 and the filtered water amount adjusting valves 29a and 29b of the concentrated water discharge line 14 are opened.
  • the filtrate filtered through the high-performance filtration membrane 3a out of the two filtration membranes 3a and 3b is filtered by the pressure of the filtrate circulation pump 25. Further, it can be sent to the filtration side of the low-performance filtration membrane 3b through the merging pipes 28a and 28b, and washing can be performed, and the washing efficiency and the long life of the filtration membrane are excellent.
  • the switching valve 20 and the filtrate amount control valves 29a and 29b are opened and the filtrate drain valves 13a and 13b and the on-off valve 3d are closed to wash the low performance filtration membrane 3b, filtration is performed.
  • the filtered water stored in the filtered water tank 10 is supplied from the filtered water circulation pump 25 to the filtered water filtered by the high-performance filtration membrane 3a, and a large amount of mixing is performed.
  • the filter membrane 3b having low performance can be washed from the filtration side with water, and the workability and certainty of filtration membrane cleaning are excellent.
  • the raw water supply pump 6 allows two filters to be opened by opening the on-off valve 3d disposed in the raw water side connecting pipe 3c that connects the raw water sides of the two filtration membranes 3a and 3b.
  • Film 3a can the raw water side of the 3b circulating washed with filtered water, filtration membranes 3a, 3b durability, excellent in long life.
  • the present invention will be specifically described by way of examples.
  • the present invention is not limited to these examples.
  • the water permeability recovery of the filtration membrane by washing was evaluated.
  • filtration and washing were repeated for 140 hours for 14 days for the water purifier 1, and the raw water-side circulation pressure and the filtration-side filtration pressure of the filtration unit 3 were measured during that time.
  • An ultrafiltration membrane (Dializer KF-15 manufactured by Kawasumi Chemical Co., Ltd.) was used as the filtration membrane.
  • the raw water supply line uses a silicon tube with an inner diameter of 3 mm, the raw water side line length is 4 m, the quantitative filtration pressure is 2.5 kPa, the membrane pressure loss is 20 Pa, and the viscosity of the raw water (test water) is 0.002 Pa ⁇ s.
  • Quantitative filtration was performed using a flow rate of about 10 ⁇ 10 ⁇ 6 m 3 / s obtained from Poiseuille's law as the flow rate of the raw water supply pump.
  • the flow rate of the filtrate circulating pump was about 7 ⁇ 10 ⁇ 6 m 3 / s.
  • the raw water (test water) used for the evaluation was adjusted so that the humic acid concentration was about 10 times that of the natural world by adding humic acid to the soil water along the coast of the Onga River. It is added.
  • FIG. 5 is a diagram showing changes in TMP (transmembrane pressure difference) when filtration and washing are repeated.
  • the horizontal axis is the number of days elapsed from the start of use
  • the vertical axis is the pressure
  • what is plotted with a black circle is the raw water-side circulation pressure
  • what is plotted with the white square is the filtration-side filtration pressure.
  • FIG. 4 only the pressure fluctuation measured during filtration or washing is plotted, and while the apparatus is at rest (one day of filtration or washing is finished, then washing or filtration is started). Is not included.
  • the period during which the raw water side circulation pressure is high and the filtration side filtration pressure is low is the state during filtration, and the period during which the raw water side circulation pressure is low and the filtration side filtration pressure is high represents the state during washing. Yes. From FIG. 5, even if the water purifier 1 is driven for 14 days for 140 hours, there is almost no change in TMP (transmembrane pressure difference), and the water permeability (filtration efficiency) of the filtration membrane is maintained almost constant by washing. I understand that. As a result, the water purifier of the present invention having a cleaning function with the bubbling filtered water can realize sufficient water permeability recovery by circulating cleaning, and the filter membrane has a long life, durability, and environmental protection. It can be said that it is excellent.
  • the present invention has a simple structure and suppresses bacterial growth by removing impurities and bacteria adhering to the filter membrane reliably and efficiently without using chemicals or by greatly reducing the amount of chemicals used.
  • Excellent filtration membrane cleaning efficiency and environmental protection can greatly improve the durability, long life, and maintainability of the filtration membrane, prevent deterioration of filtration performance over time, and stable operation
  • the purity of filtered water can be easily adjusted by controlling the electrolyte components contained in the filtered water, and the filtered water can be washed in drinking water, food, dishes, etc.

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Abstract

Disclosed is a water purification device having excellent versatility, which is capable of reliably and efficiently eliminating impurities, bacteria, or the like adhered to a filtration membrane to suppress bacterial growth with a simple configuration without using a chemical solution, has excellent washing efficiency and environmental protection performance of the filtration membrane, improves the durability, long life performance, and maintenance performance of the filtration membrane significantly, prevents the time degradation of filtration performance, has excellent stability of operation, efficiency of filtration, and energy conservation performance, is capable of controlling an electrolyte component, or the like in filtrate to easily adjust the purity of the filtrate, and is capable of using the filtrate for a wide range of applications such as drinking water, or washing water for food, tableware, or the like. Specifically disclosed is a water purification device which is provided with: a raw water tank; a raw water supply line that supplies raw water to a filtration section; a concentrated water circulation line that allows the circulation of concentrated water; a filtrate discharge line that discharges filtrate; a filtrate tank that stores the filtrate; a concentrated water discharge line that discharges the concentrated water to the raw water tank; a raw-water-side bubble generating section that bubbles the interior of the raw water tank; and a washing filtrate supply line that supplies the filtrate as washing water.

Description

浄水装置Water purifier
 本発明は、ろ過膜で部分ろ過を行う循環型の浄水装置に関し、細菌の増殖を抑えることができ、薬液による洗浄を不要とし、若しくは大幅にその頻度を減じることができ、メンテナンス性、環境保全性、省エネルギー性に優れた浄水装置に関する。 The present invention relates to a circulation type water purifier that performs partial filtration with a filtration membrane, can suppress the growth of bacteria, eliminates the need for cleaning with a chemical solution, or can greatly reduce the frequency thereof, maintainability, environmental conservation It is related with the water purifier excellent in property and energy saving.
 従来、海水およびかん水の淡水化、医療用・工業用の純水、超純水の製造、工業廃水処理、食品工業など、幅広い分野で、膜による分離技術が利用されている。
 例えば(特許文献1)には海水(又はかん水)の淡水化装置、(特許文献2)には無菌水溶液を製造する系、(特許文献3)には下水等の汚水を処理する水処理装置が開示されている。
 そして、近年では、世界規模で水不足が深刻な問題となりつつあり、産業廃水、生活廃水などを含む有機性廃水の再利用技術に対する要望が社会的に高まっている。
 中でも逆浸透膜や限外ろ過膜などの膜ろ過法を用いることにより、工業用、農業用、あるいは家庭用の用水として利用可能な極めて良好な水質を持つ再生水を造水する方法が注目されている。
Conventionally, membrane separation technology has been used in a wide range of fields such as desalination of seawater and brine, medical and industrial pure water, ultrapure water production, industrial wastewater treatment, and food industry.
For example, (Patent Document 1) includes a desalination apparatus for seawater (or brine), (Patent Document 2) includes a system for producing a sterile aqueous solution, and (Patent Document 3) includes a water treatment apparatus for processing sewage such as sewage. It is disclosed.
In recent years, water shortages are becoming a serious problem on a global scale, and there is a growing demand for technologies for recycling organic wastewater including industrial wastewater and domestic wastewater.
Of particular note is the use of membrane filtration methods such as reverse osmosis membranes and ultrafiltration membranes to produce reclaimed water with extremely good water quality that can be used as industrial, agricultural, or household water. Yes.
特開平6-23356号JP-A-6-23356 特開平7-8996号JP 7-8996 A 特開2007-244979号Japanese Patent Application Laid-Open No. 2007-244979
 しかしながら、上記従来の技術においては、以下のような課題を有していた。
(1)逆浸透膜や限外ろ過膜によるろ過では、溶液(原水)中に溶解している無機イオンや有機物などの成分を分離、除去することができるが、濃縮或いは沈殿したコロイド、難溶解性塩類、バクテリアなどの不純物が逆浸透膜(限外ろ過膜)の表面に付着又は増殖することにより、ろ過膜が目詰まりし、ろ過(透水)性能が経時的に劣化して、製造されるろ過水の純度(水質)が低下し易く、ろ過膜の長寿命性、ろ過水の水質安定性に欠けるという課題があった。
(2)また、目詰まりによってろ過性能が低下した場合、薬液循環ラインによってアルカリ性又は酸性の洗浄剤を循環させてろ過膜を洗浄した後、大量の水でろ過膜に残留した薬液を洗浄除去しなければならず、煩雑な作業が必要で、メンテナンス性、省資源性、環境保全性に欠けるという課題があった。
(3)さらに、薬液洗浄によってろ過膜の透水性が回復しても、ろ過膜自体が化学的に劣化し、水質が回復しないことがあり、その場合は、ろ過膜を交換しなければならず、省資源性、耐久性に欠けるという課題があった。
(4)また、逆浸透膜(限外ろ過膜)による逆浸透水(限外ろ過水)の製造においては、加圧ポンプが間欠運転されるが、この間欠運転は加圧ポンプに負担をかけるだけでなく、逆浸透膜(限外ろ過膜)にも脈動負荷をかけ、ろ過膜への物理的な負担が大きく、原水濃縮による膜付着物も増加し、装置及びろ過膜の長寿命性、耐久性、動作の安定性に欠けるという課題があった。
(5)膜ろ過によるろ過水の溶存酸素濃度は、原水溶存酸素濃度の影響を受けて変動し易く、品質(溶存酸素濃度)の安定性に欠けるという課題があった。
However, the above conventional techniques have the following problems.
(1) In filtration using a reverse osmosis membrane or ultrafiltration membrane, components such as inorganic ions and organic substances dissolved in the solution (raw water) can be separated and removed, but concentrated or precipitated colloids, hardly soluble Produced when impurities such as basic salts and bacteria adhere to or propagate on the surface of reverse osmosis membranes (ultrafiltration membranes), clogging the filtration membranes, and the filtration (water permeability) performance deteriorates over time There was a problem that the purity (water quality) of the filtrate was likely to be lowered, and the long-life property of the filtration membrane and the water quality stability of the filtrate were lacking.
(2) Also, if the filtration performance deteriorates due to clogging, after washing the filtration membrane by circulating an alkaline or acidic cleaning agent through the chemical solution circulation line, the chemical solution remaining on the filtration membrane is washed away with a large amount of water. There is a problem in that it requires complicated work and lacks maintainability, resource saving, and environmental conservation.
(3) Furthermore, even if the water permeability of the filtration membrane is restored by chemical cleaning, the filtration membrane itself may be chemically deteriorated and the water quality may not be restored. In that case, the filtration membrane must be replaced. There was a problem of lack of resource saving and durability.
(4) In the production of reverse osmosis water (ultrafiltration water) using a reverse osmosis membrane (ultrafiltration membrane), the pressurization pump is intermittently operated, but this intermittent operation places a burden on the pressurization pump. In addition, the reverse osmosis membrane (ultrafiltration membrane) is also subjected to pulsation load, the physical burden on the filtration membrane is large, the amount of membrane adhering due to concentration of raw water also increases, the long life of the device and filtration membrane, There was a problem of lack of durability and operational stability.
(5) The dissolved oxygen concentration of filtrated water by membrane filtration is likely to fluctuate under the influence of the raw water-soluble oxygen concentration, and there is a problem that the quality (dissolved oxygen concentration) is not stable.
 本発明は上記従来の課題を解決するもので、簡素な構成で、薬液を用いることなく、若しくは大幅に頻度を減じ、ろ過膜に付着した固体粒子や細菌などを確実かつ効率的に除去して細菌の増殖を抑制することができ、ろ過膜の洗浄効率性、環境保護性に優れ、ろ過膜の耐久性、長寿命性、メンテナンス性を大幅に向上させることができ、ろ過性能の経時劣化を防ぎ、動作の安定性、ろ過の効率性、省エネルギー性に優れると共に、ろ過水に含まれる電解質成分等をコントロールしてろ過水の電導度及び溶存酸素濃度を簡便に調整することができ、ろ過水を飲料水、食品や食器等の洗浄水など幅広い用途に使用することが可能な汎用性に優れた浄水装置の提供を目的とする。 The present invention solves the above-mentioned conventional problems, with a simple configuration, without using a chemical solution, or significantly reducing the frequency, and reliably and efficiently removing solid particles and bacteria attached to the filtration membrane. Bacteria growth can be suppressed, filtration membrane cleaning efficiency and environmental protection are excellent, and the durability, long life and maintenance of the filtration membrane can be greatly improved. Prevention, stability of operation, filtration efficiency, energy saving, and control of electrolyte components contained in filtered water, which can easily adjust the conductivity and dissolved oxygen concentration of filtered water. The purpose is to provide a water purifier with excellent versatility that can be used for a wide range of purposes such as drinking water, washing water for foods, tableware and the like.
 上記課題を解決するために本発明の浄水装置は、以下の構成を有している。
 本発明の請求項1に記載の浄水装置は、ろ過部に配設されたろ過膜で部分ろ過を行う循環型の浄水装置であって、原水が貯留される原水タンクと、前記原水タンクと前記ろ過部を接続し前記原水タンクから前記ろ過部に前記原水を供給する原水供給ポンプ及び原水供給弁を有する原水供給ラインと、前記原水供給ラインの前記原水供給ポンプより上流側と前記ろ過部を接続し前記ろ過部で固体粒子が濃縮された濃縮水を循環させる濃縮水循環ラインと、前記ろ過部に接続され前記ろ過部でろ過されたろ過水を排出するろ過水排出弁を有するろ過水排出ラインと、前記ろ過水排出ラインから排出されるろ過水を貯留するろ過水タンクと、前記濃縮水循環ラインから分岐して前記濃縮水を前記原水タンクに排出する濃縮水排出弁を有する濃縮水排出ラインと、前記濃縮水排出ラインの前記濃縮水排出弁より下流側に配設され前記原水タンク内をバブリングする原水側気泡発生部と、前記ろ過水排出ラインの前記ろ過水排出弁より上流側から分岐して前記濃縮水循環ラインの前記濃縮水排出ラインとの分岐位置より下流側で前記濃縮水循環ラインに接続されて前記ろ過水を洗浄水として供給するろ過水供給弁を有する洗浄用ろ過水供給ラインと、を備えた構成を有している。
 この構成により、以下のような作用を有する。
(1)原水が貯留される原水タンクと、原水タンクとろ過部を接続し原水タンクからろ過部に原水を供給する原水供給ポンプ及び原水供給弁を有する原水供給ラインと、原水供給ラインの原水供給ポンプより上流側とろ過部を接続しろ過部で固体粒子が濃縮された濃縮水を循環させる濃縮水循環ラインを備えるので、原水供給ポンプを連続運転して原水供給ラインとろ過部との間で濃縮水を循環させながらろ過を行うことができ、原水供給ポンプの負荷を低減することができ、耐久性、動作の安定性に優れる。
(2)濃縮水循環ラインから分岐して濃縮水を原水タンクに排出する濃縮水排出弁を有する濃縮水排出ラインを備えるので、必要に応じて濃縮水循環ラインを循環する濃縮水の一部を排出して濃縮水が過度に濃縮することを防止し、ろ過膜の目詰まりを低減することができ、ろ過の効率性に優れる。
(3)濃縮水排出ラインの濃縮水排出弁より下流側に配設され原水タンク内をバブリングする原水側気泡発生部を備えることにより、有機物又は鉄、マグネシウム、マンガン、カルシウムなどを酸化させて沈殿させることができるので、原水タンク内の上澄み液をろ過部に供給して短時間で効率的にろ過することができ、ろ過の効率性に優れる。
(4)ろ過水排出ラインのろ過水排出弁より上流側から分岐して濃縮水循環ラインの濃縮水排出ラインとの分岐位置より下流側で濃縮水循環ラインに接続されてろ過水を洗浄水として供給するろ過水供給弁を有する洗浄用ろ過水供給ラインを備えることにより、ろ過膜の原水側をろ過水で洗浄することができるので、薬液による洗浄を不要とし、若しくはその頻度を大幅に削減し、環境保護性に優れ、ろ過膜が化学的に劣化することがなく、ろ過膜の耐久性、長寿命性に優れる。
In order to solve the above problems, the water purifier of the present invention has the following configuration.
The water purification apparatus according to claim 1 of the present invention is a circulation type water purification apparatus that performs partial filtration with a filtration membrane disposed in a filtration unit, the raw water tank storing raw water, the raw water tank, and the A raw water supply line having a raw water supply pump and a raw water supply valve for connecting the filtration unit and supplying the raw water from the raw water tank to the filtration unit, and an upstream side of the raw water supply pump and the filtration unit connected to the raw water supply line A concentrated water circulation line that circulates the concentrated water in which the solid particles are concentrated in the filtration unit, and a filtered water discharge line that has a filtered water discharge valve that is connected to the filtration unit and discharges the filtered water filtered by the filtration unit; A concentrated water drain having a filtrate water tank for storing filtrate discharged from the filtrate drain line, and a concentrated water discharge valve for branching from the concentrate circulation line and discharging the concentrated water to the raw water tank. A raw water-side bubble generating part that is disposed downstream of the concentrated water discharge valve of the concentrated water discharge line and bubbles in the raw water tank, and from the upstream side of the filtered water discharge valve of the filtered water discharge line A filtered filtrate supply line for washing having a filtrate supply valve that branches and is connected to the concentrated water circulation line downstream from the branch position of the concentrated water circulation line with the concentrated water discharge line and supplies the filtrate as washing water. And a configuration provided with.
This configuration has the following effects.
(1) A raw water tank in which raw water is stored, a raw water supply line having a raw water supply pump and a raw water supply valve that connect the raw water tank and the filtration unit and supply raw water from the raw water tank to the filtration unit, and a raw water supply of the raw water supply line Concentrated between the raw water supply line and the filtration unit by continuously operating the raw water supply pump because it has a concentrated water circulation line that connects the upstream side of the pump and the filtration unit and circulates the concentrated water in which the solid particles are concentrated in the filtration unit. Filtration can be performed while circulating water, the load of the raw water supply pump can be reduced, and the durability and operational stability are excellent.
(2) A concentrated water discharge line having a concentrated water discharge valve that branches off from the concentrated water circulation line and discharges the concentrated water to the raw water tank is provided. Therefore, the concentrated water can be prevented from being excessively concentrated, clogging of the filtration membrane can be reduced, and the filtration efficiency is excellent.
(3) Oxidizing organic substances or iron, magnesium, manganese, calcium, etc., by depositing a raw water side bubble generating part that is arranged downstream from the concentrated water discharge valve of the concentrated water discharge line and bubbles inside the raw water tank Therefore, the supernatant liquid in the raw water tank can be supplied to the filtration unit and efficiently filtered in a short time, and the filtration efficiency is excellent.
(4) Branch from the filtrate drain valve upstream from the filtrate drain valve and connect to the concentrate circulation line downstream from the branch position with the concentrate drain line of the concentrate circulation line to supply filtrate as wash water By providing a washing filtrate supply line with a filtration water supply valve, the raw water side of the filtration membrane can be washed with filtered water, which eliminates the need for chemical cleaning or greatly reduces the frequency of the environment. Excellent protection, the filtration membrane does not deteriorate chemically, and the filtration membrane has excellent durability and long life.
 ここで、ろ過膜としては、限外ろ過膜や逆浸透膜、中空糸膜などを使用することができる。
 原水供給ポンプは、原水タンクから原水を吸引して、ろ過部に供給すると共に、ろ過部で濃縮される濃縮水を循環させることができるものであればよいが、遠心ポンプ等が好適に用いられる。
 原水供給弁、ろ過水排出弁、ろ過水供給弁としては、いずれも電磁弁が好適に用いられる。
 原水側気泡発生部は、気泡を発生させることができるものであればよいが、濃縮水排出ラインから濃縮水を排出する際に発生する負圧を利用して、周囲の空気を排水管内に吸い込んで気泡を発生させるものが好適に用いられる。排水エネルギーを有効に利用することができ、特別な動力を必要とせず、省エネルギー性に優れるからである。
Here, as a filtration membrane, an ultrafiltration membrane, a reverse osmosis membrane, a hollow fiber membrane, etc. can be used.
The raw water supply pump is not limited as long as it can suck the raw water from the raw water tank and supply it to the filtration unit and circulate the concentrated water concentrated in the filtration unit, but a centrifugal pump or the like is preferably used. .
As the raw water supply valve, the filtrate discharge valve, and the filtrate supply valve, electromagnetic valves are preferably used.
The raw water side bubble generating unit may be any unit that can generate bubbles, but sucks ambient air into the drainage pipe using the negative pressure generated when the concentrated water is discharged from the concentrated water discharge line. Those that generate bubbles are preferably used. This is because drainage energy can be used effectively, no special power is required, and energy saving is excellent.
 請求項2に記載の発明は、請求項1に記載の浄水装置であって、前記洗浄用ろ過水供給ラインの前記ろ過水供給弁より下流側に配設された切替弁と、前記ろ過水供給弁と前記切替弁の間で前記洗浄用ろ過水供給ラインから分岐して前記原水タンクに接続された排水ラインと、を備えた構成を有している。
 この構成により、請求項1の作用に加え、以下のような作用を有する。
(1)洗浄用ろ過水供給ラインのろ過水供給弁より下流側に配設された切替弁と、ろ過水供給弁と切替弁の間で洗浄用ろ過水供給ラインから分岐して原水タンクに接続された排水ラインを有するので、ろ過時に洗浄用ろ過水供給ラインのろ過水供給弁を閉じ、切替弁を開くことにより、洗浄用ろ過水供給ラインの一部を利用して、排水ラインから原水タンクへ濃縮水の排出を行うことができ、配管を簡素化して装置を小型化することができ、省スペース性、量産性に優れる。
(2)排水ラインが濃縮水排出ラインと並列に配設されるので、洗浄用ろ過水供給ラインの切替弁の開閉と、濃縮水排出ラインの濃縮水排出弁の開閉を選択することにより、循環中の濃縮水の排出量と原水タンク内でのバブリング量を調整することができ、濃縮水の濃度を適度に保持してろ過膜の目詰まりを防止することが可能で、ろ過の効率性に優れる。
 ここで、切替弁は洗浄用ろ過水供給ラインにおける開閉量を調整できるものがあればよいが、電磁弁が好適に用いられる。切替弁は洗浄用ろ過水供給ラインからろ過水を供給する際に、ろ過水の供給量を調整することができると共に、濃縮水循環ラインからの濃縮水の排水の有無及び濃縮水の排水量を調整することができる。
Invention of Claim 2 is a water purifier of Claim 1, Comprising: The switching valve arrange | positioned downstream from the said filtrate water supply valve of the said filtration water supply line for washing | cleaning, and the said filtrate water supply A drainage line that branches from the cleaning filtrate supply line between the valve and the switching valve and is connected to the raw water tank.
With this configuration, in addition to the operation of the first aspect, the following operation is provided.
(1) A switching valve disposed downstream from the filtrate water supply valve of the filtrate water supply line for washing and a branch from the filtrate water supply line for washing between the filtrate water supply valve and the selector valve are connected to the raw water tank. Since the drainage line is used, the filtration water supply valve of the washing filtrate supply line is closed during filtration, and the switching valve is opened, so that a part of the washing filtrate supply line is used to remove the raw water tank from the drainage line. Concentrated water can be discharged, the piping can be simplified and the apparatus can be miniaturized, and space saving and mass productivity are excellent.
(2) Since the drainage line is arranged in parallel with the concentrated water discharge line, it is possible to circulate by selecting the opening and closing of the switching valve of the washing filtrate supply line and the opening and closing of the concentrated water discharge valve of the concentrated water discharge line. The amount of concentrated water discharged and the amount of bubbling in the raw water tank can be adjusted, and the concentration of the concentrated water can be kept at a moderate level to prevent clogging of the filtration membrane. Excellent.
Here, the switching valve only needs to be able to adjust the opening / closing amount in the washing filtrate supply line, but a solenoid valve is preferably used. The switching valve can adjust the supply amount of filtrate when supplying filtrate from the washing filtrate supply line, and also adjust the drainage of concentrated water and the drainage of concentrated water from the concentrate circulation line. be able to.
 請求項3に記載の発明は、請求項1又は2に記載の浄水装置であって、前記ろ過水排出ラインの前記ろ過水排出弁より上流側と前記ろ過水タンクを接続し、前記ろ過水を循環させるろ過水循環ポンプを有するろ過水循環ラインを備えた構成を有している。
 この構成により、請求項1又は2の作用に加え、以下のような作用を有する。
(1)ろ過水排出ラインのろ過水排出弁より上流側とろ過水タンクを接続し、ろ過水を循環させるろ過水循環ポンプを有するので、ろ過水を循環させてろ過水排出ラインの管内壁にろ過水中のミネラル分などが付着することを防止でき、メンテナンス性に優れる。
 ここで、ろ過水循環ポンプは、ろ過水タンクからろ過水を吸引して循環させることができるものであればよい。
 また、ろ過水排出ラインのろ過水循環ラインとの分岐位置より下流側から分岐してろ過水取水ラインを設けることにより、ろ過水循環ポンプの動力を利用してろ過水を必要な量だけ取り出して系外に供給することができ、省エネルギー性に優れる。
Invention of Claim 3 is a water purifier of Claim 1 or 2, Comprising: The said filtered water tank is connected upstream and the said filtrate water tank of the said filtrate drain valve of the said filtrate drain line, and the said filtrate water is used. It has the structure provided with the filtrate circulating line which has the filtrate circulating pump to circulate.
With this configuration, in addition to the operation of the first or second aspect, the following operation is provided.
(1) Connect the filtrate water tank upstream with the filtrate drain valve of the filtrate drain line and have a filtrate circulating pump to circulate the filtrate, so circulate the filtrate and filter it on the inner wall of the filtrate drain line. It can prevent the adhesion of minerals in the water and is excellent in maintainability.
Here, the filtrate circulating pump may be any pump that can suck and circulate filtrate from the filtrate tank.
In addition, by providing a filtered water intake line that branches from the downstream side of the filtered water discharge line and the filtered water circulation line, the required amount of filtered water can be taken out using the power of the filtered water circulation pump. It can be supplied to and has excellent energy savings.
 請求項4に記載の発明は、請求項3に記載の浄水装置であって、前記洗浄用ろ過水供給ラインの前記ろ過水供給弁より下流側から分岐して前記ろ過水タンクに接続され前記ろ過水タンク内をバブリングするろ過水側気泡発生部を有するろ過水バブリング用ラインを備えた構成を有している。
 この構成により、請求項3の作用に加え、以下のような作用を有する。
(1)洗浄用ろ過水供給ラインのろ過水供給弁より下流側から分岐してろ過水タンクに接続されろ過水タンク内をバブリングするろ過水側気泡発生部を有するろ過水バブリング用ラインを備えることにより、ろ過水タンク内でバブリングされたろ過水を洗浄水として利用することができるので、ろ過膜に付着したコロイドや難溶解性塩類等の物質を酸化作用で剥離させることができ、化学反応による洗浄効率の向上を図ると共に、ろ過膜の劣化を抑えることができ、長寿命性に優れる。
 ここで、ろ過水側気泡発生部は、気泡を発生させることができるものであればよいが、ろ過水バブリング用ラインからろ過水を排出する際に発生する負圧を利用して、周囲の空気を排水管内に吸い込んで気泡を発生させるものが好適に用いられる。排水エネルギーを有効に利用することができ、特別な動力を必要とせず、省エネルギー性に優れるからである。
Invention of Claim 4 is a water purification apparatus of Claim 3, Comprising: It branches from the said filtrate water supply valve of the said filtrate water supply line for washing | cleaning from the downstream, and is connected to the said filtrate water tank, and the said filtration It has the structure provided with the line for filtered water bubbling which has the filtration water side bubble generation part which bubbles the inside of a water tank.
With this configuration, in addition to the operation of the third aspect, the following operation is provided.
(1) A filtration water bubbling line having a filtrate water bubble generating section that branches from the filtrate water supply valve downstream from the filtrate water supply valve and is connected to the filtrate water tank and bubbles in the filtrate water tank. Because the filtered water bubbled in the filtered water tank can be used as washing water, substances such as colloids and sparingly soluble salts adhering to the filtration membrane can be peeled off by an oxidative action, and by chemical reaction In addition to improving the cleaning efficiency, it is possible to suppress the deterioration of the filtration membrane and to have a long life.
Here, the filtered water-side bubble generating unit may be anything that can generate bubbles, but the negative pressure generated when the filtered water is discharged from the filtered water bubbling line, Those that suck air into a drain pipe to generate bubbles are preferably used. This is because drainage energy can be used effectively, no special power is required, and energy saving is excellent.
 請求項5に記載の発明は、請求項4に記載の浄水装置であって、前記原水側気泡発生部及び前記ろ過水側気泡発生部が、筒状の液体流入管と、前記液体流入管の下流側に連設され前記液体流入管の内径より大きな内径を有する筒状の液体流出管と、前記液体流出管の上流側の周壁に穿設され前記液体流出管と連通する複数の空気導入微孔と、を備えた構成を有している。
 この構成により、請求項4の作用に加え、以下のような作用を有する。
(1)原水側気泡発生部及びろ過水側気泡発生部が、筒状の液体流入管と、液体流入管の下流側に連設され液体流入管の内径より大きな内径を有する筒状の液体流出管と、液体流出管の上流側の周壁に穿設され液体流出管と連通する複数の空気導入微孔を有するので、液体流入管から流入した濃縮水やろ過水が、液体流出管を通過することにより、液体流出管の内部の圧力が外部より低くなり、外部の空気が空気導入微孔から液体流出管の内部に吸い込まれ、内部を流れる濃縮水やろ過水と混合、攪拌され濃縮水やろ過水を簡便にバブリングすることができる。
(2)濃縮水排出ラインやろ過水バブリング用ラインを通過する濃縮水やろ過水の排水エネルギーを利用してバブリングを行うことができ、別途、動力を必要とせず、省エネルギー性に優れ、構成を簡素化して装置を小型化することができ、省スペース性に優れる。
Invention of Claim 5 is a water purifier of Claim 4, Comprising: The said raw | natural water side bubble generation part and the said filtrate water side bubble generation part are a cylindrical liquid inflow pipe, and the said liquid inflow pipe A cylindrical liquid outflow pipe that is provided on the downstream side and has an inner diameter larger than the inner diameter of the liquid inflow pipe, and a plurality of air introduction pipes that are formed in the peripheral wall on the upstream side of the liquid outflow pipe and communicate with the liquid outflow pipe. And a hole.
With this configuration, in addition to the operation of the fourth aspect, the following operation is provided.
(1) A cylindrical liquid outflow in which the raw water side bubble generating part and the filtrate water side bubble generating part are connected to the cylindrical liquid inflow pipe and the downstream side of the liquid inflow pipe and have an inner diameter larger than the inner diameter of the liquid inflow pipe Since it has a plurality of air introduction micropores that are drilled in the peripheral wall on the upstream side of the pipe and the liquid outflow pipe and communicate with the liquid outflow pipe, the concentrated water and filtered water flowing in from the liquid inflow pipe pass through the liquid outflow pipe As a result, the pressure inside the liquid outflow pipe becomes lower than the outside, and external air is sucked into the liquid outflow pipe from the air introduction micropores, and is mixed and stirred with the concentrated water and filtered water flowing inside. Filtered water can be easily bubbled.
(2) Bubbling can be performed using the drainage energy of the concentrated water and filtered water that passes through the concentrated water discharge line and the filtered water bubbling line. The device can be simplified and the size can be reduced, and the space is saved.
 ここで、液体流入管、液体流出管、空気導入微孔の管径は、内部を通過する流体の流量(流速)によって適宜、選択することができるが、液体流出管の内径は液体流入管の内径の2倍~5倍に形成し、空気導入微孔の内径は液体流出管の内径の0.05倍~0.2倍に形成することが好ましい。
 液体流出管の内径が、液体流入管の管径の2倍よりも小さくなるにつれ、液体流出管を通過する流体と液体流出管の内壁面との間に形成される隙間が小さく(空気層が薄く)なり、空気導入微孔から吸い込まれる空気の量が減少して、気泡が発生し難くなる傾向があり、液体流入管の管径の5倍よりも大きくなるにつれ、液体流出管を通過する流体の速度が配管抵抗より低下し、負圧が発生し難くなって、空気の吸い込み量が減少すると共に、液体流出管を通過する流体と液体流出管の内壁面との間に形成される隙間が大きく(空気層が厚く)なり、液体流出管を通過する流体と空気導入微孔から吸い込まれる空気が混合、攪拌され難くなって、気泡発生量が低下し易くなる傾向があり、いずれも好ましくない。
Here, the diameters of the liquid inflow pipe, the liquid outflow pipe, and the air introduction microhole can be appropriately selected according to the flow rate (flow velocity) of the fluid passing through the inside, but the inner diameter of the liquid outflow pipe is that of the liquid inflow pipe. The inner diameter of the air introduction micropore is preferably 0.05 to 0.2 times the inner diameter of the liquid outflow pipe.
As the inner diameter of the liquid outflow pipe becomes smaller than twice the diameter of the liquid inflow pipe, the gap formed between the fluid passing through the liquid outflow pipe and the inner wall surface of the liquid outflow pipe becomes smaller (the air layer becomes smaller). The amount of air sucked from the air introduction micropores decreases, and bubbles tend to be less likely to be generated, and passes through the liquid outflow pipe as it becomes larger than 5 times the diameter of the liquid inflow pipe. The fluid velocity drops below the pipe resistance, making it difficult for negative pressure to occur, reducing the amount of air sucked in, and the gap formed between the fluid passing through the liquid outlet pipe and the inner wall surface of the liquid outlet pipe Is large (the air layer is thick), the fluid passing through the liquid outflow pipe and the air sucked from the air introduction micropores are difficult to mix and stir, and the amount of bubbles generated tends to decrease, both of which are preferable. Absent.
 空気導入微孔の内径が、液体流出管の内径の0.05倍よりも小さくなるにつれ、加工性が低下すると共に、目詰まりが発生し易くなり、気泡発生の安定性が低下し易くなる傾向があり、液体流出管の内径の0.2倍(=液体流入管の径と同等)よりも大きくなるにつれ、液体流出管の内部と外部の圧力差が小さくなり、液体流出管を通過する流体と空気が混合、攪拌され難くなって、気泡発生量が低下し易くなる傾向があり、いずれも好ましくない。
 尚、液体流入管及び液体流出管の断面形状は、それぞれ長手方向に一様でもよいが、必要に応じて、様々な組合せを選択することができ、液体流出管の上流端側から下流端側に向かって徐々に断面積を縮小させたり、液体流入管の上流端側から液体流出管の下流端側に向かって徐々に断面積を拡大させたりしてもよい。特に、液体流出管の断面積を上流端側から下流端側に向かって徐々に拡大させた場合、液体流出管の内部で乱流が発生し、空気導入微孔の吸引力が増大して、バブリング(エアレーション)の性能を向上させることができる。
As the inner diameter of the air introduction microhole becomes smaller than 0.05 times the inner diameter of the liquid outflow pipe, the workability is lowered and clogging is likely to occur, and the stability of bubble generation tends to be reduced. As the pressure becomes larger than 0.2 times the inner diameter of the liquid outflow pipe (= equal to the diameter of the liquid inflow pipe), the pressure difference between the inside and outside of the liquid outflow pipe becomes smaller, and the fluid passing through the liquid outflow pipe And air are less likely to be mixed and stirred, and the amount of bubbles generated tends to decrease, which is not preferable.
The cross-sectional shapes of the liquid inflow pipe and the liquid outflow pipe may be uniform in the longitudinal direction, but various combinations can be selected as necessary. From the upstream end side to the downstream end side of the liquid outflow pipe The cross-sectional area may be gradually reduced toward the bottom, or the cross-sectional area may be gradually increased from the upstream end side of the liquid inflow pipe toward the downstream end side of the liquid outflow pipe. In particular, when the cross-sectional area of the liquid outflow pipe is gradually enlarged from the upstream end side toward the downstream end side, turbulent flow is generated inside the liquid outflow pipe, and the suction force of the air introduction micropore is increased. Bubbling (aeration) performance can be improved.
 請求項6に記載の発明は、請求項1乃至5の内いずれか1項に記載の浄水装置であって、前記ろ過部が、並列に配設された性能の異なる2以上のろ過膜と、各々の前記ろ過膜のろ過側と前記ろ過水排出ラインを接続する合流管と、各々の前記合流管に配設されたろ過水量調整弁と、を備え、前記ろ過水排出ラインに電導度計が配設された構成を有している。
 この構成により、請求項1乃至5の内いずれか1項の作用に加え、以下のような作用を有する。
(1)ろ過部が、並列に配設された性能の異なる2以上のろ過膜と、各々のろ過膜のろ過側とろ過水排出ラインを接続する合流管と、各々の合流管に配設されたろ過水量調整弁と、を備え、ろ過水排出ラインに電導度計が配設されていることにより、ろ過部から排出されるろ過水の電導度を電導度計で計測しながら、各々のろ過水量調整弁の開度を調整したり、開閉を選択的に切り替えたりして、目的、用途などに応じてろ過水の浄化度(電導度)を最適に保つことが可能で、ろ過の過不足を防止することができ、ろ過の効率性、省エネルギー性に優れる。
Invention of Claim 6 is a water purifier of any one of Claims 1 thru | or 5, Comprising: The said filtration part is two or more filtration membranes from which the performance arrange | positioned in parallel, A merging pipe connecting the filtration side of each of the filtration membranes and the filtrate drainage line, and a filtrate amount adjusting valve disposed in each of the junction pipes, and a conductivity meter in the filtrate drainage line. It has an arranged configuration.
With this configuration, in addition to the operation of any one of claims 1 to 5, the following operation is provided.
(1) The filtration unit is arranged in two or more filtration membranes arranged in parallel, a merging pipe connecting the filtration side of each filtration membrane and the filtrate discharge line, and each merging pipe And an electric conductivity meter on the filtrate discharge line, so that the conductivity of the filtrate discharged from the filtration unit can be measured with the conductivity meter. By adjusting the opening of the water volume adjustment valve or selectively switching between opening and closing, it is possible to keep the purified water (conductivity) optimally according to the purpose and application. It is excellent in filtration efficiency and energy saving.
 ここで、並列に配設するろ過膜の種類としては、限外ろ過膜、逆浸透膜、ナノ膜、中空糸膜などを組合せて使用することができる。
 ろ過部のろ過膜の1つに逆浸透膜を使用した場合、逆浸透膜でろ過して得られるRO水を洗浄用ろ過水として利用することができ、ろ過膜の原水側に付着した細菌などの付着物を確実かつ効率的に剥離することが可能で、洗浄の効率性に優れる。
Here, as a kind of filtration membrane arrange | positioned in parallel, an ultrafiltration membrane, a reverse osmosis membrane, a nano membrane, a hollow fiber membrane, etc. can be used in combination.
When a reverse osmosis membrane is used as one of the filtration membranes in the filtration section, RO water obtained by filtration through the reverse osmosis membrane can be used as washing filtered water, such as bacteria adhering to the raw water side of the filtration membrane It is possible to remove the deposits reliably and efficiently, and the cleaning efficiency is excellent.
 請求項7に記載の発明は、請求項6に記載の浄水装置であって、前記ろ過部が、並列に配設された性能の異なる2つの前記ろ過膜の原水側同士を接続する原水側接続管と、前記原水側接続管に配設された開閉弁と、を備えた構成を有している。
 この構成により、請求項6の作用に加え、以下のような作用を有する。
(1)ろ過部が、並列に配設された性能の異なる2つのろ過膜の原水側同士を接続する原水側接続管と、原水側接続管に配設された開閉弁を有するので、開閉弁とろ過水排出ラインのろ過水排出弁を閉じることにより、2つのろ過膜の内、性能の高いろ過膜を通過してろ過されたろ過水をろ過水循環ポンプの圧力によって、合流管を通して性能の低いろ過膜のろ過側に送り、洗浄を行うことができ、洗浄の効率性、ろ過膜の長寿命性に優れる。
(2)ろ過水排出弁と開閉弁を閉じて性能の低いろ過膜を洗浄する際に、ろ過水供給弁を開くことにより、性能の高いろ過膜でろ過されたろ過水に、ろ過水タンクに貯留されているろ過水をろ過水循環ポンプから供給し、それらを混合した多量の混合水で、性能の低いろ過膜をろ過側から洗浄することができ、ろ過膜洗浄の作業性、確実性に優れる。
(3)原水供給ポンプ及びろ過水循環ポンプを駆動したまま原水供給ラインの原水供給弁,ろ過水排出ラインのろ過水排出弁及び濃縮水排出ラインの濃縮水排出弁を閉じ、洗浄用ろ過水供給ラインのろ過水供給弁及び切替弁を開くことにより、ろ過水タンクに貯留されたろ過水を、ろ過水循環ラインからろ過水排出ライン,洗浄用ろ過水供給ラインへ通して濃縮水循環ラインに導き、さらに原水供給ラインを通してろ過部の原水側に供給することができるが、このとき、2つのろ過膜の原水側同士を接続する原水側接続管に配設された開閉弁を開くことにより、原水供給ポンプで2つのろ過膜の原水側をろ過水で循環洗浄することができ、ろ過膜の耐久性、長寿命性に優れる。そして、濃縮水排出弁の開閉を適宜、選択することにより、洗浄に使用されたろ過水の一部を原水タンクに排出して、循環中のろ過水を新しいろ過水と交換しながら洗浄を行うことができ、洗浄の効率性、確実性に優れる。
Invention of Claim 7 is a water purifier of Claim 6, Comprising: The raw | natural water side connection which the said filtration part connects the raw | natural water side of two said filtration membranes in which the performance arrange | positioned in parallel differs It has the structure provided with the pipe | tube and the on-off valve arrange | positioned at the said raw | natural water side connection pipe.
With this configuration, in addition to the operation of the sixth aspect, the following operation is provided.
(1) Since the filtration unit has a raw water side connection pipe connecting the raw water sides of two filtration membranes arranged in parallel and having different performances, and an on-off valve arranged in the raw water side connection pipe, By closing the filtrate discharge valve of the filtrate drain line, the filtered water filtered through the high-performance filtration membrane out of the two filtration membranes has low performance through the confluence pipe by the pressure of the filtrate circulating pump It can be sent to the filtration side of the filtration membrane for cleaning, and is excellent in cleaning efficiency and long life of the filtration membrane.
(2) When washing the low-performance filtration membrane by closing the filtrate discharge valve and the on-off valve, the filtered water supply valve is opened, so that the filtrate filtered by the high-performance filtration membrane is added to the filtrate water tank. Stored filtered water is supplied from the filtered water circulation pump, and with a large amount of mixed water mixed with them, low performance filtration membranes can be washed from the filtration side, which is excellent in workability and certainty of filtration membrane cleaning. .
(3) With the raw water supply pump and the filtrate circulating pump being driven, the raw water supply valve of the raw water supply line, the filtrate discharge valve of the filtrate discharge line, and the concentrate discharge valve of the concentrate discharge line are closed, and the filtrate supply line for washing By opening the filtered water supply valve and switching valve, the filtrate water stored in the filtrate water tank is led from the filtrate water circulation line to the filtrate water discharge line and washing filtrate water supply line to the concentrated water circulation line, and then the raw water It can be supplied to the raw water side of the filtration section through the supply line. At this time, the raw water supply pump can be opened by opening an on-off valve arranged in the raw water side connecting pipe that connects the raw water sides of the two filtration membranes. The raw water side of the two filtration membranes can be circulated and washed with filtered water, and the filtration membrane is excellent in durability and long life. Then, by selecting the opening and closing of the concentrated water discharge valve as appropriate, a portion of the filtered water used for cleaning is discharged to the raw water tank, and cleaning is performed while exchanging the circulating filtered water with new filtered water. The cleaning efficiency and reliability are excellent.
 本発明の浄水装置によれば、以下のような有利な効果が得られる。
 請求項1に記載の発明によれば、以下のような効果を有する。
(1)原水側気泡発生部で気泡を発生させ、有機物、鉄、マグネシウム、マンガン、カルシウムなどを酸化させて沈殿させることにより、原水タンク内の上澄み液をろ過部に供給して短時間で効率的にろ過することができ、ろ過の効率性に優れると共に、ろ過部でろ過されたろ過水を利用してろ過膜の原水側を洗浄することができ、薬液の使用量を大幅に低減若しくは不要とすることができ、メンテナンス性、環境保護性に優れ、ろ過膜が化学的に劣化することがなく、ろ過膜の耐久性、長寿命性に優れた浄水装置を提供することができる。
According to the water purifier of the present invention, the following advantageous effects can be obtained.
According to invention of Claim 1, it has the following effects.
(1) By generating bubbles in the raw water side bubble generation unit and oxidizing and precipitating organic matter, iron, magnesium, manganese, calcium, etc., the supernatant liquid in the raw water tank is supplied to the filtration unit and efficient in a short time The filter membrane can be filtered and the raw water side of the filtration membrane can be washed using the filtered water filtered in the filtration section, greatly reducing or eliminating the use of chemicals. It is possible to provide a water purifier that is excellent in maintainability and environmental protection, that does not chemically deteriorate the filtration membrane, and that is excellent in durability and long life of the filtration membrane.
 請求項2に記載の発明によれば、請求項1の効果に加え、以下のような効果を有する。
(1)並列して配設される排水ラインの切替弁と、濃縮水排出ラインの濃縮水排出弁の開閉を制御することにより、循環中の濃縮水の排出量と原水タンク内でのバブリング量を簡便に調整することができ、濃縮水の濃度を適度に保持することが可能で、ろ過の効率性、省エネルギー性に優れた浄水装置を提供することができる。
According to invention of Claim 2, in addition to the effect of Claim 1, it has the following effects.
(1) By controlling the opening and closing of the drainage line selector valve and the concentrated water discharge valve of the concentrated water discharge line, the amount of concentrated water discharged and the amount of bubbling in the raw water tank are controlled. Can be easily adjusted, the concentration of concentrated water can be appropriately maintained, and a water purifier excellent in filtration efficiency and energy saving can be provided.
 請求項3に記載の発明によれば、請求項1又は2の効果に加え、以下のような効果を有する。
(1)ろ過水循環ポンプでろ過水を循環させることにより、ろ過水排出ラインの管内壁にろ過水中のミネラル分などが付着することを防止でき、メンテナンス性に優れると共に、必要に応じてろ過水循環ポンプの動力を利用してろ過水を供給することができる運転の効率性、省エネルギー性に優れた浄水装置を提供することができる。
According to invention of Claim 3, in addition to the effect of Claim 1 or 2, it has the following effects.
(1) By circulating the filtered water with the filtered water circulation pump, it is possible to prevent minerals in the filtered water from adhering to the inner wall of the filtered water discharge line. It is possible to provide a water purifier excellent in operation efficiency and energy saving that can supply filtered water by using the power of.
 請求項4に記載の発明によれば、請求項3の効果に加え、以下のような効果を有する。
(1)バブリングされたろ過水を洗浄水として利用することにより、ろ過膜に付着した物質を酸化作用で確実かつ効率的に剥離させることができ、洗浄の効率性に優れ、ろ過膜の劣化を抑えることができる長寿命性、省資源性に優れた浄水装置を提供することができる。
According to invention of Claim 4, in addition to the effect of Claim 3, it has the following effects.
(1) By using the bubbling filtered water as washing water, the substances adhering to the filtration membrane can be reliably and efficiently peeled off by the oxidation action, and the cleaning efficiency is excellent and the filtration membrane is deteriorated. A water purifier excellent in long life and resource saving that can be suppressed can be provided.
 請求項5に記載の発明によれば、請求項4の効果に加え、以下のような効果を有する。
(1)濃縮水やろ過水の排水エネルギー(落下エネルギー)を有効利用して周囲の空気を吸い込む(巻き込む)ことにより、濃縮水やろ過水と空気を混合、攪拌し、簡便にバブリングを行うことができ、動力が不要で省エネルギー性に優れ、構成を簡素化して装置を小型化することができる省スペース性に優れた浄水装置を提供することができる。
According to invention of Claim 5, in addition to the effect of Claim 4, it has the following effects.
(1) Concentrated water or filtered water and air are mixed and stirred by effectively using the drainage energy (falling energy) of concentrated water or filtered water to suck in (involve) the surrounding air, and bubbling can be performed easily. Therefore, it is possible to provide a water purifier that is excellent in space saving and that can be reduced in size by reducing the size of the apparatus by simplifying the configuration.
 請求項6に記載の発明によれば、請求項1乃至5の内いずれか1項の効果に加え、以下のような効果を有する。
(1)並列に配設された性能の異なる2以上のろ過膜から排出されるろ過水の排出量を調整することにより、目的、用途などに応じて最適な純度のろ過水を得ることが可能で、ろ過の過不足を防止することができるろ過の効率性、省エネルギー性に優れた浄水装置を提供することができる。
According to invention of Claim 6, in addition to the effect of any one of Claims 1 thru | or 5, it has the following effects.
(1) By adjusting the amount of filtered water discharged from two or more filtration membranes with different performance arranged in parallel, it is possible to obtain filtered water with the optimum purity according to the purpose and application. Thus, it is possible to provide a water purifier excellent in filtration efficiency and energy saving that can prevent excess or deficiency of filtration.
 請求項7に記載の発明によれば、請求項6の効果に加え、以下のような効果を有する。
(1)2つのろ過膜の原水側を接続する接続管を開閉することにより、一方のろ過膜のろ過側を洗浄することや両方のろ過膜の原水側を洗浄することができ、必要に応じてろ過膜の洗浄方法を選択することが可能なろ過膜のメンテナンス性、洗浄の効率性、ろ過膜の耐久性に優れた浄水装置を提供することができる。
According to invention of Claim 7, in addition to the effect of Claim 6, it has the following effects.
(1) By opening and closing the connecting pipe that connects the raw water sides of the two filtration membranes, the filtration side of one of the filtration membranes and the raw water side of both of the filtration membranes can be washed. Therefore, it is possible to provide a water purifier excellent in the maintenance performance of the filtration membrane, the efficiency of washing, and the durability of the filtration membrane, which can select the washing method of the filtration membrane.
実施の形態1の浄水装置の構成を示す模式図The schematic diagram which shows the structure of the water purifier of Embodiment 1. 実施の形態1の浄水装置の原水側気泡発生部の要部断面模式図Main part cross-sectional schematic diagram of the raw | natural water side bubble generation | occurrence | production part of the water purifier of Embodiment 1. FIG. 実施の形態2の浄水装置の構成を示す模式図The schematic diagram which shows the structure of the water purifier of Embodiment 2. 実施の形態3の浄水装置の構成を示す模式図The schematic diagram which shows the structure of the water purifier of Embodiment 3. ろ過と洗浄を繰り返した時のTMP(膜間差圧)の変化を示す図The figure which shows the change of TMP (transmembrane differential pressure) when filtration and washing are repeated
 本発明の浄水装置について、以下図面を参照しながら説明する。
 (実施の形態1)
 図1は実施の形態1の浄水装置の構成を示す模式図である。
 図1中、1は実施の形態1の浄水装置、2は河川、湖沼、海などから採取した原水が供給パイプ2aによって供給され貯留される浄水装置1の原水タンク、2bは原水タンク2の底部側に配設され原水タンク2内に沈殿した沈殿物や濃縮した原水を排出するための排出部、3は限外ろ過膜や逆浸透膜などのろ過膜が配設された浄水装置1のろ過部、4は原水タンク2とろ過部3を接続する原水供給ライン、4a,4bは原水タンク2からろ過部3に至る原水供給ライン4の管路、5は原水供給ライン4(管路4a)に配設され原水供給ライン4を開閉する電磁弁等を用いた原水供給弁、6は原水供給ライン4(管路4b)に配設され原水タンク2からろ過部3に原水を供給する原水供給ポンプ、7は原水供給ライン4(管路4b)に配設され原水の供給圧力を計測する圧力メータ、8は原水供給ライン4の原水供給ポンプ6より上流側とろ過部3を接続しろ過部3で濃縮された濃縮水を循環させる浄水装置1の濃縮水循環ライン、9はろ過部3に接続されろ過部3でろ過されたろ過水を排出する浄水装置1のろ過水排出ライン、9a,9b,9c,9dはろ過部3からろ過水タンク10に至るろ過水排出ライン9の管路、10はろ過水排出ライン9から排出されるろ過水を貯留する浄水装置1のろ過水タンク、11はろ過水排出ライン9(管路9aと9bの間)に配設されろ過水を逆流させてろ過部3を洗浄する際(逆洗時)にろ過膜に空気が侵入するのを防止するエアーチャンバー、12はろ過水排出ライン9(管路9b)に配設されろ過水の排水圧力を計測する圧力メータ、13a,13bはろ過水排出ライン9に並列に配設され一方若しくは両方を開放することによりろ過水の排出の圧力の調整を行う電磁弁等を用いたろ過水排出弁、14は濃縮水循環ライン8から分岐して濃縮水を原水タンク2に排出する浄水装置1の濃縮水排出ライン、15は濃縮水排出ライン14に配設され濃縮水排出ライン14を開閉する電磁弁等を用いた濃縮水排出弁、16は濃縮水排出ラインの14の濃縮水排出弁15より下流側に配設され濃縮水の逆流を防止する逆止弁、17は濃縮水排出ライン14の濃縮水排出弁15及び逆止弁16より下流側に配設され原水タンク2内をバブリングする原水側気泡発生部、18はろ過水排出ライン9のろ過水排出弁13a,13bより上流側(管路9c)から分岐し濃縮水循環ライン8の濃縮水排出ライン14との分岐位置より下流側で濃縮水循環ライン8に接続されてろ過水を洗浄水として供給する浄水装置1の洗浄用ろ過水供給ライン、18a,18b,18cはろ過水排出ライン9から分岐して濃縮水循環ライン8に至る洗浄用ろ過水供給ライン18の管路、19は洗浄用ろ過水供給ライン18(管路18a)に配設され洗浄用ろ過水供給ライン18を開閉する電磁弁等を用いたろ過水供給弁、20は洗浄用ろ過水供給ライン18のろ過水供給弁19より下流側(管路18c)に配設され濃縮水の排出と洗浄用ろ過水の供給を切替る電磁弁等を用いた切替弁、21はろ過水供給弁19と切替弁20の間で洗浄用ろ過水供給ライン18(管路18bと18cの間)から分岐して原水タンク2に接続された浄水装置1の排水ライン、21aは排水ライン21に配設され排水の圧力を調整するバネ付き逆止弁等の圧力調整弁を用いた排水調整部、21bは洗浄用ろ過水供給ライン18の管路18bに配設され管路18cから排出される濃縮水が管路18bを通ってろ過水タンク10側に流入することを防止するための逆止弁、22は洗浄用ろ過水供給ライン18のろ過水供給弁19より下流側(管路18aと18bの間)から分岐してろ過水タンク10に接続された浄水装置1のろ過水バブリング用ライン、23はろ過水バブリング用ライン22に配設されろ過水タンク10内をバブリングするろ過水側気泡発生部、24はろ過水排出ライン9のろ過水排出弁13a,13bより上流側(管路9bと9cの間)とろ過水タンク10を接続する浄水装置1のろ過水循環ライン、25はろ過水循環ライン24に配設されろ過水を循環させるろ過水循環ポンプ、26はろ過水排出ライン9のろ過水排出弁13a,13bより下流側(管路9d)から分岐して系外にろ過水を供給するためのろ過水取水ライン、26aはろ過水排出ライン9の管路9dとろ過水取水ライン26との分岐位置に配設されたろ過水取水切替弁、27は濃縮水排出ライン14から分岐して必要に応じて濃縮水を系外に廃水して原水タンク2内が濃縮することを防止する廃水ライン、27aは濃縮水排出ライン14と廃水ライン27との分岐位置に配設され濃縮水の原水タンク2への排出と系外への廃水を切り替えるための廃水切替弁である。
 尚、原水タンク2を用いないで直接、河川、湖沼、海などから原水を取水してろ過部3に供給してもよい。
The water purifier of the present invention will be described below with reference to the drawings.
(Embodiment 1)
FIG. 1 is a schematic diagram showing a configuration of a water purifier according to Embodiment 1.
In FIG. 1, 1 is the water purifier of the first embodiment, 2 is the raw water tank of the water purifier 1 where raw water collected from rivers, lakes, seas, etc. is supplied and stored by the supply pipe 2a, 2b is the bottom of the raw water tank 2 A discharge section for discharging the sediment precipitated in the raw water tank 2 and the concentrated raw water, 3 is a filtration of the water purification apparatus 1 provided with a filtration membrane such as an ultrafiltration membrane or a reverse osmosis membrane 4, 4 is a raw water supply line connecting the raw water tank 2 and the filtration unit 3, 4a and 4b are pipelines of the raw water supply line 4 from the raw water tank 2 to the filtration unit 3, and 5 is a raw water supply line 4 (pipe 4a). A raw water supply valve that uses an electromagnetic valve or the like that opens and closes the raw water supply line 4, and 6 is a raw water supply that is provided in the raw water supply line 4 (pipe 4 b) to supply raw water from the raw water tank 2 to the filtration unit 3. The pump 7 is disposed in the raw water supply line 4 (pipe 4b). A pressure meter 8 that measures the supply pressure of water, 8 is a concentrated water circulation line of the water purification apparatus 1 that connects the upstream side of the raw water supply pump 6 of the raw water supply line 4 and the filtration unit 3 and circulates the concentrated water concentrated in the filtration unit 3. , 9 is connected to the filtration unit 3 and drains the filtered water filtered by the filtration unit 3, 9 a, 9 b, 9 c, 9 d are filtered water from the filtering unit 3 to the filtered water tank 10. Pipe line of the discharge line 9, 10 is a filtrate water tank of the water purification device 1 that stores filtrate water discharged from the filtrate water discharge line 9, and 11 is provided in the filtrate water discharge line 9 (between the pipe lines 9 a and 9 b). An air chamber for preventing air from entering the filtration membrane when washing the filtration unit 3 by backflowing filtered water (during backwashing), 12 is disposed in the filtrate discharge line 9 (pipe 9b). Pressure meter that measures drainage pressure of filtered water, 1 Reference numerals a and 13b are arranged in parallel with the filtrate drain line 9, and one or both of them are opened to adjust the filtrate discharge pressure. Concentrated water discharge line 15 of the water purifier 1 for branching out from the concentrated water discharge line 14 for discharging the concentrated water to the raw water tank 2. Reference numeral 16 denotes a check valve disposed downstream of the concentrated water discharge valve 15 of the concentrated water discharge line 14 to prevent the backflow of the concentrated water, and reference numeral 17 denotes the concentrated water discharge valve 15 and the check of the concentrated water discharge line 14. A raw water-side bubble generating section disposed downstream of the valve 16 and bubbling in the raw water tank 2, 18 is branched from the filtered water discharge valves 13 a and 13 b of the filtered water discharge line 9 from the upstream side (pipe 9 c), and concentrated water is circulated. Concentrated water in line 8 The filtered filtrate supply line 18a, 18b, 18c of the water purifier 1 is connected to the concentrated water circulation line 8 downstream of the branch line with the discharge line 14 and supplies filtered water as washing water. A pipe 19 of the washing filtrate supply line 18 that branches and reaches the concentrated water circulation line 8 is an electromagnetic valve 19 that is disposed in the washing filtrate supply line 18 (pipe 18a) and opens and closes the washing filtrate supply line 18. The filtered water supply valve 20 and the like are disposed downstream of the filtered water supply valve 19 (pipe 18 c) of the washing filtrate supply line 18 and switch between discharging concentrated water and supplying washing filtrate. A switching valve 21 using a solenoid valve or the like is branched from the washing filtrate supply line 18 (between the pipes 18b and 18c) between the filtrate supply valve 19 and the switch valve 20 and connected to the raw water tank 2. Drainage line of the water purifier 1, 1a is a drainage adjusting unit using a pressure regulating valve such as a spring check valve that adjusts the pressure of drainage and is disposed in the drainage line 21, and 21b is disposed in a pipe line 18b of the filtered water supply line 18 for washing. A check valve 22 for preventing the concentrated water discharged from the passage 18 c from flowing into the filtrate water tank 10 through the pipe 18 b is provided downstream of the filtrate water supply valve 19 of the washing filtrate water supply line 18. The filtered water bubbling line 23 of the water purification apparatus 1 branched from the side (between the pipes 18a and 18b) and connected to the filtered water tank 10 is provided in the filtered water bubbling line 22 and passes through the filtered water tank 10. The filtered water side bubble generating unit 24 to be bubbled, 24 is the filtered water circulation of the purified water device 1 that connects the filtered water discharge valve 13a, 13b upstream of the filtered water discharge line 9 (between the pipe lines 9b and 9c) and the filtered water tank 10. line, 5 is a filtered water circulation pump that circulates filtered water in the filtered water circulation line 24, and 26 branches from the filtered water discharge valves 13 a and 13 b of the filtered water discharge line 9 from the downstream side (pipe 9 d) and is filtered outside the system. A filtered water intake line 26a for supplying water, 26a is a filtered water intake switching valve disposed at a branch position between the conduit 9d of the filtered water discharge line 9 and the filtered water intake line 26, and 27 is a concentrated water discharge line 14. The waste water line 27a is disposed at a branch position between the concentrated water discharge line 14 and the waste water line 27 to prevent the concentrated water from being drained out of the system and concentrated in the raw water tank 2 if necessary. This is a wastewater switching valve for switching between discharge of concentrated water to the raw water tank 2 and wastewater to the outside of the system.
In addition, you may take raw water directly from a river, a lake, the sea, etc., without using the raw water tank 2, and supply it to the filtration part 3. FIG.
 以上のように構成された浄水装置の動作について説明する。
 まず、ろ過時の動作について説明する。
 図1において、原水供給弁5を開き原水供給ポンプ6を駆動することにより、原水タンク2から吸引された原水が原水供給ライン4(管路4a,4b)を通ってろ過部3に供給される。
 ろ過水排出ライン9のろ過水排出弁13a,13bの一方若しくは両方を開き、洗浄用ろ過水供給ライン18のろ過水供給弁19を閉じることにより、ろ過部3でろ過されたろ過水はろ過水排出ライン9(管路9a~9d)を通ってろ過水タンク10に排出される。尚、本実施の形態では、ろ過水排出ライン9に2つのろ過水排出弁13a,13bを設け、一方若しくは両方を開放することにより、圧力の調整を行ったが、開度(圧力)を任意に設定できる任意バルブを用いる場合は1つでよい。
 一方、ろ過部3でろ過されずに濃縮された濃縮水は濃縮水循環ライン8を通って原水供給ライン4(管路4b)に戻り、循環される。このとき、必要に応じて、濃縮水排出ライン14の濃縮水排出弁15及び洗浄用ろ過水供給ライン18の切替弁20を開くことにより、循環する濃縮水の一部を原水タンク2に排出して濃縮水が過度に濃縮することを防止する。尚、濃縮水排出ライン14から濃縮水を排出し、原水側気泡発生部17で原水タンク2内をバブリングすることにより、有機物、鉄、マグネシウム、マンガン、カルシウムなどを酸化させて沈殿させることができ、原水タンク2内の上澄み液をろ過部3に供給してろ過に要する時間を短縮することができる。
Operation | movement of the water purifier comprised as mentioned above is demonstrated.
First, the operation during filtration will be described.
In FIG. 1, by opening the raw water supply valve 5 and driving the raw water supply pump 6, the raw water sucked from the raw water tank 2 is supplied to the filtration unit 3 through the raw water supply line 4 (pipe lines 4a and 4b). .
By opening one or both of the filtrate discharge valves 13a and 13b of the filtrate discharge line 9 and closing the filtrate supply valve 19 of the filtrate supply line 18 for washing, the filtrate filtered by the filtration unit 3 is filtered water. It is discharged to the filtrate water tank 10 through the discharge line 9 (pipe lines 9a to 9d). In this embodiment, the filtered water discharge line 9 is provided with two filtered water discharge valves 13a and 13b, and one or both are opened to adjust the pressure. However, the opening degree (pressure) is arbitrary. In the case of using an arbitrary valve that can be set to 1, one is sufficient.
On the other hand, the concentrated water concentrated without being filtered by the filtration unit 3 returns to the raw water supply line 4 (pipe 4b) through the concentrated water circulation line 8 and is circulated. At this time, a part of the circulated concentrated water is discharged to the raw water tank 2 by opening the concentrated water discharge valve 15 of the concentrated water discharge line 14 and the switching valve 20 of the washing filtrate supply line 18 as necessary. To prevent excessive concentration of concentrated water. In addition, by discharging concentrated water from the concentrated water discharge line 14 and bubbling the inside of the raw water tank 2 with the raw water side bubble generating unit 17, it is possible to oxidize and precipitate organic matter, iron, magnesium, manganese, calcium and the like. The supernatant liquid in the raw water tank 2 can be supplied to the filtration unit 3 to shorten the time required for filtration.
 ここで、実施の形態1の浄水装置の原水側気泡発生部の構造について説明する。
 図2は実施の形態1の浄水装置の原水側気泡発生部の要部断面模式図である。
 図2中、30は原水側気泡発生部17の直管状の液体流入管、30aは液体流入管30に穿設された液体流入孔、31は液体流入管30の下流側に連設され内径が液体流入管30より大径に形成された原水側気泡発生部17の直管状の液体流出管、31aは液体流出管31に穿設され液体流入孔30aに連通する液体流出孔、32は液体流出部31の上端側の周壁に穿設され液体流出孔31aと連通する複数の空気導入微孔である。
 液体流入管30の液体流入孔30aから流入した濃縮水が、液体流出管31の液体流出孔31aを通過することにより、液体流出管31の内部の圧力が外部より低くなり、外部の空気が空気導入微孔32から液体流出管31の内部に吸い込まれ、内部を流れる濃縮水やろ過水と混合、攪拌され濃縮水をバブリングする。
Here, the structure of the raw | natural water side bubble generation part of the water purifier of Embodiment 1 is demonstrated.
FIG. 2 is a schematic cross-sectional view of an essential part of a raw water side bubble generating part of the water purifier according to the first embodiment.
In FIG. 2, 30 is a straight liquid inflow pipe of the raw water side bubble generating unit 17, 30 a is a liquid inflow hole drilled in the liquid inflow pipe 30, and 31 is connected to the downstream side of the liquid inflow pipe 30 and has an inner diameter. A straight liquid outflow pipe 31a of the raw water side bubble generating section 17 formed larger in diameter than the liquid inflow pipe 30, 31a is a liquid outflow hole drilled in the liquid outflow pipe 31 and communicated with the liquid inflow hole 30a, 32 is a liquid outflow These are a plurality of air introduction micro holes formed in the peripheral wall on the upper end side of the part 31 and communicating with the liquid outflow hole 31a.
When the concentrated water flowing in from the liquid inflow hole 30a of the liquid inflow pipe 30 passes through the liquid outflow hole 31a of the liquid outflow pipe 31, the internal pressure of the liquid outflow pipe 31 becomes lower than the outside, and the external air becomes air. It is sucked into the liquid outflow pipe 31 from the introduction micropore 32, and mixed and stirred with concentrated water and filtered water flowing through the inside, and the concentrated water is bubbled.
 液体流入管30、液体流出管31、空気導入微孔32の内径は、内部を通過する濃縮水の流量(流速)や空気導入微孔32の数によって適宜、選択することができるが、本実施の形態では、液体流出管31の内径(=液体流出孔31aの径)は液体流入管30の内径(=液体流入孔30aの径)の2倍~5倍に形成し、空気導入微孔32の内径は液体流出管31の内径(=液体流出孔31aの径)の0.05倍~0.2倍に形成した。
 濃縮水の流量(流速)によっても異なるが、液体流出管31の内径が、液体流入管30の内径の2倍よりも小さくなるにつれ、液体流出孔31aを通過する濃縮水と液体流出管31の内壁面との間に形成される隙間が小さく(空気層が薄く)なり、空気導入微孔32から吸い込まれる空気の量が減少して、気泡が発生し難くなる傾向があり、液体流入管30の内径の5倍よりも大きくなるにつれ、液体流出孔31aを通過する濃縮水の速度が低下し、負圧が発生し難くなって、空気の吸い込み量が減少すると共に、液体流出孔31aを通過する濃縮水と液体流出管31の内壁面との間に形成される隙間が大きく(空気層が厚く)なり、液体流出孔31aを通過する濃縮水と空気導入微孔32から吸い込まれる空気が混合、攪拌され難くなって、気泡発生量が低下し易くなる傾向があることがわかったためである。
The inner diameters of the liquid inflow pipe 30, the liquid outflow pipe 31, and the air introduction microhole 32 can be appropriately selected depending on the flow rate (flow velocity) of the concentrated water passing through the inside and the number of the air introduction microholes 32. In this embodiment, the inner diameter of the liquid outflow pipe 31 (= the diameter of the liquid outflow hole 31a) is formed to be twice to five times the inner diameter of the liquid inflow pipe 30 (= the diameter of the liquid inflow hole 30a). The inner diameter of the liquid outflow pipe 31 is 0.05 to 0.2 times the inner diameter of the liquid outflow pipe 31 (= the diameter of the liquid outflow hole 31a).
Although depending on the flow rate (flow velocity) of the concentrated water, as the inner diameter of the liquid outflow pipe 31 becomes smaller than twice the inner diameter of the liquid inflow pipe 30, the concentrated water passing through the liquid outflow hole 31a and the liquid outflow pipe 31 There is a tendency that the gap formed between the inner wall surface is small (the air layer is thin), the amount of air sucked from the air introduction microhole 32 is reduced, and bubbles are less likely to be generated. As the inner diameter becomes larger than 5 times, the speed of the concentrated water passing through the liquid outflow hole 31a decreases, it becomes difficult to generate negative pressure, the amount of air sucked in decreases, and the liquid outflow hole 31a passes through. The gap formed between the concentrated water and the inner wall surface of the liquid outflow pipe 31 is large (the air layer is thick), and the concentrated water passing through the liquid outflow hole 31a and the air sucked from the air introduction microhole 32 are mixed. Become difficult to stir This is because the bubble generation amount is found to have a tendency to become liable to lower.
 また、空気導入微孔32の数によっても異なるが、空気導入微孔32の内径が、液体流出管31の内径の0.05倍よりも小さくなるにつれ、加工性が低下すると共に、目詰まりが発生し易くなり、気泡発生の安定性が低下し易くなる傾向があり、液体流出管31の内径の0.2倍(=液体流入管30の内径と同等)よりも大きくなるにつれ、液体流出管31の内部と外部の圧力差が小さくなり、液体流出孔31aを通過する濃縮水と空気が混合、攪拌され難くなって、気泡発生量が低下し易くなる傾向があることがわかったためである。尚、液体流出管31の内径によっても異なるが、空気導入微孔32の数は2~8個が好ましい。空気導入微孔32の数が2個よりも少なくなると、空気導入微孔32から吸い込まれる空気量が減少すると共に、濃縮水と空気が混合、攪拌され難くなって、気泡発生量が低下し易くなる傾向があり、空気導入微孔32の数が8個よりも多くなると、液体流出管31の内部と外部の圧力差が小さくなり、液体流出孔31aを通過する濃縮水と空気が混合、攪拌され難くなって、気泡発生量が低下すると共に、液体流出管31の耐久性が低下し易くなる傾向があることがわかったためである。 Further, although depending on the number of air introduction microholes 32, as the inner diameter of the air introduction microholes 32 becomes smaller than 0.05 times the inner diameter of the liquid outflow pipe 31, workability deteriorates and clogging occurs. The liquid outflow pipe tends to be easily generated and the stability of the bubble generation tends to be lowered, and becomes larger than 0.2 times the inner diameter of the liquid outflow pipe 31 (= equivalent to the inner diameter of the liquid inflow pipe 30). This is because the pressure difference between the inside and the outside of 31 becomes small, and it becomes difficult for the concentrated water and air passing through the liquid outflow hole 31a to be mixed and stirred, so that the amount of bubbles generated tends to decrease. The number of air introduction microholes 32 is preferably 2 to 8, although it varies depending on the inner diameter of the liquid outflow pipe 31. When the number of air introduction micropores 32 is less than two, the amount of air sucked from the air introduction micropores 32 is reduced, and it becomes difficult for the concentrated water and air to be mixed and stirred, and the amount of generated bubbles is likely to decrease. When the number of air introduction micro-holes 32 is more than 8, the pressure difference between the inside and outside of the liquid outflow pipe 31 becomes small, and the concentrated water and air passing through the liquid outflow hole 31a are mixed and stirred. This is because it has been found that there is a tendency that the bubble generation amount tends to decrease and the durability of the liquid outflow pipe 31 tends to decrease.
 本実施の形態では、液体流入管30及び液体流出管31の断面形状は、それぞれ長手方向に一様に形成したが、これに限定されるものではなく、必要に応じて、様々な組合せを選択することができる。例えば、液体流出管31の上流端側から下流端側に向かって徐々に断面積を縮小させたり、液体流入管30の上流端側から液体流出管31の下流端側に向かって徐々に断面積を拡大させたりしてもよい。特に、液体流出管31の断面積を上流端側から下流端側に向かって徐々に拡大させた場合、液体流出管31の内部で乱流が発生し、空気導入微孔32の吸引力が増大して、バブリング(エアレーション)の性能を向上させることができる。 In the present embodiment, the cross-sectional shapes of the liquid inflow pipe 30 and the liquid outflow pipe 31 are uniformly formed in the longitudinal direction, but the present invention is not limited to this, and various combinations can be selected as necessary. can do. For example, the cross-sectional area is gradually reduced from the upstream end side to the downstream end side of the liquid outflow pipe 31, or the cross-sectional area is gradually increased from the upstream end side of the liquid inflow pipe 30 toward the downstream end side of the liquid outflow pipe 31. May be enlarged. In particular, when the cross-sectional area of the liquid outflow pipe 31 is gradually enlarged from the upstream end side toward the downstream end side, turbulent flow is generated inside the liquid outflow pipe 31 and the suction force of the air introduction microhole 32 is increased. Thus, the bubbling (aeration) performance can be improved.
 尚、浄水装置1は、ろ過水循環ライン24を備えているので、ろ過時にろ過水循環ポンプ25を駆動することにより、ろ過水タンク10に貯留されたろ過水をろ過水排出ライン9の管路9c,9dとろ過水タンク10との間で循環させることができ、ろ過水排出ライン9の管内壁にろ過水中のミネラル分などが付着することを防止できる。
 また、ろ過水取水ライン26のろ過水取水切替弁26aをろ過水取水ライン26側に切り替えれば、ろ過水循環ポンプ25の動力を利用して系外の取水側(クライアント側)にろ過水を供給することができる。
In addition, since the water purifier 1 is provided with the filtrate water circulation line 24, the filtrate water stored in the filtrate water tank 10 can be removed from the filtrate water discharge line 9 by driving the filtrate circulation pump 25 during filtration. It can be made to circulate between 9d and the filtrate water tank 10, and it can prevent that the mineral content etc. in filtrate water adhere to the pipe inner wall of the filtrate water discharge line 9. FIG.
Moreover, if the filtered water intake switching valve 26a of the filtered water intake line 26 is switched to the filtered water intake line 26 side, filtered water is supplied to the intake side (client side) outside the system using the power of the filtrate circulating pump 25. be able to.
 次に、洗浄時の動作について説明する。
 原水供給ポンプ6及びろ過水循環ポンプ25を駆動したまま原水供給ライン4の原水供給弁5,ろ過水排出ライン9のろ過水排出弁13a,13b及び濃縮水排出ライン14の濃縮水排出弁15を閉じ、洗浄用ろ過水供給ライン18のろ過水供給弁19及び切替弁20を開くことにより、ろ過水タンク10に貯留されたろ過水が、ろ過水循環ライン24からろ過水排出ライン9の管路9c,洗浄用ろ過水供給ライン18(管路18a,18b,18c)を通って濃縮水循環ライン8に導かれ、さらに原水供給ライン4の管路4bを通ってろ過部3の原水側に供給され、ろ過水によるろ過膜の洗浄が行われる。尚、ろ過水供給弁19を通過したろ過水の一部は、原水供給ポンプ6の循環圧とろ過水循環ポンプ25の循環圧との差によって、ろ過水バブリング用ライン22を通ってろ過水タンク10に流れ込み、ろ過水側気泡発生部23の作用によってろ過水タンク10内がバブリングされ、バブリングされたろ過水がろ過水循環ライン24を通って循環する。これにより、バブリングされたろ過水を洗浄水として使用することができるので、ろ過膜に付着した物質を酸化作用で剥離させることができ、化学反応による洗浄効率の向上を図ることができる。
 このとき、必要に応じて濃縮水排出ライン14の濃縮水排出弁15を開くことにより、洗浄に使用されたろ過水の一部を原水タンク2に排出することができ、循環中のろ過水を新しいろ過水と交換しながら効率的に洗浄を行うことができる。
Next, the operation during cleaning will be described.
The raw water supply valve 5 of the raw water supply line 4, the filtrate water discharge valves 13 a and 13 b of the filtrate discharge line 9 and the concentrated water discharge valve 15 of the concentrated water discharge line 14 are closed while the raw water supply pump 6 and the filtrate circulating pump 25 are driven. The filtrate water stored in the filtrate water tank 10 is opened from the filtrate water circulation line 24 to the pipeline 9c of the filtrate discharge line 9 by opening the filtrate water supply valve 19 and the switching valve 20 of the filtrate water supply line 18 for washing. It is led to the concentrated water circulation line 8 through the filtered filtered water supply line 18 (pipe lines 18a, 18b, 18c), and further supplied to the raw water side of the filtration unit 3 through the pipe line 4b of the raw water supply line 4. The filter membrane is washed with water. A part of the filtrate water that has passed through the filtrate water supply valve 19 passes through the filtrate water bubbling line 22 due to the difference between the circulation pressure of the raw water supply pump 6 and the circulation pressure of the filtrate water circulation pump 25. The filtered water tank 10 is bubbled by the action of the filtered water side bubble generating unit 23, and the filtered water is circulated through the filtered water circulation line 24. Thereby, since the bubbled filtered water can be used as the washing water, the substance adhering to the filtration membrane can be peeled off by an oxidizing action, and the washing efficiency by chemical reaction can be improved.
At this time, by opening the concentrated water discharge valve 15 of the concentrated water discharge line 14 as necessary, a part of the filtered water used for washing can be discharged to the raw water tank 2, and the circulating filtered water can be removed. Washing can be performed efficiently while replacing with new filtered water.
 尚、ろ過水側気泡発生部23は原水側気泡発生部17と同様の構造を有するので説明を省略する。
 以上のように、ろ過時及び洗浄時を通じて、常に原水供給ポンプ6及びろ過水循環ポンプ25を駆動し続けた場合、原水供給ポンプ6及びろ過水循環ポンプ25を間欠運転する場合に比べて、原水供給ポンプ6及びろ過水循環ポンプ25を停止する際や再駆動する際に発生する負荷を低減することができ、動作の安定性、装置の耐久性に優れる。
 尚、エアーチャンバー11は必要に応じて設ければよく、省略することも可能である。
In addition, since the filtrate water side bubble generation part 23 has the same structure as the raw | natural water side bubble generation part 17, description is abbreviate | omitted.
As described above, when the raw water supply pump 6 and the filtrate circulating pump 25 are continuously driven throughout the filtration and washing, the raw water supply pump is compared with the case where the raw water supply pump 6 and the filtrate circulating pump 25 are intermittently operated. 6 and when the filtrate circulating pump 25 is stopped or re-driven, the load generated can be reduced, and the operation stability and the durability of the apparatus are excellent.
The air chamber 11 may be provided as necessary, and may be omitted.
 実施の形態1における浄水装置によれば、以下の作用を有する。
(1)原水が貯留される原水タンク2と、原水タンク2とろ過部3を接続し原水タンク2からろ過部3に原水を供給する原水供給ポンプ6及び原水供給弁5を有する原水供給ライン4と、原水供給ライン4の原水供給ポンプ6より上流側とろ過部3を接続しろ過部3で固体粒子が濃縮された濃縮水をろ過部3から原水供給ライン4の管路4bへ循環させる濃縮水循環ライン8を備えるので、原水供給ポンプ6を連続運転して濃縮水を循環させながらろ過を行うことができ、原水供給ポンプ6の停止や再起動による負荷を低減することができ、耐久性、動作の安定性に優れる。
(2)濃縮水循環ライン8から分岐して濃縮水を原水タンク2に排出する濃縮水排出弁15を有する濃縮水排出ライン14を備えるので、必要に応じて濃縮水循環ライン8を循環する濃縮水の一部を原水タンク2に排出して濃縮水が過度に濃縮することを防止し、ろ過膜の目詰まりを低減することができ、ろ過の効率性に優れる。
(3)濃縮水排出ライン8の濃縮水排出弁15より下流側に配設され原水タンク2内をバブリングする原水側気泡発生部17を備えることにより、有機物、鉄、マグネシウム、マンガン、カルシウムなどを酸化させて沈殿させることができるので、原水タンク2内の上澄み液をろ過部に供給して短時間で効率的にろ過することができ、ろ過の効率性に優れる。
(4)ろ過水排出ライン9のろ過水排出弁13a,13bより上流側(管路9c)から分岐して濃縮水循環ライン8の濃縮水排出ライン14との接続位置より下流側に接続されてろ過水を洗浄水として供給するろ過水供給弁19を有する洗浄用ろ過水供給ライン18を備えることにより、ろ過膜の原水側をろ過水で洗浄することができるので、薬液を不要とし、若しくは薬液の使用量を大幅に削減するができ、環境保護性に優れ、ろ過膜が化学的に劣化することがなく、ろ過膜の耐久性、長寿命性に優れる。
(5)洗浄用ろ過水供給ライン18のろ過水供給弁19より下流側に配設された切替弁20と、ろ過水供給弁19と切替弁20の間で洗浄用ろ過水供給ライン18から分岐して原水タンク2に接続された排水ライン21を有するので、ろ過時に洗浄用ろ過水供給ライン18のろ過水供給弁19を閉じ、切替弁20を開くことにより、洗浄用ろ過水供給ライン18の一部(管路18c)を利用して、排水ライン21から原水タンク2へ濃縮水を排出することができるので、配管を簡素化して装置を小型化することができ、省スペース性、量産性に優れる。
(6)洗浄用ろ過水供給ライン18の一部(管路18c)及び排水ライン21が濃縮水排出ライン14と並列に配設されるので、洗浄用ろ過水供給ライン18の管路18cに配設された切替弁20の開閉と、濃縮水排出ライン14の濃縮水排出弁15の開閉を選択することにより、濃縮水循環ライン8から原水タンク2に排出される濃縮水の排出量と原水タンク2内でのバブリング量を調整することができ、濃縮水の濃度を適度に保持することが可能で、ろ過の効率性に優れる。
(7)ろ過水排出ライン9のろ過水排出弁13a,13bより上流側(管路9c)とろ過水タンク10を接続し、ろ過水を循環させるろ過水循環ポンプ25を有するので、ろ過水を循環させてろ過水排出ライン9の管路9c,9dの管内壁にろ過水中のミネラル分などが付着することを防止でき、メンテナンス性に優れる。
(8)洗浄用ろ過水供給ライン18のろ過水供給弁19より下流側から分岐してろ過水タンク10に接続されろ過水タンク10内をバブリングするろ過水側気泡発生部23を有するろ過水バブリング用ライン22を備えることにより、ろ過水タンク10内でバブリングされたろ過水を洗浄水として利用することができるので、ろ過膜に付着したコロイドや難溶解性塩類等の物質を酸化作用で剥離させることができ、化学反応による洗浄効率の向上を図ると共に、ろ過膜の劣化を抑えることができ、長寿命性に優れる。
(9)原水側気泡発生部17及びろ過水側気泡発生部23が、液体流入孔30aを有する液体流入部30と、液体流入部30の下流側に連設され液体流入孔30aより大径の液体流出孔31aを有する液体流出部31と、液体流出部31の上端側の周壁に穿設され液体流出孔31aと連通する複数の空気導入微孔32を有するので、液体流入部30の液体流入孔30aから流入した濃縮水やろ過水が、液体流出部31の液体流出孔31aを通過することにより、液体流出部31の内部の圧力が外部より低くなり、外部の空気が空気導入微孔32から液体流出部31の内部に吸い込まれ、内部を流れる濃縮水やろ過水と混合、攪拌され濃縮水やろ過水を簡便にバブリングすることができる。
(10)濃縮水排出ライン14やろ過水バブリング用ライン22を通過する濃縮水やろ過水の排水エネルギーを利用してバブリングを行うことができ、別途、動力を必要とせず、省エネルギー性に優れ、構成を簡素化して装置を小型化することができ、省スペース性に優れる。
The water purifier according to Embodiment 1 has the following action.
(1) A raw water tank 2 in which raw water is stored, a raw water supply line 4 having a raw water supply pump 6 and a raw water supply valve 5 that connect the raw water tank 2 and the filtration unit 3 and supply the raw water from the raw water tank 2 to the filtration unit 3. Then, the upstream side of the raw water supply line 6 of the raw water supply line 6 is connected to the filtration unit 3, and the concentrated water in which the solid particles are concentrated in the filtration unit 3 is circulated from the filtration unit 3 to the pipe 4 b of the raw water supply line 4. Since the water circulation line 8 is provided, it is possible to perform filtration while continuously operating the raw water supply pump 6 to circulate the concentrated water, and it is possible to reduce the load caused by stopping or restarting the raw water supply pump 6. Excellent operational stability.
(2) Since the concentrated water discharge line 14 having the concentrated water discharge valve 15 that branches from the concentrated water circulation line 8 and discharges the concentrated water to the raw water tank 2 is provided, the concentrated water that circulates through the concentrated water circulation line 8 as necessary. A part is discharged to the raw water tank 2 to prevent the concentrated water from being excessively concentrated, clogging of the filtration membrane can be reduced, and the filtration efficiency is excellent.
(3) By providing the raw water side bubble generating part 17 which is disposed downstream of the concentrated water discharge valve 15 of the concentrated water discharge line 8 and bubbles in the raw water tank 2, organic substances, iron, magnesium, manganese, calcium, etc. Since it can oxidize and precipitate, the supernatant liquid in the raw | natural water tank 2 can be supplied to a filtration part, can be filtered efficiently in a short time, and it is excellent in the efficiency of filtration.
(4) Branched from the filtered water discharge valve 13a, 13b upstream of the filtered water discharge line 13a, 13b (pipe 9c) and filtered downstream from the connection position with the concentrated water discharge line 14 of the concentrated water circulation line 8. By providing the washing filtrate supply line 18 having the filtrate supply valve 19 for supplying water as washing water, the raw water side of the filtration membrane can be washed with filtered water, so that no chemical solution is required or the chemical solution The amount used can be greatly reduced, it is excellent in environmental protection, the filtration membrane is not chemically deteriorated, and the filtration membrane is excellent in durability and long life.
(5) The switching valve 20 disposed on the downstream side of the filtrate water supply valve 19 of the washing filtrate supply line 18, and the washing filtrate supply line 18 branches between the filtrate water supply valve 19 and the switching valve 20. Since the drainage line 21 connected to the raw water tank 2 is provided, the filtration filtrate supply line 19 of the washing filtrate supply line 18 is closed during filtration, and the switching valve 20 is opened to open the filtration filtrate supply line 18 for washing. Concentrated water can be discharged from the drainage line 21 to the raw water tank 2 using a part (the pipe line 18c), so that the piping can be simplified and the apparatus can be miniaturized. Excellent.
(6) Since a part (pipe line 18 c) of the washing filtrate supply line 18 and the drainage line 21 are arranged in parallel with the concentrated water discharge line 14, they are arranged in the pipe line 18 c of the washing filtrate supply line 18. By selecting opening and closing of the provided switching valve 20 and opening and closing of the concentrated water discharge valve 15 of the concentrated water discharge line 14, the amount of concentrated water discharged from the concentrated water circulation line 8 to the raw water tank 2 and the raw water tank 2 are selected. The amount of bubbling inside can be adjusted, the concentration of the concentrated water can be kept moderate, and the filtration efficiency is excellent.
(7) The filtrate water discharge line 13 is connected upstream of the filtrate water discharge valves 13a and 13b (the pipe line 9c) and the filtrate water tank 10 and has a filtrate water circulation pump 25 for circulating the filtrate water. Thus, it is possible to prevent minerals in the filtered water from adhering to the inner walls of the pipes 9c and 9d of the filtered water discharge line 9, and the maintenance is excellent.
(8) Filtrated water bubbling having a filtered water side bubble generating unit 23 that branches from the filtered water supply valve 19 of the washing filtered water supply line 18 from the downstream side and is connected to the filtered water tank 10 to bubble inside the filtered water tank 10. By providing the line 22 for use, the filtered water bubbled in the filtered water tank 10 can be used as washing water, so that substances such as colloids and hardly soluble salts adhering to the filtration membrane are peeled off by an oxidizing action. It is possible to improve the cleaning efficiency by chemical reaction, suppress the deterioration of the filtration membrane, and have excellent long life.
(9) The raw water side bubble generating part 17 and the filtered water side bubble generating part 23 are connected to the liquid inflow part 30 having the liquid inflow hole 30a and the downstream side of the liquid inflow part 30 and have a larger diameter than the liquid inflow hole 30a. Since the liquid outflow part 31 having the liquid outflow hole 31a and the plurality of air introduction micro holes 32 which are formed in the peripheral wall on the upper end side of the liquid outflow part 31 and communicate with the liquid outflow hole 31a are provided, the liquid inflow of the liquid inflow part 30 Concentrated water or filtered water flowing in from the hole 30a passes through the liquid outflow hole 31a of the liquid outflow part 31, so that the pressure inside the liquid outflow part 31 becomes lower than the outside, and the external air becomes the air introduction microhole 32. Then, it is sucked into the liquid outflow portion 31 and mixed and stirred with the concentrated water and filtered water flowing inside, so that the concentrated water and filtered water can be easily bubbled.
(10) Bubbling can be performed by using the drainage energy of the concentrated water and filtered water passing through the concentrated water discharge line 14 and the filtered water bubbling line 22, and no power is required separately. The structure can be simplified and the apparatus can be miniaturized, and the space is saved.
 (実施の形態2)
 図3は実施の形態2の浄水装置の構成を示す模式図である。尚、実施の形態1と同様のものには同じ符号を付して説明を省略する。
 図3において、実施の形態2の浄水装置1aが実施の形態1と異なるのは、ろ過部3Aが、並列に配設された性能の異なる2つのろ過膜3a,3bと、ろ過膜3a,3bの原水側同士を接続する原水側接続管3cと、各々のろ過膜3a,3bのろ過側とろ過水排出ライン9の管路9aを接続する合流管28a,28bと、各々の合流管28a,28bに配設されたろ過水量調整弁29a,29bと、ろ過水排出ライン9の管路9dに配設された電導度計35を備えている点である。
(Embodiment 2)
FIG. 3 is a schematic diagram showing the configuration of the water purifier according to the second embodiment. In addition, the same code | symbol is attached | subjected to the thing similar to Embodiment 1, and description is abbreviate | omitted.
In FIG. 3, the water purifier 1a of the second embodiment is different from the first embodiment in that the filtration unit 3A has two filtration membranes 3a and 3b having different performances arranged in parallel, and the filtration membranes 3a and 3b. The raw water side connecting pipe 3c that connects the raw water sides of each other, the merging pipes 28a, 28b that connect the filtration side of each filtration membrane 3a, 3b and the conduit 9a of the filtered water discharge line 9, and each merging pipe 28a, It is the point provided with the electrical conductivity meter 35 arrange | positioned in the pipe line 9d of the filtrate water amount adjustment valves 29a and 29b arrange | positioned by 28b, and the filtrate water discharge line 9. FIG.
 実施の形態2の浄水装置1aのろ過時の基本動作は、実施の形態1と同様であるが、ろ過部3Aに性能の異なる2つのろ過膜3a,3bが並列に配設されているので、電導度計35でろ過水の電導度(純度)を計測、確認しながら、各々のろ過水量調整弁29a,29bの開度を調整することにより、所望の電導度(純度)のろ過水を得ることができる。
 ろ過膜3a,3bとしては、限外ろ過膜、逆浸透膜、ナノ膜などを組合せて使用することができる。ろ過部3Aのろ過膜3a,3bの1つに逆浸透膜を使用した場合、逆浸透膜でろ過して得られるRO水を洗浄用ろ過水として利用することができ、ろ過膜3a,3bの原水側に付着した細菌などの付着物を確実かつ効率的に剥離することが可能で、洗浄の効率性に優れる。
 また、原水側接続管3cでろ過膜3a,3bの原水側同士を接続することにより、ろ過膜3a,3bの内の性能の高い方のろ過膜(例えば逆浸透膜)の原水側で圧力が増加した時に、その圧力を性能の低い方のろ過膜(例えば限外ろ過膜)の原水側に逃がして、ろ過膜の破損を防ぐことができ、ろ過膜の保護性に優れる。
Although the basic operation at the time of filtration of the water purifier 1a of the second embodiment is the same as that of the first embodiment, the two filtration membranes 3a and 3b having different performances are arranged in parallel in the filtration unit 3A. While measuring and confirming the conductivity (purity) of the filtrate with the conductivity meter 35, the degree of opening of each of the filtrate adjustment valves 29a and 29b is adjusted to obtain filtrate with a desired conductivity (purity). be able to.
As the filtration membranes 3a and 3b, an ultrafiltration membrane, a reverse osmosis membrane, a nano membrane and the like can be used in combination. When a reverse osmosis membrane is used for one of the filtration membranes 3a and 3b of the filtration unit 3A, RO water obtained by filtration through the reverse osmosis membrane can be used as the filtration water for washing, and the filtration membranes 3a and 3b Deposits such as bacteria attached to the raw water side can be reliably and efficiently peeled off, resulting in excellent cleaning efficiency.
Further, by connecting the raw water sides of the filtration membranes 3a and 3b with the raw water side connecting pipe 3c, the pressure is increased on the raw water side of the filtration membrane (for example, reverse osmosis membrane) having the higher performance among the filtration membranes 3a and 3b. When the pressure increases, the pressure can be released to the raw water side of the lower performance filtration membrane (for example, ultrafiltration membrane) to prevent the filtration membrane from being damaged, and the filtration membrane is excellent in protection.
 実施の形態2の浄水装置1aの洗浄時の動作については、実施の形態1と同様なので説明を省略する。
 尚、本実施の形態では、2種類のろ過膜3a,3bを並列に配設したが、3種類以上並列に配列してもよく、原水側接続管3cは省略することも可能である。
 また、電導度計35を配設する代わりに、遅延タイマ等により、時間差でろ過水量調整弁29a,29bを開閉し、各々のろ過膜3a,3bでのろ過水量を調整してもよい。
About the operation | movement at the time of washing | cleaning of the water purifier 1a of Embodiment 2, since it is the same as that of Embodiment 1, description is abbreviate | omitted.
In this embodiment, two types of filtration membranes 3a and 3b are arranged in parallel. However, three or more types of filtration membranes 3a and 3b may be arranged in parallel, and the raw water side connecting pipe 3c may be omitted.
Further, instead of providing the conductivity meter 35, the filtered water amount adjusting valves 29a and 29b may be opened and closed with a time difference by a delay timer or the like to adjust the filtered water amount in each of the filtration membranes 3a and 3b.
 実施の形態2における浄水装置によれば、実施の形態1で得られる作用に加え、以下の作用を有する。
(1)ろ過部3Aが、並列に配設された性能の異なる2以上のろ過膜3a,3bと、各々のろ過膜3a,3bのろ過側に配設されたろ過水量調整弁29a,29bと、を備え、ろ過水排出ライン9の管路9dに電導度計35が配設されていることにより、ろ過部3Aから排出されるろ過水の電導度(純度)を電導度計で計測しながら、各々のろ過水量調整弁29a,29bの開度を調整することができ、目的、用途などに応じてろ過水の電導度(純度)を最適に保つことが可能で、ろ過の過不足を防止することができ、ろ過の効率性、省エネルギー性に優れる。
According to the water purifier in Embodiment 2, in addition to the action obtained in Embodiment 1, it has the following action.
(1) The filtration unit 3A includes two or more filtration membranes 3a and 3b having different performances arranged in parallel, and filtration water amount adjusting valves 29a and 29b arranged on the filtration side of the respective filtration membranes 3a and 3b. , And the conductivity meter 35 is disposed in the conduit 9d of the filtrate discharge line 9, so that the conductivity (purity) of the filtrate discharged from the filtration unit 3A is measured with the conductivity meter. The degree of opening of each filtered water volume adjustment valve 29a, 29b can be adjusted, and the conductivity (purity) of filtered water can be kept optimal according to the purpose, application, etc., preventing excessive or insufficient filtration. It is excellent in filtration efficiency and energy saving.
 (実施の形態3)
 図4は実施の形態3の浄水装置の構成を示す模式図である。尚、実施の形態1又は2と同様のものには同じ符号を付して説明を省略する。
 図4において、実施の形態3の浄水装置1bが実施の形態2と異なるのは、ろ過部3Bが、ろ過膜3a,3bの原水側同士を接続する原水側接続管3cに配設された開閉弁3dを備えている点と、原水供給ライン4の管路4aの先端部に接続され原水タンク2に沈設された分離タンク4cを備えている点である。
 実施の形態3の浄水装置1bのろ過時の動作は、実施の形態2と同様なので説明を省略する。
(Embodiment 3)
FIG. 4 is a schematic diagram illustrating the configuration of the water purifier according to the third embodiment. In addition, the same code | symbol is attached | subjected to the thing similar to Embodiment 1 or 2, and description is abbreviate | omitted.
In FIG. 4, the water purifier 1b of the third embodiment is different from the second embodiment in that the filtration unit 3B is opened and closed disposed on the raw water side connecting pipe 3c that connects the raw water sides of the filtration membranes 3a and 3b. The point provided with the valve 3d and the point provided with the separation tank 4c connected to the tip of the pipe line 4a of the raw water supply line 4 and sunk in the raw water tank 2.
Since the operation | movement at the time of filtration of the water purifier 1b of Embodiment 3 is the same as that of Embodiment 2, description is abbreviate | omitted.
 実施の形態3の浄水装置1bのろ過側からの洗浄(逆洗)について説明する。
 ろ過膜3aを逆浸透膜のような高性能のろ過膜とし、ろ過膜3bをろ過膜3aより性能の低い限外ろ過膜のような中性能のろ過膜として、濃縮水排出ライン14の濃縮水排出弁15,切替弁20及びろ過水量調整弁29a,29bを開いた状態で、開閉弁3d,原水供給弁5,ろ過水排出ライン9のろ過水排出弁13a,13b及びろ過水供給弁19を閉じることにより、2つのろ過膜3a,3bの内、性能の高いろ過膜3aを通過してろ過されたろ過水をろ過水循環ポンプ25の圧力によって、性能の低いろ過膜3bのろ過側に送り、洗浄(逆洗)を行うことができる。
 このとき、ろ過水供給弁19を開くと、性能の高いろ過膜3aでろ過されたろ過水と、ろ過水タンク10に貯留されているろ過水を混合した多量の混合水で、性能の低いろ過膜3bをろ過側から洗浄(逆洗)することができる。
 尚、ろ過水量調整弁29a,29bの下流側のろ過水排出ライン9の管路9aにろ過水閉止弁を設けてもよい。この場合、ろ過水閉止弁を閉じれば、ろ過膜3aを通過してろ過されたろ過水を合流管28a,28b(ろ過水量調整弁29a,29b)を通して直接、ろ過膜3bのろ過側に送って洗浄(逆洗)を行うことができ、洗浄の確実性、信頼性に優れる。
 以上のように、開閉弁3dの開閉により、ろ過膜3a,3bの洗浄方法を適宜、選択することができ、汎用性に優れる。
 また、実施の形態3の浄水装置1bにおける通常の洗浄(ろ過膜3a,3bの原水側からの洗浄)時の基本動作については、実施の形態1と同様であるが、ろ過水がろ過部3Bの原水側に供給されたときに、原水側接続管3cに配設された開閉弁3dを開くことにより、原水供給ポンプ6で2つのろ過膜3a,3bの原水側をろ過水で循環洗浄することができる。尚、実施の形態1と同様に、適宜、濃縮水排出ライン14の濃縮水排出弁15を開くことにより、洗浄に使用されたろ過水の一部を原水タンク2に排出して、循環中のろ過水を新しいろ過水と交換しながら洗浄を行うことができる。
Cleaning (backwashing) from the filtration side of the water purifier 1b of Embodiment 3 will be described.
The filtration membrane 3a is a high performance filtration membrane such as a reverse osmosis membrane, and the filtration membrane 3b is a medium performance filtration membrane such as an ultrafiltration membrane having a lower performance than the filtration membrane 3a. With the discharge valve 15, the switching valve 20 and the filtrate adjustment valves 29a and 29b open, the on-off valve 3d, the raw water supply valve 5, the filtrate discharge valves 13a and 13b and the filtrate supply valve 19 of the filtrate discharge line 9 are By closing, the filtrate filtered through the high-performance filtration membrane 3a out of the two filtration membranes 3a and 3b is sent to the filtration side of the low-performance filtration membrane 3b by the pressure of the filtrate circulating pump 25, Washing (back washing) can be performed.
At this time, when the filtrate water supply valve 19 is opened, filtration with low performance is performed with a large amount of mixed water obtained by mixing the filtrate filtered through the high-performance filtration membrane 3a and the filtrate stored in the filtrate tank 10. The membrane 3b can be washed (backwashed) from the filtration side.
In addition, you may provide a filtered water shut-off valve in the pipe line 9a of the filtered water discharge line 9 on the downstream side of the filtered water amount adjusting valves 29a and 29b. In this case, if the filtrate shut-off valve is closed, the filtrate filtered through the filtration membrane 3a is sent directly to the filtration side of the filtration membrane 3b through the merge pipes 28a and 28b (filtrate adjustment valves 29a and 29b). Washing (back washing) can be performed, and cleaning reliability and reliability are excellent.
As described above, the cleaning method for the filtration membranes 3a and 3b can be appropriately selected by opening and closing the on-off valve 3d, and the versatility is excellent.
Moreover, although the basic operation | movement at the time of normal washing | cleaning (washing | cleaning from the raw | natural water side of the filtration membranes 3a and 3b) in the water purifier 1b of Embodiment 3 is the same as that of Embodiment 1, filtered water is the filtration part 3B. When the raw water side is supplied, by opening the on-off valve 3d disposed in the raw water side connecting pipe 3c, the raw water side of the two filtration membranes 3a and 3b is circulated and washed with filtered water by the raw water supply pump 6. be able to. As in the first embodiment, by appropriately opening the concentrated water discharge valve 15 of the concentrated water discharge line 14, a part of the filtrate used for washing is discharged to the raw water tank 2 and is being circulated. Washing can be performed while replacing the filtered water with new filtered water.
 分離タンク4cは有底の筒型に形成され、周壁面に複数の貫通孔が穿設されている。これにより、原水中のSS(浮遊物質)が貫通孔から分離タンク4cの内部に侵入し難く、分離タンク4cの外周面で分離されて原水タンク2に沈降し、ろ過部3Bに供給される原水中のSSの量を減らして、ろ過部3Bの負荷を低減することができ、ろ過の効率性、ろ過膜3a,3bの長寿命性を向上させることができる。
 尚、貫通孔の孔径は水の表面張力やSSの粒径に応じて、適宜、選択することができる。
The separation tank 4c is formed in a cylindrical shape with a bottom, and a plurality of through holes are formed in the peripheral wall surface. As a result, SS (floating matter) in the raw water does not easily enter the inside of the separation tank 4c from the through hole, is separated at the outer peripheral surface of the separation tank 4c, settles in the raw water tank 2, and is supplied to the filtration unit 3B. By reducing the amount of SS in the water, the load on the filtration unit 3B can be reduced, and the efficiency of filtration and the long life of the filtration membranes 3a and 3b can be improved.
In addition, the hole diameter of a through-hole can be suitably selected according to the surface tension of water and the particle size of SS.
 実施の形態3における浄水装置によれば、実施の形態1又は2で得られる作用に加え、以下の作用を有する。
(1)ろ過部3Bが、並列に配設された性能の異なる2つのろ過膜3a,3bの原水側同士を接続する原水側接続管3cと、原水側接続管3cに配設された開閉弁3dを有するので、濃縮水排出ライン14の濃縮水排出弁15,切替弁20及びろ過水量調整弁29a,29bを開いた状態で、開閉弁3d,原水供給弁5,ろ過水排出ライン9のろ過水排出弁13a,13b及びろ過水供給弁19を閉じることにより、2つのろ過膜3a,3bの内、性能の高いろ過膜3aを通過してろ過されたろ過水をろ過水循環ポンプ25の圧力によって、合流管28a,28bを通して性能の低いろ過膜3bのろ過側に送り、洗浄を行うことができ、洗浄の効率性、ろ過膜の長寿命性に優れる。
(2)濃縮水排出弁15,切替弁20及びろ過水量調整弁29a,29bを開き、ろ過水排出弁13a,13bと開閉弁3dを閉じて性能の低いろ過膜3bを洗浄する際に、ろ過水供給弁19を開くことにより、性能の高いろ過膜3aでろ過されたろ過水に、ろ過水タンク10に貯留されているろ過水をろ過水循環ポンプ25から供給し、それらを混合した多量の混合水で、性能の低いろ過膜3bをろ過側から洗浄することができ、ろ過膜洗浄の作業性、確実性に優れる。
(3)原水供給ポンプ6及びろ過水循環ポンプ25を駆動したまま原水供給ライン4の原水供給弁5,ろ過水排出ライン9のろ過水排出弁13a,13b及び濃縮水排出ライン18の濃縮水排出弁15を閉じ、洗浄用ろ過水供給ライン18のろ過水供給弁19及び切替弁20を開くことにより、ろ過水タンク10に貯留されたろ過水を、ろ過水循環ライン24からろ過水排出ライン9の管路9c,洗浄用ろ過水供給ライン18(管路18a,18b,18c)へ通して濃縮水循環ライン8に導き、さらに原水供給ライン4の管路4bを通してろ過部3Bの原水側に供給することができるが、このとき、2つのろ過膜3a,3bの原水側同士を接続する原水側接続管3cに配設された開閉弁3dを開くことにより、原水供給ポンプ6で2つのろ過膜3a,3bの原水側をろ過水で循環洗浄することができ、ろ過膜3a,3bの耐久性、長寿命性に優れる。
According to the water purifier in Embodiment 3, in addition to the action obtained in Embodiment 1 or 2, it has the following action.
(1) The raw water side connection pipe 3c that connects the raw water sides of the two filtration membranes 3a and 3b having different performances arranged in parallel with the filtration unit 3B, and the on-off valve provided in the raw water side connection pipe 3c 3d, the open / close valve 3d, the raw water supply valve 5, and the filtered water discharge line 9 are filtered while the concentrated water discharge valve 15, the switching valve 20 and the filtered water amount adjusting valves 29a and 29b of the concentrated water discharge line 14 are opened. By closing the water discharge valves 13a and 13b and the filtrate supply valve 19, the filtrate filtered through the high-performance filtration membrane 3a out of the two filtration membranes 3a and 3b is filtered by the pressure of the filtrate circulation pump 25. Further, it can be sent to the filtration side of the low-performance filtration membrane 3b through the merging pipes 28a and 28b, and washing can be performed, and the washing efficiency and the long life of the filtration membrane are excellent.
(2) When the concentrated membrane discharge valve 15, the switching valve 20 and the filtrate amount control valves 29a and 29b are opened and the filtrate drain valves 13a and 13b and the on-off valve 3d are closed to wash the low performance filtration membrane 3b, filtration is performed. By opening the water supply valve 19, the filtered water stored in the filtered water tank 10 is supplied from the filtered water circulation pump 25 to the filtered water filtered by the high-performance filtration membrane 3a, and a large amount of mixing is performed. The filter membrane 3b having low performance can be washed from the filtration side with water, and the workability and certainty of filtration membrane cleaning are excellent.
(3) The raw water supply valve 6 of the raw water supply line 4, the filtered water discharge valves 13 a and 13 b of the filtered water discharge line 9, and the concentrated water discharge valve of the concentrated water discharge line 18 while driving the raw water supply pump 6 and the filtrate circulating pump 25. 15 is closed, and the filtrate water supply valve 19 and the switching valve 20 of the washing filtrate supply line 18 are opened, so that filtrate water stored in the filtrate water tank 10 is piped from the filtrate circulation line 24 to the filtrate discharge line 9. The water is fed to the concentrated water circulation line 8 through the passage 9c and the filtered filtered water supply line 18 (pipe lines 18a, 18b, 18c), and further supplied to the raw water side of the filtration unit 3B through the pipe line 4b of the raw water supply line 4. However, at this time, the raw water supply pump 6 allows two filters to be opened by opening the on-off valve 3d disposed in the raw water side connecting pipe 3c that connects the raw water sides of the two filtration membranes 3a and 3b. Film 3a, can the raw water side of the 3b circulating washed with filtered water, filtration membranes 3a, 3b durability, excellent in long life.
 以下、本発明を実施例により具体的に説明する。なお、本発明はこれらの実施例に限定されるものではない。
 実施の形態1で説明した浄水装置を用いて、洗浄によるろ過膜の透水性の回復について評価した。
 評価の方法としては、浄水装置1につき、14日間で延べ140時間、ろ過と洗浄を繰り返し、その間のろ過部3の原水側循環圧とろ過側ろ過圧の測定を行った。
 ろ過膜には限外ろ過膜(川澄化学工業株式会社製ダイアライザーKF-15)を使用した。原水供給ラインの配管には内径3mmのシリコンチューブを使用し、原水側ライン長4m、定量ろ過圧2.5kPa、膜の圧損20Pa、原水(試験水)の粘性係数0.002Pa・sの時にハーゲンポアズイユの法則から求めた流量約10×10-6/sを原水供給ポンプの流量として定量ろ過を行った。また、ろ過水循環ポンプの流量は約7×10-6/sとした。
 尚、評価に用いた原水(試験水)は、遠賀川沿岸部の土壌水にフミン酸を加え、フミン酸濃度が自然界の10倍程度となるように調整し、さらに微量の硫酸銅とニッケルを加えたものである。
Hereinafter, the present invention will be specifically described by way of examples. The present invention is not limited to these examples.
Using the water purifier described in Embodiment 1, the water permeability recovery of the filtration membrane by washing was evaluated.
As a method of evaluation, filtration and washing were repeated for 140 hours for 14 days for the water purifier 1, and the raw water-side circulation pressure and the filtration-side filtration pressure of the filtration unit 3 were measured during that time.
An ultrafiltration membrane (Dializer KF-15 manufactured by Kawasumi Chemical Co., Ltd.) was used as the filtration membrane. The raw water supply line uses a silicon tube with an inner diameter of 3 mm, the raw water side line length is 4 m, the quantitative filtration pressure is 2.5 kPa, the membrane pressure loss is 20 Pa, and the viscosity of the raw water (test water) is 0.002 Pa · s. Quantitative filtration was performed using a flow rate of about 10 × 10 −6 m 3 / s obtained from Poiseuille's law as the flow rate of the raw water supply pump. The flow rate of the filtrate circulating pump was about 7 × 10 −6 m 3 / s.
In addition, the raw water (test water) used for the evaluation was adjusted so that the humic acid concentration was about 10 times that of the natural world by adding humic acid to the soil water along the coast of the Onga River. It is added.
 その結果を図5に示す。
 図5は、ろ過と洗浄を繰り返した時のTMP(膜間差圧)の変化を示す図である。
 図5中、横軸は使用開始からの経過日数、縦軸は圧力であり、黒丸でプロットしたものが原水側循環圧、白四角でプロットしたものがろ過側ろ過圧である。尚、図4には、ろ過時又は洗浄時に測定した圧力の変動のみがプロットしてあり、装置が休止している間(ある日のろ過又は洗浄が終了し、次に洗浄又はろ過を開始するまでの間)は含まれていない。
 原水側循環圧が高く、ろ過側ろ過圧が低くなっている期間がろ過時の状態であり、原水側循環圧が低く、ろ過側ろ過圧が高くなっている期間が洗浄時の状態を表している。
 図5から、浄水装置1を14日間で延べ140時間駆動しても、TMP(膜間差圧)にほとんど変化がなく、洗浄によってろ過膜の透水性(ろ過効率)がほぼ一定に維持されていることがわかる。
 これにより、バブリングしたろ過水による洗浄機能を備えた本発明の浄水装置は、循環洗浄によって十分な透水性の回復を実現することができ、ろ過膜の長寿命性、耐久性、環境保護性に優れるものと言える。
The result is shown in FIG.
FIG. 5 is a diagram showing changes in TMP (transmembrane pressure difference) when filtration and washing are repeated.
In FIG. 5, the horizontal axis is the number of days elapsed from the start of use, the vertical axis is the pressure, what is plotted with a black circle is the raw water-side circulation pressure, and what is plotted with the white square is the filtration-side filtration pressure. In FIG. 4, only the pressure fluctuation measured during filtration or washing is plotted, and while the apparatus is at rest (one day of filtration or washing is finished, then washing or filtration is started). Is not included.
The period during which the raw water side circulation pressure is high and the filtration side filtration pressure is low is the state during filtration, and the period during which the raw water side circulation pressure is low and the filtration side filtration pressure is high represents the state during washing. Yes.
From FIG. 5, even if the water purifier 1 is driven for 14 days for 140 hours, there is almost no change in TMP (transmembrane pressure difference), and the water permeability (filtration efficiency) of the filtration membrane is maintained almost constant by washing. I understand that.
As a result, the water purifier of the present invention having a cleaning function with the bubbling filtered water can realize sufficient water permeability recovery by circulating cleaning, and the filter membrane has a long life, durability, and environmental protection. It can be said that it is excellent.
 本発明は、簡素な構成で、薬液を用いることなく、若しくは薬液の使用量を大幅に低減して、ろ過膜に付着した不純物や細菌などを確実かつ効率的に除去して細菌の増殖を抑制することができ、ろ過膜の洗浄効率性、環境保護性に優れ、ろ過膜の耐久性、長寿命性、メンテナンス性を大幅に向上させることができ、ろ過性能の経時劣化を防ぎ、動作の安定性、ろ過の効率性、省エネルギー性に優れると共に、ろ過水に含まれる電解質成分等をコントロールしてろ過水の純度を簡便に調整することができ、ろ過水を飲料水、食品や食器等の洗浄水など幅広い用途に使用することが可能な汎用性に優れた浄水装置の提供を行うことにより、水不足の解消に大きく貢献することができる。 The present invention has a simple structure and suppresses bacterial growth by removing impurities and bacteria adhering to the filter membrane reliably and efficiently without using chemicals or by greatly reducing the amount of chemicals used. Excellent filtration membrane cleaning efficiency and environmental protection, can greatly improve the durability, long life, and maintainability of the filtration membrane, prevent deterioration of filtration performance over time, and stable operation In addition to being excellent in performance, filtration efficiency and energy saving, the purity of filtered water can be easily adjusted by controlling the electrolyte components contained in the filtered water, and the filtered water can be washed in drinking water, food, dishes, etc. By providing a water purifier with excellent versatility that can be used for a wide range of uses such as water, it can greatly contribute to the elimination of water shortages.
1,1a,1b 浄水装置
2 原水タンク
2a 供給パイプ
2b 排出部
3,3A,3B ろ過部
3a,3b ろ過膜
3c 原水側接続管
3d 開閉弁
4 原水供給ライン
4a,4b,9a,9b,9c,9d,18a,18b,18c 管路
4c 分離タンク
5 原水供給弁
6 原水供給ポンプ
7,12 圧力メータ
8 濃縮水循環ライン
9 ろ過水排出ライン
10 ろ過水タンク
11 エアーチャンバー
13a,13b ろ過水排出弁
14 濃縮水排出ライン
15 濃縮水排出弁
16,21b 逆止弁
17 原水側気泡発生部
18 洗浄用ろ過水供給ライン
19 ろ過水供給弁
20 切替弁
21 排水ライン
21a 排水調整部
22 ろ過水バブリング用ライン
23 ろ過水側気泡発生部
24 ろ過水循環ライン
25 ろ過水循環ポンプ
26 ろ過水取水ライン
26a ろ過水取水切替弁
27 廃水ライン
27a 廃水切替弁
28a,28b 合流管
29a,29b ろ過水量調整弁
30 液体流入管
30a 液体流入孔
31 液体流出管
31a 液体流出孔
32 空気導入微孔
35 電導度計
1, 1a, 1b Water purification device 2 Raw water tank 2a Supply pipe 2b Discharge part 3, 3A, 3B Filtration part 3a, 3b Filtration membrane 3c Raw water side connection pipe 3d Open / close valve 4 Raw water supply lines 4a, 4b, 9a, 9b, 9c 9d, 18a, 18b, 18c Pipe line 4c Separation tank 5 Raw water supply valve 6 Raw water supply pump 7, 12 Pressure meter 8 Concentrated water circulation line 9 Filtrated water discharge line 10 Filtrated water tank 11 Air chamber 13a, 13b Filtrated water discharge valve 14 Concentration Water discharge line 15 Concentrated water discharge valve 16, 21 b Check valve 17 Raw water side bubble generation part 18 Washing filtrate supply line 19 Filtration water supply valve 20 Switching valve 21 Drain line 21 a Drain adjustment part 22 Filtration water bubbling line 23 Filtration Water-side bubble generating part 24 Filtrated water circulation line 25 Filtrated water circulation pump 26 Filtered water intake line 26a Filtered water intake switching valve 27 Wastewater line 27a Wastewater switching valves 28a and 28b Merge pipes 29a and 29b Filtration water amount adjustment valve 30 Liquid inflow pipe 30a Liquid inflow hole 31 Liquid outflow pipe 31a Liquid outflow hole 32 Air introduction microhole 35 Conductivity meter

Claims (7)

  1.  ろ過部に配設されたろ過膜で部分ろ過を行う循環型の浄水装置であって、
     原水が貯留される原水タンクと、前記原水タンクと前記ろ過部を接続し前記原水タンクから前記ろ過部に前記原水を供給する原水供給ポンプ及び原水供給弁を有する原水供給ラインと、前記原水供給ラインの前記原水供給ポンプより上流側と前記ろ過部を接続し前記ろ過部で濃縮された濃縮水を循環させる濃縮水循環ラインと、前記ろ過部に接続され前記ろ過部でろ過されたろ過水を排出するろ過水排出弁を有するろ過水排出ラインと、前記ろ過水排出ラインから排出されるろ過水を貯留するろ過水タンクと、前記濃縮水循環ラインから分岐して前記濃縮水を前記原水タンクに排出する濃縮水排出弁を有する濃縮水排出ラインと、前記濃縮水排出ラインの前記濃縮水排出弁より下流側に配設され前記原水タンク内をバブリングする原水側気泡発生部と、前記ろ過水排出ラインの前記ろ過水排出弁より上流側から分岐して前記濃縮水循環ラインの前記濃縮水排出ラインとの分岐位置より下流側で前記濃縮水循環ラインに接続されて前記ろ過水を洗浄水として供給するろ過水供給弁を有する洗浄用ろ過水供給ラインと、を備えたことを特徴とする浄水装置。
    A circulation type water purifier that performs partial filtration with a filtration membrane disposed in a filtration unit,
    A raw water tank in which raw water is stored, a raw water supply line having a raw water supply pump and a raw water supply valve that connect the raw water tank and the filtration unit and supply the raw water from the raw water tank to the filtration unit, and the raw water supply line The concentrated water circulation line for connecting the upstream side of the raw water supply pump and the filtration unit to circulate the concentrated water concentrated in the filtration unit, and discharging the filtered water connected to the filtration unit and filtered by the filtration unit A filtrate drain line having a filtrate drain valve, a filtrate tank storing the filtrate discharged from the filtrate drain line, and a concentration branching off from the concentrate circulation line and discharging the concentrate to the raw water tank A concentrated water discharge line having a water discharge valve, and a raw water side bubble that is disposed downstream of the concentrated water discharge valve of the concentrated water discharge line and bubbles in the raw water tank The filtrate is connected to the concentrated water circulation line downstream from the branch position between the raw part and the concentrated water discharge line of the concentrated water circulation line after branching from the upstream side of the filtered water discharge valve of the filtered water discharge line A water purification apparatus comprising: a filtrate water supply line for washing having a filtrate water supply valve for supplying water as washing water.
  2.  前記洗浄用ろ過水供給ラインの前記ろ過水供給弁より下流側に配設された切替弁と、前記ろ過水供給弁と前記切替弁の間で前記洗浄用ろ過水供給ラインから分岐して前記原水タンクに接続された排水ラインと、を備えたことを特徴とする請求項1に記載の浄水装置。 A switching valve disposed downstream of the filtrate water supply valve in the washing filtrate supply line, and the raw water branched from the washing filtrate supply line between the filtrate water supply valve and the switching valve. The water purifier according to claim 1, further comprising a drain line connected to the tank.
  3.  前記ろ過水排出ラインの前記ろ過水排出弁より上流側と前記ろ過水タンクを接続し、前記ろ過水を循環させるろ過水循環ポンプを有するろ過水循環ラインを備えたことを特徴とする請求項1又は2に記載の浄水装置。 The filtered water circulation line which has the filtered water circulation pump which connects the upstream side and the filtrate water tank from the filtrate water discharge valve of the filtrate water discharge line, and circulates the filtrate water is characterized by the above-mentioned. The water purifier according to 1.
  4.  前記洗浄用ろ過水供給ラインの前記ろ過水供給弁より下流側から分岐して前記ろ過水タンクに接続され前記ろ過水タンク内をバブリングするろ過水側気泡発生部を有するろ過水バブリング用ラインを備えたことを特徴とする請求項3に記載の浄水装置。 A filtration water bubbling line having a filtrate water-side bubble generating part that branches from the filtrate water supply valve downstream of the filtrate water supply valve and is connected to the filtrate water tank and bubbles in the filtrate water tank. The water purifier according to claim 3.
  5.  前記原水側気泡発生部及び前記ろ過水側気泡発生部が、筒状の液体流入管と、前記液体流入管の下流側に連設され前記液体流入管の内径より大きな内径を有する筒状の液体流出管と、前記液体流出管の上流側の周壁に穿設され前記液体流出管と連通する複数の空気導入微孔と、を備えたことを特徴とする請求項4に記載の浄水装置。 The raw water side bubble generating section and the filtrate water side bubble generating section are connected to a cylindrical liquid inflow pipe and a downstream side of the liquid inflow pipe, and a cylindrical liquid having an inner diameter larger than the inner diameter of the liquid inflow pipe. 5. The water purifier according to claim 4, comprising an outflow pipe and a plurality of air introduction micropores that are formed in a peripheral wall on the upstream side of the liquid outflow pipe and communicate with the liquid outflow pipe.
  6.  前記ろ過部が、並列に配設された性能の異なる2以上のろ過膜と、各々の前記ろ過膜のろ過側と前記ろ過水排出ラインを接続する合流管と、各々の前記合流管に配設されたろ過水量調整弁と、を備え、前記ろ過水排出ラインに電導度計が配設されたことを特徴とする請求項1乃至5の内いずれか1項に記載の浄水装置。 The filtration unit is arranged in parallel at two or more filtration membranes having different performances, a merging pipe connecting the filtration side of each of the filtration membranes and the filtrate discharge line, and each merging pipe A water purifier according to any one of claims 1 to 5, further comprising an electric conductivity meter disposed in the filtrate drain line.
  7.  前記ろ過部が、並列に配設された性能の異なる2つの前記ろ過膜の原水側同士を接続する原水側接続管と、前記原水側接続管に配設された開閉弁と、を備えたことを特徴とする請求項6に記載の浄水装置。 The filtration unit was provided with a raw water side connection pipe connecting the raw water sides of the two filtration membranes having different performance arranged in parallel, and an on-off valve arranged in the raw water side connection pipe. The water purifier according to claim 6.
PCT/JP2011/052929 2010-02-13 2011-02-10 Water purification device WO2011099578A1 (en)

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WO2014061695A1 (en) * 2012-10-18 2014-04-24 東レ株式会社 Fresh water generation method
CN104965419A (en) * 2015-06-01 2015-10-07 小米科技有限责任公司 Concentrated water discharging method and apparatus
WO2016119708A1 (en) * 2015-01-30 2016-08-04 艾欧史密斯(中国)热水器有限公司 Water tank assembly for water purifier, and water purifier

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WO2014061695A1 (en) * 2012-10-18 2014-04-24 東レ株式会社 Fresh water generation method
JPWO2014061695A1 (en) * 2012-10-18 2016-09-05 東レ株式会社 Fresh water generation method
WO2016119708A1 (en) * 2015-01-30 2016-08-04 艾欧史密斯(中国)热水器有限公司 Water tank assembly for water purifier, and water purifier
CN104965419A (en) * 2015-06-01 2015-10-07 小米科技有限责任公司 Concentrated water discharging method and apparatus
CN104965419B (en) * 2015-06-01 2018-06-08 小米科技有限责任公司 Condensed water discharge method and device

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