JP6028538B2 - Pure water production equipment - Google Patents

Description

  The present invention relates to a pure water production apparatus including a reverse osmosis membrane module that separates permeate from supply water, and an electrodeionization stack that demineralizes the permeate to obtain demineralized water.

  In semiconductor manufacturing processes, electronic component cleaning, medical instrument cleaning, and the like, high-purity pure water that does not contain impurities is used. When manufacturing this kind of pure water, a pure water manufacturing apparatus may be used. As pure water production equipment, reverse osmosis membrane module (hereinafter also referred to as “RO membrane module”) that separates permeate from feed water, and permeate separated by reverse osmosis membrane module is desalted to obtain demineralized water. There is known a pure water production apparatus including an obtained electrodeionization stack (hereinafter also referred to as “EDI stack”) (for example, see Patent Document 1). In such a pure water production apparatus, in general, raw water such as groundwater or tap water is treated with an RO membrane module using a reverse osmosis membrane, so that permeated water from which most of the dissolved salts have been removed from the raw water. To separate. Thereafter, the purity is further increased by purifying the permeate with an EDI stack.

JP 2001-259376 A

  In the pure water manufacturing apparatus described in Patent Document 1, the EDI stack may be clogged due to leakage of suspended solids associated with long-term use of the RO membrane module. When supply water is supplied to the RO membrane module by a pressure pump or the like in a state where the EDI stack is clogged, the back pressure of the RO membrane module arranged on the upstream side of the EDI stack increases, and the RO membrane May be damaged. In addition, when the EDI stack is clogged, the flow rate of water flowing through the concentration chamber or the like decreases, and therefore the risk of scale generation increases on the surface of the ion exchange membrane.

  Therefore, there is a demand for a pure water production apparatus that can prevent membrane breakage in a reverse osmosis membrane module and can prevent scale generation in an electrodeionization stack.

  An object of this invention is to provide the pure water manufacturing apparatus which can prevent the breakage of the membrane in a reverse osmosis membrane module, and can prevent generation | occurrence | production of the scale in an electrodeionization stack.

The present invention includes a reverse osmosis membrane module that separates permeated water from supply water, an electrodeionization stack that obtains demineralized water by desalting the permeated water separated by the reverse osmosis membrane module, and reverse feed water to the reverse A supply water line that circulates to the osmosis membrane module, a permeate line that circulates the permeate separated by the reverse osmosis membrane module to the electrodeionization stack, and deionized water obtained by the electrodeionization stack A demineralized water line that is sent out toward the water supply, a pressure pump that is provided in the feed water line and discharges the feed water toward the downstream side, and a pressure measuring means that measures the pressure of the permeated water flowing through the permeate water line And a notification means for reporting an alarm, and when the pressure value of the permeate flowing through the permeate line exceeds a predetermined pressure threshold after driving the pressurizing pump, demineralized water is supplied to the demand point. From water sampling state, the control to transition to the standby state without supplying demineralized water to the demand position to stop the pressure pump, and a control unit for controlling to perform the notification by the notification means The present invention relates to a pure water production apparatus.

  In addition, the first circulating water line for returning the permeated water separated by the reverse osmosis membrane module to the upstream side of the reverse osmosis membrane module, and the demineralized water obtained by the electrodeionization stack of the reverse osmosis membrane module A second circulating water line that returns to the upstream side, and the control unit, when the pressure value of the permeated water flowing through the permeated water line is lower than a predetermined pressure threshold after driving the pressurizing pump. Performs a first step of returning the permeated water separated by the reverse osmosis membrane module to the upstream side of the reverse osmosis membrane module via the first circulating water line, and after the execution of the first step, It is preferable to execute a second step of returning demineralized water obtained in the electrodeionization stack to the upstream side of the reverse osmosis membrane module via the second circulating water line.

  In addition, after the notification by the notification unit is performed, the control unit shifts from the standby state to the water sampling state when the notification by the notification unit is reset and there is a request to supply demineralized water. It is preferable to control.

  ADVANTAGE OF THE INVENTION According to this invention, while being able to prevent the membrane of a reverse osmosis membrane module from being damaged, the pure water manufacturing apparatus which can prevent generation | occurrence | production of the scale of an electrodeionization stack can be provided.

It is a whole block diagram of the pure water manufacturing apparatus 1 which concerns on one Embodiment. It is a flowchart which shows the process sequence of operation | movement of the pure water manufacturing apparatus. It is a flowchart which shows the process sequence of operation | movement of the pure water manufacturing apparatus.

  The pure water manufacturing apparatus 1 which concerns on one Embodiment of this invention is demonstrated referring drawings. FIG. 1 is an overall configuration diagram of a pure water production apparatus 1 according to an embodiment. The pure water production apparatus 1 according to the present embodiment is applied to, for example, a pure water production apparatus that produces demineralized water from raw water (for example, tap water). The desalted water produced by the pure water production apparatus is sent as pure water to a demand location or the like. In the pure water production apparatus of the present embodiment, supplying pure water to a demand location or the like is also referred to as “water sampling”.

  As shown in FIG. 1, the pure water manufacturing apparatus 1 according to the present embodiment includes an activated carbon filter 2, a prefilter 3, a raw water tank 4, a pressurizing pump 5, an inverter 6, and a reverse osmosis membrane module. First RO membrane module 11 and second RO membrane module 12, EDI stack 20 as an electrodeionization stack, control unit 30, notification unit 31 as notification means, input operation unit 32, and DC power supply device 33 .

  The pure water production apparatus 1 includes a raw water replenishment valve 61, a first flow path switching valve 62, a second flow path switching valve 63 as a delivery means, a third flow path switching valve 64, and a desalted water return valve. 65, first RO valve 101 to fourth RO valve 104, first EDI valve 201 to sixth EDI valve 206, water level sensor 41, in-tank electrical conductivity sensor 42, in-tank temperature sensor 43, and first electrical conduction Rate sensor 51, pressure sensor 52 as pressure measuring means, first flow sensor 53, second flow sensor 54, second electrical conductivity sensor 55, third flow sensor 56, and fourth flow sensor 57. And comprising.

  In FIG. 1, the electrical connection path is omitted, but the control unit 30 performs the raw water supply valve 61, the first flow path switching valve 62, the second flow path switching valve 63, the water level sensor 41, and the electric conductivity in the tank. Sensor 42, tank internal temperature sensor 43, first electrical conductivity sensor 51, second electrical conductivity sensor 55, pressure sensor 52, first flow sensor 53, second flow sensor 54, third flow sensor 56, and fourth flow rate. The sensor 57 is electrically connected. Moreover, in this embodiment, the 3rd flow-path switching valve 64, the desalted water return valve 65, the 1st RO valve 101-the 4th RO valve 104, and the 1st EDI valve 201-the 6th EDI valve 206 switch an open / close state by manual operation. Or the valve opening degree can be adjusted.

  The pure water production apparatus 1 includes a raw water line L1 as a supply water line, a first permeate water line L2 and a second permeate water line L3 as permeate water lines, a first RO concentrated water return line L5, and a first RO. Concentrated water discharge line L41, second RO concentrated water return line L6, second RO permeate return line L7 as the first circulating water line, second RO permeated water discharge line L42, demineralized water line L8, and second circulation A demineralized water return line L9, an EDI concentrated water return line L10, an EDI concentrated water discharge line L43, and an EDI electrode water discharge line L44 as water lines are provided. The “line” in the present specification is a general term for lines capable of flowing a fluid such as a flow path, a radial path, and a pipeline.

  Raw water W1 (supply water) flows through the raw water line L1. The raw water line L1 is a line through which the raw water W1 is circulated to the first RO membrane module 11. The raw water line L1 includes a first raw water line L11 and a second raw water line L12.

  The first raw water line L11 is a line connecting a supply source (not shown) of the raw water W1 and the raw water tank 4. The upstream end of the first raw water line L11 is connected to a supply source (not shown) of the raw water W1. Further, the downstream end of the first raw water line L <b> 11 is connected to the raw water tank 4.

  The first raw water line L11 is provided with a raw water replenishment valve 61, an activated carbon filter 2, a prefilter 3, and a raw water tank 4 in order from the upstream side. The raw water supply valve 61 is a valve capable of opening and closing the first raw water line L11. The raw water supply valve 61 is electrically connected to the control unit 30. The opening / closing operation of the raw water supply valve 61 is controlled by a flow path opening / closing signal from the control unit 30.

  The activated carbon filter 2 is a device that removes a chlorine component (mainly free chlorine) contained in the raw water W1. The activated carbon filter 2 has a filter medium bed made of activated carbon in a pressure tank. The activated carbon filter 2 purifies the raw water W1 by decomposing and removing chlorine components contained in the raw water W1, and adsorbing and removing organic components and capturing suspended substances.

  The prefilter 3 is a filter that removes fine particles contained in the raw water W1 filtered by the activated carbon filter 2. The prefilter 3 is configured by accommodating a filter element in a housing. As the filter element, for example, a nonwoven fabric filter element or a thread wound filter element having a filtration accuracy of 1 to 50 μm is used. The raw water tank 4 is a tank for storing raw water W1 purified through the activated carbon filter 2 and the prefilter 3 as supply water.

  The second raw water line L12 is a line connecting the raw water tank 4 and the first RO membrane module 11. The upstream end of the second raw water line L12 is connected to the raw water tank 4. Further, the downstream end of the second raw water line L12 is connected to the primary inlet port (the inlet of the raw water W1) of the first RO membrane module 11.

  The second raw water line L12 is provided with a pressurizing pump 5, a first RO valve 101, and a first RO membrane module 11 in order from the upstream side. The first RO valve 101 is provided between the pressurizing pump 5 and the first RO membrane module 11 in the second raw water line L12. The first RO valve 101 is a valve capable of adjusting the flow rate of the raw water W1 flowing through the second raw water line L12.

  The pressurizing pump 5 is a device that sucks the raw water W1 flowing through the second raw water line L12 and pumps (discharges) the raw water W1 toward the first RO membrane module 11. The pressurizing pump 5 is supplied with driving power whose frequency is converted from the inverter 6. The pressurizing pump 5 is driven at a rotational speed corresponding to the frequency of the supplied driving power (hereinafter also referred to as “driving frequency”).

  The inverter 6 is an electric circuit (or a device having the circuit) that supplies driving power whose frequency is converted to the pressure pump 5. The inverter 6 is electrically connected to the control unit 30. A command signal is input to the inverter 6 from the control unit 30. The inverter 6 outputs driving power having a driving frequency corresponding to the command signal (current value signal or voltage value signal) input by the control unit 30 to the pressurizing pump 5.

  The 1st RO membrane module 11 isolate | separates the raw | natural water W1 pumped by the pressurization pump 5 into the 1st permeated water W2 from which the dissolved salt was removed, and the concentrated water W3 in which the dissolved salt was concentrated. The first RO membrane module 11 is configured by accommodating a single or a plurality of spiral RO membrane elements in a pressure vessel (vessel). Examples of the RO membrane used in the RO membrane element include a crosslinked aromatic polyamide composite membrane. As RO membrane elements comprising a crosslinked aromatic polyamide composite membrane, Toray Industries, Inc .: model name “TMG20-400”, Eunjin Chemical Co., Ltd .: model name “RE8040-BLF”, Nitto Denko Corporation: model name “ESPA1” Are commercially available, and these elements can be suitably used.

  The first RO concentrated water return line L5 is a line for returning a part of the concentrated water W3 separated by the first RO membrane module 11 to the raw water tank 4. The first RO concentrated water return line L5 includes an upstream first RO concentrated water return line L51 and a downstream first RO concentrated water return line L52.

  The upstream end of the upstream first RO concentrated water return line L51 is connected to the primary outlet port (the outlet of the concentrated water W3) of the first RO membrane module 11. The downstream end of the upstream first RO concentrated water return line L51 is branched into a downstream first RO concentrated water return line L52 and a first RO concentrated water discharge line L41 at a branch portion J11.

  The upstream end of the downstream first RO concentrated water return line L52 is connected to the branch portion J11. The downstream end of the downstream first RO concentrated water return line L52 is connected to the raw water tank 4. A second RO valve 102 is provided in the downstream first RO concentrated water return line L52. The 2nd RO valve 102 is a valve which can adjust the flow volume of the concentrated water W3 which distribute | circulates the downstream 1st RO concentrated water return line L52.

  The 1st RO concentrated water discharge line L41 is a line which distribute | circulates so that the remainder of the concentrated water W3 isolate | separated by the 1st RO membrane module 11 may be discharged | emitted out of the apparatus from the middle of the 1st RO concentrated water return line L5. The upstream end of the first RO concentrated water discharge line L41 is connected to the branch portion J11. The downstream side of the first RO concentrated water discharge line L41 is connected or opened to a drain pit (not shown), for example. The first RO concentrated water discharge line L41 is provided with a third RO valve 103. The third RO valve 103 is a valve capable of adjusting the waste water flow rate of the concentrated water W3 discharged to the outside of the apparatus via the first RO concentrated water discharge line L41.

  The first permeate line L <b> 2 is a line through which the first permeate W <b> 2 separated by the first RO membrane module 11 flows to the second RO membrane module 12. The upstream end of the first permeate line L2 is connected to the secondary port (the outlet of the first permeate W2) of the first RO membrane module 11. The downstream end of the first permeate line L2 is connected to the primary inlet port (the inlet of the first permeate W2) of the second RO membrane module 12.

  The second RO membrane module 12 is composed of the first permeated water W2 separated by the first RO membrane module 11 and pumped by the pressurizing pump 5, and the second permeated water W4 from which dissolved salts are removed from the first permeated water W2. And the concentrated water W5 in which the dissolved salts are concentrated. The second RO membrane module 12 is configured by accommodating a single or a plurality of spiral RO membrane elements in a pressure vessel (vessel). In the first RO membrane module 11, the same RO membrane element as that of the second RO membrane module 12 can be used.

  The second RO concentrated water return line L6 is a line for returning the concentrated water W5 separated by the second RO membrane module 12 to the raw water tank 4. The upstream end of the second RO concentrated water return line L6 is connected to the primary outlet port (concentrated water outlet) of the second RO membrane module 12. The downstream end of the second RO concentrated water return line L6 is connected to the raw water tank 4. A fourth RO valve 104 is provided in the second RO concentrated water return line L6. The fourth RO valve 104 is a valve capable of adjusting the flow rate of the concentrated water W3 flowing through the second RO concentrated water return line L6.

  The second permeated water line L3 is a line through which the second permeated water W4 separated by the second RO membrane module 12 flows through the EDI stack 20. The second permeate line L3 includes a front-stage permeate line L31, a middle-stage permeate line L32, a desalting chamber inflow line L321, a concentration chamber inflow line L322, and an electrode chamber inflow line L323.

  The upstream end of the front-stage permeate line L31 is connected to the secondary port (the outlet of the second permeate W4) of the second RO membrane module 12. The downstream end of the front-stage permeate line L31 is connected to the middle-stage permeate line L32 and the second RO permeate return line L7 via the first flow path switching valve 62.

  The first flow path switching valve 62 allows the second permeated water W4 separated by the second RO membrane module 12 to flow toward the EDI stack 20 via the middle-stage permeated water line L32 (water sampling side flow path). ) Or a valve that can be switched to a flow path (circulation side flow path and drain side flow path) that flows toward the third flow path switching valve 64 via the second RO permeate return line L7. The first flow path switching valve 62 is configured by, for example, an electric or electromagnetic three-way valve. The first flow path switching valve 62 is electrically connected to the control unit 30. The switching of the flow path in the first flow path switching valve 62 is controlled by a flow path switching signal from the control unit 30.

  The second RO permeated water return line L7 is a line for returning the second permeated water W4 separated by the second RO membrane module 12 to the raw water tank 4 on the upstream side of the first RO membrane module 11. The second RO permeate return line L7 includes an upstream second RO permeate return line L71 and a downstream second RO permeate return line L72.

  The upstream end of the upstream second RO permeate return line L71 is connected to the first flow path switching valve 62. The downstream end of the upstream second RO permeate return line L71 is connected to the third flow path switching valve 64.

  The third flow path switching valve 64 allows the second permeated water W4 flowing through the upstream second RO permeate return line L71 to flow toward the raw water tank 4 via the downstream second RO permeate return line L72. This is a valve that can be switched to a channel (circulation side channel) or a channel (drainage side channel) that circulates so as to be discharged to the outside of the apparatus via the second RO permeated water discharge line L42. The third flow path switching valve 64 is a valve that can be manually switched between open and closed states.

  The upstream end of the downstream second RO permeate return line L72 is connected to the third flow path switching valve 64. The downstream end of the downstream second RO permeate return line L72 is connected to the raw water tank 4.

  The second RO permeate discharge line L42 is a line through which the second permeate W4 separated by the second RO membrane module 12 joins the second RO permeate return line L7 and is discharged out of the apparatus. The upstream end of the second RO permeate discharge line L42 is connected to the third flow path switching valve 64. The downstream side of the third flow path switching valve 64 is connected or opened to a drainage pit (not shown), for example.

  The second RO permeated water discharge line L42 is joined to the first RO concentrated water discharge line L41 at the connection portion J12. The connection part J12 is arrange | positioned rather than the 3rd RO valve 103 in the 1st RO concentrated water discharge line L41. The portion of the second RO permeated water discharge line L42 on the downstream side of the connection portion J12 is common to the portion of the first RO concentrated water discharge line L41 on the downstream side of the connection portion J12.

  The upstream end of the middle permeate line L32 is connected to the first flow path switching valve 62. The downstream end of the middle-stage permeate line L32 is branched into a desalting chamber inflow line L321, a concentration chamber inflow line L322, and an electrode chamber inflow line L323 at a branch portion J4.

  The downstream ends of the desalination chamber inflow line L321, the enrichment chamber inflow line L322, and the electrode chamber inflow line L323 are the primary ports of the EDI stack 20 (each inlet side of the desalination chamber 21, the concentration chamber 22, and the electrode chamber 23). )It is connected to the.

  The EDI stack 20 is a water treatment device that desalinates the second permeated water W4 separated from the first permeated water W2 by the second RO membrane module 12 to obtain desalted water W6, concentrated water W7, and electrode water W8. is there. The EDI stack 20 is electrically connected to the DC power supply device 33. A DC voltage is input from the DC power supply device 33 to the EDI stack 20. The EDI stack 20 is energized and operated by the DC voltage input from the DC power supply device 33.

  The DC power supply device 33 applies a DC voltage between the pair of electrodes of the EDI stack 20. The DC power supply device 33 is electrically connected to the control unit 30. The DC power supply device 33 outputs a DC voltage to the EDI stack 20 in response to the command signal input by the control unit 30.

  In the EDI stack 20, a cation exchange membrane and an anion exchange membrane (not shown) are alternately arranged between a pair of electrodes. The inside of the EDI stack 20 is partitioned into a desalting chamber 21, a concentration chamber 22, and an electrode chamber 23 by these ion exchange membranes. The desalting chamber 21 is filled with an ion exchanger (not shown). As the ion exchanger filled in the desalting chamber 21, for example, an ion exchange resin, an ion exchange fiber, or the like is used. In FIG. 1, a plurality of desalting chambers 21, concentration chambers 22, and electrode chambers 23 partitioned inside the EDI stack 20 are schematically shown.

  A desalting chamber inflow line L321 through which the second permeated water W4 flows is connected to the inlet side of the desalting chamber 21. On the outlet side of the desalting chamber 21, a desalting water line L <b> 8 through which the desalted water W <b> 6 discharged from the ions in the desalting chamber 21 is circulated is connected. A concentrating chamber inflow line L322 through which the second permeated water W4 flows is connected to the inlet side of the concentrating chamber 22. An EDI concentrated water return line L10 that circulates the concentrated water W7 that has been concentrated and discharged is connected to the outlet side of the concentration chamber 22. An electrode chamber inflow line L323 through which the second permeated water W4 flows is connected to the inlet side of the electrode chamber 23. An electrode water discharge line L44 through which the electrode water W8 flows is connected to the outlet side of the electrode chamber 23.

  A first EDI valve 201 is provided in the desalination chamber inflow line L321. A second EDI valve 202 is provided in the concentration chamber inflow line L322. A third EDI valve 202 is provided in the electrode chamber inflow line L323. The first EDI valve 201 is a valve capable of adjusting the flow rate of the second permeated water W4 flowing through the demineralization chamber inflow line L321 (that is, the flow rate of the demineralized water W6 flowing through the demineralization chamber 21). The second EDI valve 202 is a valve capable of adjusting the flow rate of the second permeated water W4 flowing through the concentration chamber inflow line L322 (that is, the flow rate of the concentrated water W7 flowing through the concentration chamber 22). The third EDI valve 203 is a valve capable of adjusting the flow rate of the second permeated water W4 flowing through the electrode chamber inflow line L323 (that is, the flow rate of the electrode water W8 flowing through the electrode chamber 23).

  The second permeated water W4 flowing through the second permeated water line L3 flows into each of the desalting chamber 21, the concentration chamber 22, and the electrode chamber 23. Residual ions contained in the second permeated water W4 are captured by an ion exchanger (not shown) filled in the desalting chamber 21 to become desalted water W6. The desalted water W6 is sent to the demand point via the desalted water line L8 (described later). Further, residual ions captured by the ion exchanger in the desalting chamber 21 move to the concentration chamber 22 by the applied electric energy. And the water containing a residual ion is discharged | emitted as the concentrated water W7 from the concentration chamber 22 via the EDI concentrated water return line L10 and the EDI concentrated water discharge line L43 (after-mentioned). The second permeated water W4 that has flowed into the electrode chamber 23 is discharged out of the apparatus as electrode water W8 from the electrode chamber 23 via the EDI electrode water discharge line L44.

  The desalted water line L8 is a line that sends the desalted water W6 obtained in the EDI stack 20 as pure water toward the demand point. The demineralized water line L8 includes an upstream demineralized water line L81 and a downstream demineralized water line L82.

  The upstream end of the upstream demineralized water line L81 is connected to the secondary port of the EDI stack 20 (the outlet side of the demineralized chamber 21). The downstream end of the upstream demineralized water line L81 is connected to the downstream demineralized water line L82 and the demineralized water return line L9 (described later) via the second flow path switching valve 63.

  The second flow path switching valve 63 is a flow path (water sampling side flow path) for sending the desalted water W6 obtained in the desalination chamber 21 of the EDI stack 20 toward the demand point via the downstream desalted water line L82. ) Or a valve that can be switched to a flow path (circulation side flow path) that circulates toward the raw water tank 4 via the desalted water return line L9. The second flow path switching valve 63 is configured by, for example, an electric or electromagnetic three-way valve. The second flow path switching valve 63 is electrically connected to the control unit 30. Switching of the flow path in the second flow path switching valve 63 is controlled by a flow path switching signal from the control unit 30.

  The second flow path switching valve 63 performs a process of sending the demineralized water W6 obtained in the EDI stack 20 from the demineralized water line L8 to the demand point by being switched to the water sampling side flow path by the control unit 30. It functions as an executable sending means.

  An upstream end portion of the downstream demineralized water line L <b> 82 is connected to the second flow path switching valve 63. The downstream end of the downstream desalted water line L82 is connected to a device or the like (not shown) at the demand point.

  The desalted water return line L9 is a line for returning the desalted water W6 obtained in the desalting chamber 21 of the EDI stack 20 to the raw water tank 4 on the upstream side of the first RO membrane module 11 from the middle of the desalted water line L8. . In the present embodiment, the upstream end of the desalted water return line L9 is connected to the second flow path switching valve 63. The downstream end of the desalted water return line L9 is connected to the raw water tank 4. The desalted water return line L <b> 9 returns the desalted water W <b> 6 obtained in the desalting chamber 21 of the EDI stack 20 to the raw water tank 4. A desalted water return valve 65 is provided in the desalted water return line L9.

  The EDI concentrated water return line L10 is a line that joins the concentrated water W7 discharged from the concentration chamber 22 of the EDI stack 20 to the desalted water return line L9 and returns it to the raw water tank 4. The upstream end of the EDI concentrated water return line L10 is connected to the secondary port of the EDI stack 20 (the outlet side of the concentration chamber 22). The downstream end of the EDI concentrated water return line L10 is connected to the raw water tank 4.

  The EDI concentrated water return line L10 is joined to the demineralized water return line L9 at the connection J13. The connecting portion J13 is disposed between the raw water tank 4 and the desalted water return valve 65 in the desalted water return line L9. The portion downstream of the connection portion J13 in the EDI concentrated water return line L10 is common to the portion from the connection portion J13 to the raw water tank 4 in the desalted water return line L9. A fifth EDI valve 205 is provided on the upstream side of the connection portion J13 in the EDI concentrated water return line L10.

  The EDI concentrated water discharge line L43 is a line through which the concentrated water W7 discharged from the concentration chamber 22 of the EDI stack 20 is circulated so as to be discharged out of the apparatus from the middle of the EDI concentrated water return line L10. The upstream end portion of the EDI concentrated water discharge line L43 is connected to the connection portion J9. The connecting portion J9 is disposed between the concentrating chamber 22 and the fifth EDI valve 205 in the EDI concentrated water return line L10. The downstream side of the EDI concentrated water discharge line L43 is connected or opened to a drain pit (not shown), for example. A sixth EDI valve 206 is provided in the EDI concentrated water discharge line L43.

  The electrode water discharge line L44 is a line through which the electrode water W8 discharged from the electrode chamber 23 of the EDI stack 20 is circulated out of the apparatus. The upstream end of the electrode water discharge line L44 is connected to the electrode chamber 23 of the EDI stack 20. The electrode water discharge line L44 is joined to the EDI concentrated water discharge line L43 at the connection portion J10. The connecting portion J10 is disposed on the downstream side of the sixth EDI valve 206 in the EDI concentrated water discharge line L43. A portion of the electrode water discharge line L44 on the downstream side of the connection portion J10 is common to a portion of the EDI concentrated water discharge line L43 on the downstream side of the connection portion J10.

  The water level sensor 41 is a device that measures the water level of the raw water W1 stored in the raw water tank 4. The water level sensor 41 is disposed on the lower side inside the raw water tank 4. Further, the water level sensor 41 is electrically connected to the control unit 30. The water level of the raw water tank 4 measured by the water level sensor 41 is transmitted to the control unit 30 as a detection signal. In the present embodiment, the water level sensor 41 is a continuous level sensor, and for example, a capacitive sensor, a pressure sensor, an ultrasonic sensor, or the like is used. FIG. 1 shows an example in which a pressure sensor is provided on the outer wall surface near the bottom of the raw water tank 4 as the water level sensor 41. The water level sensor 41 is not limited to a continuous level sensor, and may be a level switch, for example. The level switch is a preset liquid level position detector, and is configured to detect, for example, a plurality of liquid level positions. As the level switch, for example, a float type or an electrode type is used.

  The in-tank electrical conductivity sensor 42 is a device that measures the electrical conductivity of the raw water W1 stored in the raw water tank 4. The in-tank electrical conductivity sensor 42 is disposed on the lower side inside the raw water tank 4.

  The 1st electrical conductivity sensor 51 is an apparatus which measures the electrical conductivity of the 2nd permeated water W4 which distribute | circulates the 2nd permeated water line L3. The first electrical conductivity sensor 51 is connected to the second permeated water line L3 at the connection portion J1. The connection portion J1 is disposed between the second RO membrane module 12 and the first flow path switching valve 62 in the second permeated water line L3. The 2nd electrical conductivity sensor 55 is an apparatus which measures the electrical conductivity of the desalted water W6 which distribute | circulates the desalted water line L8. The second electrical conductivity sensor 55 is connected to the demineralized water line L8 at the connection portion J6. The connecting portion J6 is disposed between the EDI stack 20 and the fourth EDI valve 204 in the desalted water line L8.

  The in-tank electrical conductivity sensor 42, the first electrical conductivity sensor 51, and the second electrical conductivity sensor 55 are electrically connected to the control unit 30. The electrical conductivity of the raw water W1 measured by the in-tank electrical conductivity sensor 42, the electrical conductivity of the second permeated water W4 measured by the first electrical conductivity sensor 51, and the second electrical conductivity sensor 55 were measured. The electrical conductivity of the desalted water W6 is transmitted to the control unit 30 as a detection signal.

  The in-tank temperature sensor 43 is a device that measures the temperature of the raw water W1 stored in the raw water tank 4. The tank internal temperature sensor 43 is disposed on the lower side of the raw water tank 4. The tank internal temperature sensor 43 is electrically connected to the control unit 30. The temperature of the raw water W1 measured by the tank temperature sensor 43 is transmitted to the control unit 30 as a detection signal.

  The first flow rate sensor 53 is a device that measures the flow rate of the second permeated water W4 flowing through the second permeated water line L3. The first flow rate sensor 53 is connected to the second permeated water line L3 at the connection portion J3. The connecting portion J3 is disposed between the second RO membrane module 12 and the first flow path switching valve 62 in the second permeated water line L3. The second flow rate sensor 54 is a device that measures the flow rate of the desalted water W6 that flows through the desalted water line L8. The second flow rate sensor 54 measures the flow rate of the water flowing through the desalting chamber 21 by measuring the flow rate of the desalted water W6 flowing through the desalted water line L8. The second flow rate sensor 54 is connected to the desalted water line L8 at the connection portion J5. The connecting portion J5 is disposed between the EDI stack 20 and the fourth EDI valve 204 in the desalted water line L8.

  The third flow rate sensor 56 is a device that measures the flow rate of the second permeated water W4 flowing through the concentration chamber inflow line L322. The third flow rate sensor 56 measures the flow rate of the water flowing through the concentration chamber 22 by measuring the flow rate of the second permeated water W4 flowing through the concentration chamber inflow line L322. The third flow sensor 56 is connected to the enrichment chamber inflow line L322 at the connection portion J7. The connecting portion J7 is disposed between the EDI stack 20 and the second EDI valve 202 in the concentration chamber inflow line L322. The fourth flow rate sensor 57 is a device that measures the flow rate of the second permeated water W4 flowing through the electrode chamber inflow line L323. The fourth flow rate sensor 57 measures the flow rate of the water flowing through the electrode chamber 23 by measuring the flow rate of the second permeated water W4 flowing through the electrode chamber inflow line L323. The fourth flow rate sensor 57 is connected to the electrode chamber inflow line L323 at the connection portion J8. The connecting portion J8 is disposed between the electrode chamber 23 of the EDI stack 20 and the third EDI valve 203 in the electrode chamber inflow line L323.

  The first flow sensor 53, the second flow sensor 54, the third flow sensor 56, and the fourth flow sensor 57 are electrically connected to the control unit 30. The flow rate of the second permeate water W4 measured by the first flow rate sensor 53, the flow rate of the desalted water W6 measured by the second flow rate sensor 54, the flow rate of the second permeate water W4 measured by the third flow rate sensor 56, and The flow rate of the second permeated water W4 measured by the fourth flow rate sensor 57 is transmitted to the control unit 30 as a detection signal.

  The pressure sensor 52 is a device that measures the pressure of the second permeated water W4 flowing through the second permeated water line L3. The pressure sensor 52 is connected to the second permeated water line L3 at the connection portion J2. The pressure sensor 52 is electrically connected to the control unit 30. The connecting portion J2 is disposed between the second RO membrane module 12 and the first flow path switching valve 62. The pressure of the second permeated water W4 measured by the pressure sensor 52 is transmitted to the control unit 30 as a detection signal.

  The notification unit 31 notifies a predetermined alarm. The notification unit 31 is electrically connected to the control unit 30. The notification is, for example, one or more of display, sound, light emission, and the like. That is, the notification unit 31 includes one or more of a display device (liquid crystal display or the like), a buzzer, a speaker, a lamp, and the like.

  The input operation unit 32 is an input interface that receives input operations of a user or an administrator for selection related to the operation mode of the device (for example, selection of operation / stop, release of alarm, etc.) and various settings related to the operation conditions of the device. It is. The input operation unit 32 includes an operation panel that combines a display and button switches, a touch panel that directly operates on the display, and the like. The input operation unit 32 is electrically connected to the control unit 30. Information input from the input operation unit 32 is transmitted to the control unit 30.

  Next, the control unit 30 will be described. The control unit 30 is configured by a microprocessor (not shown) including a CPU and a memory. In the control unit 30, various programs for controlling the pure water production apparatus 1 are stored in the memory of the microprocessor. Further, the memory of the microprocessor includes, for example, threshold values for the electrical conductivity of the second permeated water W4 and the desalted water W6, and threshold values for the flow rates of the desalted water W6, the concentrated water W7, and the electrode water W8 discharged from the EDI stack 20. The data etc. are stored.

  In the control unit 30, the CPU of the microprocessor executes various controls described later according to a predetermined program read from the memory. In the control unit 30, an integrated timer unit for managing time measurement and the like is incorporated in the microprocessor.

  The control unit 30 controls to execute the first process and the second process. The first process executed by the control unit 30 refers to the second permeated water W4 separated by the first RO membrane module 11 and the second RO membrane module 12, and the second RO permeated water return line L7 (first circulating water line). It is the process of returning to the upstream of the 1st RO membrane module 11 via. Specifically, in the first step, the first flow path switching valve 62 is switched to the circulation side flow path in a state where the third flow path switching valve 64 is set as the circulation side flow path. By driving 5, the second permeated water W <b> 4 separated by the first RO membrane module 11 and the second RO membrane module 12 is returned to the raw water tank 4.

  The second step executed by the control unit 30 is to return the desalted water W6 obtained in the EDI stack 20 to the upstream side of the first RO membrane module 11 via the desalted water return line L9 (second circulating water line). It is a process to do. Specifically, in the second step, the first flow path switching valve 62 is switched to the water sampling side flow path, and the second flow path switching valve 63 is switched to the circulation side flow path to drive the pressure pump 5. By doing so, the demineralized water W6 obtained in the EDI stack 20 is returned to the raw water tank 4.

  The control unit 30 executes the first step at the time of starting the apparatus, and after the second step is further executed after the first step, the supply of the desalted water W6 (water sampling) to the demand point is started. Thus, the second flow path switching valve 63 is controlled.

  Moreover, the control part 30 is controlled so that it may transfer to a 2nd process after 1st time progress after starting execution of a 1st process. When the electric conductivity of the second permeated water W4 flowing through the second permeated water line L3 exceeds the predetermined first conductivity threshold at the time when the first time has elapsed, the control unit 30 notifies the notifying unit 31. Control to run. As the predetermined first conductivity threshold value, for example, a raw water of standard water quality is subjected to a reverse osmosis membrane treatment under predetermined operating conditions (operating pressure, recovery rate, water temperature, etc.) using an RO membrane module without deterioration or blockage. Sometimes the electrical conductivity value of the permeate obtained is set.

  In addition, at the start of the second step, the control unit 30 sets the time during which the flow rates of the water flowing through the desalination chamber 21, the concentration chamber 22, and the electrode chamber 23 of the EDI stack 20 exceed a predetermined first set value, respectively. If the operation continues for 2 hours, the EDI stack 20 is controlled to start operation (that is, energization). Further, the control unit 30 determines that the time during which any one of the flow rates of water flowing through the desalination chamber 21, the concentration chamber 22, and the electrode chamber 23 of the EDI stack 20 falls below a predetermined second set value is less than the second time. When the third time is continued for a long time, control is performed so that the notification by the notification unit 31 is executed. The predetermined first set value of the flow rate is normally set to a different flow rate value for each chamber (desalting chamber 21, concentration chamber 22, and electrode chamber 23). The same applies to the predetermined second set value of the flow rate.

  The reason why the predetermined setting value of the flow rate of the water flowing through the desalination chamber 21, the concentration chamber 22 and the electrode chamber 23 of the EDI stack 20 is used as a condition for starting the operation of the EDI stack 20 is that the desalted water W6, the concentration This is because when there is no flow rate equal to or higher than a predetermined value in the water W7 and the electrode water W8, the risk of scale generation or the like increases on the surface of the ion exchange membrane or electrode.

  As the predetermined first set value of the flow rate, for example, a lower limit flow rate value at which the desalination chamber 21, the concentration chamber 22, and the electrode chamber 23 function normally and no risk of scale generation or the like occurs is set. As the predetermined second set value of the flow rate, for example, an upper limit flow rate value in which the desalination chamber 21, the concentration chamber 22 and the electrode chamber 23 function normally and a risk of scale generation or the like occurs is set. Note that the predetermined first set value and the predetermined second set value of the flow rate set for the desalting chamber 21 may be the same value. The same applies to the predetermined first set value and the predetermined second set value of the flow rate set for the concentration chamber 22 and the electrode chamber 23, respectively.

  In addition, when the fourth time has elapsed since the operation of the EDI stack 20 has started, the control unit 30 has a case where the electrical conductivity of the desalted water W6 flowing through the desalted water line L8 is lower than a predetermined second conductivity threshold value. The second flow path switching valve 63 is controlled so that the supply of the demineralized water W6 to the demand point by the second flow path switching valve 63 is started. The control unit 30 controls the notification unit 31 to perform notification when the electrical conductivity of the desalted water W6 flowing through the desalted water line L8 exceeds a predetermined third conductivity threshold value.

  As the predetermined second conductivity threshold value, for example, the electrical conductivity value of pure water that is continuously required at the demand point is set. As the predetermined third conductivity threshold value, for example, an upper limit electric conductivity value that is temporarily allowed at a demand point is set.

  The predetermined second conductivity threshold value and the predetermined third conductivity threshold value may be different values or the same value. In this embodiment, the case where the predetermined second conductivity threshold and the predetermined third conductivity threshold are the same value will be described. In the following description, the predetermined second conductivity threshold and the predetermined third conductivity will be described. The rate threshold will be described as a predetermined second conductivity threshold.

  Here, regarding the notification by the notification unit 31, the control unit 30 forcibly executes the circulation step including the second step, forcibly starts the supply of the desalted water W6 to the demand point, or the desalted water W6 to the demand point. The notification by the notification unit 31 is executed so that the user can select forcible stop of the supply. As a result, the user can sample water (forcibly start the supply of demineralized water to the demand point), circulate (forcibly execute the circulation process consisting of the second step), and wait (supply of the demineralized water to the demand point). Can be selected and executed by operating the input operation unit 32.

  Moreover, the control part 30 performs a 1st process, when there exists a water supply request | requirement from a demand location in a standby state. When there is a request for pure water from the demand point during sampling, the control unit 30 controls the pure water production apparatus 1 to continue sampling, and the request for pure water is sent from the demand point during sampling. When there is not, it controls so that the pure water manufacturing apparatus 1 may transfer to a standby state. Further, the control unit 30 stops the operation of the pure water production apparatus 1 when the operation switch of the pure water production apparatus 1 is OFF (stopped) during sampling.

  In addition, the control unit 30 performs control so as to shift to a sampling operation when sampling is selected on the selection screen for selecting sampling, circulation, or standby displayed on the notification unit 31 or the input operation unit 32. Then, when circulation is selected, control is performed so as to shift to a circulation operation, or when standby is selected, control is performed so as to shift to a standby state.

  When the pressure value of the second permeate W4 flowing through the second permeate line L3 exceeds the predetermined pressure threshold after the pressurization pump 5 is driven, the control unit 30 supplies the desalted water W6 to the demand point. Control is performed so as to shift from a water state to a standby state in which demineralized water W6 is not supplied to the demand point, and control is performed so that notification by the notification unit 31 is executed.

  Moreover, the control part 30 performs a 1st process, when the pressure value of the 2nd permeate water W4 which distribute | circulates the 2nd permeate line L3 after the drive of the pressurization pump 5 is less than a predetermined pressure threshold value, After the execution of the first step, the second step is further executed. As the predetermined pressure threshold value, for example, the allowable back pressure of the second RO membrane module 12 (the upper limit value of the secondary side pressure that is unlikely to damage the RO membrane) is set.

  After the notification by the notification unit 31 is performed, the control unit 30 shifts from the standby state to the water sampling state when the notification by the notification unit 31 is reset and there is a water supply request for demineralized water W6 (pure water). To control.

  Next, operation | movement of the pure water manufacturing apparatus 1 which concerns on this embodiment is demonstrated. 2 and 3 are flowcharts showing the processing procedure of the operation of the pure water production apparatus 1. FIG. The operation of the pure water production apparatus 1 is started when the operation switch is turned on (operation). The process of the flowchart shown in FIG.2 and FIG.3 is repeatedly performed during the driving | operation of the pure water manufacturing apparatus 1. FIG.

  In step ST110 shown in FIG. 2, the deionized water production apparatus 1 enters a standby state when the power is turned on and the operation switch is turned on.

  In step ST111, the control unit 30 determines whether the notification by the notification unit 31 is reset. For example, during the operation of the pure water production apparatus 1, the notification unit 31 may notify the user, and the notification by the notification unit 31 may not be reset, and the pure water production apparatus 1 may enter a standby state. In this case, when the notification by the notification unit 31 is reset by the user and there is a pure water supply request, the control unit 30 controls the apparatus to shift from the standby state to the water collection state. For example, when the back pressure abnormality of the second RO membrane module 12 (abnormality of the pressure value of the second permeated water W4 is high) is notified, the user performs an operation of resetting the notification, whereby the pressure pump 5 Can be shifted from the stopped state to the driven state. When it determines with the alerting | reporting by the alerting | reporting part 31 having been reset (YES), a process progresses to step ST120. When it determines with the alerting | reporting by the alerting | reporting part 31 not being reset (NO), a process returns to step ST111 and repeats step ST111.

  In step ST120, the control unit 30 determines whether or not there is a request to send pure water from the demand point during the standby state. When it is determined that there is a request for pure water from the demand point during the standby state (YES), the process proceeds to step ST130. If it is determined that there is no request for pure water from the demand point during the standby state (NO), the process repeats step ST120.

  In step ST121, the control unit 30 starts driving the pressurizing pump 5. Specifically, when the control unit 30 outputs a current value signal (frequency command signal) to the inverter 6, the inverter 6 pressurizes the driving power converted into the frequency specified by the input current value signal. 5 is supplied. As a result, the pressurization pump 5 is driven at a rotational speed corresponding to the drive frequency input from the inverter 6.

  In step ST122, the controller 30 determines whether the pressure value of the second permeated water W4 flowing through the second permeated water line L3 falls below a predetermined pressure threshold (for example, 0.5 MPa) after the pressurization pump 5 is driven. Determine whether or not. If it is determined that the pressure value of the second permeated water W4 is below the pressure threshold (YES), the process proceeds to step ST130. If it is determined that the pressure value of the second permeated water W4 exceeds the pressure threshold value (NO), the process proceeds to step ST123, and after notifying the back pressure abnormality alarm, the process proceeds to step ST110. The abnormal back pressure refers to a state where the secondary pressure of the second RO membrane module 12 exceeds the pressure threshold so that the RO membrane is damaged. As a result, the user can recognize that an abnormality such as clogging of the EDI stack has occurred on the secondary side of the second RO membrane module 12.

  In step ST130, the control unit 30 starts executing the first step. Specifically, under the state where the third flow path switching valve 64 is set as the circulation side flow path, the control unit 30 returns the second permeated water W4 to the raw water tank 4 so that the first flow path switching valve is returned. 62 is switched to the circulation side flow path. In this state, the control unit 30 drives the pressurizing pump 5. As a result, the second permeated water W4 separated by the second RO membrane module 12 is returned to the raw water tank 4 via the second RO permeated water return line L7.

  In step ST140, the control unit 30 determines whether or not a first time (for example, 60 seconds) has elapsed since the execution of the first step was started. If it is determined that the first time has elapsed since the start of the first step (YES), the process proceeds to step ST150. If it is determined that the first time has not elapsed since the execution of the first process has started (NO), the process returns to step ST140 and the first process is continued.

  In step ST150, the control unit 30 determines that the electrical conductivity value (EC value) of the second permeated water W4 is a predetermined first conductivity threshold value (EC value) at the time when the first time has elapsed since the start of the first process. For example, it is determined whether it is less than 15 μS / cm). When it determines with the electrical conductivity value of the 2nd permeated water W4 exceeding a 1st conductivity threshold value (NO), a process progresses to step ST151, and after alert | reporting an alarm, it progresses to step ST160. When it is determined that the electrical conductivity value of the second permeated water W4 is lower than the first conductivity threshold value (YES), the process proceeds to step ST160 as it is.

  In step ST160, the control unit 30 starts executing the second process. Specifically, the control unit 30 switches the first flow path switching valve 62 to the water sampling side flow path, and sets the second flow path switching valve 63 to the circulation side flow so as to return the desalted water W6 to the raw water tank 4. Switch to the road. In this state, the control unit 30 drives the pressurizing pump 5. Thereby, the desalinated water W6 obtained in the EDI stack 20 is returned to the raw water tank 4 through the desalted water return line L9.

  As described above, the second permeated water W4 having poor water quality can be returned to the upstream side of the first RO membrane module 11 by performing the first step and the second step at the time of startup of the apparatus. Can be returned to the upstream side of the first RO membrane module 11. After step ST160, the process proceeds to step ST210.

  In step ST210 shown in FIG. 3, at the start of the second step, the control unit 30 sets the flow rates of the water flowing through the desalination chamber 21, the concentration chamber 22 and the electrode chamber 23 of the EDI stack 20 to a predetermined first level. It is determined whether or not the set value is exceeded. If it is determined that the flow rates of the water flowing through the desalination chamber 21, the concentration chamber 22 and the electrode chamber 23 of the EDI stack 20 exceed the predetermined first set values (YES), the process proceeds to step ST220. Transition. When it is determined that the flow rates of the water flowing through the desalination chamber 21, the concentration chamber 22, and the electrode chamber 23 of the EDI stack 20 do not exceed the predetermined first set values (NO), the process is performed in step ST211. Migrate to

  In step ST220, the control unit 30 sets the second time during which the flow rate of each of the water flowing through the desalination chamber 21, the concentration chamber 22 and the electrode chamber 23 of the EDI stack 20 exceeds a predetermined first set value (for example, 5 seconds) It is determined whether or not the operation has continued. If the time during which the flow rates of the water flowing through the desalination chamber 21, the concentration chamber 22 and the electrode chamber 23 of the EDI stack 20 exceed the predetermined first set values continues for the second time (YES), the process Proceed to ST230. When the time when the flow rate of the water flowing through the desalination chamber 21, the concentration chamber 22 and the electrode chamber 23 of the EDI stack 20 exceeds the predetermined first set value does not continue for the second time (NO), the process is performed as a step. Return to ST210.

  In step ST <b> 230, the control unit 30 transmits a command signal that causes the EDI stack 20 to output a DC voltage to the DC power supply device 33. Thereby, the EDI stack 20 is energized and the operation of the EDI stack 20 is started.

  If it is determined in step ST210 that the flow rates of the water flowing through the desalination chamber 21, the concentration chamber 22, and the electrode chamber 23 of the EDI stack 20 do not exceed the predetermined first set values (NO), step ST210 is performed. In ST211, the control unit 30 determines whether any of the flow rates of water flowing through the desalination chamber 21, the concentration chamber 22, and the electrode chamber 23 of the EDI stack 20 is below a predetermined second set value. To do. When it is determined that any one of the flow rates of the water flowing through the desalination chamber 21, the concentration chamber 22 and the electrode chamber 23 of the EDI stack 20 is below a predetermined second set value (YES), the processing is performed. The process proceeds to step ST212. When it is determined that any one of the flow rates of the water flowing through the desalination chamber 21, the concentration chamber 22 and the electrode chamber 23 of the EDI stack 20 does not fall below the predetermined second set value (NO), the processing is performed. Return to step ST210.

  In step ST212, the control unit 30 sets the time during which the flow rates of the water flowing through the desalination chamber 21, the concentration chamber 22, and the electrode chamber 23 of the EDI stack 20 are less than a predetermined second set value for a third time (for example, 10 seconds) It is determined whether or not the operation has been continued. When the time during which the respective flow rates of water flowing through the desalination chamber 21, the concentration chamber 22 and the electrode chamber 23 of the EDI stack 20 are lower than a predetermined second set value continues for a third time (YES), It progresses to step ST213. When the time during which the respective flow rates of the water flowing through the desalination chamber 21, the concentration chamber 22 and the electrode chamber 23 of the EDI stack 20 are less than the predetermined second set value does not continue for the third time (NO), It returns to step ST211.

  In step ST213, the control part 30 alert | reports the warning of abnormal flow from the alerting | reporting part 31. FIG. Thereafter, the process returns to step ST210.

  In step ST240, the control unit 30 determines whether or not a fourth time (for example, 60 seconds) has elapsed since the operation of the EDI stack 20 was started. If it is determined that the fourth time has elapsed since the operation of the EDI stack 20 was started (YES), the process proceeds to step ST250. If it is determined that the fourth time has not elapsed since the operation of the EDI stack 20 was started (NO), the process repeats step ST240.

  In step ST250, the control unit 30 determines that the electric conductivity (EC value) of the demineralized water W6 flowing through the demineralized water line L8 is a predetermined second when a fourth time has elapsed since the operation of the EDI stack 20 was started. It is determined whether or not a conductivity threshold value (for example, 1 μS / cm) is exceeded. When the electrical conductivity of the desalted water flowing through the desalted water line L8 is lower than the predetermined second conductivity threshold (YES), the process proceeds to step ST260. When the electrical conductivity of the desalted water W6 flowing through the desalted water line L8 exceeds a predetermined second conductivity threshold value (NO), the process proceeds to step ST251.

  In step ST260, the control unit 30 starts collecting pure water and supplies demineralized water W6 to a demand point or the like. Specifically, the control unit 30 switches the second flow path switching valve 63 to the water sampling side flow path so as to supply the desalted water W6 to the demand point. Thereby, the desalinated water W6 obtained by the EDI stack 20 is sent out to be supplied to the demand point via the desalted water line L8. Thereby, pure water sampling is performed toward the demand point.

  In step ST270, the control unit 30 determines whether or not there is a request to send pure water from the demand point during sampling. If it is determined that there is no request for pure water from the demand point during sampling (YES), the process proceeds to step ST110, and the pure water production apparatus 1 is in a standby state (that is, ends sampling). ) When it is determined that there is a request for pure water from the demand point during sampling (NO), the process proceeds to step ST280.

  In step ST280, the control part 30 determines whether the operation switch of the pure water manufacturing apparatus 1 is OFF (stop). When the operation switch of the pure water production apparatus 1 is OFF (stop) (YES), the operation of the pure water production apparatus 1 is stopped, and the process ends. When the operation switch of the pure water production apparatus 1 is ON (operation) (NO), the process returns to step ST270 and continues to collect pure water.

  When the electrical conductivity of the demineralized water W6 flowing through the demineralized water line L8 in step ST250 exceeds a predetermined second conductivity threshold value (NO), in step ST251, the control unit 30 notifies a water quality abnormality alarm. 31.

  In step ST252, the control unit 30 collects water (forcibly starts supply of demineralized water to the demand point), circulates (forcibly executes the circulation step consisting of the second step), and waits (for removal to the demand point). A selection screen for allowing the user to make a selection about the forced stop of the supply of salt water is displayed on the notification unit 31 or the input operation unit 32, and control is performed so that the input operation unit 32 can enter an input. Thereby, when the electrical conductivity of the desalted water W6 flowing through the desalted water line L8 exceeds a predetermined second conductivity threshold, the user selects any one of water sampling, circulation, and standby to produce pure water. The device 1 can be operated.

  In step ST253, the control unit 30 determines whether or not water sampling is selected on the selection screen displayed on the notification unit 31 or the input operation unit 32. When sampling is selected (YES), the process proceeds to step ST260 and starts sampling. When sampling is not selected (NO), the process proceeds to step ST254.

  In step ST254, the control unit 30 determines whether or not circulation is selected on the selection screen displayed on the notification unit 31 or the input operation unit 32. If circulation is selected (YES), the process proceeds to step ST230 and energizes the EDI stack 20. If circulation is not selected (NO), the process proceeds to step ST110, and the pure water production apparatus 1 enters a standby state.

  According to the pure water manufacturing apparatus 1 which concerns on this embodiment mentioned above, the following effects are show | played, for example.

  The pure water production apparatus 1 according to the present embodiment includes the first RO membrane module 11 and the second RO membrane module 12, the EDI stack 20, and the second permeated water W4 separated by the first RO membrane module 11 and the second RO membrane module 12. The second permeated water line L3 that circulates through the EDI stack 20, the desalted water line L8, the pressurizing pump 5 that discharges the raw water W1 toward the downstream side, and the second permeated water that circulates through the second permeated water line L3. A pressure sensor 52 that measures the pressure of W4, a notification unit 31 that notifies an alarm, and a pressure value of the second permeate W4 that flows through the second permeate line L3 after driving the pressurizing pump 5 is a predetermined pressure threshold. Is exceeded, it controls so that it may transfer to the standby state which does not supply demineralized water W6 to a demand location from the sampling state which supplies demineralized water W6 to a demand location, and alert | reports by the alerting | reporting part 31 is performed. And a control unit 30, a controlling so.

  Therefore, when the pressure value of the 2nd permeate water W4 which distribute | circulates the 2nd permeate water line L3 exceeds a predetermined pressure threshold value, it can be made to transfer to a standby state from a water sampling state. Thereby, when the back pressure of the 2nd RO membrane module 12 is high, it can be made to shift to a waiting state, and damage to the membrane of the 2nd RO membrane module 12 can be prevented. Moreover, even if the flow rate of the second permeated water W4 decreases with the increase in the back pressure of the second RO membrane module 12, generation of scale in the EDI stack 20 can be prevented. Furthermore, when the back pressure of the second RO membrane module 12 is high, the user can be made aware that an abnormality such as clogging of the EDI stack 20 has occurred. This can prompt the user to perform maintenance such as cleaning or replacement of the EDI stack 20.

  Further, in the present embodiment, when the pressure value of the second permeated water W4 flowing through the second permeated water line L3 after driving the pressurizing pump 5 is lower than a predetermined pressure threshold value, the control unit 30 The first step of returning the second permeated water W4 separated by the 2RO membrane module to the upstream side of the first RO membrane module 11 through the second RO permeated water return line L7 (first circulating water line) is performed. After the execution of the step, a second step of returning the desalted water W6 obtained in the EDI stack 20 to the upstream side of the first RO membrane module 11 through the desalted water return line L9 (second circulating water line) is executed.

  Therefore, when the pressure value of the 2nd permeate water W4 which distribute | circulates the 2nd permeate line L3 is less than a predetermined pressure threshold value, the 1st process and the 2nd process are performed, and the 2nd RO membrane module 12 The water quality of the second permeated water W4 can be recovered while returning the two permeated water W4 to the upstream side of the first RO membrane module 11, and the desalted water W6 from the EDI stack 20 is sent to the upstream side of the first RO membrane module 11. The water quality of the desalted water W6 can be recovered while returning it. Thereby, when the back pressure of the 2nd RO membrane module 12 is normal, the desalinated water W6 by which the water quality was recovered can be supplied to a demand location.

Moreover, in this embodiment, after the alerting | reporting by the alerting | reporting part 31 performs the alerting | reporting by the alerting | reporting part 31, when the alerting | reporting by the alerting | reporting part 31 is reset and there exists a water supply request | requirement of the desalted water W6, it will sample water from a standby state. Control to shift to the state.
Therefore, when the back pressure abnormality of the second RO membrane module 12 (abnormality of the pressure value of the second permeated water W4 is high) is notified, the user performs an operation for resetting the notification, whereby the pressure pump 5 Water can be promptly executed by shifting the state from the stopped state to the driven state.

  The preferred embodiments of the present invention have been described above. However, the present invention is not limited to the above-described embodiments, and can be implemented in various forms. For example, in the above-described embodiment, the reverse osmosis membrane module has a configuration in which the first RO membrane module 11 and the second RO membrane module 12 are arranged in two stages in series, but is not limited thereto. The reverse osmosis membrane module may be constituted by one stage of only the first RO membrane module 11.

  Moreover, in the said embodiment, in the process sequence of operation | movement of the pure water manufacturing apparatus 1, when the control part 30 determines with the pressure value of the 2nd permeated water W4 exceeding a pressure threshold value in step ST122 (NO). Although the control is made so as to shift to the standby state (step ST110) after notifying the back pressure abnormality alarm (step ST123), the present invention is not limited to this. When it is determined in step ST122 that the pressure value of the second permeated water W4 exceeds the pressure threshold value (NO), the control unit 30 performs control so as to notify an alarm of abnormal back pressure after shifting to the standby state. Alternatively, it may be controlled so that the transition to the standby state and the notification of the abnormal back pressure are performed at the same time.

DESCRIPTION OF SYMBOLS 1 Pure water manufacturing apparatus 5 Pressure pump 11 1st RO membrane module (reverse osmosis membrane module)
12 Second RO membrane module (reverse osmosis membrane module)
20 EDI stack (Electrodeionization stack)
30 Control unit 31 Notification unit (notification means)
52 Pressure sensor (pressure measuring means)
L1 Raw water line (supply water line)
L2 1st permeate line (permeate line)
L3 Second permeate line (permeate line)
L7 Second RO permeate return line (first circulating water line)
L8 Demineralized water line L9 Demineralized water return line (second circulating water line)
W1 Raw water (supply water)
W2 First permeate (permeate)
W4 Second permeated water (permeated water)
W6 Demineralized water

Claims (3)

A reverse osmosis membrane module for separating permeate from feed water;
An electrodeionization stack for obtaining desalted water by desalting the permeated water separated by the reverse osmosis membrane module;
A supply water line for distributing supply water to the reverse osmosis membrane module;
A permeate line for circulating permeate separated by the reverse osmosis membrane module to the electrodeionization stack;
A demineralized water line for sending demineralized water obtained in the electrodeionization stack toward a demand point;
A pressure pump that is provided in the supply water line and discharges the supply water toward the downstream side;
Pressure measuring means for measuring the pressure of the permeate flowing through the permeate line,
An informing means for informing the alarm;
When the pressure value of the permeate flowing through the permeate line exceeds the predetermined pressure threshold after the pressurization pump is driven , the pressurization pump is stopped from the sampling state where demineralized water is supplied to the demand point. Control to shift to a standby state in which demineralized water is not supplied to the demand point, and a control unit to control to execute notification by the notification unit;
A pure water production apparatus comprising: A first circulating water line for returning the permeated water separated by the reverse osmosis membrane module to the upstream side of the reverse osmosis membrane module;
A second circulating water line for returning demineralized water obtained in the electrodeionization stack to the upstream side of the reverse osmosis membrane module,
When the pressure value of the permeate flowing through the permeate line is lower than a predetermined pressure threshold after the pressurizing pump is driven, the control unit removes the permeate separated by the reverse osmosis membrane module. A first step of returning to the upstream side of the reverse osmosis membrane module through one circulating water line is performed, and further after the first step, demineralized water obtained in the electrodeionization stack is further recycled to the second circulation. The pure water manufacturing apparatus of Claim 1 which performs the 2nd process of returning to the upstream of the said reverse osmosis membrane module via a water line. The control unit performs control so as to shift from the standby state to the water sampling state when the notification by the notification unit is reset after the notification by the notification unit is executed and there is a request to supply demineralized water. The pure water manufacturing apparatus according to claim 1 or 2.

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