Classifications

• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F1/00—Treatment of water, waste water, or sewage
  • C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
  • C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F1/00—Treatment of water, waste water, or sewage
  • C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
  • C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
  • C02F1/46104—Devices therefor; Their operating or servicing
  • C02F1/46109—Electrodes
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F1/00—Treatment of water, waste water, or sewage
  • C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
  • C02F1/4602—Treatment of water, waste water, or sewage by electrochemical methods for prevention or elimination of deposits
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F1/00—Treatment of water, waste water, or sewage
  • C02F1/50—Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F1/00—Treatment of water, waste water, or sewage
  • C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
  • C02F1/4608—Treatment of water, waste water, or sewage by electrochemical methods using electrical discharges
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F1/00—Treatment of water, waste water, or sewage
  • C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
  • C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
  • C02F1/46104—Devices therefor; Their operating or servicing
  • C02F1/46109—Electrodes
  • C02F2001/46119—Cleaning the electrodes
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F1/00—Treatment of water, waste water, or sewage
  • C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
  • C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
  • C02F1/46104—Devices therefor; Their operating or servicing
  • C02F1/46109—Electrodes
  • C02F2001/46133—Electrodes characterised by the material
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
  • C02F2103/02—Non-contaminated water, e.g. for industrial water supply
  • C02F2103/023—Water in cooling circuits
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F2201/00—Apparatus for treatment of water, waste water or sewage
  • C02F2201/46—Apparatus for electrochemical processes
  • C02F2201/461—Electrolysis apparatus
  • C02F2201/46105—Details relating to the electrolytic devices
  • C02F2201/4612—Controlling or monitoring
  • C02F2201/46125—Electrical variables
  • C02F2201/46135—Voltage
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F2201/00—Apparatus for treatment of water, waste water or sewage
  • C02F2201/46—Apparatus for electrochemical processes
  • C02F2201/461—Electrolysis apparatus
  • C02F2201/46105—Details relating to the electrolytic devices
  • C02F2201/4612—Controlling or monitoring
  • C02F2201/46125—Electrical variables
  • C02F2201/4614—Current
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F2201/00—Apparatus for treatment of water, waste water or sewage
  • C02F2201/46—Apparatus for electrochemical processes
  • C02F2201/461—Electrolysis apparatus
  • C02F2201/46105—Details relating to the electrolytic devices
  • C02F2201/4616—Power supply
  • C02F2201/4617—DC only
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F2209/00—Controlling or monitoring parameters in water treatment
  • C02F2209/04—Oxidation reduction potential [ORP]

Definitions

• the present invention electrically converts scale components in cooling water circulating between a condenser and a cooling tower of an air conditioner used for cooling water and cooling equipment for offices and factories.
• the present invention relates to a purification device for circulating water to be removed.
• FIG. 9 is an explanatory diagram of an air conditioning system.
• the air conditioner 64 includes a compressor (not shown) that compresses the refrigerant gas, a condenser 66 that cools the compressed refrigerant gas to a refrigerant liquid with cooling water, and the refrigerant liquid is an expansion valve. And an evaporator (not shown) flowing in under reduced pressure.
• the condenser 66 In order to cool the refrigerant flowing in the condenser 66, the condenser 66 is provided in the cooling tank 70.
• the cooling tower 68 for circulating and supplying cooling water to the cooling tank 70 has a cylindrical tower main body 72 and a water receiving tank 74 provided in the lower part thereof, and the water receiving tank 74 and the cooling tank 70 are supplied with piping. The circulating water in the water receiving tank 74 is sent to the cooling tank 70.
• a packed body 78 having a large number of passages through which circulating water and cooling air flow is incorporated in the tower main body 72.
• a spray nozzle 80 is attached to the tower main body 72, and the spray nozzle 80 is connected to the cooling tank 70 by a piping 82 and is connected to the inside of the cooling tank 70.
• the circulating water is supplied to the spray nozzle 80 by a circulation pump 84 provided in the supply pipe 76! /.
• the circulating water sprayed from the spray nozzle 80 onto the filler 78 flows through a number of passages formed in the filler 78 and falls into the water receiving tank 74.
• the cooling tower 68, the cooling tank 70, the supply pipe 76 connecting them, and the return pipe 82 form a circulation water channel through which water circulates, and water flows through the circulation water channel by driving the circulation pump 84. It will be.
• a blower 86 is provided in the tower main body 72, and after the lower force flows into the tower main body 72 by the blower 86, the air flow flows backward through the passage in the packing 78. Is formed. As a result, the circulating water is directly contacted with the air to exchange heat and is cooled by the latent heat of evaporation of the circulating water. In order to replenish the circulating water reduced by the evaporation of the circulating water, the tower body 72 is replenished with cooling water via a replenishing pipe 90 opened and closed by a float 88.
• the cooling tower 68 cools the circulating water for cooling by using the latent heat of evaporation of water as described above, the circulating water is constantly evaporated in the cooling tower 68.
• tap water and groundwater used as the circulating water of the cooling tower 68 contain metal ions such as calcium ion, magnesium ion and dissolved silica.
• tap water and groundwater are constantly replenished to the circulating water that has decreased due to evaporation.
• the concentration of metal ions contained in the circulating water gradually increases.
• the electrical conductivity of the tap water initially supplied is 100-200 SZcm force, which rises more than 1 000 / z SZcm in a few days to a week.
• These metal ions aggregate to form a scale that adheres to the heat exchange surface of the condenser 66 and reduces the heat exchange efficiency.
• Increasing distribution resistance caused problems.
• the purification device power that electrolyzes the circulating water and electrically removes the metal ions in the circulating water is disclosed. — 18982, JP 61-181591, JP 58-35400, JP 2001-137891, JP 9-103797, JP 2001-137858, JP 9-38668, JP 11-114335, etc. Various proposals have been made!
• a purification apparatus for example, an electrode plate unit having an electrode plate opposed to each other is placed in an electrolytic purification tank, the circulating water is guided into the electrolytic purification tank, and positive and negative voltages are applied to each electrode plate.
• a purification device has been proposed in which metal ions contained in circulating water are deposited as a scale on the surface of the electrode plate on the negative electrode side to remove metal ions from the circulating water.
• Patent Document 1 Japanese Patent Laid-Open No. 2001-259690
• Patent Document 2 Japanese Patent Laid-Open No. 4-18982
• Patent Document 3 Japanese Patent Application Laid-Open No. 61-181591
• Patent Document 4 JP-A-58-35400
• Patent Document 5 JP 2001-137891
• Patent Document 6 Japanese Patent Laid-Open No. 9-103797
• Patent Document 7 Japanese Patent Laid-Open No. 2001-137858
• Patent Document 8 Japanese Patent Laid-Open No. 9-38668
• Patent Document 9 JP-A-11-114335
• this type of purifier uses an expensive precious metal material such as Pt as an electrode plate, or uses a material that quickly depletes, such as Al, SUS, or Fe. There was also a problem that it was expensive and maintenance costs were very high.
• the present invention eliminates the troublesome cleaning work of removing the electrode plate from the electrolytic cleaning tank and removing the scale in the electrolytic cleaning tank from the cost of maintenance as much as possible. It is an object of the present invention to provide a method and an apparatus for purifying circulating water.
• circulating water to be purified is passed between opposing electrode plates, a voltage is applied between the electrode plates, and metal ions in the circulating water are removed from the negative electrode plate.
• the circulating water is purified by electrolytic deposition.
• a titanium plate is used as the electrode plate.
• the voltage applied to the anodic acid coating formed on the surface of the positive electrode plate of the electrode plates is increased to forcibly break down the anodic oxide coating, and a desired amount is obtained. Let the current flow.
• the polarity of the voltage applied between the electrode plates may be switched every predetermined time.
• the applied voltage is reduced by passing a constant current against the formation of the anodic acid coating. You may make it raise.
• the current flowing between the electrode plates is preferably 0.1 to 20 A per unit area (lm 2 ) of the positive electrode plate. This is because if the current is less than 0.1 lAZm 2 , the circulating water cannot be sufficiently purified, and if it exceeds 20 AZm 2 , the electrode plate corrodes quickly and becomes unusable.
• the electrical conductivity of the circulating water is higher than a predetermined value, the current flowing between the electrode plates is increased, and if the electrical conductivity of the circulating water is lower than the predetermined value, the electrode Try reducing the current flowing between the plates! ⁇ .
• the predetermined value of the electric conductivity of the circulating water is preferably ⁇ to 500-1000 ⁇ S / cm! / ⁇ .
• the redox potential of the circulating water is higher than a predetermined value, the current flowing between the electrode plates is increased, and when the redox potential of the circulating water is lower than the predetermined value, the electrode Try to reduce the current flowing between the plates! ⁇ .
• the predetermined value of the redox potential of the circulating water is preferably +100 to 1 lOOmV! /.
• the circulating water purifying apparatus comprises a purifying tank that receives and discharges the circulating water to be purified, one or more first electrode plates installed in the purifying tank, A DC voltage is applied between the first electrode plate and the second electrode plate, and one or more second electrode plates installed in the purification tank at a predetermined interval from the first electrode plate. DC power supply.
• each of the first electrode plate and the second electrode plate is made of a titanium plate
• the DC power supply device is an anodic oxide film formed on the surface of the first electrode plate or the second electrode plate. DC power supply power that outputs a voltage that peels off and removes them by insulation breakdown.
• the circulating water purifier further includes a polarity switching device that switches the polarity of the voltage applied from the DC power supply device to the first electrode plate and the second electrode plate every predetermined time. Well, okay.
• the circulating water purifier may use a constant current power supply as the DC power supply.
• the constant current power supply device has the ability to flow a constant current of 0.1 to 20 A per unit area (lm 2 ) of either one of the electrode plates serving as a positive electrode between the first electrode plate and the second electrode plate Is preferred.
• the circulating water purifier is an electrical conductivity measuring the electrical conductivity of the circulating water. And the electrical conductivity obtained by the electrical conductivity meter is higher than a predetermined value, the output voltage of the DC power supply device is increased to increase the current flowing between the electrode plates, and the electrical conductivity When the electrical conductivity obtained by the conductivity meter is lower than a predetermined value, a current control device may be provided to reduce the current flowing between the electrode plates by lowering the output voltage of the DC power supply device.
• the purification apparatus for circulating water includes an oxidation-reduction potentiometer that measures the oxidation-reduction potential of the circulating water, and a redox potential obtained by the oxidation-reduction potentiometer that is higher than a predetermined value. If the redox potential obtained by the redox potentiometer is lower than a predetermined value by increasing the output voltage of the direct current power supply device to increase the current flowing between the electrode plates, the direct current power supply device A current control device is provided which reduces the current flowing between the electrode plates by lowering the output voltage.
• the predetermined value of the oxidation-reduction potential of the circulating water it is preferable to employ +100 to 1 lOOmV, more desirably 50 to OmV.
• the anodic acid coating formed on the surface of the positive electrode plate is forced to break down, and an amount of current necessary to remove the scale component is generated by the anodic oxide coating. Since it flows in the circulating water against the formation of water, the scale components in the circulating water are efficiently removed, and the circulating water is maintained within the desired electric conductivity range.
• the case component attached and generated on the surface of the electrode plate works. Since it is removed maintenance-free without any removal work by the operator, it can be effective if the maintenance cost is low.
• both the opposing electrode plates do not consume only one side of the opposing electrode plates.
• the expensive titanium plate can be used effectively.
• the electric current flowing between the electrode plates is increased when the electrical conductivity of the circulating water becomes higher than a predetermined value, the anode generated on the surface of the positive electrode plate The oxide film is forced to break down, and the amount of current necessary to remove the scale component flows through the circulating water against the formation of the anodic acid coating, effectively removing the scale component in the circulating water.
• the electric current flowing between the electrode plates is reduced when the electrical conductivity of the circulating water becomes lower than a predetermined value, the consumption of the electrode plates can be suppressed.
• the surface of the positive electrode plate is increased.
• the generated anodic acid coating is forced to break down, and the amount of current necessary to remove scale components flows through the circulating water against the formation of the anodic acid coating, and the scale in the circulating water If the components are removed efficiently and the current flowing between the electrode plates is reduced when the acid reduction potential of the circulating water is lower than the predetermined value, the consumption of the electrode plates is suppressed! Has a ⁇ ⁇ effect.
• FIG. 1 is an explanatory view of a cooling tower circulating water purifier according to an embodiment of the present invention
• FIG. 2 is an explanatory view of an electrode plate unit used in the purifier of FIG. .
• reference numeral 10 denotes a purification apparatus.
• the purification apparatus 10 includes an electrolytic purification tank 12, an electrode plate unit 14 accommodated in the electrolytic purification tank 12, and a direct current to the electrode plate unit 14. And a DC power supply device 16 for supplying a current.
• the electrolytic septic tank 12 is a box-like container, and is removed from a water receiving tank 74 of a cooling tower 68 (to be described later) via a water supply pump 20 at a position close to the side of the electrolytic septic tank 12 at the bottom 18 of the electrolytic septic tank 12.
• a water supply port 22 for receiving circulating water is provided.
• the size (capacity) of the electrolytic septic tank 12 and the feed water pump 20 is made according to the size (capacity) of the cooling tower 68.
• the electrode plate unit 14 includes a plurality of first electrode plates 24 and a plurality of second electrode plates 26.
• the first electrode plates 24 and the second electrode plates 26 are alternately arranged in parallel at predetermined intervals. Has been placed.
• the size of the electrode plate unit 14 is made according to the size (capacity) of the target cooling tower.
• the first electrode plate 24 of the electrode plate unit 14 is connected to the positive output terminal of the DC power supply device 16, and the second electrode plate 26 is connected to the negative output terminal of the DC power supply device 16.
• the DC power supply 16 has a stable DC power supply capable of supplying a current of about 0.1 to 20 A per unit area [m 2 ] of the first electrode plate 24.
• the two parallel overflow partitions 30 are slightly shifted up and down in a place opposite to the water supply port 22. It is installed approximately vertically with a predetermined interval.
• an outlet 32 for allowing the purified circulating water to flow out is provided at an upper position on the side where the overflow partition 30 is provided.
• an electrical conductivity meter 34 for measuring the electrical conductivity of the circulating water is installed near the outlet 32, and the electrical conductivity meter 34 is Connected to the alarm device 38, the alarm lamp 40 lights up or the alarm buzzer 42 sounds when the electrical conductivity of the circulating water exceeds the predetermined value.
• a float switch 36 is installed in the upper part of the electrolytic septic tank 12, and the float switch 36 accumulates a scale in the filtration part 60 of the receiving tank 44, which acts as a resistance to the flow of the treated water, and from the electrolytic septic tank 12.
• Alarm lamp 40 lights up and alarm buzzer 42 sounds when discharge is obstructed
• a receiving tank 44 for temporarily storing the circulated water purified in the electrolytic cleaning tank 12 is provided below the electrolytic cleaning tank 12, and the outlet 32 is received via the outflow pipe 46. Connected to tank 44.
• a return pump 48 for returning the purified circulating water in the receiving tank 44 to the cooling tower 68 is installed in the vicinity of the receiving tank 44, and the return pump 48 is installed in the receiving tank 44 when the received circulating water exceeds a predetermined height.
• a float switch 50 is provided to operate 48 and return the circulating water in the receiving tank 44 to the cooling tank 68.
• a discharge port 52 for discharging the peeled scale is provided near the center of the bottom 18 of the electrolysis tank 12 so that the bottom 18 of the electrolysis tank 12 is lowered toward the discharge 52.
• the inclination angle is in the range of 25 to 35 degrees.
• the discharge device 54 On the back side of the bottom 18 of the electrolytic septic tank 12, there is a discharge device at the part where the discharge port 52 is provided. A device 54 is provided facing downward.
• the discharge device 54 includes a discharge valve 56 which is an opening / closing device, and the discharge valve 56 is controlled by a discharge timer 58 for opening and closing timing and time.
• the outlet side of the discharge device 54 is open without being connected to another pipe, and the scale discharged together with the circulating water is separated on the receiving tank 44 directly below the discharge device 54.
• a filtration unit 60 is provided.
• the discharge capacity of the discharge device 54 is such that the maximum flow rate of water that is discharged when the discharge tank 56 is fully opened and the water is placed in the electrolytic purification tank 12 to a predetermined height is 30 liters Z It has become more than minutes.
• FIG. 3 is an explanatory diagram of an air conditioning system incorporating the purifier of FIG. 1
• FIG. 4 is an explanatory diagram of the control mechanism of the cooling tower circulating water purifier according to one embodiment of the present invention. is there.
• the supplied circulating water immerses the electrode plate unit 14 passes through the overflow partition 30, overflows from the outlet 32 to the outside of the electrolytic purification tank 12, and enters the receiving tank 44.
• the float switch 50 of the receiving tank 44 is set so that the switch enters at a predetermined height, and when the amount of circulating water in the receiving tank 44 reaches the set height, the float switch 50 enters and the return pump 48 is activated, and the circulating water that has entered the receiving tank 44 is returned to the water receiving tank 74 of the cooling tower 68 by the return pump 48.
• a DC constant current power supply device is used as the DC power supply device 16, and when a constant current is passed between the first electrode plate 24 and the second electrode plate 26, An anodized film is formed on the surface of the one electrode plate 24, and the resistance value of the surface of the first electrode plate 24 increases.
• the resistance value increases, the voltage applied to the anodic oxide film on the surface of the first electrode plate 24 increases in proportion to the resistance value, and the anodic oxide film on the surface of the first electrode plate 24 breaks down. The oxide film is peeled off from the first electrode plate 24, and the resistance value of the surface of the first electrode plate 24 decreases.
• an operating time and a holding time are set in advance in the discharge timer 58, and after the preset operation time has elapsed, the discharge valve 56 is opened by the discharge timer 58, and the inside of the electrolytic septic tank 12 The accumulated water accumulates on the bottom 18 and is discharged through the discharge device 54 together with the scale.
• the discharged scale of the circulating water is filtered and removed by the filtration unit 60, and the circulating water enters the receiving tank 44.
• the discharge valve 56 is closed, and the circulating water begins to accumulate again in the electrolytic tank 12.
• the scale remaining in the filtration unit 60 is sequentially removed and removed when it accumulates to some extent.
• the electrical conductivity meter 34 installed near the outlet of the electrolytic septic tank 12 constantly measures the electrical conductivity of the circulating water, and the electrical conductivity of the circulating water exceeded the set value. In this case, the alarm device 38 is activated, the alarm lamp 40 is lit, and the alarm buzzer 42 sounds.
• the float switch 36 in the upper part of the electrolytic septic tank 12 monitors that the scale accumulates in the filtration part 60 of the receiving tank 44 and becomes the resistance of the treated water flow, and the resistance becomes a predetermined value or more. If the water level rises, the float switch 36 senses, the alarm lamp 40 lights, and the alarm buzzer 42 sounds.
• Circulating water of the cooling tower of 120 refrigeration tons was extracted from the circulation path, purified through the apparatus of the present invention, and returned to the circulation path after purification.
• the electrode plate unit 14 of the device of the present invention there were used 72 titanium plates each having a width of 300 mm, a height of 600 mm, and a thickness of 1 mm, each facing 36 plates at a pitch of 24 mm.
• the DC power supply 16 used a DC constant current power supply, and supplied a constant current of 6 A from the DC power supply 16 to the electrode plate unit 14.
• the conductivity of the circulating water at this time was initially 1000 SZcm as shown in FIG. 6, but gradually decreased and stabilized at 700 to 850 / z SZcm. Also, as shown in Fig. 6, the oxidation-reduction potential gradually decreased from the initial force of 470 mV and stabilized at -60 mV.
• a muddy substance deposited on the bottom of the electrolytic cell was analyzed, and as a result, it was mainly composed of silica, calcium, magnesium, and dielectrically oxidized titanium oxide.
• the value was increased or decreased. That is, when the electrical conductivity exceeded 1000 SZcm, the current was increased approximately twice, and when the electrical conductivity was less than 700 SZcm, the current was returned to the original value.
• 1040 SZ cm is 690 ⁇ S / cm when the current is increased approximately twice
• 690 ⁇ S / cm is 810 ⁇ S / cm when the current is restored to the original value. Increased to. From this result, it is understood that the target performance can be controlled by increasing or decreasing the current supplied to the electrode plate unit 14.
• the scale component in the circulating water was efficiently removed.
• the electrical conductivity is within the allowable range, it is not necessary to pass an unnecessary current, so that the power cost is saved and unnecessary corrosion and consumption of the electrode plate are prevented.
• Example 4 As in Example 4, a redox potential meter that measures the redox potential of circulating water and a constant current power supply device were used, depending on the level of the redox potential obtained by the redox potential meter. The amount of current supplied to the electrode plate unit 14 was increased. That is, when the redox potential exceeded 200 mV, the current was increased by 100%. As a result, as shown in Fig. 8, 280mV decreased to -60mV when increased by 100%. This result shows that the target performance can be controlled by increasing or decreasing the current supplied to the electrode plate unit 14.
• a DC constant current power supply is used as the DC power supply, but a DC constant voltage power supply may be used as the DC power supply.
• the current value flowing between the electrode plates is monitored by an ammeter (not shown), and the power supply voltage is changed to a high value when the current value falls below a predetermined value.
• the power supply voltage is changed to a high value, the anodic oxide film on the surface of the electrode plates breaks down and peels off, reducing the resistance between the electrode plates.
• the present invention is applicable not only to purification of circulating water in a cooling tower, but also to purification water such as 24-hour bath circulating water, pool circulating water, and artificial pond circulating water.
• FIG. 1 is an explanatory diagram of a cooling tower circulating water purifier according to an embodiment of the present invention.
• FIG. 2 is an explanatory diagram of an electrode plate unit used in the purification apparatus shown in FIG.
• FIG. 3 is an explanatory diagram of an air conditioning system in which the purification apparatus of FIG. 1 is inserted.
• FIG. 4 is an explanatory diagram of a control mechanism of the cooling tower circulating water purifier according to the embodiment of the present invention.
• FIG. 5 is a graph showing the relationship between the voltage applied between the electrode plates, electrical conductivity, and redox potential.
• FIG. 6 is a graph showing changes in electrical conductivity and oxidation-reduction potential due to increase / decrease in voltage.
• FIG. 7 is a graph showing the relationship between the magnitude of current density (AZm 2 ) and the rate of decrease in electrical conductivity ( ⁇ S / cm).
• FIG. 8 is a graph showing changes in electrical conductivity and redox potential due to increase / decrease in current.
• FIG. 9 is an explanatory diagram of an air conditioning system.

Landscapes

• Chemical & Material Sciences (AREA)
• Life Sciences & Earth Sciences (AREA)
• Hydrology & Water Resources (AREA)
• Engineering & Computer Science (AREA)
• Environmental & Geological Engineering (AREA)
• Water Supply & Treatment (AREA)
• Organic Chemistry (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Electrochemistry (AREA)
• General Chemical & Material Sciences (AREA)
• Water Treatment By Electricity Or Magnetism (AREA)

Priority Applications (4)

Applications Claiming Priority (2)

Related Child Applications (1)

Publications (1)

Family

ID=36991401

Family Applications (1)

Country Status (6)

Cited By (6)

Families Citing this family (19)

Citations (4)

Family Cites Families (17)

• 2005
  • 2005-03-16 JP JP2005074243A patent/JP4126307B2/ja not_active Expired - Lifetime
  • 2005-04-25 KR KR1020077021056A patent/KR100920989B1/ko not_active Expired - Fee Related
  • 2005-04-25 CN CN201210298567.2A patent/CN102786149B/zh not_active Expired - Fee Related
  • 2005-04-25 US US11/886,412 patent/US7901620B2/en not_active Expired - Fee Related
  • 2005-04-25 CN CN2005800483260A patent/CN101124167B/zh not_active Expired - Fee Related
  • 2005-04-25 WO PCT/JP2005/007781 patent/WO2006098041A1/ja not_active Ceased
  • 2005-04-25 EP EP05734548.0A patent/EP1860071B1/en not_active Ceased
• 2011
  • 2011-01-06 US US12/985,954 patent/US8349190B2/en not_active Expired - Fee Related

Patent Citations (4)

Non-Patent Citations (1)

Also Published As

Similar Documents

Legal Events