WO2021020138A1 - Water treatment device - Google Patents

Water treatment device Download PDF

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Publication number
WO2021020138A1
WO2021020138A1 PCT/JP2020/027611 JP2020027611W WO2021020138A1 WO 2021020138 A1 WO2021020138 A1 WO 2021020138A1 JP 2020027611 W JP2020027611 W JP 2020027611W WO 2021020138 A1 WO2021020138 A1 WO 2021020138A1
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WO
WIPO (PCT)
Prior art keywords
water
drug
pipe
water treatment
backwash
Prior art date
Application number
PCT/JP2020/027611
Other languages
French (fr)
Japanese (ja)
Inventor
崇 榊原
和大 齋藤
海野 毘
Original Assignee
パナソニックIpマネジメント株式会社
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
Priority claimed from JP2019140415A external-priority patent/JP7281617B2/en
Priority claimed from JP2019140418A external-priority patent/JP2021023835A/en
Priority claimed from JP2019140417A external-priority patent/JP7316492B2/en
Priority claimed from JP2019140416A external-priority patent/JP7329728B2/en
Priority claimed from JP2019142643A external-priority patent/JP2021023865A/en
Priority claimed from JP2019142645A external-priority patent/JP7361246B2/en
Priority claimed from JP2019142644A external-priority patent/JP2021023866A/en
Application filed by パナソニックIpマネジメント株式会社 filed Critical パナソニックIpマネジメント株式会社
Publication of WO2021020138A1 publication Critical patent/WO2021020138A1/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/71Feed mechanisms
    • B01F35/712Feed mechanisms for feeding fluids
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D24/00Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof
    • B01D24/46Regenerating the filtering material in the filter
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D29/00Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/62Regenerating the filter material in the filter
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D29/00Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/62Regenerating the filter material in the filter
    • B01D29/66Regenerating the filter material in the filter by flushing, e.g. counter-current air-bumps
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D35/00Filtering devices having features not specifically covered by groups B01D24/00 - B01D33/00, or for applications not specifically covered by groups B01D24/00 - B01D33/00; Auxiliary devices for filtration; Filter housing constructions
    • B01D35/16Cleaning-out devices, e.g. for removing the cake from the filter casing or for evacuating the last remnants of liquid
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F21/00Dissolving
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/71Feed mechanisms
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/71Feed mechanisms
    • B01F35/717Feed mechanisms characterised by the means for feeding the components to the mixer
    • B01F35/7176Feed mechanisms characterised by the means for feeding the components to the mixer using pumps
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J4/00Feed or outlet devices; Feed or outlet control devices
    • B01J4/02Feed or outlet devices; Feed or outlet control devices for feeding measured, i.e. prescribed quantities of reagents
    • 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
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/28Treatment of water, waste water, or sewage by sorption
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/58Treatment of water, waste water, or sewage by removing specified dissolved compounds
    • C02F1/62Heavy metal compounds
    • C02F1/64Heavy metal compounds of iron or manganese
    • 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

Definitions

  • This disclosure relates to a water treatment device that purifies water by filtration.
  • a chemical supply device that brings a solid oxidant into contact with water has been used to supply the oxidant in the water treatment device.
  • a chemical supply device that gradually dissolves solid calcium hypochlorite.
  • FIG. 13 is a schematic view showing the configuration of the conventional solid drug supply device 101.
  • the solid drug supply device 101 allows raw water to flow in from the intake port 102 to bring the raw water into contact with the water-soluble solid drug 103. Therefore, in the solid drug supply device 101, as the flow rate of the raw water increases, the water level in the drug contact phase 104 rises, so that the amount of the water-soluble solid drug 103 to be contacted can be increased. That is, according to this mechanism, in the solid drug supply device 101, even when the flow rate of raw water increases, the amount of drug elution increases, and it is possible to suppress a decrease in the concentration of the drug.
  • an object of the present disclosure is to provide a water treatment device capable of stabilizing the drug concentration even when used for a long period of time.
  • the water treatment apparatus includes a filtration unit containing a filter medium, a raw water inflow pipe for inflowing raw water into the filtration unit, a chemical supply unit for adding a chemical in the path of the raw water inflow pipe, and filtration. It has a purified water discharge pipe for taking out purified water after filtration from the section, and the drug placement location in the drug supply section is located higher in the vertical direction than the filter section, raw water inflow pipe, and purified water discharge pipe in the installed state. It is placed.
  • the water treatment apparatus can stabilize the drug concentration even when used for a long period of time.
  • FIG. 1 is a schematic view showing the overall configuration of the water treatment apparatus according to the first embodiment of the present disclosure.
  • FIG. 2 is a perspective view showing the internal structure of the water treatment apparatus.
  • FIG. 3 is a cross-sectional view of the filtration portion of the water treatment apparatus.
  • FIG. 4 is a schematic view showing the flow of water during the filtration treatment of the water treatment apparatus.
  • FIG. 5 is a schematic view showing the flow of water during the backwashing treatment of the water treatment apparatus.
  • FIG. 6 is a schematic view showing the flow of water during the rinsing treatment of the water treatment apparatus.
  • FIG. 7 is a perspective view of the drug supply unit of the water treatment apparatus.
  • FIG. 8 is a cross-sectional view of the drug supply section.
  • FIG. 1 is a schematic view showing the overall configuration of the water treatment apparatus according to the first embodiment of the present disclosure.
  • FIG. 2 is a perspective view showing the internal structure of the water treatment apparatus.
  • FIG. 3 is a cross-sectional
  • FIG. 9A is a cross-sectional view of a main part of the drug supply section.
  • FIG. 9B is an enlarged cross-sectional view of a main part of the drug supply section.
  • FIG. 10 is a cross-sectional view of an air supply valve used in the water treatment apparatus.
  • FIG. 11 is a side view showing the peripheral structure of the filtration portion of the water treatment apparatus.
  • FIG. 12 is an exterior perspective view of the water treatment device.
  • FIG. 13 is a schematic view showing the configuration of a conventional solid drug supply device.
  • the water treatment apparatus is composed of a filter unit containing a filter medium, a raw water inflow pipe for inflowing raw water into the filter unit, a chemical supply unit for adding a chemical in the route of the raw water inflow pipe, and a filter unit. It has a purified water discharge pipe for taking out purified water after filtration, and the chemical storage place in the chemical supply unit is arranged at a position higher in the vertical direction than the filtration unit, the raw water inflow pipe and the purified water discharge pipe in the installed state. It is a thing.
  • the water treatment apparatus since the drug storage place of the drug supply unit is provided at a position higher than other pipes and the filtration part in the installed state, air is introduced above the drug storage place. It can be in a state of being satisfied. Therefore, during the operation of the water treatment apparatus according to the present disclosure, only the lower part of the drug in the drug supply section is immersed in water, and when the water treatment device is stopped, the water can escape from the drug supply section to suppress the sticking of the drug. Therefore, the water treatment apparatus according to the present disclosure can stabilize the drug concentration even when used for a long period of time.
  • the water treatment device 1 uses the water stored in the well water or the water source of the water tank as raw water, and performs a filtration treatment for removing metal ions and turbid components contained in the raw water, and a filtration treatment in the system.
  • a backwash treatment is performed to discharge the accumulated metal ion aggregates and turbid components to the outside of the system.
  • FIG. 1 is a schematic view showing the overall configuration of the water treatment device 1
  • FIG. 2 is a perspective view showing the internal structure of the water treatment device 1.
  • the vertical direction (hereinafter, also simply referred to as “vertical”) in the state where the water treatment device 1 is installed (hereinafter, also referred to as “installed state”) is referred to. It may be described as the vertical direction.
  • the water treatment apparatus 1 has a filtration unit 2 containing a filter medium 2a (see FIG. 3) and a drug supply unit 3 for adding a drug to raw water, and the filtration unit 2 ,
  • the drug supply unit 3 is connected by a pipe as described later.
  • the filtration unit 2 purifies the raw water by removing metal ions and turbid components from the raw water, and is, so to speak, the heart of the water treatment device 1.
  • the pipe on the side that sends raw water to the filtration unit 2 is the raw water inflow pipe 10, and the pipe that sends the water purified by the filtration unit 2 (hereinafter, also referred to as “purified water”) from the filtration unit 2 is the purified water discharge pipe 20.
  • the water treatment device 1 has a raw water inflow pipe 10 for inflowing raw water into the filtration unit 2, and a purified water discharge pipe 20 for taking out purified water after filtration from the filtration unit 2.
  • the raw water inflow pipe 10 is indicated by diagonally hatched arrows
  • the purified water discharge pipe 20 is indicated by grid-shaped hatched arrows.
  • the purified water is stored in a water purification tank and used as domestic water when needed.
  • Raw water is sent to the water treatment device 1 by an electric pump 4 connected to the inlet side (opposite side of the filtration unit 2) of the raw water inflow pipe 10.
  • the method of sending the raw water to the water treatment device 1 may be another method that does not use the electric pump 4. That is, the method of sending the raw water to the water treatment device 1 may be a method in which the water storage tank is provided at a high place and the raw water is sent to the water treatment device 1 depending on the height difference between the water storage tank and the water treatment device 1. Further, the method of sending raw water to the water treatment device 1 may be a method of directly connecting tap water jointly operated in a region or the like.
  • the water source according to the present embodiment shall include devices for sending out raw water in addition to wells, water tanks, water supplies, and the like.
  • the electric pump 4 is a pump driven by an electric motor that sucks up and discharges well water or water stored in a water storage tank.
  • a centrifugal pump such as a vortex pump or a turbine pump, a vortex pump (cascade pump), a jet pump, etc.
  • Axial flow pumps, mixed flow pumps, etc. are used.
  • the depth of the well needs to be about 1 to 10 meters for a shallow well and 10 to 30 meters or more for a deep well.
  • the electric pump 4 should have a lift of 20 meters or more, such as a vortex pump or a jet pump.
  • the flow rate discharged by the electric pump is, for example, about 5 liters to 50 liters per minute, but when the water treatment device 1 is used in a general household, the electric pump 4 is 5 liters to 15 liters per minute. Those having a degree of flow rate characteristics are more preferable.
  • the raw water inflow pipe 10 and the purified water discharge pipe 20 may be made of a material and a structure that can withstand the water pressure of the electric pump 4. Specifically, from the viewpoint of durability and ease of processing, the raw water inflow pipe 10 and the purified water discharge pipe 20 are used, for example, vinyl chloride resin or steel pipe, or straight pipes or pipe joints using these composite materials. it can.
  • the inner diameters of the raw water inflow pipe 10 and the purified water discharge pipe 20 are preferably large so as to reduce the head loss, for example, 13 mm to 50 mm, and preferably 1 mm to 5 mm in thickness.
  • the drug supply unit 3 is provided in the path of the raw water inflow pipe 10. As will be described in detail later, the chemical supply unit 3 adds an oxidizing agent, which is a chemical, to the raw water, aggregates the metal ions contained in the raw water as a substance poorly soluble in water, and collects them in the filtration unit 2. It works to make it easier.
  • an oxidizing agent which is a chemical
  • FIG. 3 is a cross-sectional view of the filtration unit 2.
  • the filtration unit 2 includes a tank 2b, a filter medium 2a filled inside the tank 2b, a distribution plug 2c for connecting a pipe to the tank 2b, and a lead-out pipe 2d for taking out purified water after filtration.
  • the tank 2b in the present embodiment is a substantially cylindrical container, and the bottom thereof is formed in a bowl shape (it does not have to be bowl-shaped).
  • the distribution plug 2c is provided at the top of the tank 2b and communicates with the inside and outside of the filtration part 2.
  • a water discharge port and a discharge pipe connection port are provided on the inner side of the distribution plug 2c, the outlet pipe connection port and the purified water discharge pipe 20 communicate with each other, and the raw water inflow pipe 10 and the water discharge port communicate with each other.
  • Two pipes extend in the horizontal direction on the outer side of the distribution plug 2c, and each pipe is connected to the raw water inflow pipe 10 and the purified water discharge pipe 20.
  • the two pipes extending outward from the distribution plug 2c are arranged substantially in a straight line and extend in the opposite direction from the center of the distribution plug 2c.
  • the lead-out pipe 2d is arranged so as to be substantially vertical inside the tank 2b, the upper end is connected to the lead-out pipe connection port of the distribution plug 2c, and the lower end is an open end near the bottom surface of the tank 2b.
  • the lead-out pipe 2d is for discharging the filtered water from the lower side to the upper side during the filtration treatment, and may be a pipe having a small head loss and being difficult to block.
  • a straight pipe having a diameter of 20 mm or more can be used.
  • the material is preferably one that is not easily corroded, and for example, resin or metal is preferable.
  • a lower strainer 2e is attached to the lower end of the lead-out pipe 2d so that the filter medium 2a and the like do not enter the lead-out pipe 2d.
  • the spout provided in the distribution tap 2c and the raw water inflow pipe 10 communicate with each other.
  • Raw water will flow into the filtration unit 2 from the spout.
  • An upper strainer 2f is provided at the spout so as to cover the opening. The upper strainer 2f prevents the filter medium 2a from being discharged to the outside of the filtration unit 2 in the backwashing treatment described later.
  • the upper strainer 2f and the lower strainer 2e are arranged in order to prevent the filter medium 2a in the filtration unit 2 from flowing out from the filtration unit 2. That is, the upper strainer 2f is installed so as to cover the spout so that the filter medium 2a does not flow out from the filtration unit 2 during the backwashing treatment.
  • the lower strainer 2e is installed so as to cover the opening at the lower end of the lead-out pipe 2d so that the filter medium 2a does not flow out from the filtration unit 2 during the filtration process.
  • the upper strainer 2f and the lower strainer 2e may have a mesh shape, a slit shape, or the like, and may have a pore width of 0.3 to 1 mm or a gap smaller than that of the filter medium 2a.
  • the material is preferably one that is not easily corroded like the lead-out pipe 2d, and for example, resin or metal is preferable.
  • the filter medium 2a included in the filtration unit 2 is the most basic member for exhibiting the performance of the water treatment device 1.
  • the filter medium 2a is used to capture and remove coarse particles and agglomerates having a particle diameter of about 10 micrometers or more to reduce the turbidity of raw water.
  • the filter medium 2a can remove particles having a surface potential that are adsorbed on the filter medium 2a, particles having a particle diameter of about 1 micrometer to 10 micrometers, and chromaticity depending on the presence of ions and the like in the raw water.
  • the filter medium 2a those suitable for the object to be removed, such as filtered sand and pelletized fiber filter media, can be used.
  • the material of the filter medium 2a may be, for example, sand, anthracite, garnet, ceramics, granular activated carbon, iron oxyhydroxide, manganese sand, or the like, which has a hardness that does not easily deform under pressure.
  • the particle size may be, for example, 0.3 mm to 5.0 mm, an equality coefficient 1.2 to 2.0, or the like.
  • the specific gravity of the filter medium 2a differs depending on the material. For example, in the case of sand, about 2.5 g per cubic centimeter, to 2.7 g per cubic centimeter, and in the case of anthracite, 1.4 g per cubic centimeter to 1 It ranges from 1.8 grams per cubic centimeter, or 3.8 grams per cubic centimeter to 4.1 grams per cubic centimeter for garnets.
  • the multi-layer filtration method in which a plurality of types of filter media are mixed and used is a method in which particles having different sizes are laminated in order from the bottom as a layer to be filtered by utilizing such a difference in specific gravity.
  • the multi-layer filtration method it is common to mix particles having a large specific gravity and a small size and particles having a small specific gravity and a large size to form a multilayer structure.
  • the multi-layer filtration method is preferable because it has advantages such as high filtration efficiency per unit volume and low head loss as compared with using a single type of filter medium.
  • the granular filter medium for example, garnet having a particle size of 0.3 mm, sand having a particle size of 0.6 mm, and anthracite having a particle size of 1.0 mm are mixed at a ratio of 2: 1: 1. Although it is used, it is desirable to adjust the mixing ratio and particle size according to the particle characteristics of the turbid material.
  • the filling amount of the filter medium 2a is preferably determined in consideration of filtration performance, durability, head loss, and the like. By increasing the filter medium 2a, the removal performance and the amount of turbidity retained can be increased, the interval until cleaning can be extended and the frequency of cleaning can be reduced, but the head loss increases and the flow rate decreases. Problems may occur.
  • the filter medium 2a is composed of three layers using activated carbon as the upper layer, manganese sand as the middle layer, and gravel as the lower layer.
  • the above-mentioned filtration action works mainly on the upper layer and the middle layer.
  • the gravel layer having a relatively large particle size in the lowermost layer manganese sand and activated carbon are added to the lower strainer 2e so as to improve the flow of water to the lower strainer 2e and prevent the filter medium 2a from flowing out from the lower strainer 2e. It also acts as a cover to prevent it from reaching.
  • rectification is performed in the lowermost layer in order to facilitate the backwashing water ejected from the lower strainer 2e to flow to the middle layer and the upper layer.
  • the withstand voltage of the filtration unit 2 containing the filter medium 2a has a capacity equal to or higher than the maximum output head of the electric pump 4 to be used.
  • a metal, a resin, a resin reinforced with glass fiber, or the like is suitable.
  • the filtration unit 2 is required to have sufficient water resistance and weather resistance because it may be installed and used outdoors where a well is provided as well as in contact with water. Water resistance and weather resistance can be ensured by the material, wall thickness, or composite material such as coating. It is preferable that the size of the filtration unit 2 can secure a volume of about 1.5 to 3 times the total amount of the filter medium 2a to be put inside in consideration of the space developed by the filter medium 2a during backwashing.
  • the shape of the filtering unit 2 is preferably a cylindrical shape, a spherical shape, an ellipsoidal spherical shape, or the like having high durability against pressure, but if the container can be strengthened by a wall thickness or the like to ensure durability, a rectangular parallelepiped or a cube or the like can be obtained. Containers can also be used.
  • the particulate matter (dirt, turbid components, metal aggregates) collected in the filtration unit 2 is collected. It has a function to perform a backwash treatment that discharges) to the outside of the system by backwashing.
  • the piping configuration in the water treatment apparatus 1 and the flow of water in the filtration treatment and the backwash treatment will be described.
  • FIG. 4 is a schematic view showing the flow of water during the filtration process of the water treatment device 1.
  • the raw water inflow pipe 10 is connected to the filtration unit 2 from the raw water inlet 11 on the water source side via the chemical supply unit 3 during the filtration process.
  • the purified water discharge pipe 20 is connected from the filtration unit 2 to the water purification outlet 21 of the water treatment device 1 during the filtration process.
  • FIG. 5 is a schematic view showing the flow of water during the backwash treatment.
  • the water treatment device 1 sends water from the purified water discharge pipe 20 side to the filtration unit 2 and discharges water from the raw water inflow pipe 10 side in the filtration unit 2.
  • the water treatment device 1 can perform filtration treatment and backwash treatment by using one water source (electric pump 4) as one. Therefore, in order to allow the raw water to flow from the purified water discharge pipe 20 side in the filtration unit 2 during the backwash treatment, a backwash water pipe 80 that connects the raw water inflow pipe 10 and the purified water discharge pipe 20 is provided.
  • a branch portion 13 between the chemical supply unit 3 and the filtration unit 2 is provided between the chemical supply unit 3 and the backwash drain pipe 40 for discharging the backwash drain that flows out from the filtration unit 2 during the backwash treatment. It is provided as a first branch. Further, a branch portion 12 of the backwash water pipe 80 with the raw water inflow pipe 10 is provided as a second branch portion, and a branch portion 22 of the backwash water pipe 80 and the purified water discharge pipe 20 is provided as a third branch portion. There is.
  • the water treatment device 1 has a backwash drain pipe 40 branched downward from the branch portion 13 as the first branch portion and a backwash water pipe 80 branched at the branch portion 12 as the second branch portion.
  • water will flow as follows during the filtration process (see Fig. 4). That is, the water (raw water) flows in the order of the raw water inlet 11, (raw water inflow pipe 10), the branch portion 12, the chemical supply portion 3, and the branch portion 13, and flows into the filtration unit 2. Then, the water (purified water) that has exited the filtration unit 2 flows in the order of (purified water discharge pipe 20), the branch portion 22, and the water purification outlet 21, and finally flows into the water purification tank.
  • a check valve 62 (see FIG. 2) is provided in the path of the purified water discharge pipe 20.
  • the purified water taken out from the purified water outlet 21 is often connected to a water purification tank provided at a high place by piping.
  • the check valve 62 stops the backflow of purified water from a water purification tank provided at a high place and prevents the backflow of water into the filtration unit 2.
  • water will flow as follows (see Fig. 5). That is, the water flows in the order of the raw water inlet 11, (raw water inflow pipe 10), branch portion 12, (backwash water pipe 80), branch portion 22, (purified water discharge pipe 20), and flows into the filtration unit 2.
  • the water that has exited the filtration section 2 flows in the order of (raw water inflow pipe 10), branch section 13, (backwash drain pipe 40), and backwash drain port 41, and is discharged to the outside of the system.
  • the water treatment device 1 is provided with an on-off valve for switching the communication direction between the branch portion 12, the branch portion 13, and the branch portion 22 so that the water flows in the filtration treatment and the backwash treatment. ..
  • the on-off valve used in this embodiment uses the same type of manual valve, and when it is opened, the longitudinal direction of the handle is parallel to the pipe, and when it is closed, the longitudinal direction of the handle is orthogonal to the pipe. To. In the following, the direction of the handle shall mean the longitudinal direction of the handle.
  • the water treatment device 1 of the present embodiment realizes the above switching with four on-off valves (two-way valves). That is, the water treatment device 1 opens and closes the backwash water supply valve 81 provided in the backwash water pipe 80, the chemical supply valve 14, the purified water take-out valve 23, and the backwash valve 42 provided in the backwash drain pipe 40. Depending on the combination, the flow of water for filtration treatment and backwash treatment is switched.
  • the chemical supply valve 14 is located between the branch portion 12 and the chemical supply portion 3 in the raw water inflow pipe 10
  • the purified water take-out valve 23 is located between the branch portion 22 and the purified water outlet 21 in the purified water discharge pipe 20. It is provided in each.
  • the water treatment device 1 opens the chemical supply valve 14 and the purified water take-out valve 23, and closes the backwash water supply valve 81 and the backwash valve 42. That is, in the water treatment device 1, the raw water inlet 11 (water source) and the drug supply section 3 communicate with each other at the branch section 12 as the second branch section, and the drug supply section 3 communicates with the drug supply section 13 as the first branch section. Communicate with the filtration unit 2. Further, in the water treatment device 1, at the branch portion 22 as the third branch portion, the filtration unit 2 and the water purification outlet 21 (that is, the terminal side of the purified water discharge pipe 20) are communicated with each other.
  • the water treatment device 1 closes the chemical supply valve 14 and the purified water take-out valve 23, and opens the backwash water supply valve 81 and the backwash valve 42. That is, in the water treatment device 1, the raw water inlet 11 (water source) and the backwash water pipe 80 communicate with each other at the branch portion 12 as the second branch portion, and the filtration unit 2 at the branch portion 13 as the first branch portion. (The connection side of the filtration unit 2 with the raw water inflow pipe 10) and the backwash drain pipe 40 (backwash drain port 41) are communicated with each other. Further, in the water treatment device 1, at the branch portion 22 as the third branch portion, the backwash water pipe 80 and the filtration unit 2 (the connection side of the filtration unit 2 with the purified water discharge pipe 20) are communicated with each other.
  • the water treatment device 1 switches the communication direction of the branch portion 12 by the chemical supply valve 14 and the backwash water supply valve 81. Further, in the water treatment device 1, the water outlet is determined by the purified water take-out valve 23 and the backwash valve 42.
  • the water treatment apparatus 1 according to the present embodiment uses a two-way valve and switches the piping route without using a three-way valve having a complicated structure. Therefore, the water treatment device 1 according to the present embodiment can suppress clogging of pipes and can reduce the cost of the device as compared with the case of using a three-way valve.
  • the backwash water supply valve 81 and the backwash valve 42 are arranged so that the water supply direction is vertical, and the chemical supply valve 14 and the purified water take-out valve 23 are arranged so that the water supply direction is horizontal.
  • the handles of the backwash water supply valve 81, the backwash valve 42, the chemical supply valve 14, and the purified water take-out valve 23 are all oriented in the horizontal direction during the filtration process.
  • the handles of the backwash water supply valve 81, the backwash valve 42, the chemical supply valve 14, and the purified water take-out valve 23 are all oriented in the vertical direction, which makes it look good and makes it easy for the user to understand the operating state. There is a merit.
  • the water treatment device 1 requires a relatively large flow rate when performing the backwash treatment. That is, the water treatment device 1 has a smaller flow rate during the filtration process than the flow rate during the backwash process. Therefore, the water treatment device 1 is provided with a throttle portion 24 in a part of the pipe passing through during the filtration treatment so as to suppress the flow rate during the filtration treatment. Specifically, in the purified water discharge pipe 20, the throttle portion 24 is provided on the downstream side of the branch portion 22 (see FIG. 2). In the water treatment device 1, the flow rate at the time of filtration treatment is set to a desired design value by the combination of the throttle portion 24 and the electric pump 4.
  • the piping during the backwash treatment does not have a portion having a reduced diameter such as the throttle portion 24, a larger flow rate than during the filtration treatment can be secured and the backwash treatment can be performed efficiently. That is, the minimum diameter portion of the pipe used only for backwashing, the backwashing water pipe 80, and the backwashing drain pipe 40 is larger than the opening of the drawing portion 24. That is, the minimum diameter portion of the purified water discharge pipe 20 is smaller than the diameter portion adopted by the backwash water pipe 80 or the backwash drain pipe 40, and the water purification discharge pipe 20 has a branch portion 22 as a third branch portion and a filtration portion 2. Is provided on the opposite side.
  • the water treatment device 1 of the present embodiment can perform a "rinse treatment" for discharging foreign matter remaining in the pipe during the backwash treatment. This rinsing process will be described with reference to FIG.
  • FIG. 6 is a schematic view showing the flow of water during the rinsing treatment of the water treatment device 1.
  • the pipe for performing the rinsing treatment includes a branch portion 26, a rinsing drain pipe 27, and a rinsing drain valve 28 in the purified water discharge pipe 20.
  • the branch portion 26 is provided between the branch portion 22 and the water purification outlet 21 in the water purification discharge pipe 20. Then, the branch portion 26 branches the rinse drain pipe 27 from the purified water discharge pipe 20.
  • the rinse drain valve 28 opens and closes the rinse drain pipe 27, and when the rinse drain pipe 27 is opened, the water flowing through the purified water discharge pipe 20 flows to the rinse drain port 29.
  • the rinse drain valve 28 is closed during the filtration treatment and the backwash treatment (see FIGS. 4 and 5).
  • the water treatment device 1 opens the chemical supply valve 14, closes the purified water take-out valve 23, and closes the backwash water supply valve 81 and the backwash valve 42. Further, the water treatment device 1 opens the rinse drain valve 28.
  • water flows as follows during the rinsing process That is, the water flows in the order of the raw water inlet 11, (raw water inflow pipe 10), the branch portion 12, the chemical supply portion 3, and the branch portion 13, and flows into the filtration unit 2.
  • the water that has exited the filtration section 2 flows in the order of (purified water discharge pipe 20), branch section 22, (squeezing section 24), branch section 26, and rinse drain port 29, and is discharged to the outside of the system. That is, the flow of water up to the branch portion 26 is the same as that during the filtration process.
  • the water treatment device 1 of the present embodiment is provided with a direct drainage pipe 70 that bypasses the throttle portion 24 which is the minimum diameter portion of the purified water discharge pipe 20, and a direct drainage valve 71 that opens and closes the direct drainage pipe 70. .. Since the throttle portion 24 is a portion in which the pipe diameter is reduced, foreign matter is easily clogged. Therefore, it is preferable to directly open the drain valve 71 and bypass the narrowing portion 24, which is the minimum diameter portion, for the water during the rinsing treatment for discharging the foreign matter.
  • the drain valve 71 may be opened directly.
  • the degree of contamination of the accumulated well water is large immediately after the water treatment device 1 is installed, and if the well water is filtered (passed through the filtration unit 2) as it is, the desired purification performance cannot be obtained and foreign substances are removed. The contained water will flow out from the water purification outlet 21. Therefore, it is advisable to drain the initial raw water immediately after installation without filtering.
  • the raw water taken into the system does not pass through the filtration unit 2 and the chemical supply unit 3. It can be drained directly. Also in this case, the direct drain valve 71 may be opened.
  • the raw water taken into the system does not pass through the filtration unit 2 and the chemical supply unit 3. It can also be taken out directly.
  • the water treatment device 1 opens the chemical supply valve 14 and the purified water take-out valve 23, and closes the backwash water supply valve 81 and the backwash valve 42, as shown in FIG. Then, when the electric pump 4 is operated, the raw water sent in the raw water inflow pipe 10 is added with a chemical in the chemical supply unit 3 and flows into the filtration unit 2. Then, as shown in FIG. 3, the raw water flowing into the filtration unit 2 passes through the upper strainer 2f and then from the upper side to the lower side of the filter medium 2a, and at this time, the turbid component is filtered by the filter medium 2a. Will be removed. Finally, after flowing into the lower strainer 2e, it passes through the inside of the outlet pipe 2d, exits the filtration unit 2, and purified water is obtained from the purified water discharge pipe 20.
  • the suspended substance is first captured by the activated carbon layer in the upper layer, and the aggregation of metal ions is promoted.
  • the middle manganese sand layer aggregates of metal ions aggregated mainly in the upper layer are trapped.
  • the water treatment device 1 closes the chemical supply valve 14 and the purified water take-out valve 23, and opens the backwash water supply valve 81 and the backwash valve 42. Then, when the electric pump 4 is operated, the raw water flows back from the branch portion 12 through the backwash water pipe 80 to the purified water discharge pipe 20 and flows into the filtration portion 2. In the filtration unit 2, as shown in FIG. 3, the raw water flows downward in the outlet pipe 2d and infiltrates into the tank 2b from the lower strainer 2e. Raw water flows from bottom to top in tank 2b.
  • the water treatment device 1 separates the suspended substances and aggregates collected by the filter medium 2a from the filter medium 2a, and the filter unit is separated from the connection port of the raw water inflow pipe 10. 2 It is discharged to the outside.
  • FIG. 7 is a perspective view of the drug supply unit 3 of the water treatment device 1
  • FIG. 8 is a cross-sectional view of the drug supply unit 3.
  • 9A is a cross-sectional view of a main part of the drug supply unit 3
  • FIG. 9B is an enlarged cross-sectional view of a portion shown by a dotted line in FIG. 9A.
  • the drug supply unit 3 is arranged at the uppermost part of the water treatment device 1. That is, the chemical supply unit 3 is provided in the raw water inflow pipe 10 at the upper part of the pipe that rises upward from the raw water inlet 11. That is, the drug loading location (drug loading section 53) in the drug supply section 3 is arranged at a position higher in the vertical direction than the filtration section 2, the raw water inflow pipe 10, and the purified water discharge pipe 20 in the installed state. ..
  • the pipe from the outlet (outflow path 34, see FIG. 8) of the drug supply unit 3 extends downward and is connected to the filtration unit 2 via the branch portion 13.
  • the drug supply unit 3 has an inflow path 31, a drug path 32, a bypass path 33, and an outflow path 34.
  • the inflow path 31 is connected to the raw water inflow pipe 10 and allows the raw water to flow into the chemical supply unit 3.
  • the drug passage 32 branches from the inflow path 31 and dissolves the drug.
  • the bypass path 33 is also branched from the inflow path 31 and is provided to adjust the chemical solution to a required concentration.
  • the outflow passage 34 merges with the chemical passage 32 and the bypass passage 33, is connected to the raw water inflow pipe 10 again, and sends out the raw water containing the chemical to the raw water inflow pipe 10. That is, the drug supply unit 3 has a bottomed tubular housing 51, and has an inflow path 31, an outflow path 34, a drug path 32, and a branch portion 35 of the bypass path 33 inside the housing 51. ..
  • the drug passage 32 is formed inside the tubular housing 51.
  • the housing 51 has a bowl-shaped lower base 51a provided at the lower part and an upper cover 51b that covers the lower base 51a.
  • the housing 51 has a truncated cone shape with a smaller diameter toward the top.
  • An inflow path 31, a bypass path 33, and an outflow path 34 are connected to the lower base 51a, and a branch (branch portion 35) is formed inside the lower base 51a.
  • the raw water flowing in from the inflow passage 31 is branched into the chemical passage 32, the outflow passage 34 and the bypass passage 33 at the branch portion 35.
  • the lower base 51a is bowl-shaped and has an inflow passage 31, an outflow passage 34, and a branch portion 35 of the medicine passage 32 inside.
  • the drug passage 32 is a housing, which is an ejection pipe 52 that rises in the vertical direction after branching, a drug placing portion 53 that comes into contact with the drug at the upper part of the ejection tube 52 and elutes the drug, and an outer circumference of the ejection pipe 52. It is composed of a collection unit 54 that is inside the 51. That is, the drug passage 32 is erected upward from the branch portion 35, and the drug placement section 53 is provided above the drug path 32.
  • the chemical solution (raw water containing the drug) produced in the drug passage 32 is sent to the outflow channel 34 from the recovery opening 55 that communicates between the recovery unit 54 and the outflow channel 34. That is, in the housing 51, the outflow passage 34 is provided with an opening (recovery opening 55) for collecting the fluid that has passed through the drug passage 32.
  • the upper part of the ejection pipe 52 that is, the outer diameter of the ejection pipe 52 in the drug placing portion 53 has a larger diameter than the lower part of the ejection pipe 52, so that a desired amount of drug can be held. That is, the outer diameter of the lower part of the ejection pipe 52 is smaller than the outer diameter of the drug placing portion 53. Further, the water treatment device 1 secures the horizontal cross-sectional area of the recovery unit 54 by reducing the outer diameter of the lower portion of the ejection pipe 52.
  • the bypass road 33 merges at the outlet side (merging portion 36) of the outflow passage 34 in the state of raw water (see FIG. 7).
  • the raw water flowing through the outflow passage 34 merges with the chemical solution made in the chemical passage 32 at the recovery opening 55, and further downstream of the outflow passage 34, merges with the bypass passage 33 at the merging portion 36.
  • the drug solution having a desired concentration is delivered from the drug supply unit 3.
  • the raw water that has flowed into the drug supply section 3 is branched into the drug path 32, the bypass path 33, and the outflow path 34 at the branch section 35.
  • the water treatment device 1 adjusts the flow rate of the raw water flowing through the chemical passage 32, and adjusts the contact amount between the chemical and the raw water, which will be described later. Therefore, the raw water that comes into contact with the drug in the drug path 32 becomes a drug solution having a desired concentration.
  • the raw water that has passed through the drug passage 32 merges with the raw water that flows through the outflow passage 34 at the recovery opening 55.
  • the raw water of the outflow channel 34 branched at the branch portion 35 at a desired ratio merges with the drug solution of the drug path 32 adjusted to a desired concentration and flow rate at the recovery opening 55 to obtain a drug solution having a desired concentration.
  • the chemical solution in the drug passage 32 and the raw water in the outflow channel 34 merged at the recovery opening 55 are supposed to further merge with the raw water flowing in the bypass path 33 at the confluence 36, but the concentration of the drug after the confluence 36 It is advisable to adjust the flow rate of the bypass path 33 after confirming.
  • the ejection pipe 52 is a small-diameter pipe line and is erected with a drug placing portion 53 at the top.
  • the ejection pipe 52 supports the drug placing portion 53 inside the housing 51. As a result, the drug placing portion 53 is fixed at a position higher than the center of the housing 51.
  • the drug placing portion 53 has a dish shape or a box shape with an open upper part.
  • the bottom of the drug loading portion 53 is provided with an opening, is connected to the ejection pipe 52, and communicates the ejection pipe 52 with the inside of the drug loading portion 53.
  • the horizontal diameter of the ejection pipe 52 at the height of the drug placing portion 53 is larger than the diameter of the lower portion of the ejection pipe 52.
  • the water treatment device 1 first realizes that the raw water is brought into contact with the chemical at a desired flow rate by reducing the diameter of the lower portion of the ejection pipe 52 and providing the chemical loading portion 53 on the upper portion of the ejection pipe 52.
  • the drug placing portion 53 has a size for securing the amount (number) of the drugs to be placed so that a drug solution having a desired concentration can be obtained with respect to the flow rate of the raw water.
  • the drug solution in which the drug is dissolved flows out from the loading section outlet 58 (see FIG. 9B) provided on the side surface of the drug loading section 53 to the inside of the housing 51, that is, to the collecting section 54.
  • the chemical solution in which the drug is dissolved is stored in the lower part of the housing 51 (lower base 51a), and then flows out from the recovery opening 55 to the outflow path 34. Since the diameter of the ejection pipe 52 is reduced and the distance from the inner wall surface of the housing 51 is secured, the raw water in which the chemicals that have flowed down into the housing 51 has the liquid level relative to the height of the housing 51. , 1/2 or less.
  • the housing 51 when the housing 51 is filled with the chemical solution in the operating state of the water treatment device 1, the elution amount of the chemical solution placed in the chemical loading portion 53 becomes large, and the chemical solution having a desired concentration cannot be obtained, or the chemical solution is not obtained. May melt and disappear. Therefore, it is necessary to keep the liquid level in the housing 51 low.
  • the water treatment device 1 includes a solid drug, that is, a water-soluble solid drug 60 in the drug placing portion 53. That is, the drug passage 32 has an ejection pipe 52 erected upward in the housing 51, and has a drug placing portion 53 on which a solid drug is placed above the ejection pipe 52.
  • a solid drug that is, a water-soluble solid drug 60 in the drug placing portion 53.
  • the drug passage 32 has an ejection pipe 52 erected upward in the housing 51, and has a drug placing portion 53 on which a solid drug is placed above the ejection pipe 52.
  • tablets or granules may be used as the water-soluble solid drug 60. This is because the surface area of the water-soluble solid drug 60 can be increased and a stable solvent concentration can be maintained.
  • the size of the water-soluble solid drug 60 may be 30 mm in diameter and 10 mm to 20 mm in height for tablets, and 5 to 15 mm in diameter for granules.
  • the water treatment device 1 uses the water-soluble solid drug 60 having the above-mentioned size in order to supply the drug solution having a desired concentration.
  • the drug placing portion 53 is provided with a guide (not shown) so that the water-soluble solid drug 60 of the tablet can be held in the vertical direction. That is, the guide has a long rail shape in the vertical direction, and by inserting the water-soluble solid drug 60 between the two rails, the water-soluble solid drug 60 is held as if it were stacked in the vertical direction. Therefore, the water-soluble solid drug 60 dissolves in the raw water from below, and a drug solution having a desired concentration can be obtained.
  • the water-soluble solid drug 60 has a function of oxidizing metal ions contained in raw water to form agglomerates that are poorly soluble in water.
  • Various oxidizing agents can be used as the water-soluble solid drug 60, but the water-soluble solid drug 60 is soluble in water during the operation of the water treatment device 1, that is, when the drug is added to the raw water. Easy ones are good.
  • the water treatment device 1 is stopped or backwashed, that is, when the addition of the drug is interrupted, it is preferable that the water treatment device 1 retains its solid shape and does not flow out from the drug placing portion 53.
  • the water treatment apparatus 1 uses trichloroisocyanuric acid.
  • each member of the drug supply unit 3 may be in contact with the drug for a long time, it is preferable to select a material having low reactivity to the drug such as PVC (polyvinyl chloride), PMMA (polymethyl methacrylate), PP (polypropylene). ..
  • the material of the ejection tube 52 is vinyl chloride or ABS (acrylonitrile, butadiene, styrene), which is stronger than PP, considering compatibility with the drug. It is preferable to select such as. It is better to suppress the outer diameter of the ejection pipe 52 to 1/4 or less of the inner diameter of the lower base 51a.
  • a space (recovery unit 54) for temporarily storing the solution after the drug is supplied discharged from the mounting unit outlet 58 can be provided on the outside of the ejection pipe 52, and the water level in the housing 51 suddenly rises. This is because it can be prevented from rising and reaching the drug placing portion 53.
  • a vinyl chloride pipe having an outer diameter of about 25 mm to 40 mm may be used. That is, the outer diameter of the ejection pipe 52 may be 1/3 or less of the inner diameter of the housing 51 (lower base 51a).
  • the upper cover 51b has a truncated cone shape
  • the lower base 51a has a substantially cylindrical bottom
  • the inner diameter of the lower base 51a is the maximum inner diameter of the housing 51.
  • the ejection pipe 52 has a partition plate 56 that vertically partitions the inside of the ejection pipe 52.
  • the drug placing portion 53 is provided on the partition plate 56, and the water-soluble solid drug 60 is placed on the drug placing portion 53.
  • the partition plate 56 is provided with a mounting portion inlet 57 into which raw water sent from the ejection pipe 52 flows.
  • the mounting portion entrance 57 is provided near the central portion of the partition plate 56, but does not have to be the center.
  • the partition plate 56 has a mortar-shaped outer peripheral portion raised and the vicinity of the mounting portion entrance 57 lowered. That is, the partition plate 56 is provided with an inclination that descends from the outer edge side to the mounting portion entrance 57 side.
  • the mounting portion entrance 57 may be formed by forming a net-like central portion of the partition plate 56.
  • the mounting portion entrance 57 may be at least one donut-shaped slit formed so as to surround the central portion of the partition plate 56, or a plurality of small hole groups.
  • a mounting portion outlet 58 from which raw water containing a dissolved drug flows out.
  • the mounting portion outlet 58 is provided at a position higher than the top of the outer peripheral portion of the partition plate 56.
  • the water-soluble solid drug 60 is arranged on the partition plate 56 in the radial direction between the mounting portion inlet 57 and the mounting portion outlet 58.
  • the ejection pipe 52 has a partition plate 56 that partitions the inside vertically, and a mounting portion inlet 57 opened in the partition plate 56. Further, the mounting portion inlet 57 is provided closer to the central axis of the ejection pipe 52 than the mounting portion outlet 58, and the mounting portion outlet 58 is above the partition plate 56 and is on the side wall side of the ejection pipe 52. It is provided in. Further, the drug loading section 53 is for loading the drug on the partition plate 56, and a part of the drug loading section 53 is arranged between the loading section inlet 57 and the loading section outlet 58. ing. That is, the loading portion outlet 58 is provided above the lowest point of the drug loading portion 53.
  • the water-soluble solid drug 60 is arranged closer to the center on the mortar-shaped partition plate 56. Then, the raw water sent from the ejection pipe 52 infiltrates from the loading portion inlet 57, comes into contact with the water-soluble solid drug 60 placed near the center, and dissolves the water-soluble solid drug 60 to become a chemical solution. The raw water in which the drug is dissolved rises upward and flows out from the outlet 58 of the mounting section into the housing 51 of the drug supply section 3. At this time, since the water-soluble solid drug 60 is arranged between the mounting portion inlet 57 and the mounting portion outlet 58 in both the radial direction and the vertical direction, it always comes into contact with the raw water and is placed as a chemical solution. It flows out from the part outlet 58. In addition, the degree of contact of the water-soluble solid drug 60 can be ensured with respect to a predetermined flow rate, and the drug solution can be obtained in a desired concentration range.
  • the water-soluble solid chemicals 60 above the loading portion outlet 58 from containing water, so that the water-soluble solid chemicals 60 can be prevented from sticking to each other and sticking to the wall surface. It is possible. Since it is possible to prevent the water-soluble solid agents 60 from sticking to each other, when the water-soluble solid agents 60 in the lower layer are eluted and disappear, the upper solid agents are lowered by gravity, and the water-soluble solid agents 60 are placed in the lower part. Can be supplied. That is, the water-soluble solid drug 60 and raw water can be continuously brought into contact with each other. Then, the drug concentration can be stabilized even when the drug supply device is used for a long period of time.
  • the outer wall surface of the ejection pipe 52 and the drug placing portion 53 is an angle formed by a straight line lowered vertically downward from an arbitrary position on the outer wall surface and the outer wall surface below the loading portion outlet 58 (in FIG. 9A).
  • the angle ⁇ ) is preferably 0 to 45 degrees.
  • the raw water flowing out from the loading portion outlet 58 is allowed to flow down along the outer wall surface of the ejection pipe 52 and the drug loading portion 53 so as not to form blisters in the housing 51. By doing so, it is possible to prevent the drug solution having a desired concentration from being obtained.
  • a throttle portion is provided immediately after (downstream side) the branch portion 35.
  • This throttle portion is provided in order to adjust the distribution of the raw water flowing through the drug passage 32, the bypass path 33, and the outflow path 34, and to make the concentration of the drug in the raw water flowing out from the drug supply section 3 a desired concentration.
  • the bypass path 33 is provided with an on-off valve 33a (see FIG. 7), and the bypass path 33 can be closed.
  • the opening area of the throttle portion provided in the outflow passage 34 is larger than the opening area of the other throttle portions provided in the drug passage 32 (spout pipe 52) and the bypass passage 33. Thereby, the concentration of the drug solution flowing out from the drug supply unit 3 can be adjusted to a desired range.
  • the housing 51 of the drug supply unit 3 is designed so that the upper cover 51b can be removed from the lower base 51a. That is, the housing 51 has a tubular shape that can be vertically divided into an upper cover 51b and a lower base 51a. Since dirty raw water flows into the drug supply unit 3, regular maintenance is required. Therefore, the upper cover 51b is removed so that the inside can be cleaned. Further, the ejection pipe 52 can be removed at the branch portion 35. As described above, the drug passage 32 (spout pipe 52), the bypass passage 33, and the outflow passage 34 are each provided with a throttle on the downstream side of the branch portion 35, and foreign matter may be present in the throttle portion depending on long-term use. It is possible that it will adhere. Therefore, in the water treatment device 1, the ejection pipe 52 is removed at the branch portion 35 portion, and the inside of the pipe can be cleaned.
  • Part or all of the upper cover 51b should be transparent. By making the upper cover 51b transparent, the presence of the water-soluble solid drug 60 can be confirmed inside, and it can be replenished if necessary.
  • the upper portion of the upper cover 51b which is above the liquid level of the chemical solution in the housing 51, is transparent.
  • the top surface of the upper cover 51b may be a supply port for the water-soluble solid drug 60, and this supply port may be transparent. Further, as described above, since the water-soluble solid drug 60 is supported by the guide and arranged side by side, it is easy to confirm the input amount from the outside.
  • the water surface inside the housing 51 is designed to be at least half the height of the housing 51 during operation.
  • the loading portion outlet 58 is provided on the side surface of the drug loading portion 53. That is, the water treatment device 1 has a loading section outlet 58 on the side surface of the drug loading section 53 for discharging the drug solution in which the drug has been dissolved. Therefore, since the raw water does not reach the vicinity of the top surface of the housing 51, the vicinity of the supply port of the water-soluble solid chemical 60 is hard to get dirty. That is, the water treatment device 1 makes the supply port transparent so that the water-soluble solid drug 60 of the drug placing portion 53 can be easily visually recognized.
  • FIG. 10 is a cross-sectional view of the air supply valve 43 used in the water treatment device 1.
  • the backwash drain pipe 40 is formed by piping the backwash drain port 41 from the branch portion 13 (see FIG. 5). That is, the backwash drain pipe 40 extends downward from the branch portion 13 as the first branch portion.
  • An air supply valve 43 is provided on the downstream side of the backwash valve 42 in the middle of the path of the backwash drain pipe 40 (see FIG. 2).
  • One of the air supply valves 43 is connected to the backwash drain pipe 40, and the other is open to the atmosphere side (see FIG. 10).
  • the air supply valve 43 has a check valve structure, which enables inflow from the atmosphere side and prevents outflow from the backwash drain pipe 40 side.
  • the water treatment device 1 is provided with an air supply valve 43 in the path of the backwash drain pipe 40, which opens one end to the atmosphere and allows the water to flow into the pipe from the atmosphere side. Further, the air supply valve 43 is a check valve that can only flow in from the atmosphere side.
  • the air supply valve 43 is provided with a valve structure portion at a position where it rises upward from the backwash drain pipe 40. That is, the air supply valve 43 is provided at a position higher than the branch point 44 to the air supply valve 43 in the backwash drain pipe 40.
  • the backwash valve 42 is closed, and the backwash drain pipe 40 on the downstream side of the backwash valve 42 is filled with air. Then, when the backwash treatment is switched, as shown in FIG. 5, the backwash valve 42 is opened, so that the air in the backwash drain pipe 40 moves upward and enters the drug supply unit 3. Will supply air to.
  • the drug supply unit 3 is filled with air, the water-soluble solid drug 60 is exposed to air instead of being immersed in raw water. Therefore, it is possible to prevent the water-soluble solid drug 60 from being unnecessarily dissolved and to be prevented from being dissolved and fixed.
  • the backwashing drain pipe 40 since the backwashing drain pipe 40 is backwashed, drain water flows and is filled with the drain water.
  • the backwash valve 42 is closed again, and air is sent from the air supply valve 43 into the backwash drain pipe 40. Therefore, at times other than the backwash treatment, the backwash drain pipe 40 is filled with air, and air can be sent to the chemical supply unit 3 at the time of the next backwash treatment.
  • the water treatment device 1 fills the inside of the air supply valve 43 with air by providing the air supply valve 43 upward from the branch point 44 of the backwash drain pipe 40 with respect to the backwash drain pipe 40. It has a structure that suppresses the ingress of water. That is, the structure of the water treatment device 1 protects the air replenishment valve 43 from dirty water so that air replenishment can be reliably performed.
  • the horizontal height of the backwash drain pipe 40 in the piping path from the branch point 44 to the air supply valve 43 to the drug supply section 3 is the lowest at the branch point 44, and the drug supply section 3 It rises toward the outlet of the inflow path 31 of.
  • the air supply valve 43 is used as a check valve, but other types of valves may be used as long as air can be sent into the backwash drain pipe 40.
  • a manual valve may be used.
  • the method of sending air into the backwash drain pipe 40 is a method of sending air into the backwash drain pipe 40 when the backwash treatment is completed, or a drain hole and a stopper are provided in the path of the backwash drain pipe 40. When the backwash treatment is completed, the stopper may be removed, the water in the backwash drain pipe 40 may be drained, and air may be filled.
  • FIG. 11 is a side view showing the peripheral structure of the filtration unit 2 of the water treatment device 1
  • FIG. 12 is an exterior perspective view of the water treatment device 1.
  • the performance of the filter medium 2a filled in the filter unit 2 deteriorates due to long-term use even if it is backwashed. Therefore, the filtration unit 2 requires regular maintenance.
  • the water treatment device 1 of the present embodiment can remove the filtration unit 2.
  • connection joint 15 has an inflow side joint provided on the raw water inflow pipe 10 side and an outflow side joint provided on the purified water discharge pipe 20 side, and is filtered by the connection of the connection joint 15 having these two joints.
  • the part 2 is connected to the piping in the main body.
  • the outer shell is covered with a panel to form a housing.
  • the inspection panel 61 is a panel in one direction and the opposite surface to the filtration unit 2 among the outer panels. Maintenance of the filtration unit 2 can be performed by removing both or one of the inspection panels 61.
  • the filtration unit 2 can be translated toward one inspection panel 61 or the inspection panels 61 provided at two locations facing each other, and maintenance of the filtration unit 2 can be performed with a small inspection space. It will be possible.
  • the water treatment device 1 allows the filtration unit 2 to move in one direction and the opposite direction, it may be in only one direction.
  • the connection surface on the other side (opposite side of the filtration unit 2) of the connection joint 15 may be directed to one direction. That is, the connection surface on the piping side facing the connection joint 15 faces in one direction in which the filtration unit 2 moves, or the connection surface of the connection joint 15 is arranged parallel to the direction in which the filtration unit 2 moves. It suffices if it is done. According to such an arrangement, the filtration unit 2 can move in at least one direction.
  • the water treatment device is a water treatment device that can supply a sufficient amount of clean backwash water for backwashing and can be installed in a space-saving manner as compared with conventional products, and is therefore used for purifying well water and stored water. It is also useful as a small household water treatment device.

Abstract

The water treatment device (1) has a filter unit (2) that contains a filter medium, a raw water inlet pipe (10) for raw water to flow into the filter unit (2), a chemical supply unit (3) that adds a chemical in the channel of the raw water inlet pipe (10), and a purified water discharge pipe (20) for removing filtered purified water from the filter unit (2). The location where the chemical is placed in the chemical supply unit (3) is disposed higher than the filter unit (2), the raw water inlet pipe (10), and the purified water discharge pipe (20) in the vertical direction in an installed state.

Description

水処理装置Water treatment equipment
 本開示は、濾過によって水を浄化する水処理装置に関するものである。 This disclosure relates to a water treatment device that purifies water by filtration.
 従来、水処理装置における酸化剤の供給には固体の酸化剤を水に接触させる薬剤供給装置が用いられている。例えば、井戸水を浄水処理する場合には、固体の次亜塩素酸カルシウムを徐々に溶かす薬剤供給装置を用いて、浄水処理対象となる原水を酸化させることが可能である。 Conventionally, a chemical supply device that brings a solid oxidant into contact with water has been used to supply the oxidant in the water treatment device. For example, in the case of purifying well water, it is possible to oxidize the raw water to be treated by using a chemical supply device that gradually dissolves solid calcium hypochlorite.
 この薬剤供給装置として、定量ポンプで薬剤を注入するシステム、もしくは流量に関わらず一定量の薬剤を溶出させる薬剤供給装置を用いた場合、流量あるいは圧力が増加した際に薬剤濃度が低下してしまうことがある。これに対しては、次のような構造の固形薬剤供給装置が用いられる(例えば、特許文献1)。 When a system that injects a drug with a metering pump or a drug supply device that elutes a certain amount of drug regardless of the flow rate is used as this drug supply device, the drug concentration decreases when the flow rate or pressure increases. Sometimes. For this purpose, a solid drug supply device having the following structure is used (for example, Patent Document 1).
 図13は、従来の固形薬剤供給装置101の構成を示す模式図である。 FIG. 13 is a schematic view showing the configuration of the conventional solid drug supply device 101.
 図13に示す通り、固形薬剤供給装置101は、取水口102から原水を流入させて水溶性固形薬剤103に原水を接触させている。そのため、固形薬剤供給装置101では、原水の流量が増えると、薬剤接触相104内の水位が上昇するので、接触させる水溶性固形薬剤103の量を増加させることが可能である。すなわち、本機構により、固形薬剤供給装置101では、原水の流量が上昇した際も薬剤溶出量が上昇し、薬剤の濃度低下を抑えることが可能である。 As shown in FIG. 13, the solid drug supply device 101 allows raw water to flow in from the intake port 102 to bring the raw water into contact with the water-soluble solid drug 103. Therefore, in the solid drug supply device 101, as the flow rate of the raw water increases, the water level in the drug contact phase 104 rises, so that the amount of the water-soluble solid drug 103 to be contacted can be increased. That is, according to this mechanism, in the solid drug supply device 101, even when the flow rate of raw water increases, the amount of drug elution increases, and it is possible to suppress a decrease in the concentration of the drug.
実公昭58-49836号公報Jikken Sho 58-49863
 このような従来の固形薬剤供給装置においては、長期に使用した場合、固体の酸化剤が壁面に固着し、薬剤が原水と接触する位置まで下がってこなくなり、原水に薬剤が供給できなくなるという課題を有している。例えば、急激な流路の変更、ポンプの動作点が変わることにより、薬剤接触相に流入する流量が一時的に上昇し薬剤接触相の上端に達すると、薬剤接触相内の酸化剤が固着し、上層の薬剤が原水と薬剤の接触位置まで降下しなくなってしまう。結果として、従来の固形薬剤供給装置では、原水に安定した濃度の薬剤が供給できなくなってしまう場合があるという問題がある。 In such a conventional solid drug supply device, when used for a long period of time, the solid oxidant adheres to the wall surface and does not come down to the position where the drug comes into contact with the raw water, so that the drug cannot be supplied to the raw water. Have. For example, when the flow rate flowing into the drug contact phase temporarily increases and reaches the upper end of the drug contact phase due to a sudden change in the flow path or the operating point of the pump, the oxidizing agent in the drug contact phase sticks. , The upper layer chemicals will not drop to the contact position between the raw water and the chemicals. As a result, there is a problem that the conventional solid drug supply device may not be able to supply a drug having a stable concentration to the raw water.
 そこで、本開示は、長期に使用した場合にも薬剤濃度を安定させることが可能な水処理装置を提供することを目的とする。 Therefore, an object of the present disclosure is to provide a water treatment device capable of stabilizing the drug concentration even when used for a long period of time.
 そして、本開示に係る水処理装置は、濾材を内包した濾過部と、濾過部に原水を流入させるための原水流入配管と、原水流入配管の経路内で薬剤を添加する薬剤供給部と、濾過部から濾過後の浄水を取り出すための浄水吐出配管とを有し、薬剤供給部内の薬剤載置場所は、設置状態において、濾過部、原水流入配管及び浄水吐出配管よりも鉛直方向に高い位置に配置されたものである。 The water treatment apparatus according to the present disclosure includes a filtration unit containing a filter medium, a raw water inflow pipe for inflowing raw water into the filtration unit, a chemical supply unit for adding a chemical in the path of the raw water inflow pipe, and filtration. It has a purified water discharge pipe for taking out purified water after filtration from the section, and the drug placement location in the drug supply section is located higher in the vertical direction than the filter section, raw water inflow pipe, and purified water discharge pipe in the installed state. It is placed.
 本開示に係る水処理装置は、長期に使用した場合にも薬剤濃度を安定させることができる。 The water treatment apparatus according to the present disclosure can stabilize the drug concentration even when used for a long period of time.
図1は、本開示の実施の形態1に係る水処理装置の全体構成を示す概略図である。FIG. 1 is a schematic view showing the overall configuration of the water treatment apparatus according to the first embodiment of the present disclosure. 図2は、同水処理装置の内部構造を示す斜視図である。FIG. 2 is a perspective view showing the internal structure of the water treatment apparatus. 図3は、同水処理装置の濾過部の断面図である。FIG. 3 is a cross-sectional view of the filtration portion of the water treatment apparatus. 図4は、同水処理装置の濾過処理時の水の流れを示す概略図である。FIG. 4 is a schematic view showing the flow of water during the filtration treatment of the water treatment apparatus. 図5は、同水処理装置の逆洗処理時の水の流れを示す概略図である。FIG. 5 is a schematic view showing the flow of water during the backwashing treatment of the water treatment apparatus. 図6は、同水処理装置のリンス処理時の水の流れを示す概略図である。FIG. 6 is a schematic view showing the flow of water during the rinsing treatment of the water treatment apparatus. 図7は、同水処理装置の薬剤供給部の斜視図である。FIG. 7 is a perspective view of the drug supply unit of the water treatment apparatus. 図8は、同薬剤供給部の断面図である。FIG. 8 is a cross-sectional view of the drug supply section. 図9Aは、同薬剤供給部の要部の断面図である。FIG. 9A is a cross-sectional view of a main part of the drug supply section. 図9Bは、同薬剤供給部の要部の拡大断面図である。FIG. 9B is an enlarged cross-sectional view of a main part of the drug supply section. 図10は、同水処理装置に用いられる空気補給弁の断面図である。FIG. 10 is a cross-sectional view of an air supply valve used in the water treatment apparatus. 図11は、同水処理装置の濾過部の周辺構造を示す側面図である。FIG. 11 is a side view showing the peripheral structure of the filtration portion of the water treatment apparatus. 図12は、同水処理装置の外装斜視図である。FIG. 12 is an exterior perspective view of the water treatment device. 図13は、従来の固形薬剤供給装置の構成を示す模式図である。FIG. 13 is a schematic view showing the configuration of a conventional solid drug supply device.
 本開示に係る水処理装置は、濾材を内包した濾過部と、濾過部に原水を流入させるための原水流入配管と、原水流入配管の経路内で薬剤を添加する薬剤供給部と、濾過部から濾過後の浄水を取り出すための浄水吐出配管とを有し、薬剤供給部内の薬剤載置場所は、設置状態において、濾過部、原水流入配管及び浄水吐出配管よりも鉛直方向に高い位置に配置されたものである。 The water treatment apparatus according to the present disclosure is composed of a filter unit containing a filter medium, a raw water inflow pipe for inflowing raw water into the filter unit, a chemical supply unit for adding a chemical in the route of the raw water inflow pipe, and a filter unit. It has a purified water discharge pipe for taking out purified water after filtration, and the chemical storage place in the chemical supply unit is arranged at a position higher in the vertical direction than the filtration unit, the raw water inflow pipe and the purified water discharge pipe in the installed state. It is a thing.
 本開示に係る水処理装置では、薬剤供給部の薬剤載置場所が、設置状態において、他の配管及び濾過部よりも高い位置に設けられているので、薬剤載置場所の上部には空気が満たされる状態となり得る。そのため、本開示に係る水処理装置の運転中には、薬剤供給部の薬剤の下部のみが水に浸され、停止中には薬剤供給部から水がぬけて薬剤の固着を抑制し得る。従って、本開示に係る水処理装置は、長期に使用した場合にも薬剤濃度を安定させることができる。 In the water treatment apparatus according to the present disclosure, since the drug storage place of the drug supply unit is provided at a position higher than other pipes and the filtration part in the installed state, air is introduced above the drug storage place. It can be in a state of being satisfied. Therefore, during the operation of the water treatment apparatus according to the present disclosure, only the lower part of the drug in the drug supply section is immersed in water, and when the water treatment device is stopped, the water can escape from the drug supply section to suppress the sticking of the drug. Therefore, the water treatment apparatus according to the present disclosure can stabilize the drug concentration even when used for a long period of time.
 以下、本開示の実施の形態について図面を参照しながら説明する。 Hereinafter, embodiments of the present disclosure will be described with reference to the drawings.
 (実施の形態1)
 (全体構成)
 本実施の形態に係る水処理装置1は、井戸水または貯水槽の水源に蓄えた水を原水とし、この原水に含まれる金属イオンや濁質成分を除去する濾過処理と、濾過処理によって系内に蓄積された金属イオンの凝集物、濁質成分を系外へ排出する逆洗処理を行うものである。
(Embodiment 1)
(overall structure)
The water treatment device 1 according to the present embodiment uses the water stored in the well water or the water source of the water tank as raw water, and performs a filtration treatment for removing metal ions and turbid components contained in the raw water, and a filtration treatment in the system. A backwash treatment is performed to discharge the accumulated metal ion aggregates and turbid components to the outside of the system.
 まず、本実施の形態に係る水処理装置1の全体構成について、図1及び図2を用いて説明する。図1は、水処理装置1の全体構成を示す概略図であり、図2は、水処理装置1の内部構造を示す斜視図である。 First, the overall configuration of the water treatment device 1 according to the present embodiment will be described with reference to FIGS. 1 and 2. FIG. 1 is a schematic view showing the overall configuration of the water treatment device 1, and FIG. 2 is a perspective view showing the internal structure of the water treatment device 1.
 なお、説明の都合上、以下では、図2に示すように水処理装置1が設置された状態(以下、「設置状態」ともいう)での鉛直方向(以下、単に「鉛直」ともいう)を上下方向として記載する場合がある。 For convenience of explanation, in the following, as shown in FIG. 2, the vertical direction (hereinafter, also simply referred to as “vertical”) in the state where the water treatment device 1 is installed (hereinafter, also referred to as “installed state”) is referred to. It may be described as the vertical direction.
 図1及び図2に示すように、水処理装置1は、濾材2a(図3参照)を内包した濾過部2と、原水に対して薬剤を添加する薬剤供給部3を有し、濾過部2、薬剤供給部3を後述するように配管で接続して構成される。濾過部2は、詳細は後述するが、原水から金属イオンや濁質成分を除去し、原水を浄化するものであり、いわば、水処理装置1の心臓部である。濾過部2に対して、原水を送る側の配管を原水流入配管10とし、濾過部2で浄化された水(以下、「浄水」ともいう)を濾過部2から送出する配管を浄水吐出配管20とする。すなわち、水処理装置1は、濾過部2に原水を流入させるための原水流入配管10と、濾過部2から濾過後の浄水を取り出すための浄水吐出配管20とを有する。なお、図1では、原水流入配管10を斜線でハッチングされた矢印で示し、浄水吐出配管20を格子状にハッチングされた矢印で示している。浄化された水は、浄水タンクなどに貯められ、必要な時に生活水として使われることになる。 As shown in FIGS. 1 and 2, the water treatment apparatus 1 has a filtration unit 2 containing a filter medium 2a (see FIG. 3) and a drug supply unit 3 for adding a drug to raw water, and the filtration unit 2 , The drug supply unit 3 is connected by a pipe as described later. Although the details will be described later, the filtration unit 2 purifies the raw water by removing metal ions and turbid components from the raw water, and is, so to speak, the heart of the water treatment device 1. The pipe on the side that sends raw water to the filtration unit 2 is the raw water inflow pipe 10, and the pipe that sends the water purified by the filtration unit 2 (hereinafter, also referred to as “purified water”) from the filtration unit 2 is the purified water discharge pipe 20. And. That is, the water treatment device 1 has a raw water inflow pipe 10 for inflowing raw water into the filtration unit 2, and a purified water discharge pipe 20 for taking out purified water after filtration from the filtration unit 2. In FIG. 1, the raw water inflow pipe 10 is indicated by diagonally hatched arrows, and the purified water discharge pipe 20 is indicated by grid-shaped hatched arrows. The purified water is stored in a water purification tank and used as domestic water when needed.
 水処理装置1に対しては、原水流入配管10の入口側(濾過部2の反対側)に接続された電動ポンプ4によって原水が送られる。なお、水処理装置1に対して原水を送る方法は、電動ポンプ4を使用しない他の方法でもよい。すなわち、水処理装置1に対して原水を送る方法は、貯水槽を高所に設け、貯水槽と水処理装置1との高低差によって原水を水処理装置1に送る方法でもよい。また、水処理装置1に対して原水を送る方法は、地域などで共同運営している水道水を直接接続する方法でもよい。本実施の形態に係る水源は、井戸、貯水槽、水道等に加え、原水を送り出す装置類を含むものとする。 Raw water is sent to the water treatment device 1 by an electric pump 4 connected to the inlet side (opposite side of the filtration unit 2) of the raw water inflow pipe 10. The method of sending the raw water to the water treatment device 1 may be another method that does not use the electric pump 4. That is, the method of sending the raw water to the water treatment device 1 may be a method in which the water storage tank is provided at a high place and the raw water is sent to the water treatment device 1 depending on the height difference between the water storage tank and the water treatment device 1. Further, the method of sending raw water to the water treatment device 1 may be a method of directly connecting tap water jointly operated in a region or the like. The water source according to the present embodiment shall include devices for sending out raw water in addition to wells, water tanks, water supplies, and the like.
 電動ポンプ4は、井戸水または貯水槽へ蓄えた水を吸い上げ、吐出する電動機で駆動するポンプであって、例えば、渦巻きポンプ、タービンポンプなどの遠心ポンプや、渦流ポンプ(カスケードポンプ)、ジェットポンプ、軸流ポンプ、斜流ポンプなどが用いられる。一般家庭で用いる場合、井戸の深さは、浅井戸であれば1メートルから10メートル程度、深井戸であれば10メートルから30メートル以上吸い上げる必要がある。後段の配管や水処理装置1の損失水頭を考慮すると、一般家庭で水処理装置1を用いる場合には、電動ポンプ4は、20メートル以上の揚程があるものがよく、渦流ポンプやジェットポンプなどがより好ましい。一般的に、電動ポンプで吐出する流量は、例えば5リットルから50リットル毎分程度であるが、一般家庭で水処理装置1を用いる場合には、電動ポンプ4は、5リットルから15リットル毎分程度の流量特性をもつものがより好ましい。 The electric pump 4 is a pump driven by an electric motor that sucks up and discharges well water or water stored in a water storage tank. For example, a centrifugal pump such as a vortex pump or a turbine pump, a vortex pump (cascade pump), a jet pump, etc. Axial flow pumps, mixed flow pumps, etc. are used. When used in a general household, the depth of the well needs to be about 1 to 10 meters for a shallow well and 10 to 30 meters or more for a deep well. Considering the piping in the subsequent stage and the head loss of the water treatment device 1, when the water treatment device 1 is used in a general household, the electric pump 4 should have a lift of 20 meters or more, such as a vortex pump or a jet pump. Is more preferable. Generally, the flow rate discharged by the electric pump is, for example, about 5 liters to 50 liters per minute, but when the water treatment device 1 is used in a general household, the electric pump 4 is 5 liters to 15 liters per minute. Those having a degree of flow rate characteristics are more preferable.
 原水流入配管10及び浄水吐出配管20は、電動ポンプ4の水圧に耐えられる材質、構造であればよい。具体的には、耐久性、加工のしやすさから、原水流入配管10及び浄水吐出配管20は、例えば、塩化ビニル樹脂や鋼管、あるいは、これらの複合材料を用いた直管や配管継手が使用できる。なお、原水流入配管10及び浄水吐出配管20の内径は損失水頭が低くなるよう大きい方が好ましく、例えば13ミリメートルから50ミリメートルのもので、厚みは1ミリメートルから5ミリメートル程度のものが好ましい。 The raw water inflow pipe 10 and the purified water discharge pipe 20 may be made of a material and a structure that can withstand the water pressure of the electric pump 4. Specifically, from the viewpoint of durability and ease of processing, the raw water inflow pipe 10 and the purified water discharge pipe 20 are used, for example, vinyl chloride resin or steel pipe, or straight pipes or pipe joints using these composite materials. it can. The inner diameters of the raw water inflow pipe 10 and the purified water discharge pipe 20 are preferably large so as to reduce the head loss, for example, 13 mm to 50 mm, and preferably 1 mm to 5 mm in thickness.
 薬剤供給部3は、原水流入配管10の経路内に設けられている。詳しくは、後述するが、薬剤供給部3は、原水に対して薬剤である酸化剤を添加し、原水に含まれる金属イオンを水に難溶な物質として凝集させ、濾過部2において捕集しやすくする働きをする。 The drug supply unit 3 is provided in the path of the raw water inflow pipe 10. As will be described in detail later, the chemical supply unit 3 adds an oxidizing agent, which is a chemical, to the raw water, aggregates the metal ions contained in the raw water as a substance poorly soluble in water, and collects them in the filtration unit 2. It works to make it easier.
 (濾過部)
 次に、濾過部2の構成について、図3を用いて説明する。図3は、濾過部2の断面図である。
(Filtration section)
Next, the configuration of the filtration unit 2 will be described with reference to FIG. FIG. 3 is a cross-sectional view of the filtration unit 2.
 図3に示すように、濾過部2は、タンク2bと、タンク2bの内部に充填された濾材2aと、タンク2bに配管を接続する分配栓2cと、濾過後の浄水を取り出す導出管2dを有している。本実施の形態におけるタンク2bは、略円筒状の容器であって、底部は椀状に構成されている(椀状でなくてもよい)。分配栓2cは、タンク2bの頂部に備えられ、濾過部2の内外を連通している。分配栓2cの内部側には吐水口と導出管接続口が設けられ、導出管接続口と浄水吐出配管20とが連通し、原水流入配管10と吐水口とが連通している。分配栓2cの外部側には、2つの管が水平方向に延出され、それぞれの管が、原水流入配管10と、浄水吐出配管20とに接続されている。本実施の形態では、分配栓2cから外方向に延出した2つの管は、略一直線上に配置され、分配栓2cの中心から反対方向に延出している。 As shown in FIG. 3, the filtration unit 2 includes a tank 2b, a filter medium 2a filled inside the tank 2b, a distribution plug 2c for connecting a pipe to the tank 2b, and a lead-out pipe 2d for taking out purified water after filtration. Have. The tank 2b in the present embodiment is a substantially cylindrical container, and the bottom thereof is formed in a bowl shape (it does not have to be bowl-shaped). The distribution plug 2c is provided at the top of the tank 2b and communicates with the inside and outside of the filtration part 2. A water discharge port and a discharge pipe connection port are provided on the inner side of the distribution plug 2c, the outlet pipe connection port and the purified water discharge pipe 20 communicate with each other, and the raw water inflow pipe 10 and the water discharge port communicate with each other. Two pipes extend in the horizontal direction on the outer side of the distribution plug 2c, and each pipe is connected to the raw water inflow pipe 10 and the purified water discharge pipe 20. In the present embodiment, the two pipes extending outward from the distribution plug 2c are arranged substantially in a straight line and extend in the opposite direction from the center of the distribution plug 2c.
 導出管2dは、タンク2b内部において、略鉛直になるように配置され、上端を分配栓2cの導出管接続口に接続し、下端は、タンク2bの底面近傍で開放端となっている。導出管2dは、濾過処理の際に濾過水を下方から上方に排出するためのものであり、水頭損失が少なく、閉塞しにくいような管であればよい。例えば直径が20ミリメートル以上の直管などが使用できる。材質は腐食しにくいものがよく、例えば樹脂、金属などが好ましい。なお、詳しくは後述するが、導出管2dの下端には、下部ストレーナ2eが取り付けられており、導出管2d内に濾材2aなどが入り込まないようになっている。 The lead-out pipe 2d is arranged so as to be substantially vertical inside the tank 2b, the upper end is connected to the lead-out pipe connection port of the distribution plug 2c, and the lower end is an open end near the bottom surface of the tank 2b. The lead-out pipe 2d is for discharging the filtered water from the lower side to the upper side during the filtration treatment, and may be a pipe having a small head loss and being difficult to block. For example, a straight pipe having a diameter of 20 mm or more can be used. The material is preferably one that is not easily corroded, and for example, resin or metal is preferable. As will be described in detail later, a lower strainer 2e is attached to the lower end of the lead-out pipe 2d so that the filter medium 2a and the like do not enter the lead-out pipe 2d.
 上述のように、分配栓2cに設けられた吐水口と原水流入配管10とが連通している。 As described above, the spout provided in the distribution tap 2c and the raw water inflow pipe 10 communicate with each other.
 吐水口から濾過部2内に原水が流入することになる。吐水口には、上部ストレーナ2fが開口を覆うように設けられている。上部ストレーナ2fは、後述する逆洗処理において、濾材2aを濾過部2外へ排出しないようにしている。 Raw water will flow into the filtration unit 2 from the spout. An upper strainer 2f is provided at the spout so as to cover the opening. The upper strainer 2f prevents the filter medium 2a from being discharged to the outside of the filtration unit 2 in the backwashing treatment described later.
 上部ストレーナ2fと下部ストレーナ2eは、濾過部2内の濾材2aが濾過部2から外部へ流出することを防止するためにそれぞれ配置したものである。すなわち、上部ストレーナ2fは、吐水口を覆うように設置して逆洗処理の際に濾材2aが濾過部2から流出しないようにするものである。下部ストレーナ2eは、導出管2dの下端部の開口を覆うように設置して濾過処理の際に濾材2aが濾過部2から流出しないようにするためのものである。上部ストレーナ2f、下部ストレーナ2eは、メッシュ状、スリット状などの形状で、濾材2aよりも開口幅が小さく0.3から1ミリメートルの細孔か隙間を持つものが使用できる。材質は、導出管2dと同様に腐食しにくいものがよく、例えば樹脂、金属などが好ましい。 The upper strainer 2f and the lower strainer 2e are arranged in order to prevent the filter medium 2a in the filtration unit 2 from flowing out from the filtration unit 2. That is, the upper strainer 2f is installed so as to cover the spout so that the filter medium 2a does not flow out from the filtration unit 2 during the backwashing treatment. The lower strainer 2e is installed so as to cover the opening at the lower end of the lead-out pipe 2d so that the filter medium 2a does not flow out from the filtration unit 2 during the filtration process. The upper strainer 2f and the lower strainer 2e may have a mesh shape, a slit shape, or the like, and may have a pore width of 0.3 to 1 mm or a gap smaller than that of the filter medium 2a. The material is preferably one that is not easily corroded like the lead-out pipe 2d, and for example, resin or metal is preferable.
 濾過部2に内包されている濾材2aは、水処理装置1の性能を発揮するための最も基本となる部材である。濾材2aは、粒子径約10マイクロメートル以上の粗大粒子や凝集物を捕捉して除去し、原水の濁度を低減するために用いられる。濾材2aによって、濾材2aに吸着するような表面電位を持つ粒子や、原水中のイオン等の存在状態によっては粒子径約1マイクロメートル~10マイクロメートルの粒子や色度も除去可能となる。 The filter medium 2a included in the filtration unit 2 is the most basic member for exhibiting the performance of the water treatment device 1. The filter medium 2a is used to capture and remove coarse particles and agglomerates having a particle diameter of about 10 micrometers or more to reduce the turbidity of raw water. The filter medium 2a can remove particles having a surface potential that are adsorbed on the filter medium 2a, particles having a particle diameter of about 1 micrometer to 10 micrometers, and chromaticity depending on the presence of ions and the like in the raw water.
 濾材2aとしては、濾過砂をはじめ、ペレット状の繊維濾材等、除去対象物に適したものを用いることができる。濾材2aの材質は、例えば、砂、アンスラサイト、ガーネット、セラミックス、粒状活性炭、オキシ水酸化鉄、マンガン砂など、水中で沈降し、圧力で変形しにくい硬度をもつものであればよい。粒子径は、例えば0.3ミリメートルから5.0ミリメートル、均等係数1.2から2.0などのものを用いるとよい。 As the filter medium 2a, those suitable for the object to be removed, such as filtered sand and pelletized fiber filter media, can be used. The material of the filter medium 2a may be, for example, sand, anthracite, garnet, ceramics, granular activated carbon, iron oxyhydroxide, manganese sand, or the like, which has a hardness that does not easily deform under pressure. The particle size may be, for example, 0.3 mm to 5.0 mm, an equality coefficient 1.2 to 2.0, or the like.
 また、濾材2aは材質によって比重が異なり、例えば砂であればおよそ2.5グラム毎立法センチメートル、から2.7グラム毎立方センチメートル、アンスラサイトであれば、1.4グラム毎立法センチメートルから1.8グラム毎立方センチメートル、ガーネットであれば3.8グラム毎立法センチメートルから4.1グラム毎立方センチメートルである。複数の種類の濾材を混合して使用する複層濾過法は、このような比重の違いを利用し、濾過を行う層としてサイズの異なる粒子を小さい粒子から順に下から積層する方法である。複層濾過法では、比重が大きくサイズが小さい粒子と、比重が小さくサイズが大きい粒子を混合して多層構造にするのが一般的である。複層濾過法は、単一の種類の濾材を用いるのに比べて、単位体積あたりの濾過効率が高く、一方で損失水頭が低く抑えられるなどのメリットがあるため好ましい。粒状濾材としては、例えば、粒子径が0.3ミリメートルのガーネットと、粒子径が0.6ミリメートルの砂と、粒子径が1.0ミリメートルのアンスラサイトを、2:1:1で混合して使用するが、濁質の粒子特性に応じて混合比率や粒子径を調整することが望ましい。濾材2aの充填量は濾過性能と耐久性、損失水頭などを考慮して決定することが好ましい。濾材2aを増やすと、除去性能や濁質の保持量が増加し、洗浄までの間隔を延ばす事ができて洗浄頻度を減らす事ができる一方、損失水頭が上昇するため、流量が減少するなどの不具合が生じる場合がある。 In addition, the specific gravity of the filter medium 2a differs depending on the material. For example, in the case of sand, about 2.5 g per cubic centimeter, to 2.7 g per cubic centimeter, and in the case of anthracite, 1.4 g per cubic centimeter to 1 It ranges from 1.8 grams per cubic centimeter, or 3.8 grams per cubic centimeter to 4.1 grams per cubic centimeter for garnets. The multi-layer filtration method in which a plurality of types of filter media are mixed and used is a method in which particles having different sizes are laminated in order from the bottom as a layer to be filtered by utilizing such a difference in specific gravity. In the multi-layer filtration method, it is common to mix particles having a large specific gravity and a small size and particles having a small specific gravity and a large size to form a multilayer structure. The multi-layer filtration method is preferable because it has advantages such as high filtration efficiency per unit volume and low head loss as compared with using a single type of filter medium. As the granular filter medium, for example, garnet having a particle size of 0.3 mm, sand having a particle size of 0.6 mm, and anthracite having a particle size of 1.0 mm are mixed at a ratio of 2: 1: 1. Although it is used, it is desirable to adjust the mixing ratio and particle size according to the particle characteristics of the turbid material. The filling amount of the filter medium 2a is preferably determined in consideration of filtration performance, durability, head loss, and the like. By increasing the filter medium 2a, the removal performance and the amount of turbidity retained can be increased, the interval until cleaning can be extended and the frequency of cleaning can be reduced, but the head loss increases and the flow rate decreases. Problems may occur.
 本実施の形態においては、濾材2aは、上層として活性炭、中層にはマンガン砂、下層には砂利を用いた3層で構成されている。本実施の形態の濾過部2は、上層、中層を中心に上述の濾過の作用が働く。一方、最下層に比較的粒径の大きい砂利層では、下部ストレーナ2eに至るまでの水の流れを良くするとともに、下部ストレーナ2eから濾材2aが流出しないように下部ストレーナ2eにマンガン砂、活性炭が到達しないよう、覆う役割も果たしている。また、後述する逆洗処理の場合には、下部ストレーナ2eから噴出する逆洗用の水が、中層・上層に流れやすくするため、最下層で整流を行っている。 In the present embodiment, the filter medium 2a is composed of three layers using activated carbon as the upper layer, manganese sand as the middle layer, and gravel as the lower layer. In the filtration unit 2 of the present embodiment, the above-mentioned filtration action works mainly on the upper layer and the middle layer. On the other hand, in the gravel layer having a relatively large particle size in the lowermost layer, manganese sand and activated carbon are added to the lower strainer 2e so as to improve the flow of water to the lower strainer 2e and prevent the filter medium 2a from flowing out from the lower strainer 2e. It also acts as a cover to prevent it from reaching. Further, in the case of the backwash treatment described later, rectification is performed in the lowermost layer in order to facilitate the backwashing water ejected from the lower strainer 2e to flow to the middle layer and the upper layer.
 また、濾材2aを内包する濾過部2の耐圧は使用する電動ポンプ4の最高出力揚程以上の能力があることが好ましい。濾過部2の素材としては、金属、樹脂、あるいはガラス繊維で強化した樹脂などが好適である。そして、濾過部2は、水に接するだけでなく、井戸が設けられた屋外に設置して使用する場合があるため、十分な耐水性、耐候性を有することが要求される。耐水性、耐候性は、材質や肉厚、あるいはコーティングなどの複合素材によって確保することができる。濾過部2の大きさは、逆洗浄の際に濾材2aが展開するスペースを考慮して、内部に入れる濾材2aの総量の約1.5から3倍程度の容積を確保できることが好ましい。また、濾過部2の形状は、圧力に対する耐久性が高い円筒型や球型、楕円球型などが好ましいが、容器を肉厚などで強化して耐久性が確保できれば直方体や立方体などの角型容器を使用することもできる。 Further, it is preferable that the withstand voltage of the filtration unit 2 containing the filter medium 2a has a capacity equal to or higher than the maximum output head of the electric pump 4 to be used. As the material of the filtration unit 2, a metal, a resin, a resin reinforced with glass fiber, or the like is suitable. The filtration unit 2 is required to have sufficient water resistance and weather resistance because it may be installed and used outdoors where a well is provided as well as in contact with water. Water resistance and weather resistance can be ensured by the material, wall thickness, or composite material such as coating. It is preferable that the size of the filtration unit 2 can secure a volume of about 1.5 to 3 times the total amount of the filter medium 2a to be put inside in consideration of the space developed by the filter medium 2a during backwashing. The shape of the filtering unit 2 is preferably a cylindrical shape, a spherical shape, an ellipsoidal spherical shape, or the like having high durability against pressure, but if the container can be strengthened by a wall thickness or the like to ensure durability, a rectangular parallelepiped or a cube or the like can be obtained. Containers can also be used.
 (配管構成)
 本実施の形態の水処理装置1は、濾過部2において、原水を濾過し、浄水として取り出す濾過処理のほかに、濾過部2で捕集された粒状物質(よごれ、濁質成分、金属凝集物など)を逆洗によって系外へ排出する逆洗処理を行う機能を有している。次に、水処理装置1内の配管構成と、濾過処理、逆洗処理における水の流れを説明する。
(Piping configuration)
In the water treatment apparatus 1 of the present embodiment, in addition to the filtration treatment in which the raw water is filtered and taken out as purified water in the filtration unit 2, the particulate matter (dirt, turbid components, metal aggregates) collected in the filtration unit 2 is collected. It has a function to perform a backwash treatment that discharges) to the outside of the system by backwashing. Next, the piping configuration in the water treatment apparatus 1 and the flow of water in the filtration treatment and the backwash treatment will be described.
 図4は、水処理装置1の濾過処理時における水の流れを示した概略図である。図4に示すように、原水流入配管10は、濾過処理時において、水源側の原水入口11から薬剤供給部3を経由して濾過部2へと接続するものである。浄水吐出配管20は、濾過処理時において、濾過部2から水処理装置1の浄水出口21へと接続するものである。 FIG. 4 is a schematic view showing the flow of water during the filtration process of the water treatment device 1. As shown in FIG. 4, the raw water inflow pipe 10 is connected to the filtration unit 2 from the raw water inlet 11 on the water source side via the chemical supply unit 3 during the filtration process. The purified water discharge pipe 20 is connected from the filtration unit 2 to the water purification outlet 21 of the water treatment device 1 during the filtration process.
 一方、図5は、逆洗処理時の水の流れを示した概略図である。図5に示すように、逆洗処理時には、濾過部2内の水の流れが逆になる。従って、水処理装置1は、逆洗処理時には、濾過部2では、浄水吐出配管20側から濾過部2へ水を送り、原水流入配管10側から水を出す。 On the other hand, FIG. 5 is a schematic view showing the flow of water during the backwash treatment. As shown in FIG. 5, during the backwashing process, the flow of water in the filtration unit 2 is reversed. Therefore, during the backwashing process, the water treatment device 1 sends water from the purified water discharge pipe 20 side to the filtration unit 2 and discharges water from the raw water inflow pipe 10 side in the filtration unit 2.
 本実施の形態による水処理装置1は、水源(電動ポンプ4)をひとつにして、濾過処理及び逆洗処理を行うことができる。従って、逆洗処理時に濾過部2において原水を浄水吐出配管20側から流すようにするため、原水流入配管10と浄水吐出配管20とを接続する逆洗送水管80が設けられている。 The water treatment device 1 according to the present embodiment can perform filtration treatment and backwash treatment by using one water source (electric pump 4) as one. Therefore, in order to allow the raw water to flow from the purified water discharge pipe 20 side in the filtration unit 2 during the backwash treatment, a backwash water pipe 80 that connects the raw water inflow pipe 10 and the purified water discharge pipe 20 is provided.
 ここで、原水流入配管10において、薬剤供給部3と濾過部2との間には、逆洗処理時に濾過部2から流出する逆洗ドレンを排出する逆洗ドレン管40との分岐部13が第一分岐部として設けられている。また、逆洗送水管80の原水流入配管10との分岐部12が第二分岐部として、逆洗送水管80と浄水吐出配管20との分岐部22が第三分岐部として、それぞれ設けられている。 Here, in the raw water inflow pipe 10, a branch portion 13 between the chemical supply unit 3 and the filtration unit 2 is provided between the chemical supply unit 3 and the backwash drain pipe 40 for discharging the backwash drain that flows out from the filtration unit 2 during the backwash treatment. It is provided as a first branch. Further, a branch portion 12 of the backwash water pipe 80 with the raw water inflow pipe 10 is provided as a second branch portion, and a branch portion 22 of the backwash water pipe 80 and the purified water discharge pipe 20 is provided as a third branch portion. There is.
 すなわち、水処理装置1は、第一分岐部としての分岐部13から下方に分岐した逆洗ドレン管40と第二分岐部として分岐部12で分岐した逆洗送水管80とを有する。 That is, the water treatment device 1 has a backwash drain pipe 40 branched downward from the branch portion 13 as the first branch portion and a backwash water pipe 80 branched at the branch portion 12 as the second branch portion.
 このような配管構成において、濾過処理時には、以下のように水が流れることになる(図4参照)。すなわち、水(原水)は、原水入口11、(原水流入配管10)、分岐部12、薬剤供給部3、分岐部13の順に流れ、濾過部2へ流入する。そして、濾過部2を出た水(浄水)は、(浄水吐出配管20)、分岐部22、浄水出口21の順に流れ、最終的に浄水タンクへ流入する。 In such a piping configuration, water will flow as follows during the filtration process (see Fig. 4). That is, the water (raw water) flows in the order of the raw water inlet 11, (raw water inflow pipe 10), the branch portion 12, the chemical supply portion 3, and the branch portion 13, and flows into the filtration unit 2. Then, the water (purified water) that has exited the filtration unit 2 flows in the order of (purified water discharge pipe 20), the branch portion 22, and the water purification outlet 21, and finally flows into the water purification tank.
 なお、浄水吐出配管20の経路内には、逆止弁62(図2参照)が設けられている。浄水出口21から取り出した浄水は、高所に設けた浄水タンクへと配管接続される場合が多い。逆止弁62は、高所に設けられた浄水タンクからの浄水の逆流を制止し、濾過部2内への水の逆流入を防ぐものである。 A check valve 62 (see FIG. 2) is provided in the path of the purified water discharge pipe 20. The purified water taken out from the purified water outlet 21 is often connected to a water purification tank provided at a high place by piping. The check valve 62 stops the backflow of purified water from a water purification tank provided at a high place and prevents the backflow of water into the filtration unit 2.
 一方、逆洗処理時には、以下のように水が流れることになる(図5参照)。即ち、水は、原水入口11、(原水流入配管10)、分岐部12、(逆洗送水管80)、分岐部22、(浄水吐出配管20)の順に流れ、濾過部2へ流入する。濾過部2を出た水は、(原水流入配管10)、分岐部13、(逆洗ドレン管40)、逆洗ドレン口41の順に流れ、系外へ排出される。 On the other hand, during the backwash treatment, water will flow as follows (see Fig. 5). That is, the water flows in the order of the raw water inlet 11, (raw water inflow pipe 10), branch portion 12, (backwash water pipe 80), branch portion 22, (purified water discharge pipe 20), and flows into the filtration unit 2. The water that has exited the filtration section 2 flows in the order of (raw water inflow pipe 10), branch section 13, (backwash drain pipe 40), and backwash drain port 41, and is discharged to the outside of the system.
 濾過処理、逆洗処理において、上記水の流れとなるように、水処理装置1には、分岐部12、分岐部13、分岐部22での連通方向を切り替えるための開閉バルブが設けられている。本実施の形態で用いる開閉バルブは、同じ種類の手動弁を用い、開放する場合には、取っ手の長手方向を配管と平行にし、閉鎖する場合には、取っ手の長手方向を配管と直交する向きにする。以下では、取っ手の方向とは、取っ手の長手方向のことをいうものとする。 The water treatment device 1 is provided with an on-off valve for switching the communication direction between the branch portion 12, the branch portion 13, and the branch portion 22 so that the water flows in the filtration treatment and the backwash treatment. .. The on-off valve used in this embodiment uses the same type of manual valve, and when it is opened, the longitudinal direction of the handle is parallel to the pipe, and when it is closed, the longitudinal direction of the handle is orthogonal to the pipe. To. In the following, the direction of the handle shall mean the longitudinal direction of the handle.
 本実施の形態の水処理装置1は、4個の開閉バルブ(二方弁)で上記切り替えを実現している。すなわち、水処理装置1は、逆洗送水管80に設けた逆洗送水バルブ81と、薬剤供給バルブ14と、浄水取出バルブ23と、逆洗ドレン管40に設けた逆洗バルブ42の開閉の組み合わせによって濾過処理、逆洗処理の水の流れを切り替えている。 The water treatment device 1 of the present embodiment realizes the above switching with four on-off valves (two-way valves). That is, the water treatment device 1 opens and closes the backwash water supply valve 81 provided in the backwash water pipe 80, the chemical supply valve 14, the purified water take-out valve 23, and the backwash valve 42 provided in the backwash drain pipe 40. Depending on the combination, the flow of water for filtration treatment and backwash treatment is switched.
 ここで、薬剤供給バルブ14は、原水流入配管10において、分岐部12と薬剤供給部3との間に、浄水取出バルブ23は、浄水吐出配管20において、分岐部22と浄水出口21との間にそれぞれ設けられている。 Here, the chemical supply valve 14 is located between the branch portion 12 and the chemical supply portion 3 in the raw water inflow pipe 10, and the purified water take-out valve 23 is located between the branch portion 22 and the purified water outlet 21 in the purified water discharge pipe 20. It is provided in each.
 濾過処理時には、図4に示すように、水処理装置1は、薬剤供給バルブ14と浄水取出バルブ23を開放し、逆洗送水バルブ81と逆洗バルブ42を閉鎖する。すなわち、水処理装置1は、第二分岐部としての分岐部12では、原水入口11(水源)と薬剤供給部3を連通させ、第一分岐部としての分岐部13では、薬剤供給部3と濾過部2とを連通させる。また、水処理装置1は、第三分岐部としての分岐部22では、濾過部2と浄水出口21(つまり浄水吐出配管20の末端側)とを連通させる。 During the filtration process, as shown in FIG. 4, the water treatment device 1 opens the chemical supply valve 14 and the purified water take-out valve 23, and closes the backwash water supply valve 81 and the backwash valve 42. That is, in the water treatment device 1, the raw water inlet 11 (water source) and the drug supply section 3 communicate with each other at the branch section 12 as the second branch section, and the drug supply section 3 communicates with the drug supply section 13 as the first branch section. Communicate with the filtration unit 2. Further, in the water treatment device 1, at the branch portion 22 as the third branch portion, the filtration unit 2 and the water purification outlet 21 (that is, the terminal side of the purified water discharge pipe 20) are communicated with each other.
 一方、逆洗処理時には、図5に示すように、水処理装置1は、薬剤供給バルブ14と浄水取出バルブ23を閉鎖し、逆洗送水バルブ81と逆洗バルブ42を開放する。すなわち、水処理装置1は、第二分岐部としての分岐部12では、原水入口11(水源)と逆洗送水管80とを連通させ、第一分岐部としての分岐部13では、濾過部2(濾過部2の原水流入配管10との接続側)と逆洗ドレン管40(逆洗ドレン口41)とを連通させる。また、水処理装置1は、第三分岐部としての分岐部22では、逆洗送水管80と濾過部2(濾過部2の浄水吐出配管20との接続側)を連通させる。 On the other hand, during the backwash treatment, as shown in FIG. 5, the water treatment device 1 closes the chemical supply valve 14 and the purified water take-out valve 23, and opens the backwash water supply valve 81 and the backwash valve 42. That is, in the water treatment device 1, the raw water inlet 11 (water source) and the backwash water pipe 80 communicate with each other at the branch portion 12 as the second branch portion, and the filtration unit 2 at the branch portion 13 as the first branch portion. (The connection side of the filtration unit 2 with the raw water inflow pipe 10) and the backwash drain pipe 40 (backwash drain port 41) are communicated with each other. Further, in the water treatment device 1, at the branch portion 22 as the third branch portion, the backwash water pipe 80 and the filtration unit 2 (the connection side of the filtration unit 2 with the purified water discharge pipe 20) are communicated with each other.
 すなわち、水処理装置1は、薬剤供給バルブ14と逆洗送水バルブ81によって分岐部12の連通方向を切り替えている。また、水処理装置1は、浄水取出バルブ23と逆洗バルブ42によって水の取り出し口を決定している。このように、本実施の形態に係る水処理装置1は、二方弁を用い、構造の複雑な三方弁を使用せずに配管経路の切り替えを行っている。従って、本実施の形態に係る水処理装置1は、三方弁を使用する場合と比較し、配管の詰まりの抑制ができるとともに、装置にかかるコストを抑えることができる。 That is, the water treatment device 1 switches the communication direction of the branch portion 12 by the chemical supply valve 14 and the backwash water supply valve 81. Further, in the water treatment device 1, the water outlet is determined by the purified water take-out valve 23 and the backwash valve 42. As described above, the water treatment apparatus 1 according to the present embodiment uses a two-way valve and switches the piping route without using a three-way valve having a complicated structure. Therefore, the water treatment device 1 according to the present embodiment can suppress clogging of pipes and can reduce the cost of the device as compared with the case of using a three-way valve.
 また、本実施の形態では、逆洗送水バルブ81、逆洗バルブ42は送水方向が鉛直になるよう配置され、薬剤供給バルブ14、浄水取出バルブ23は送水方向が水平になるよう配置される。このような配置により、濾過処理時には、逆洗送水バルブ81、逆洗バルブ42、薬剤供給バルブ14、浄水取出バルブ23の取っ手は全て水平方向に向けられることになる。また、逆洗処理時には、逆洗送水バルブ81、逆洗バルブ42、薬剤供給バルブ14、浄水取出バルブ23の取っ手は全て鉛直方向に向けられることになり、見た目もよく、ユーザーにとって運転状態がわかり易いというメリットがある。 Further, in the present embodiment, the backwash water supply valve 81 and the backwash valve 42 are arranged so that the water supply direction is vertical, and the chemical supply valve 14 and the purified water take-out valve 23 are arranged so that the water supply direction is horizontal. With such an arrangement, the handles of the backwash water supply valve 81, the backwash valve 42, the chemical supply valve 14, and the purified water take-out valve 23 are all oriented in the horizontal direction during the filtration process. In addition, during the backwash treatment, the handles of the backwash water supply valve 81, the backwash valve 42, the chemical supply valve 14, and the purified water take-out valve 23 are all oriented in the vertical direction, which makes it look good and makes it easy for the user to understand the operating state. There is a merit.
 また、水処理装置1は、逆洗処理を行う際には、比較的大きな流量を必要とする。すなわち、水処理装置1は、逆洗処理時の流量よりも濾過処理時の流量を小さくしている。そのため、水処理装置1は、濾過処理時に通過する配管の一部に絞り部24を設け、濾過処理時における流量を抑えるようにしている。具体的には、浄水吐出配管20のうち、分岐部22の下流側で絞り部24が設けられている(図2参照)。水処理装置1は、絞り部24と電動ポンプ4との組み合わせによって、濾過処理時の流量を所望の設計値にしている。 Further, the water treatment device 1 requires a relatively large flow rate when performing the backwash treatment. That is, the water treatment device 1 has a smaller flow rate during the filtration process than the flow rate during the backwash process. Therefore, the water treatment device 1 is provided with a throttle portion 24 in a part of the pipe passing through during the filtration treatment so as to suppress the flow rate during the filtration treatment. Specifically, in the purified water discharge pipe 20, the throttle portion 24 is provided on the downstream side of the branch portion 22 (see FIG. 2). In the water treatment device 1, the flow rate at the time of filtration treatment is set to a desired design value by the combination of the throttle portion 24 and the electric pump 4.
 一方、逆洗処理時の配管には、絞り部24のような径を小さくした部分がないので、濾過処理時よりも大きな流量を確保し、逆洗処理を効率的に行うことができる。すなわち、逆洗時のみに用いる配管、逆洗送水管80、逆洗ドレン管40の最小径部は、絞り部24の開口よりも大きくなっている。つまり、浄水吐出配管20の最小径部は、逆洗送水管80または逆洗ドレン管40の採用径部より小さく、浄水吐出配管20において第三分岐部としての分岐部22に対し濾過部2とは反対側に設けられている。 On the other hand, since the piping during the backwash treatment does not have a portion having a reduced diameter such as the throttle portion 24, a larger flow rate than during the filtration treatment can be secured and the backwash treatment can be performed efficiently. That is, the minimum diameter portion of the pipe used only for backwashing, the backwashing water pipe 80, and the backwashing drain pipe 40 is larger than the opening of the drawing portion 24. That is, the minimum diameter portion of the purified water discharge pipe 20 is smaller than the diameter portion adopted by the backwash water pipe 80 or the backwash drain pipe 40, and the water purification discharge pipe 20 has a branch portion 22 as a third branch portion and a filtration portion 2. Is provided on the opposite side.
 なお、本実施の形態の水処理装置1は、逆洗処理時に配管内に残った異物を排出するための「リンス処理」を行うことができる。このリンス処理について、図6を用いて説明する。 Note that the water treatment device 1 of the present embodiment can perform a "rinse treatment" for discharging foreign matter remaining in the pipe during the backwash treatment. This rinsing process will be described with reference to FIG.
 図6は、水処理装置1のリンス処理時の水の流れを示す概略図である。図6に示すように、リンス処理を行うための配管は、浄水吐出配管20において、分岐部26と、リンスドレン管27と、リンスドレンバルブ28を備えている。分岐部26は、浄水吐出配管20において、分岐部22と浄水出口21の間に設けられている。そして、分岐部26は、浄水吐出配管20からリンスドレン管27を分岐している。リンスドレンバルブ28は、リンスドレン管27の開閉を行い、開放したときに浄水吐出配管20を流れてきた水をリンスドレン口29へと流すものである。濾過処理、逆洗処理時には、リンスドレンバルブ28は閉鎖である(図4及び図5参照)。 FIG. 6 is a schematic view showing the flow of water during the rinsing treatment of the water treatment device 1. As shown in FIG. 6, the pipe for performing the rinsing treatment includes a branch portion 26, a rinsing drain pipe 27, and a rinsing drain valve 28 in the purified water discharge pipe 20. The branch portion 26 is provided between the branch portion 22 and the water purification outlet 21 in the water purification discharge pipe 20. Then, the branch portion 26 branches the rinse drain pipe 27 from the purified water discharge pipe 20. The rinse drain valve 28 opens and closes the rinse drain pipe 27, and when the rinse drain pipe 27 is opened, the water flowing through the purified water discharge pipe 20 flows to the rinse drain port 29. The rinse drain valve 28 is closed during the filtration treatment and the backwash treatment (see FIGS. 4 and 5).
 水処理装置1は、リンス処理時には、薬剤供給バルブ14を開放し、浄水取出バルブ23を閉鎖し、逆洗送水バルブ81と逆洗バルブ42を閉鎖する。さらに、水処理装置1は、リンスドレンバルブ28を開放する。このようなバルブ操作によって、リンス処理時には、以下のように水が流れることになる。即ち、水は、原水入口11、(原水流入配管10)、分岐部12、薬剤供給部3、分岐部13の順に流れ、濾過部2へ流入する。濾過部2を出た水は、(浄水吐出配管20)、分岐部22、(絞り部24)、分岐部26、リンスドレン口29の順に流れ、系外へ排出される。すなわち、水の流れは、分岐部26までは濾過処理時と同じである。 At the time of rinsing, the water treatment device 1 opens the chemical supply valve 14, closes the purified water take-out valve 23, and closes the backwash water supply valve 81 and the backwash valve 42. Further, the water treatment device 1 opens the rinse drain valve 28. By such a valve operation, water flows as follows during the rinsing process. That is, the water flows in the order of the raw water inlet 11, (raw water inflow pipe 10), the branch portion 12, the chemical supply portion 3, and the branch portion 13, and flows into the filtration unit 2. The water that has exited the filtration section 2 flows in the order of (purified water discharge pipe 20), branch section 22, (squeezing section 24), branch section 26, and rinse drain port 29, and is discharged to the outside of the system. That is, the flow of water up to the branch portion 26 is the same as that during the filtration process.
 逆洗処理が終わった直後には、濾過部2内、あるいは、水処理装置1の配管内には、濾過部2の逆洗によって洗い出された異物が残っている。そのため、リンス処理によって、分岐部26までは濾過処理時と同じように水を流すことで、濾過部2内、あるいは、水処理装置1の配管内に残った異物を系外へ排出し、次に濾過処理を行う際に異物が浄水に混入してしまうことを抑制ことができる。 Immediately after the backwashing process is completed, foreign matter washed out by the backwashing of the filtration unit 2 remains in the filtration unit 2 or in the piping of the water treatment device 1. Therefore, by the rinsing treatment, water is allowed to flow up to the branch portion 26 in the same manner as in the filtration treatment, so that the foreign matter remaining in the filtration portion 2 or the piping of the water treatment device 1 is discharged to the outside of the system, and then It is possible to prevent foreign substances from being mixed into the purified water when the filtration treatment is performed.
 また、本実施の形態の水処理装置1は、浄水吐出配管20の最小径部である絞り部24を迂回する直接排水管70と直接排水管70の開閉を行う直接排水バルブ71を設けている。絞り部24は、配管径を小さくした部分であるので、異物が詰まり易くなっている。そのため、異物を排出するリンス処理時に水は、直接排水バルブ71を開放し、最小径部となる絞り部24を迂回して流すとよい。 Further, the water treatment device 1 of the present embodiment is provided with a direct drainage pipe 70 that bypasses the throttle portion 24 which is the minimum diameter portion of the purified water discharge pipe 20, and a direct drainage valve 71 that opens and closes the direct drainage pipe 70. .. Since the throttle portion 24 is a portion in which the pipe diameter is reduced, foreign matter is easily clogged. Therefore, it is preferable to directly open the drain valve 71 and bypass the narrowing portion 24, which is the minimum diameter portion, for the water during the rinsing treatment for discharging the foreign matter.
 また、原水の汚れ度合によっては、濾過部2を通さず、そのまま排水したほうが良い場合がある。このような場合には、直接排水バルブ71を開放するとよい。例えば、原水として井戸水用いる場合などにおいて、水処理装置1の設置直後は貯まった井戸水の汚れ度合が大きく、そのまま濾過処理(濾過部2を通す)すると、所望の浄化性能が得られず、異物を含んだ水が浄水出口21から流出することになる。そのため、設置直後の初期の原水は濾過せずそのまま排水するとよい。すなわち、逆洗送水バルブ81、リンスドレンバルブ28を開放し、薬剤供給バルブ14、浄水取出バルブ23を閉鎖することによって、系内に取り入れた原水を濾過部2、薬剤供給部3を通さずに直接排水することができる。この場合にも、直接排水バルブ71は開放するとよい。 Also, depending on the degree of contamination of the raw water, it may be better to drain the water as it is without passing through the filtration unit 2. In such a case, the drain valve 71 may be opened directly. For example, when well water is used as raw water, the degree of contamination of the accumulated well water is large immediately after the water treatment device 1 is installed, and if the well water is filtered (passed through the filtration unit 2) as it is, the desired purification performance cannot be obtained and foreign substances are removed. The contained water will flow out from the water purification outlet 21. Therefore, it is advisable to drain the initial raw water immediately after installation without filtering. That is, by opening the backwash water supply valve 81 and the rinse drain valve 28 and closing the chemical supply valve 14 and the purified water take-out valve 23, the raw water taken into the system does not pass through the filtration unit 2 and the chemical supply unit 3. It can be drained directly. Also in this case, the direct drain valve 71 may be opened.
 また、逆洗送水バルブ81、浄水取出バルブ23を開放し、薬剤供給バルブ14、リンスドレンバルブ28を閉鎖することによって、系内に取り入れた原水を濾過部2、薬剤供給部3を通さずに直接取り出すこともできる。 Further, by opening the backwash water supply valve 81 and the purified water take-out valve 23 and closing the chemical supply valve 14 and the rinse drain valve 28, the raw water taken into the system does not pass through the filtration unit 2 and the chemical supply unit 3. It can also be taken out directly.
 (濾過、逆洗作用)
 上記の構成によって行われる、本実施の形態の水処理装置1における濾過処理、逆洗処理について、図3~図5を用いて説明する。
(Filtration, backwashing action)
The filtration treatment and the backwash treatment in the water treatment apparatus 1 of the present embodiment, which are performed by the above configuration, will be described with reference to FIGS. 3 to 5.
 水処理装置1は、濾過処理時には、図4に示すように、薬剤供給バルブ14と浄水取出バルブ23を開放し、逆洗送水バルブ81と逆洗バルブ42を閉鎖する。そして、電動ポンプ4を運転すると、原水流入配管10内を送られる原水は、薬剤供給部3で薬剤を添加され、濾過部2に流入する。そして、濾過部2に流入した原水は、図3に示すように、上部ストレーナ2fを通過した後、濾材2aの上側から下側に通過し、この際に濁質成分が濾材2aの濾過作用により除去される。最後に、下部ストレーナ2eに流入した後、導出管2dの内側を通過して、濾過部2を出て、浄水吐出配管20より浄水が得られる。 During the filtration process, the water treatment device 1 opens the chemical supply valve 14 and the purified water take-out valve 23, and closes the backwash water supply valve 81 and the backwash valve 42, as shown in FIG. Then, when the electric pump 4 is operated, the raw water sent in the raw water inflow pipe 10 is added with a chemical in the chemical supply unit 3 and flows into the filtration unit 2. Then, as shown in FIG. 3, the raw water flowing into the filtration unit 2 passes through the upper strainer 2f and then from the upper side to the lower side of the filter medium 2a, and at this time, the turbid component is filtered by the filter medium 2a. Will be removed. Finally, after flowing into the lower strainer 2e, it passes through the inside of the outlet pipe 2d, exits the filtration unit 2, and purified water is obtained from the purified water discharge pipe 20.
 濾過部2内部では、まず上層の活性炭層で懸濁物質が捕捉されるとともに、金属イオンの凝集が促進される。中層のマンガン砂層では、主として上層で凝集された金属イオンの凝集物が捕捉されるのである。 Inside the filtration unit 2, the suspended substance is first captured by the activated carbon layer in the upper layer, and the aggregation of metal ions is promoted. In the middle manganese sand layer, aggregates of metal ions aggregated mainly in the upper layer are trapped.
 一方、逆洗処理時には、図5に示すように、水処理装置1は、薬剤供給バルブ14と浄水取出バルブ23を閉鎖し、逆洗送水バルブ81と逆洗バルブ42を開放する。そして、電動ポンプ4を運転すると、原水は、分岐部12から逆洗送水管80を経て浄水吐出配管20を逆流して濾過部2へ流入する。濾過部2では、図3に示すように、原水は導出管2d内を下方に向けて流れ、下部ストレーナ2eからタンク2b内へと浸入する。タンク2b内で原水は、下から上へと流れる。その際、上層の活性炭を撹拌及び展開することで、水処理装置1は、濾材2aで捕集された懸濁物質、凝集物を濾材2aから剥離させ、原水流入配管10の接続口から濾過部2外へと排出するのである。 On the other hand, during the backwash treatment, as shown in FIG. 5, the water treatment device 1 closes the chemical supply valve 14 and the purified water take-out valve 23, and opens the backwash water supply valve 81 and the backwash valve 42. Then, when the electric pump 4 is operated, the raw water flows back from the branch portion 12 through the backwash water pipe 80 to the purified water discharge pipe 20 and flows into the filtration portion 2. In the filtration unit 2, as shown in FIG. 3, the raw water flows downward in the outlet pipe 2d and infiltrates into the tank 2b from the lower strainer 2e. Raw water flows from bottom to top in tank 2b. At that time, by stirring and deploying the activated carbon in the upper layer, the water treatment device 1 separates the suspended substances and aggregates collected by the filter medium 2a from the filter medium 2a, and the filter unit is separated from the connection port of the raw water inflow pipe 10. 2 It is discharged to the outside.
 (薬剤供給部)
 次に、薬剤供給部3について、図2及び図7~図9Bを用いて説明する。図7は、水処理装置1の薬剤供給部3の斜視図であり、図8は、薬剤供給部3の断面図である。図9Aは、薬剤供給部3の要部の断面図であり、図9Bは、図9Aにおいて点線で示す箇所の拡大断面図である。
(Drug supply department)
Next, the drug supply unit 3 will be described with reference to FIGS. 2 and 7 to 9B. FIG. 7 is a perspective view of the drug supply unit 3 of the water treatment device 1, and FIG. 8 is a cross-sectional view of the drug supply unit 3. 9A is a cross-sectional view of a main part of the drug supply unit 3, and FIG. 9B is an enlarged cross-sectional view of a portion shown by a dotted line in FIG. 9A.
 図2に示すように、薬剤供給部3は、水処理装置1の最上部に配置されている。すなわち、薬剤供給部3は、原水流入配管10において、原水入口11から上方に向けて立ち上がった配管の上部に備えられている。つまり、薬剤供給部3内の薬剤載置場所(薬剤載置部53)は、設置状態において、濾過部2、原水流入配管10及び浄水吐出配管20よりも鉛直方向に高い位置に配置されている。 As shown in FIG. 2, the drug supply unit 3 is arranged at the uppermost part of the water treatment device 1. That is, the chemical supply unit 3 is provided in the raw water inflow pipe 10 at the upper part of the pipe that rises upward from the raw water inlet 11. That is, the drug loading location (drug loading section 53) in the drug supply section 3 is arranged at a position higher in the vertical direction than the filtration section 2, the raw water inflow pipe 10, and the purified water discharge pipe 20 in the installed state. ..
 また、図2に示すように、薬剤供給部3の出口(流出路34、図8参照)からの配管は、下方に伸びた後、分岐部13を経て濾過部2へと接続されている。 Further, as shown in FIG. 2, the pipe from the outlet (outflow path 34, see FIG. 8) of the drug supply unit 3 extends downward and is connected to the filtration unit 2 via the branch portion 13.
 図8に示すように、薬剤供給部3は、流入路31、薬剤路32、バイパス路33、流出路34を有している。流入路31は、原水流入配管10と接続され、原水を薬剤供給部3に流入させるものである。薬剤路32は、流入路31から分岐し、薬剤を溶かすものである。バイパス路33は、同じく流入路31から分岐し、薬液を必要な濃度に調整するために設けられている。流出路34は、薬剤路32、バイパス路33と合流し、再び原水流入配管10に接続し、原水流入配管10に薬剤の含まれた原水を送り出すものである。すなわち、薬剤供給部3は、有底筒状の筐体51を有し、筐体51の内部に流入路31、流出路34、薬剤路32及びバイパス路33の分岐部35を有している。 As shown in FIG. 8, the drug supply unit 3 has an inflow path 31, a drug path 32, a bypass path 33, and an outflow path 34. The inflow path 31 is connected to the raw water inflow pipe 10 and allows the raw water to flow into the chemical supply unit 3. The drug passage 32 branches from the inflow path 31 and dissolves the drug. The bypass path 33 is also branched from the inflow path 31 and is provided to adjust the chemical solution to a required concentration. The outflow passage 34 merges with the chemical passage 32 and the bypass passage 33, is connected to the raw water inflow pipe 10 again, and sends out the raw water containing the chemical to the raw water inflow pipe 10. That is, the drug supply unit 3 has a bottomed tubular housing 51, and has an inflow path 31, an outflow path 34, a drug path 32, and a branch portion 35 of the bypass path 33 inside the housing 51. ..
 以下、薬剤供給部3の各構成についてより詳細に説明する。 Hereinafter, each configuration of the drug supply unit 3 will be described in more detail.
 図8に示すように、薬剤路32は、筒状の筐体51の内部に形成されている。筐体51は、下部に設けた椀状の下部基台51aと、下部基台51aを覆う上部カバー51bとを有している。 As shown in FIG. 8, the drug passage 32 is formed inside the tubular housing 51. The housing 51 has a bowl-shaped lower base 51a provided at the lower part and an upper cover 51b that covers the lower base 51a.
 さらに詳しくは、筐体51は、上部にむけて径の小さくなる円錐台形状を有している。下部基台51aには、流入路31、バイパス路33、流出路34が接続され、下部基台51aの内部で分岐(分岐部35)している。流入路31から流入した原水は、分岐部35で、薬剤路32、流出路34及びバイパス路33に分岐される。すなわち、下部基台51aは、椀状で、内部に流入路31、流出路34及び薬剤路32の分岐部35を有する。 More specifically, the housing 51 has a truncated cone shape with a smaller diameter toward the top. An inflow path 31, a bypass path 33, and an outflow path 34 are connected to the lower base 51a, and a branch (branch portion 35) is formed inside the lower base 51a. The raw water flowing in from the inflow passage 31 is branched into the chemical passage 32, the outflow passage 34 and the bypass passage 33 at the branch portion 35. That is, the lower base 51a is bowl-shaped and has an inflow passage 31, an outflow passage 34, and a branch portion 35 of the medicine passage 32 inside.
 薬剤路32は、分岐後、鉛直方向に立ち上がる噴出管52と、噴出管52の上部で薬剤に接触し、薬剤を溶出させる薬剤載置部53と、噴出管52の外周であって、筐体51の内部となる回収部54とで構成される。すなわち、薬剤路32は、分岐部35から上方に向けて立設し、薬剤路32の上部には、薬剤載置部53が設けられている。薬剤路32で作られた薬液(薬剤を含んだ原水)は、回収部54と流出路34とを連通する回収開口55から流出路34へと送られる。すなわち、筐体51内において、流出路34には、薬剤路32を経由した流体を回収する開口(回収開口55)が設けられている。 The drug passage 32 is a housing, which is an ejection pipe 52 that rises in the vertical direction after branching, a drug placing portion 53 that comes into contact with the drug at the upper part of the ejection tube 52 and elutes the drug, and an outer circumference of the ejection pipe 52. It is composed of a collection unit 54 that is inside the 51. That is, the drug passage 32 is erected upward from the branch portion 35, and the drug placement section 53 is provided above the drug path 32. The chemical solution (raw water containing the drug) produced in the drug passage 32 is sent to the outflow channel 34 from the recovery opening 55 that communicates between the recovery unit 54 and the outflow channel 34. That is, in the housing 51, the outflow passage 34 is provided with an opening (recovery opening 55) for collecting the fluid that has passed through the drug passage 32.
 噴出管52の上部、すなわち、薬剤載置部53における噴出管52の外径は、噴出管52の下部より大きな径を有し、所望の量の薬剤を保有できるようになっている。すなわち、噴出管52の下部の外径は、薬剤載置部53の外径よりも小さい。また、水処理装置1は、噴出管52の下部の外径を小さくすることによって回収部54の水平断面積を確保している。 The upper part of the ejection pipe 52, that is, the outer diameter of the ejection pipe 52 in the drug placing portion 53 has a larger diameter than the lower part of the ejection pipe 52, so that a desired amount of drug can be held. That is, the outer diameter of the lower part of the ejection pipe 52 is smaller than the outer diameter of the drug placing portion 53. Further, the water treatment device 1 secures the horizontal cross-sectional area of the recovery unit 54 by reducing the outer diameter of the lower portion of the ejection pipe 52.
 バイパス路33は、分岐部35で分岐した後、原水のままの状態で流出路34の出口側(合流部36)で合流する(図7参照)。 After branching at the branching portion 35, the bypass road 33 merges at the outlet side (merging portion 36) of the outflow passage 34 in the state of raw water (see FIG. 7).
 分岐部35で分岐後、流出路34を流れる原水は、薬剤路32で作られた薬液と回収開口55で合流し、さらに流出路34の下流で、合流部36でバイパス路33と合流する。これにより、所望の濃度の薬液が薬剤供給部3から送出される。 After branching at the branching portion 35, the raw water flowing through the outflow passage 34 merges with the chemical solution made in the chemical passage 32 at the recovery opening 55, and further downstream of the outflow passage 34, merges with the bypass passage 33 at the merging portion 36. As a result, the drug solution having a desired concentration is delivered from the drug supply unit 3.
 すなわち、薬剤供給部3に流入した原水は、分岐部35において、薬剤路32、バイパス路33、流出路34に分岐される。この分岐によって、水処理装置1は、薬剤路32に流れる原水の流量を調整し、後述する薬剤と原水との接触量を調整している。従って、薬剤路32で薬剤と接触した原水は所望の濃度の薬液となる。次に、薬剤路32を経由した原水は、回収開口55で流出路34を流れる原水と合流する。分岐部35で所望の割合で分岐された流出路34の原水は、所望の濃度と流量で調整された薬剤路32の薬液と回収開口55で合流し、所望の濃度の薬液となるのである。なお、回収開口55で合流した薬剤路32の薬液及び流出路34の原水は、合流部36でバイパス路33を流れる原水とさらに合流することになっているが、合流部36後の薬剤の濃度を確認して、バイパス路33の流量を調整するとよい。 That is, the raw water that has flowed into the drug supply section 3 is branched into the drug path 32, the bypass path 33, and the outflow path 34 at the branch section 35. By this branching, the water treatment device 1 adjusts the flow rate of the raw water flowing through the chemical passage 32, and adjusts the contact amount between the chemical and the raw water, which will be described later. Therefore, the raw water that comes into contact with the drug in the drug path 32 becomes a drug solution having a desired concentration. Next, the raw water that has passed through the drug passage 32 merges with the raw water that flows through the outflow passage 34 at the recovery opening 55. The raw water of the outflow channel 34 branched at the branch portion 35 at a desired ratio merges with the drug solution of the drug path 32 adjusted to a desired concentration and flow rate at the recovery opening 55 to obtain a drug solution having a desired concentration. The chemical solution in the drug passage 32 and the raw water in the outflow channel 34 merged at the recovery opening 55 are supposed to further merge with the raw water flowing in the bypass path 33 at the confluence 36, but the concentration of the drug after the confluence 36 It is advisable to adjust the flow rate of the bypass path 33 after confirming.
 噴出管52は小径の管路で上部に薬剤載置部53を備えて立設されている。噴出管52は、筐体51の内部で薬剤載置部53を支えていることになる。これにより、薬剤載置部53は、筐体51の中央より高い位置に固定される。 The ejection pipe 52 is a small-diameter pipe line and is erected with a drug placing portion 53 at the top. The ejection pipe 52 supports the drug placing portion 53 inside the housing 51. As a result, the drug placing portion 53 is fixed at a position higher than the center of the housing 51.
 図9Aに示すように、薬剤載置部53は、上部が開口した皿状、あるいは、箱状となっている。薬剤載置部53の底部は、開口が設けられ、噴出管52と接続し、噴出管52と薬剤載置部53内部を連通している。薬剤載置部53の高さにおける噴出管52の水平方向の径は、噴出管52の下部の径よりも大きくなっている。水処理装置1は、まず、噴出管52の下部の径を小さくし、薬剤載置部53を噴出管52の上部に設けることによって、原水を所望の流量で薬剤と接触させることを実現している。薬剤載置部53は、原水の流量に対し、所望の濃度の薬液が得られるよう、置く薬剤の量(数)を確保するための大きさとなる。 As shown in FIG. 9A, the drug placing portion 53 has a dish shape or a box shape with an open upper part. The bottom of the drug loading portion 53 is provided with an opening, is connected to the ejection pipe 52, and communicates the ejection pipe 52 with the inside of the drug loading portion 53. The horizontal diameter of the ejection pipe 52 at the height of the drug placing portion 53 is larger than the diameter of the lower portion of the ejection pipe 52. The water treatment device 1 first realizes that the raw water is brought into contact with the chemical at a desired flow rate by reducing the diameter of the lower portion of the ejection pipe 52 and providing the chemical loading portion 53 on the upper portion of the ejection pipe 52. There is. The drug placing portion 53 has a size for securing the amount (number) of the drugs to be placed so that a drug solution having a desired concentration can be obtained with respect to the flow rate of the raw water.
 薬剤を溶かした薬液は、薬剤載置部53の側面に設けられた載置部出口58(図9B参照)から筐体51内部、すなわち、回収部54へ流出する。図8に示すように、回収部54において、薬剤を溶かした薬液は、筐体51の下部(下部基台51a)に貯まり、その後、回収開口55から流出路34へと流れだす。噴出管52の径を小さくし、筐体51の内壁面との距離を確保してあるので、筐体51内に流下した薬剤の溶けた原水は、液面を筐体51の高さに対し、1/2程度、あるいはそれ以下にすることができている。薬液が所望の深さで筐体51内に貯まることによって、流出路34において原水と混合する割合が調整されている。 The drug solution in which the drug is dissolved flows out from the loading section outlet 58 (see FIG. 9B) provided on the side surface of the drug loading section 53 to the inside of the housing 51, that is, to the collecting section 54. As shown in FIG. 8, in the recovery unit 54, the chemical solution in which the drug is dissolved is stored in the lower part of the housing 51 (lower base 51a), and then flows out from the recovery opening 55 to the outflow path 34. Since the diameter of the ejection pipe 52 is reduced and the distance from the inner wall surface of the housing 51 is secured, the raw water in which the chemicals that have flowed down into the housing 51 has the liquid level relative to the height of the housing 51. , 1/2 or less. By accumulating the chemical solution in the housing 51 at a desired depth, the ratio of mixing with the raw water in the outflow passage 34 is adjusted.
 また、水処理装置1の運転状態において、筐体51内に薬液が充満すると、薬剤載置部53に置いた薬剤の溶出量が大きくなり、所望の濃度の薬液が得られなくなる、あるいは、薬剤が溶けてなくなってしまうことがある。そのため、筐体51内での液面は低く抑えることが必要となる。 Further, when the housing 51 is filled with the chemical solution in the operating state of the water treatment device 1, the elution amount of the chemical solution placed in the chemical loading portion 53 becomes large, and the chemical solution having a desired concentration cannot be obtained, or the chemical solution is not obtained. May melt and disappear. Therefore, it is necessary to keep the liquid level in the housing 51 low.
 水処理装置1は、図9A及び図9Bに示すように、薬剤載置部53に、固形薬剤、すなわち水溶性固形薬剤60を備えている。すなわち、薬剤路32は、筐体51内に上方に向けて立設した噴出管52を有し、噴出管52の上方に、固形の薬剤を載せる薬剤載置部53を有する。水溶性固形薬剤60としては、タブレットや顆粒状のものを用いることがよい。なぜなら、水溶性固形薬剤60の表面積が大きくでき安定した溶剤濃度を保つことができるからである。水溶性固形薬剤60の大きさは、タブレットであれば、直径30ミリメートル、高さ10ミリメートル~20ミリメートルのもの、顆粒状であれば直径5ミリメートルから15ミリメートルのものを使用するとよい。水溶性固形薬剤60の大きさが小さい場合には、隣り合った薬剤が同時に水に接触して薬剤同士が固着してしまう。固着すると、薬剤の下部だけが水に接触して所望の濃度の薬液が得られなくなることがある。あるいは、水溶性固形薬剤60の大きさが小さい場合には、噴出管52から供給される水との接触面積が大きくなって所望の濃度の薬液が得られなくなる。そのため、水処理装置1は、所望の濃度の薬液を供給するため、上述の大きさの水溶性固形薬剤60を用いている。 As shown in FIGS. 9A and 9B, the water treatment device 1 includes a solid drug, that is, a water-soluble solid drug 60 in the drug placing portion 53. That is, the drug passage 32 has an ejection pipe 52 erected upward in the housing 51, and has a drug placing portion 53 on which a solid drug is placed above the ejection pipe 52. As the water-soluble solid drug 60, tablets or granules may be used. This is because the surface area of the water-soluble solid drug 60 can be increased and a stable solvent concentration can be maintained. The size of the water-soluble solid drug 60 may be 30 mm in diameter and 10 mm to 20 mm in height for tablets, and 5 to 15 mm in diameter for granules. When the size of the water-soluble solid drug 60 is small, the adjacent drugs come into contact with water at the same time and the drugs stick to each other. If stuck, only the lower part of the drug may come into contact with water and the desired concentration of the drug solution may not be obtained. Alternatively, when the size of the water-soluble solid drug 60 is small, the contact area with water supplied from the ejection pipe 52 becomes large, and a drug solution having a desired concentration cannot be obtained. Therefore, the water treatment device 1 uses the water-soluble solid drug 60 having the above-mentioned size in order to supply the drug solution having a desired concentration.
 本実施の形態では、薬剤載置部53は、錠剤の水溶性固形薬剤60を上下方向に保持できるよう、ガイド(図示せず)が設けられている。すなわち、ガイドは、縦方向に長いレール形状を有し、2本のレール間に水溶性固形薬剤60を投入することによって、水溶性固形薬剤60を上下方向に積んだように保持される。そのため、水溶性固形薬剤60は下方から原水に溶け出すことになり、所望の濃度の薬液が得られる。 In the present embodiment, the drug placing portion 53 is provided with a guide (not shown) so that the water-soluble solid drug 60 of the tablet can be held in the vertical direction. That is, the guide has a long rail shape in the vertical direction, and by inserting the water-soluble solid drug 60 between the two rails, the water-soluble solid drug 60 is held as if it were stacked in the vertical direction. Therefore, the water-soluble solid drug 60 dissolves in the raw water from below, and a drug solution having a desired concentration can be obtained.
 また、水溶性固形薬剤60は、上述のように、原水に含まれる金属イオンを酸化して水に難溶な凝集物を生成する働きをする。水溶性固形薬剤60としては、種々の酸化剤を用いることができるが、水処理装置1の運転中、すなわち、原水に対して薬剤を添加する場合には、水溶性固形薬剤60は水に溶けやすいものがよい。また、水処理装置1の停止中、あるいは逆洗処理中、すなわち、薬剤の添加を中断しているときには、固形形状を保持し、薬剤載置部53から流れ出さないものがよい。本実施の形態に係る水処理装置1は、トリクロロイソシアヌル酸を用いている。 Further, as described above, the water-soluble solid drug 60 has a function of oxidizing metal ions contained in raw water to form agglomerates that are poorly soluble in water. Various oxidizing agents can be used as the water-soluble solid drug 60, but the water-soluble solid drug 60 is soluble in water during the operation of the water treatment device 1, that is, when the drug is added to the raw water. Easy ones are good. Further, when the water treatment device 1 is stopped or backwashed, that is, when the addition of the drug is interrupted, it is preferable that the water treatment device 1 retains its solid shape and does not flow out from the drug placing portion 53. The water treatment apparatus 1 according to the present embodiment uses trichloroisocyanuric acid.
 薬剤供給部3の各部材は、薬剤と長時間接する可能性があるのでPVC(ポリ塩化ビニル)、PMMA(ポリメタクリル酸メチル)、PP(ポリプロピレン)など薬剤に対する反応性が低い素材を選ぶとよい。一方、噴出管52には薬剤載置部53を支えるための強度が必要なので、薬剤に対する相性を考慮すると、噴出管52の材質はPPより強度がある塩化ビニルやABS(アクリロニトリル・ブタジエン・スチレン)などを選択することが好ましい。噴出管52の外径は、下部基台51aの内径の4分の1以下に抑えるとよりよい。上述のように、噴出管52の外側に載置部出口58から排出された薬剤供給後の溶液を一時貯留する空間(回収部54)を設けることができ、筐体51内の水位が急激に上昇し薬剤載置部53まで到達することを抑制できるからである。例えば、下部基台51aの内径が130ミリメートルの場合、外径25ミリメートル~40ミリメートル程度の塩ビ管などを使用するとよい。すなわち、筐体51(下部基台51a)の内径に対し、噴出管52の外径は1/3以下にするとよい。このように、噴出管52の外径を小さくすることによって回収部54における水平断面積、すなわち、回収部54に貯まる薬液水面の面積を大きく確保することができる。従って、回収部54に貯まる薬液の液面高さを低く抑え、結果として薬剤の溶出量を適切に設定でき、所望の濃度の薬液が得られるのである。なお、本実施の形態では、上部カバー51bを円錐台形状とし、下部基台51aを有底の略円筒としていて、下部基台51aの内径が筐体51の最大内径となっている。 Since each member of the drug supply unit 3 may be in contact with the drug for a long time, it is preferable to select a material having low reactivity to the drug such as PVC (polyvinyl chloride), PMMA (polymethyl methacrylate), PP (polypropylene). .. On the other hand, since the ejection pipe 52 needs to have strength to support the drug placing portion 53, the material of the ejection tube 52 is vinyl chloride or ABS (acrylonitrile, butadiene, styrene), which is stronger than PP, considering compatibility with the drug. It is preferable to select such as. It is better to suppress the outer diameter of the ejection pipe 52 to 1/4 or less of the inner diameter of the lower base 51a. As described above, a space (recovery unit 54) for temporarily storing the solution after the drug is supplied discharged from the mounting unit outlet 58 can be provided on the outside of the ejection pipe 52, and the water level in the housing 51 suddenly rises. This is because it can be prevented from rising and reaching the drug placing portion 53. For example, when the inner diameter of the lower base 51a is 130 mm, a vinyl chloride pipe having an outer diameter of about 25 mm to 40 mm may be used. That is, the outer diameter of the ejection pipe 52 may be 1/3 or less of the inner diameter of the housing 51 (lower base 51a). In this way, by reducing the outer diameter of the ejection pipe 52, it is possible to secure a large horizontal cross-sectional area in the recovery section 54, that is, a large area of the chemical solution water surface stored in the recovery section 54. Therefore, the height of the chemical solution stored in the recovery unit 54 can be kept low, and as a result, the elution amount of the chemical solution can be appropriately set, and the chemical solution having a desired concentration can be obtained. In the present embodiment, the upper cover 51b has a truncated cone shape, the lower base 51a has a substantially cylindrical bottom, and the inner diameter of the lower base 51a is the maximum inner diameter of the housing 51.
 また、図9A及び図9Bに示すように、噴出管52は、噴出管52の内部を上下に仕切る仕切り板56を有している。仕切り板56上に薬剤載置部53が設けられ、薬剤載置部53上に水溶性固形薬剤60が置かれることになる。仕切り板56には、噴出管52から送られる原水が流入する載置部入口57が設けられている。載置部入口57は、仕切り板56の中央部近傍に設けられているが、中心でなくてもよい。また、仕切り板56は、すり鉢状に外周部を高く、載置部入口57近傍を低くしてある。すなわち、仕切り板56には、外縁側から載置部入口57側に下る傾斜が設けられている。載置部入口57は、仕切り板56の中央部を網状にして形成してもよい。あるいは、載置部入口57は、仕切り板56の中央部を囲むように形成された少なくとも1つのドーナツ状のスリット、あるいは、複数の小孔群であってもよい。また、噴出管52の側面には、溶けた薬剤を含んだ原水が流出する載置部出口58を有している。載置部出口58は、仕切り板56の外周部の頂部よりも高い位置に設けられている。そして、水溶性固形薬剤60は、仕切り板56上であって、径方向には、載置部入口57と載置部出口58の間に配置されることになる。 Further, as shown in FIGS. 9A and 9B, the ejection pipe 52 has a partition plate 56 that vertically partitions the inside of the ejection pipe 52. The drug placing portion 53 is provided on the partition plate 56, and the water-soluble solid drug 60 is placed on the drug placing portion 53. The partition plate 56 is provided with a mounting portion inlet 57 into which raw water sent from the ejection pipe 52 flows. The mounting portion entrance 57 is provided near the central portion of the partition plate 56, but does not have to be the center. Further, the partition plate 56 has a mortar-shaped outer peripheral portion raised and the vicinity of the mounting portion entrance 57 lowered. That is, the partition plate 56 is provided with an inclination that descends from the outer edge side to the mounting portion entrance 57 side. The mounting portion entrance 57 may be formed by forming a net-like central portion of the partition plate 56. Alternatively, the mounting portion entrance 57 may be at least one donut-shaped slit formed so as to surround the central portion of the partition plate 56, or a plurality of small hole groups. Further, on the side surface of the ejection pipe 52, there is a mounting portion outlet 58 from which raw water containing a dissolved drug flows out. The mounting portion outlet 58 is provided at a position higher than the top of the outer peripheral portion of the partition plate 56. The water-soluble solid drug 60 is arranged on the partition plate 56 in the radial direction between the mounting portion inlet 57 and the mounting portion outlet 58.
 すなわち、噴出管52は、内部を上下に仕切る仕切り板56と、仕切り板56に開口した載置部入口57とを有する。また、載置部入口57は、載置部出口58よりも噴出管52の中心軸寄りに設けられ、載置部出口58は、仕切り板56よりも上方であって、噴出管52の側壁側に設けられている。また、薬剤載置部53は、仕切り板56上に薬剤が載置されるものであり、薬剤載置部53の一部が載置部入口57と載置部出口58との間に配置されている。つまり、載置部出口58は、薬剤載置部53の最下点よりも上方に設けられている。 That is, the ejection pipe 52 has a partition plate 56 that partitions the inside vertically, and a mounting portion inlet 57 opened in the partition plate 56. Further, the mounting portion inlet 57 is provided closer to the central axis of the ejection pipe 52 than the mounting portion outlet 58, and the mounting portion outlet 58 is above the partition plate 56 and is on the side wall side of the ejection pipe 52. It is provided in. Further, the drug loading section 53 is for loading the drug on the partition plate 56, and a part of the drug loading section 53 is arranged between the loading section inlet 57 and the loading section outlet 58. ing. That is, the loading portion outlet 58 is provided above the lowest point of the drug loading portion 53.
 このような構成によれば、すり鉢状になった仕切り板56上には、中央寄りに水溶性固形薬剤60が配置される。そして、噴出管52から送られる原水は、載置部入口57から浸入し、中央寄りに置かれた水溶性固形薬剤60と接触し、水溶性固形薬剤60を溶かして薬液となる。薬剤の溶け込んだ原水は、上方に上昇し、載置部出口58から薬剤供給部3の筐体51内へと流出する。このとき、水溶性固形薬剤60は、径方向にも上下方向にも載置部入口57と載置部出口58の間に配置されているので、原水に必ず接触し、薬液となって載置部出口58から流出する。また、所定の流量に対し、水溶性固形薬剤60の接触度合を確保し、所望の濃度範囲の薬液とすることができる。 According to such a configuration, the water-soluble solid drug 60 is arranged closer to the center on the mortar-shaped partition plate 56. Then, the raw water sent from the ejection pipe 52 infiltrates from the loading portion inlet 57, comes into contact with the water-soluble solid drug 60 placed near the center, and dissolves the water-soluble solid drug 60 to become a chemical solution. The raw water in which the drug is dissolved rises upward and flows out from the outlet 58 of the mounting section into the housing 51 of the drug supply section 3. At this time, since the water-soluble solid drug 60 is arranged between the mounting portion inlet 57 and the mounting portion outlet 58 in both the radial direction and the vertical direction, it always comes into contact with the raw water and is placed as a chemical solution. It flows out from the part outlet 58. In addition, the degree of contact of the water-soluble solid drug 60 can be ensured with respect to a predetermined flow rate, and the drug solution can be obtained in a desired concentration range.
 また、上記構成によれば、載置部出口58よりも上部の水溶性固形薬剤60に水分を含ませることを防止できるので、水溶性固形薬剤60同士の固着、壁面への固着を防ぐことが可能である。水溶性固形薬剤60同士の固着を防ぐことができるので、下層の水溶性固形薬剤60が溶出して無くなった場合には、上部の固形薬剤が重力によって降下し、下部に水溶性固形薬剤60を供給させることができる。つまり、水溶性固形薬剤60と原水を継続的に接触させることが可能である。そして、薬剤供給装置を長期に使用した場合にも薬剤濃度を安定させることが可能となる。 Further, according to the above configuration, it is possible to prevent the water-soluble solid chemicals 60 above the loading portion outlet 58 from containing water, so that the water-soluble solid chemicals 60 can be prevented from sticking to each other and sticking to the wall surface. It is possible. Since it is possible to prevent the water-soluble solid agents 60 from sticking to each other, when the water-soluble solid agents 60 in the lower layer are eluted and disappear, the upper solid agents are lowered by gravity, and the water-soluble solid agents 60 are placed in the lower part. Can be supplied. That is, the water-soluble solid drug 60 and raw water can be continuously brought into contact with each other. Then, the drug concentration can be stabilized even when the drug supply device is used for a long period of time.
 また、噴出管52、薬剤載置部53の外壁面は、載置部出口58よりも下方において、外壁面の任意の位置から鉛直下方に降ろした直線と外壁面との成す角(図9Aにおける角度α)は0~45度であることが望ましい。外壁面を急角度で絞らないことによって、載置部出口58から流出する原水は、噴出管52、薬剤載置部53の外壁面を伝って流下し、筐体51内で貯まった原水(薬液)と静かに混合する。そのため、液面で水泡ができにくくなる。 Further, the outer wall surface of the ejection pipe 52 and the drug placing portion 53 is an angle formed by a straight line lowered vertically downward from an arbitrary position on the outer wall surface and the outer wall surface below the loading portion outlet 58 (in FIG. 9A). The angle α) is preferably 0 to 45 degrees. By not squeezing the outer wall surface at a steep angle, the raw water flowing out from the loading portion outlet 58 flows down along the outer wall surface of the ejection pipe 52 and the drug loading portion 53, and the raw water (chemical solution) stored in the housing 51. ) And gently mix. Therefore, it becomes difficult for blisters to form on the liquid surface.
 一方、薬剤を含んだ原水が、噴出管52、薬剤載置部53の外壁面から離れて空中に流れ出る場合には、筐体51内で貯まった原水(薬液)と混合する際に水泡を作ることになる。水泡は、筐体51内に充満して、見かけ上の水位を上昇させることになる。あるいは、できた水泡が薬液とともに流出路34から排出されるため、筐体51内の空気が減少し、結果として回収部54における水位が上昇する。すなわち、上昇した水位によって水溶性固形薬剤60に水が浸かることになり、結果として薬剤を過度に溶かし、所望の濃度の薬液が得られなくなってしまう。これに対し、本実施の形態では、載置部出口58から流出する原水は、噴出管52、薬剤載置部53の外壁面を伝って流下させ、筐体51内で水泡を作らないようにすることで、所望の濃度の薬液が得らなくなることを抑制している。 On the other hand, when the raw water containing the drug flows out into the air away from the outer wall surface of the ejection pipe 52 and the drug placing portion 53, blisters are formed when the raw water (chemical solution) stored in the housing 51 is mixed. It will be. The blisters fill the inside of the housing 51 and raise the apparent water level. Alternatively, since the formed blisters are discharged from the outflow passage 34 together with the chemical solution, the air in the housing 51 is reduced, and as a result, the water level in the recovery unit 54 rises. That is, the increased water level causes water to be immersed in the water-soluble solid drug 60, and as a result, the drug is excessively dissolved, and a drug solution having a desired concentration cannot be obtained. On the other hand, in the present embodiment, the raw water flowing out from the loading portion outlet 58 is allowed to flow down along the outer wall surface of the ejection pipe 52 and the drug loading portion 53 so as not to form blisters in the housing 51. By doing so, it is possible to prevent the drug solution having a desired concentration from being obtained.
 また、薬剤路32(噴出管52)、バイパス路33、流出路34には、分岐部35の直後(下流側)に絞り部が設けられている。この絞り部は、薬剤路32、バイパス路33、流出路34に流れる原水の配分を調整し、薬剤供給部3から流出する原水の薬剤の濃度を所望の濃度にするために設けられている。なお、バイパス路33には、開閉バルブ33aが設けられており(図7参照)、バイパス路33を閉じることも可能となっている。流出路34に設けた絞り部の開口面積は、薬剤路32(噴出管52)、バイパス路33に設けた他の絞り部の開口面積よりも大きくしてある。これにより、薬剤供給部3から流出する薬液の濃度を所望の範囲に調整することができる。 Further, in the drug passage 32 (spout pipe 52), the bypass passage 33, and the outflow passage 34, a throttle portion is provided immediately after (downstream side) the branch portion 35. This throttle portion is provided in order to adjust the distribution of the raw water flowing through the drug passage 32, the bypass path 33, and the outflow path 34, and to make the concentration of the drug in the raw water flowing out from the drug supply section 3 a desired concentration. The bypass path 33 is provided with an on-off valve 33a (see FIG. 7), and the bypass path 33 can be closed. The opening area of the throttle portion provided in the outflow passage 34 is larger than the opening area of the other throttle portions provided in the drug passage 32 (spout pipe 52) and the bypass passage 33. Thereby, the concentration of the drug solution flowing out from the drug supply unit 3 can be adjusted to a desired range.
 また、薬剤供給部3の筐体51は、下部基台51aから上部カバー51bを外せるようになっている。すなわち、筐体51は、上部カバー51bと下部基台51aとに上下に分割可能な筒状である。薬剤供給部3には、汚れた原水が流入するので定期的なメンテナンスが必要となっている。そのため、上部カバー51bを外し、内部の清掃が可能なようになっている。さらに、噴出管52は、分岐部35で取り外すことが可能になっている。上述のように、薬剤路32(噴出管52)、バイパス路33、流出路34は、分岐部35の下流側にそれぞれ絞りが設けられており、長期間の使用によっては、絞り部に異物が付着することが考えられる。そのため、水処理装置1は、噴出管52を分岐部35部分で取り外し、配管内の清掃を可能にしている。 Further, the housing 51 of the drug supply unit 3 is designed so that the upper cover 51b can be removed from the lower base 51a. That is, the housing 51 has a tubular shape that can be vertically divided into an upper cover 51b and a lower base 51a. Since dirty raw water flows into the drug supply unit 3, regular maintenance is required. Therefore, the upper cover 51b is removed so that the inside can be cleaned. Further, the ejection pipe 52 can be removed at the branch portion 35. As described above, the drug passage 32 (spout pipe 52), the bypass passage 33, and the outflow passage 34 are each provided with a throttle on the downstream side of the branch portion 35, and foreign matter may be present in the throttle portion depending on long-term use. It is possible that it will adhere. Therefore, in the water treatment device 1, the ejection pipe 52 is removed at the branch portion 35 portion, and the inside of the pipe can be cleaned.
 上部カバー51bは、一部あるいは全部を透明にするとよい。上部カバー51bを透明にすることによって、内部に水溶性固形薬剤60の存在を確認でき、必要な場合には補給することができる。特に、筐体51内で薬液の液面よりも上方となる上部カバー51bの上部は透明にするとよい。また、上部カバー51bの天面は水溶性固形薬剤60の補給口とし、この補給口を透明にするとよい。また、上述のとおり、水溶性固形薬剤60はガイドに支持されて並んで配置されるので、外部から投入量の確認が容易となる。 Part or all of the upper cover 51b should be transparent. By making the upper cover 51b transparent, the presence of the water-soluble solid drug 60 can be confirmed inside, and it can be replenished if necessary. In particular, it is preferable that the upper portion of the upper cover 51b, which is above the liquid level of the chemical solution in the housing 51, is transparent. Further, the top surface of the upper cover 51b may be a supply port for the water-soluble solid drug 60, and this supply port may be transparent. Further, as described above, since the water-soluble solid drug 60 is supported by the guide and arranged side by side, it is easy to confirm the input amount from the outside.
 薬剤供給部3の筐体51内は、汚れを含んだ原水が流入するので内部が汚れることになる。しかし、上述のとおり、運転中には、筐体51の内部の水面は筐体51の1/2以下の高さとなるように設計されている。また、載置部出口58は、薬剤載置部53の側面に設けられている。すなわち、水処理装置1は、薬剤載置部53において、側面に薬剤の溶けだした薬液を排出する載置部出口58を有する。そのため、筐体51の天面付近には原水は到達しないので、水溶性固形薬剤60の補給口付近は汚れにくい構造となっている。すなわち、水処理装置1は、補給口を透明とすることによって、薬剤載置部53の水溶性固形薬剤60を視認しやすくしている。 Since raw water containing dirt flows into the housing 51 of the drug supply unit 3, the inside becomes dirty. However, as described above, the water surface inside the housing 51 is designed to be at least half the height of the housing 51 during operation. Further, the loading portion outlet 58 is provided on the side surface of the drug loading portion 53. That is, the water treatment device 1 has a loading section outlet 58 on the side surface of the drug loading section 53 for discharging the drug solution in which the drug has been dissolved. Therefore, since the raw water does not reach the vicinity of the top surface of the housing 51, the vicinity of the supply port of the water-soluble solid chemical 60 is hard to get dirty. That is, the water treatment device 1 makes the supply port transparent so that the water-soluble solid drug 60 of the drug placing portion 53 can be easily visually recognized.
 (空気補給弁)
 ここで、逆洗処理時における特別な構成と、作用について、図2、図4、図5及び図10を用いて説明する。図10は、水処理装置1に用いられる空気補給弁43の断面図である。
(Air supply valve)
Here, the special configuration and the action during the backwashing treatment will be described with reference to FIGS. 2, 4, 5, and 10. FIG. 10 is a cross-sectional view of the air supply valve 43 used in the water treatment device 1.
 上述のとおり、逆洗ドレン管40は、分岐部13から逆洗ドレン口41を配管したものである(図5参照)。ずなわち、逆洗ドレン管40は、第一分岐部としての分岐部13から下方に延伸している。この逆洗ドレン管40の経路途中であって、逆洗バルブ42の下流側には、空気補給弁43が設けられている(図2参照)。空気補給弁43は、一方を逆洗ドレン管40に接続し、他方を大気側に開放したものである(図10参照)。空気補給弁43は、逆止弁構造となっており、大気側からの流入を可能とし、逆洗ドレン管40側からの流出はできなくしている。すなわち、水処理装置1には、逆洗ドレン管40の経路内に、一端を大気中に開放し、大気側から配管内への流入を行う空気補給弁43が設けられている。また、空気補給弁43は、大気側からの流入のみが可能な逆止弁である。 As described above, the backwash drain pipe 40 is formed by piping the backwash drain port 41 from the branch portion 13 (see FIG. 5). That is, the backwash drain pipe 40 extends downward from the branch portion 13 as the first branch portion. An air supply valve 43 is provided on the downstream side of the backwash valve 42 in the middle of the path of the backwash drain pipe 40 (see FIG. 2). One of the air supply valves 43 is connected to the backwash drain pipe 40, and the other is open to the atmosphere side (see FIG. 10). The air supply valve 43 has a check valve structure, which enables inflow from the atmosphere side and prevents outflow from the backwash drain pipe 40 side. That is, the water treatment device 1 is provided with an air supply valve 43 in the path of the backwash drain pipe 40, which opens one end to the atmosphere and allows the water to flow into the pipe from the atmosphere side. Further, the air supply valve 43 is a check valve that can only flow in from the atmosphere side.
 また、図2及び図10に示すように、空気補給弁43は、逆洗ドレン管40から上方に立ち上がったところに弁構造部分が設けられている。すなわち、空気補給弁43は、逆洗ドレン管40における空気補給弁43への分岐点44よりも高い位置に設けられている。 Further, as shown in FIGS. 2 and 10, the air supply valve 43 is provided with a valve structure portion at a position where it rises upward from the backwash drain pipe 40. That is, the air supply valve 43 is provided at a position higher than the branch point 44 to the air supply valve 43 in the backwash drain pipe 40.
 このような構造において、空気補給弁43の作用を説明する。 The operation of the air supply valve 43 in such a structure will be described.
 図4に示すように、濾過処理時には、逆洗バルブ42が閉鎖され、逆洗バルブ42よりも下流側の逆洗ドレン管40内には空気が充満している。そして、逆洗処理に切り替えた際には、図5に示すように、逆洗バルブ42が開放されるため、逆洗ドレン管40内の空気は、上方へと移動し、薬剤供給部3内に空気を供給することになる。薬剤供給部3内に空気が充満することにより、水溶性固形薬剤60は、原水に浸かった状態ではなく、空気にさらされる。従って、水溶性固形薬剤60が無駄に溶け出すこともなく、また、溶けて固着することを防止することができる。 As shown in FIG. 4, during the filtration process, the backwash valve 42 is closed, and the backwash drain pipe 40 on the downstream side of the backwash valve 42 is filled with air. Then, when the backwash treatment is switched, as shown in FIG. 5, the backwash valve 42 is opened, so that the air in the backwash drain pipe 40 moves upward and enters the drug supply unit 3. Will supply air to. When the drug supply unit 3 is filled with air, the water-soluble solid drug 60 is exposed to air instead of being immersed in raw water. Therefore, it is possible to prevent the water-soluble solid drug 60 from being unnecessarily dissolved and to be prevented from being dissolved and fixed.
 一方、逆洗ドレン管40内は、逆洗処理を行うため、ドレン水が流れ、ドレン水で満たされる。逆洗処理が終わると、再び、逆洗バルブ42は閉鎖され、逆洗ドレン管40内に向けて空気補給弁43から空気が送られることになる。従って、逆洗処理以外の時には、逆洗ドレン管40内に空気が充満し、次の逆洗処理の時に薬剤供給部3へ空気を送ることができる。 On the other hand, since the backwashing drain pipe 40 is backwashed, drain water flows and is filled with the drain water. When the backwash treatment is completed, the backwash valve 42 is closed again, and air is sent from the air supply valve 43 into the backwash drain pipe 40. Therefore, at times other than the backwash treatment, the backwash drain pipe 40 is filled with air, and air can be sent to the chemical supply unit 3 at the time of the next backwash treatment.
 なお、水処理装置1は、空気補給弁43を逆洗ドレン管40に対し、逆洗ドレン管40の分岐点44から上方に立ち上げて設けたことにより、空気補給弁43内を空気で満たした状態にして、水の浸入を抑える構造としている。すなわち、この水処理装置1の構造は、汚れた水から空気補給弁43を守り、空気補給を確実に行うことができるようにしている。 The water treatment device 1 fills the inside of the air supply valve 43 with air by providing the air supply valve 43 upward from the branch point 44 of the backwash drain pipe 40 with respect to the backwash drain pipe 40. It has a structure that suppresses the ingress of water. That is, the structure of the water treatment device 1 protects the air replenishment valve 43 from dirty water so that air replenishment can be reliably performed.
 なお、図2に示すように、逆洗ドレン管40における空気補給弁43への分岐点44から薬剤供給部3までの配管経路における水平高さは、分岐点44で最も低く、薬剤供給部3の流入路31の流出口に向けて高くなっている。 As shown in FIG. 2, the horizontal height of the backwash drain pipe 40 in the piping path from the branch point 44 to the air supply valve 43 to the drug supply section 3 is the lowest at the branch point 44, and the drug supply section 3 It rises toward the outlet of the inflow path 31 of.
 また、本実施の形態に係る水処理装置1は、空気補給弁43を逆止弁としたが、空気を逆洗ドレン管40内に送ることができれば他の種類の弁でもよい。他の種類の弁は、例えば、手動弁を用いてもよい。空気を逆洗ドレン管40内に送る方法は、逆洗処理が終了した時点で逆洗ドレン管40内に空気を送る方法や、逆洗ドレン管40の経路内に水抜き穴と栓を設け、逆洗処理が終了した時点で栓を抜き、逆洗ドレン管40内の水を抜き、空気を満たす方法でもよい。 Further, in the water treatment device 1 according to the present embodiment, the air supply valve 43 is used as a check valve, but other types of valves may be used as long as air can be sent into the backwash drain pipe 40. For other types of valves, for example, a manual valve may be used. The method of sending air into the backwash drain pipe 40 is a method of sending air into the backwash drain pipe 40 when the backwash treatment is completed, or a drain hole and a stopper are provided in the path of the backwash drain pipe 40. When the backwash treatment is completed, the stopper may be removed, the water in the backwash drain pipe 40 may be drained, and air may be filled.
 (濾過部配置)
 濾過部2の配置について、図11及び図12を用いて説明する。図11は、水処理装置1の濾過部2の周辺構造を示す側面図であり、図12は、水処理装置1の外装斜視図である。
(Arrangement of filtration part)
The arrangement of the filtration unit 2 will be described with reference to FIGS. 11 and 12. FIG. 11 is a side view showing the peripheral structure of the filtration unit 2 of the water treatment device 1, and FIG. 12 is an exterior perspective view of the water treatment device 1.
 濾過部2に充填された濾材2aは、逆洗したとしても長期間の使用により性能が劣化する。そのため、濾過部2は定期的なメンテナンスが必要になる。濾過部2をメンテナンスするため、本実施の形態の水処理装置1は、濾過部2を取り外すことが可能になっている。 The performance of the filter medium 2a filled in the filter unit 2 deteriorates due to long-term use even if it is backwashed. Therefore, the filtration unit 2 requires regular maintenance. In order to maintain the filtration unit 2, the water treatment device 1 of the present embodiment can remove the filtration unit 2.
 図11に示すように、濾過部2を所定の方向から見た時、配管類(原水流入配管10、浄水吐出配管20、逆洗送水管80、逆洗ドレン管40など)、薬剤供給部3は、濾過部2と分離されて配置されている。すなわち、濾過部2と原水流入配管10、浄水吐出配管20との接続部に設けた接続接手15を開放したとき、濾過部2は一方向及びその反対方向にスライドして移動が可能となる。図11では、濾過部2は紙面に対し垂直方向に移動が可能となる。そのために、接続接手15の相手側の接続面は、濾過部2の移動する一方向に平行に設けている。接続接手15としては、原水流入配管10側に設けられた流入側接手、浄水吐出配管20側に設けられた流出側接手を有しており、この2つの接手を有する接続接手15の接続によって濾過部2は本体内の配管と接続される。 As shown in FIG. 11, when the filtration unit 2 is viewed from a predetermined direction, pipes (raw water inflow pipe 10, purified water discharge pipe 20, backwash water pipe 80, backwash drain pipe 40, etc.), chemical supply part 3 Is arranged separately from the filtration unit 2. That is, when the connection joint 15 provided at the connection portion between the filtration unit 2, the raw water inflow pipe 10 and the purified water discharge pipe 20 is opened, the filtration unit 2 can slide and move in one direction and the opposite direction. In FIG. 11, the filtration unit 2 can move in the direction perpendicular to the paper surface. Therefore, the connection surface on the other side of the connection joint 15 is provided parallel to the moving direction of the filtration unit 2. The connection joint 15 has an inflow side joint provided on the raw water inflow pipe 10 side and an outflow side joint provided on the purified water discharge pipe 20 side, and is filtered by the connection of the connection joint 15 having these two joints. The part 2 is connected to the piping in the main body.
 また、図12にしめすように、本実施の形態の水処理装置1は、配管類を保護するため、外郭をパネルで覆って筐体を構成している。上述のとおり、濾過部2は一方向とその反対方向に移動が可能なので、外郭パネルのうち、濾過部2に対して一方向とその対向面のパネルを点検パネル61としている。濾過部2のメンテナンスは、点検パネル61のうち両方もしくはどちらか一方を外すことによって行うことができる。 Further, as shown in FIG. 12, in the water treatment device 1 of the present embodiment, in order to protect the pipes, the outer shell is covered with a panel to form a housing. As described above, since the filtration unit 2 can move in one direction and the opposite direction, the inspection panel 61 is a panel in one direction and the opposite surface to the filtration unit 2 among the outer panels. Maintenance of the filtration unit 2 can be performed by removing both or one of the inspection panels 61.
 このように、濾過部2は、1つの点検パネル61、あるいは、対向して2か所に設けた点検パネル61側に向けて平行移動が可能になり、少ない点検スペースで濾過部2のメンテナンスが可能となる。 In this way, the filtration unit 2 can be translated toward one inspection panel 61 or the inspection panels 61 provided at two locations facing each other, and maintenance of the filtration unit 2 can be performed with a small inspection space. It will be possible.
 なお、本実施の形態に係る水処理装置1は、濾過部2を一方向とその反対方向に移動可能としたが、一方向のみとしてもよい。その場合には、接続接手15の相手側(濾過部2とは反対側)の接続面は、一方向側に向けてもよい。すなわち、接続接手15と対向する配管側の接続面が、濾過部2の移動する一方向に向いている、あるいは、接続接手15の接続面が、濾過部2の移動する一方向に平行に配置されていればよい。このような配置によれば、濾過部2は、少なくとも一方向に向けて移動が可能となる。 Although the water treatment device 1 according to the present embodiment allows the filtration unit 2 to move in one direction and the opposite direction, it may be in only one direction. In that case, the connection surface on the other side (opposite side of the filtration unit 2) of the connection joint 15 may be directed to one direction. That is, the connection surface on the piping side facing the connection joint 15 faces in one direction in which the filtration unit 2 moves, or the connection surface of the connection joint 15 is arranged parallel to the direction in which the filtration unit 2 moves. It suffices if it is done. According to such an arrangement, the filtration unit 2 can move in at least one direction.
 本開示に係る水処理装置は、逆洗に十分量の清浄な逆洗水を供給可能で、従来品と比較し省スペース設置可能な水処理装置であるため、井戸水や貯留水の浄化に使用される家庭用小型水処理装置等としても有用である。 The water treatment device according to the present disclosure is a water treatment device that can supply a sufficient amount of clean backwash water for backwashing and can be installed in a space-saving manner as compared with conventional products, and is therefore used for purifying well water and stored water. It is also useful as a small household water treatment device.
 1  水処理装置
 2  濾過部
 2a  濾材
 2b  タンク
 2c  分配栓
 2d  導出管
 2e  下部ストレーナ
 2f  上部ストレーナ
 3  薬剤供給部
 4  電動ポンプ
 10  原水流入配管
 11  原水入口
 12  分岐部
 13  分岐部
 14  薬剤供給バルブ
 15  接続接手
 20  浄水吐出配管
 21  浄水出口
 22  分岐部
 23  浄水取出バルブ
 24  絞り部
 26  分岐部
 27  リンスドレン管
 28  リンスドレンバルブ
 29  リンスドレン口
 31  流入路
 32  薬剤路
 33  バイパス路
 33a  開閉バルブ
 34  流出路
 35  分岐部
 36  合流部
 40  逆洗ドレン管
 41  逆洗ドレン口
 42  逆洗バルブ
 43  空気補給弁
 44  分岐点
 51  筐体
 51a  下部基台
 51b  上部カバー
 52  噴出管
 53  薬剤載置部
 54  回収部
 55  回収開口
 56  仕切り板
 57  載置部入口
 58  載置部出口
 60  水溶性固形薬剤
 61  点検パネル
 62  逆止弁
 70  直接排水管
 71  直接排水バルブ
 80  逆洗送水管
 81  逆洗送水バルブ
 101  固形薬剤供給装置
 102  取水口
 103  水溶性固形薬剤
 104  薬剤接触相
 α  角度
1 Water treatment device 2 Filter 2a Filter material 2b Tank 2c Distributor 2d Outlet pipe 2e Lower strainer 2f Upper strainer 3 Chemical supply unit 4 Electric pump 10 Raw water inflow pipe 11 Raw water inlet 12 Branch part 13 Branch part 14 Chemical supply valve 15 Connection 20 Purified water discharge pipe 21 Purified water outlet 22 Branch part 23 Purified water take-out valve 24 Squeezing part 26 Branch part 27 Rinse drain pipe 28 Rinse drain valve 29 Rinse drain port 31 Inflow path 32 Chemical path 33 Bypass path 33a Open / close valve 34 Outflow path 35 Branch 36 Confluence 40 Backwash drain pipe 41 Backwash drain port 42 Backwash valve 43 Air supply valve 44 Branch point 51 Housing 51a Lower base 51b Upper cover 52 Ejection pipe 53 Drug loading part 54 Recovery part 55 Recovery opening 56 Partition Plate 57 Mounting part inlet 58 Mounting part outlet 60 Water-soluble solid chemicals 61 Inspection panel 62 Check valve 70 Direct drain pipe 71 Direct drain valve 80 Backwash water supply pipe 81 Backwash water supply valve 101 Solid chemicals supply device 102 Water intake 103 Water-soluble solid drug 104 Drug contact phase α angle

Claims (17)

  1.  濾材を内包した濾過部と、
     前記濾過部に原水を流入させるための原水流入配管と、
     前記原水流入配管の経路内で薬剤を添加する薬剤供給部と、
     前記濾過部から濾過後の浄水を取り出すための浄水吐出配管とを有し、
     前記薬剤供給部内の薬剤載置場所は、設置状態において、前記濾過部、前記原水流入配管及び前記浄水吐出配管よりも鉛直方向に高い位置に配置された
     ことを特徴とする水処理装置。
    A filter unit containing a filter medium and
    A raw water inflow pipe for allowing raw water to flow into the filtration section,
    A drug supply unit that adds a drug in the path of the raw water inflow pipe,
    It has a purified water discharge pipe for taking out purified water after filtration from the filtration unit.
    A water treatment apparatus characterized in that the drug placement location in the drug supply section is arranged at a position higher in the vertical direction than the filtration section, the raw water inflow pipe, and the purified water discharge pipe in the installed state.
  2.  前記水処理装置は、さらに
     前記原水流入配管の経路内であって、設置状態において、前記薬剤供給部と前記濾過部との間の第一分岐部から下方に分岐した逆洗ドレン管と、
     前記原水流入配管の経路内であって、前記原水が蓄えられている水源と前記薬剤供給部との間の第二分岐部で分岐した逆洗送水管とを有し、
     前記逆洗送水管は、前記浄水吐出配管の経路内の第三分岐部で前記浄水吐出配管に合流し、
     濾過処理時には、
     前記第一分岐部は、前記薬剤供給部と前記濾過部とを連通させ、
     前記第二分岐部は、前記水源と前記薬剤供給部とを連通させ、
     前記第三分岐部は、前記濾過部と前記浄水吐出配管の末端側とを連通させ、
     逆洗処理時には、
     前記第一分岐部は、前記逆洗ドレン管と前記濾過部とを連通させ、
     前記第二分岐部は、前記水源と前記逆洗送水管とを連通させ、
     前記第三分岐部は、前記逆洗送水管と前記濾過部とを連通させる
     ことを特徴とする請求項1に記載の水処理装置。
    The water treatment device further includes a backwash drain pipe that is in the path of the raw water inflow pipe and that branches downward from the first branch portion between the chemical supply unit and the filtration unit in the installed state.
    It has a backwash water pipe that is in the path of the raw water inflow pipe and is branched at a second branch between the water source in which the raw water is stored and the chemical supply part.
    The backwash water pipe joins the purified water discharge pipe at a third branch in the path of the purified water discharge pipe.
    At the time of filtration processing
    The first branching portion communicates the drug supply portion with the filtration portion.
    The second branch portion communicates the water source with the drug supply portion.
    The third branch portion communicates the filtration portion with the terminal side of the purified water discharge pipe.
    During backwashing
    The first branch portion communicates the backwash drain pipe with the filtration portion.
    The second branch portion communicates the water source with the backwash water pipe.
    The water treatment apparatus according to claim 1, wherein the third branch portion communicates the backwash water pipe and the filtration portion.
  3.  前記浄水吐出配管の最小径部は、前記逆洗送水管または前記逆洗ドレン管の最小径部よりも小さく、前記浄水吐出配管において前記第三分岐部に対し前記濾過部とは反対側に設けられた
     ことを特徴とする請求項2に記載の水処理装置。
    The minimum diameter portion of the purified water discharge pipe is smaller than the minimum diameter portion of the backwash water pipe or the backwash drain pipe, and is provided on the opposite side of the third branch portion of the purified water discharge pipe from the filtration portion. The water treatment apparatus according to claim 2, wherein the water treatment apparatus has been obtained.
  4.  前記水処理装置は、さらに
     前記浄水吐出配管の前記最小径部を迂回する直接排水管を有した
     ことを特徴とする請求項3に記載の水処理装置。
    The water treatment device according to claim 3, further comprising a direct drainage pipe that bypasses the minimum diameter portion of the purified water discharge pipe.
  5.  前記逆洗ドレン管は、設置状態において、前記第一分岐部から下方に延伸し、
     前記水処理装置は、さらに
     前記逆洗ドレン管の経路内に、一端を大気中に開放し、大気側から配管内への流入を行う空気補給弁を有した
     ことを特徴とする請求項2に記載の水処理装置。
    The backwash drain pipe extends downward from the first branch portion in the installed state.
    The second aspect of the present invention is characterized in that the water treatment apparatus further includes an air supply valve in the path of the backwash drain pipe, which has one end open to the atmosphere and allows inflow from the atmosphere side into the pipe. The water treatment apparatus described.
  6.  前記空気補給弁は、大気側からの流入のみが可能な逆止弁である
     ことを特徴とする請求項5に記載の水処理装置。
    The water treatment apparatus according to claim 5, wherein the air supply valve is a check valve capable of only flowing in from the atmosphere side.
  7.  前記逆洗ドレン管における前記空気補給弁への分岐点から前記薬剤供給部までの配管経路における設置状態での水平高さは、前記分岐点で最も低く、前記薬剤供給部の流出口に向けて高くなるようにした
     ことを特徴とする請求項5または6に記載の水処理装置。
    The horizontal height of the backwash drain pipe in the installed state in the piping path from the branch point to the air supply valve to the drug supply section is the lowest at the branch point and toward the outlet of the drug supply section. The water treatment apparatus according to claim 5 or 6, characterized in that the height is increased.
  8.  前記空気補給弁は、設置状態において、前記分岐点よりも高い位置に設けられた
     ことを特徴とする請求項7に記載の水処理装置。
    The water treatment device according to claim 7, wherein the air supply valve is provided at a position higher than the branch point in the installed state.
  9.  前記薬剤供給部は、有底筒状の筐体を有し、前記筐体の内部に流入路、流出路、薬剤路及びバイパス路の分岐部を有し、
     前記筐体内において、前記流出路に、前記薬剤路を経由した流体を回収する開口を設けた
    ことを特徴とする請求項1に記載の水処理装置。
    The drug supply unit has a bottomed tubular housing, and has an inflow path, an outflow path, a drug path, and a branch portion of a bypass path inside the housing.
    The water treatment apparatus according to claim 1, wherein the outflow passage is provided with an opening for collecting a fluid that has passed through the chemical passage in the housing.
  10.  前記筐体は、設置状態において、上部カバーと下部基台とに上下に分割可能な筒状であり、
     前記下部基台は、椀状で、内部に前記流入路、前記流出路及び前記薬剤路の前記分岐部を有した
     ことを特徴とする請求項9に記載の水処理装置。
    The housing has a tubular shape that can be vertically divided into an upper cover and a lower base in the installed state.
    The water treatment apparatus according to claim 9, wherein the lower base is bowl-shaped and has the inflow passage, the outflow passage, and the branch portion of the chemical passage inside.
  11.  前記薬剤路は、設置状態において、前記分岐部から上方に向けて立設し、上部に前記薬剤載置場所である薬剤載置部を設けた
     ことを特徴とする請求項10に記載の水処理装置。
    The water treatment according to claim 10, wherein the drug passage is erected upward from the branch portion in an installed state, and a drug placement portion, which is a drug placement place, is provided at the upper portion. apparatus.
  12.  前記薬剤路は、前記筐体内に、設置状態において上方に向けて立設した噴出管を有し、
     前記噴出管は、前記分岐部において取り外し可能とした
     ことを特徴とする請求項11に記載の水処理装置。
    The drug passage has an ejection pipe erected upward in the installed state in the housing.
    The water treatment apparatus according to claim 11, wherein the ejection pipe is removable at the branch portion.
  13.  前記薬剤路は、前記筐体内に、設置状態において上方に向けて立設した噴出管を有し、前記薬剤載置場所であって、前記噴出管の上方に、固形の薬剤を載せる薬剤載置部を有し、
     前記薬剤載置部は、側面に薬剤の溶けだした薬液を排出する載置部出口を有し、
     前記噴出管の設置状態における下部の外径は、前記薬剤載置部の外径よりも小さい
     ことを特徴とする請求項9に記載の水処理装置。
    The drug passage has an ejection pipe erected upward in the housing in the installed state, and is a drug placing place, and a drug placing on which a solid drug is placed above the ejection tube. Has a part
    The drug loading section has a loading section outlet on the side surface for discharging the drug solution in which the drug has been dissolved.
    The water treatment apparatus according to claim 9, wherein the outer diameter of the lower part of the ejection pipe in the installed state is smaller than the outer diameter of the drug placing portion.
  14.  前記噴出管は、
     設置状態において、内部を上下に仕切る仕切り板と、
     前記仕切り板に開口した載置部入口とを有し、
     前記載置部入口は、前記載置部出口よりも前記噴出管の中心軸寄りに設けられ、
     前記載置部出口は、設置状態において、前記仕切り板よりも上方であって、前記噴出管の側壁側に設けられ、
     前記薬剤載置部は、前記仕切り板上に薬剤が載置されるものであり、前記薬剤載置部の一部が前記載置部入口と前記載置部出口との間に配置された
     ことを特徴とする請求項13に記載の水処理装置。
    The ejection pipe
    In the installed state, the partition plate that divides the inside up and down,
    It has a mounting portion entrance opened in the partition plate, and has
    The above-mentioned place entrance is provided closer to the central axis of the ejection pipe than the above-mentioned place outlet.
    In the installed state, the above-mentioned place outlet is provided above the partition plate and on the side wall side of the ejection pipe.
    The drug placing portion is for placing the drug on the partition plate, and a part of the drug placing portion is arranged between the entrance of the previously described placing portion and the outlet of the previously described placing portion. 13. The water treatment apparatus according to claim 13.
  15.  前記載置部出口は、設置状態において、前記薬剤載置部の最下点よりも上方に設けられた
     ことを特徴とする請求項14に記載の水処理装置。
    The water treatment apparatus according to claim 14, wherein the outlet of the above-mentioned placing portion is provided above the lowest point of the medicine placing portion in the installed state.
  16.  前記仕切り板には、設置状態において、外縁側から前記載置部入口側に下る傾斜を設けた
     ことを特徴とする請求項15に記載の水処理装置。
    The water treatment apparatus according to claim 15, wherein the partition plate is provided with an inclination that descends from the outer edge side to the entrance side of the previously described placing portion in the installed state.
  17.  前記薬剤は、錠剤とした
     ことを特徴とする請求項13~16いずれか一項に記載の水処理装置。
    The water treatment device according to any one of claims 13 to 16, wherein the drug is a tablet.
PCT/JP2020/027611 2019-07-31 2020-07-16 Water treatment device WO2021020138A1 (en)

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