WO1994020420A1 - Improvements to ionic disinfection systems - Google Patents

Improvements to ionic disinfection systems Download PDF

Info

Publication number
WO1994020420A1
WO1994020420A1 PCT/GB1994/000488 GB9400488W WO9420420A1 WO 1994020420 A1 WO1994020420 A1 WO 1994020420A1 GB 9400488 W GB9400488 W GB 9400488W WO 9420420 A1 WO9420420 A1 WO 9420420A1
Authority
WO
WIPO (PCT)
Prior art keywords
electrodes
voltage
ratio
level
power supply
Prior art date
Application number
PCT/GB1994/000488
Other languages
French (fr)
Inventor
John Hayes
Original Assignee
Tarn Pure Technology Corp.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Tarn Pure Technology Corp. filed Critical Tarn Pure Technology Corp.
Priority to EP94909194A priority Critical patent/EP0691936A1/en
Publication of WO1994020420A1 publication Critical patent/WO1994020420A1/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/4606Treatment of water, waste water, or sewage by electrochemical methods for producing oligodynamic substances to disinfect the water

Definitions

  • the present invention relates to ionic disinfection systems.
  • a number of systems have been developed that are designed to release copper and/or silver ions into a liquid eg. water for disinfection, and it has been seen that some systems are less effective than others in controlling the growth of algae and/or bacteria. From experience, it has been shown that the voltage applied to the emitting electrodes determines the form of copper released into solution, namely that, at higher voltages, cupric (Cu2) copper is released and at lower voltages cuprous (Cul) copper is released. Cupric (Cu2) has two electrons missing whereas cuprous (Cul) has one missing.
  • the present invention contains circuitry that maintains a voltage on the electrodes so that cupric (Cu2) copper is released.
  • control is obtained by providing a pulsating output and adjusting the mark/space ratio or on/off time of the output. For instance, it is proposed that the polarity of the voltage applied to the electrodes will be reversed at periodic intervals eg. 30 sees to avoid plating out problems.
  • the number of seconds that current will flow may be set between 1 and 30 seconds in each direction thus allowing full control of output, but maintaining full voltage and ensuring cupric (Cu2) ions are released.
  • a further development may be included to control, other than manually, the mark/space ratio or on/off time by sensing the flow of current between the electrodes in a manner that should the current be reduced the 'on 1 ratio is increased and conversely if the current increases the 'on' time is reduced, thus maintaining a constant level of ion release.
  • Fig. 1 is a block diagram of an ionic disinfection system according to the present invention
  • Fig. 2 is a block diagram of a modified form of ionic disinfection system according to the present invention.
  • Fig. 3 is a graph for aiding understanding of the operation of a part of the system shown in Fig. 2.
  • an ionic disinfection system comprises a power supply 10 for producing a stabilized DC output voltage at a pre-settable level from a mains supply.
  • the output voltage from the power supply 10 is applied to two or more electrodes 12 via a polarity switching module 14 which periodically reverses the polarity of the output from the power s ⁇ pply.
  • the power supply operates on either 110/240v 50/60HZ.
  • Output - low voltage depending on size of system may be between 15-50v.
  • the nominal output may be 30v.
  • Preset adjustment allows, say, lOv higher or lower (tapped transformer) to compensate for water or liquid conductivity. If conductivity is high, current may be excessive therefore voltage may have to be dropped or electrodes spaced further apart. Conversely, with low conductivity, maximum voltage is required to obtain sufficient current or electrodes may need to be placed closer to each other. (Obviously more, or larger, electrodes can be fitted to increase current).
  • the power supply will vary in size depending on the amount of current required.
  • the electrodes can be of copper and/or silver and if both copper and silver are present the ratio of the two metals can be varied depending on the size of system being constructed and the water being treated. It is also possible to replace all or part of the silver content by another noble metal such as gold or platinum. This has been found to be efficacious where a high level of chlorides are present in the liquid to be treated eg. brine or salt water. Under these conditions it has been found that silver ions form silver chloride which is only partly soluble, thus reducing the efficacy of the silver content.
  • a mark/space ratio module 16 Connected to the switching module 14 is a mark/space ratio module 16 provided with a ratio control device 17 whereby the output of the switching module 14 can be inhibited for a period of time so as to produce a pulsating output the on time of which is adjustable to vary the time average of current supplied to the electrodes 12 at the then prevailing polarity and preset voltage.
  • the switching module 14 feeds the power to electrodes 12 and contains silicon controlled rectifiers which reverse the output polarity to the electrodes. This is triggered by the polarity and mark/space ratio timing circuit 16.
  • the mark/space or on/off ratio is controlled by a potentiometer that will set the 'on' time during each polarity reversal. For instance, if the polarity is switched ever 30 seconds, the control will allow power to flow from 1 to 30 seconds depending on the setting of the control. Therefore, at full output, current will flow for a full 30 seconds, then polarity will be reversed and full output for another 30 seconds. If half output is required, the current will flow 15 seconds in every 30 seconds.
  • the ratio control device 17 in the form of a potentiometer can manually adjustable and form the only adjustment of the mark/space ratio of the pulses. Additionally, it is possible to use the device 17 simply as an initial setting device and incorporate a feedback loop 20 incorporating a resistance coupled to one of the electrodes for feeding back to the mark/space ratio module 16 a signal representative of the current flowing in the electrodes so that if the conductivity of the liquid in which the electrodes are immersed changes, the on/off ratio will be adjusted automatically.
  • Fig. 2 shows an arrangement similar to Fig. 1 and in which like parts are indicated by like reference numbers.
  • the current detection in the feedback loop is achieved by an inductive loop 21.
  • Fig. 3 shows the relationship between current flowing in the electrodes sensed by the feedback device and the on time or pulse width for both the arrangements shown in Figs. 1 and 2. If the conductivity of the water changes the on/off ratio will automatically adjust ie. if current drops, the 'on' time or pulse width will be lengthened to maintain the average current and the desired level. Conversely, if the current increases the unit will produce a shorter pulse of current.
  • the level of currents output from the power supply can very depending on a number of factors such as the conductivity of the liquid. Typically, currents of the order of hundreds of milliamps will be used but it is possible for currents of 1 amp or more to occur.
  • the power supply should be chosen to have a sufficient capacity to allow the supply of power at an appropriate current level for the application to which the apparatus is put.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General 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)
  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

An ionic disinfection system comprises a chamber through which liquid e.g. water to be disinfected is arranged to pass. Electrodes of copper and a noble metal such as silver are dispersed in the chamber and a DC power supply is connected to the electrodes. The voltage of the power supply is set at a level to ensure production of cupric (Cu2) ions and adjustment to the level of dosing the liquid with ions is achieved by providing a pulsating output from the power supply with an adjustable on/off ratio.

Description

Improvements to Ionic Disinfection Systems
The present invention relates to ionic disinfection systems.
A number of systems have been developed that are designed to release copper and/or silver ions into a liquid eg. water for disinfection, and it has been seen that some systems are less effective than others in controlling the growth of algae and/or bacteria. From experience, it has been shown that the voltage applied to the emitting electrodes determines the form of copper released into solution, namely that, at higher voltages, cupric (Cu2) copper is released and at lower voltages cuprous (Cul) copper is released. Cupric (Cu2) has two electrons missing whereas cuprous (Cul) has one missing.
It has been shown that there is a synergistic effect, increasing the efficacy, when silver and copper ions are released together. Efficacy is further enhanced if the copper is released in its cupric (Cu2) form and brings about a greater attraction to the targeted organisms.
Commercial equipment must have the ability to increase or decrease the number of ions released so that the correct level is obtained, depending on the amount of water or liquid to be treated. Previously the method of achieving control was to vary the applied voltage to the electrodes thus setting the desired current. The disadvantage of this is that it is not possible to apply the full voltage to the electrodes if the output has to be reduced, thus a system running at half output would be running at half voltage. Where water conductivity is high, maximum current is reached at a reduced voltage, thus cuprous (Cul) ions are released.
The present invention contains circuitry that maintains a voltage on the electrodes so that cupric (Cu2) copper is released. To allow adjustment to the level of dosing, instead of varying the applied voltage, control is obtained by providing a pulsating output and adjusting the mark/space ratio or on/off time of the output. For instance, it is proposed that the polarity of the voltage applied to the electrodes will be reversed at periodic intervals eg. 30 sees to avoid plating out problems. To adjust or set the output of ions to the desired level, the number of seconds that current will flow may be set between 1 and 30 seconds in each direction thus allowing full control of output, but maintaining full voltage and ensuring cupric (Cu2) ions are released.
A further development may be included to control, other than manually, the mark/space ratio or on/off time by sensing the flow of current between the electrodes in a manner that should the current be reduced the 'on1 ratio is increased and conversely if the current increases the 'on' time is reduced, thus maintaining a constant level of ion release.
Features and advantages of the present invention will become apparent from the following description of embodiment thereof given by way of example with reference to the accompanying drawings, in which:-
Fig. 1 is a block diagram of an ionic disinfection system according to the present invention;
Fig. 2 is a block diagram of a modified form of ionic disinfection system according to the present invention; and
Fig. 3 is a graph for aiding understanding of the operation of a part of the system shown in Fig. 2.
As shown in Fig. 1, an ionic disinfection system comprises a power supply 10 for producing a stabilized DC output voltage at a pre-settable level from a mains supply. The output voltage from the power supply 10 is applied to two or more electrodes 12 via a polarity switching module 14 which periodically reverses the polarity of the output from the power sμpply.
The power supply operates on either 110/240v 50/60HZ. Output - low voltage depending on size of system may be between 15-50v. For example, for a specific model, the nominal output may be 30v. Preset adjustment allows, say, lOv higher or lower (tapped transformer) to compensate for water or liquid conductivity. If conductivity is high, current may be excessive therefore voltage may have to be dropped or electrodes spaced further apart. Conversely, with low conductivity, maximum voltage is required to obtain sufficient current or electrodes may need to be placed closer to each other. (Obviously more, or larger, electrodes can be fitted to increase current). Also note the power supply will vary in size depending on the amount of current required.
The electrodes can be of copper and/or silver and if both copper and silver are present the ratio of the two metals can be varied depending on the size of system being constructed and the water being treated. It is also possible to replace all or part of the silver content by another noble metal such as gold or platinum. This has been found to be efficacious where a high level of chlorides are present in the liquid to be treated eg. brine or salt water. Under these conditions it has been found that silver ions form silver chloride which is only partly soluble, thus reducing the efficacy of the silver content.
Connected to the switching module 14 is a mark/space ratio module 16 provided with a ratio control device 17 whereby the output of the switching module 14 can be inhibited for a period of time so as to produce a pulsating output the on time of which is adjustable to vary the time average of current supplied to the electrodes 12 at the then prevailing polarity and preset voltage.
The switching module 14 feeds the power to electrodes 12 and contains silicon controlled rectifiers which reverse the output polarity to the electrodes. This is triggered by the polarity and mark/space ratio timing circuit 16. The mark/space or on/off ratio is controlled by a potentiometer that will set the 'on' time during each polarity reversal. For instance, if the polarity is switched ever 30 seconds, the control will allow power to flow from 1 to 30 seconds depending on the setting of the control. Therefore, at full output, current will flow for a full 30 seconds, then polarity will be reversed and full output for another 30 seconds. If half output is required, the current will flow 15 seconds in every 30 seconds.
If desired, the ratio control device 17 in the form of a potentiometer can manually adjustable and form the only adjustment of the mark/space ratio of the pulses. Additionally, it is possible to use the device 17 simply as an initial setting device and incorporate a feedback loop 20 incorporating a resistance coupled to one of the electrodes for feeding back to the mark/space ratio module 16 a signal representative of the current flowing in the electrodes so that if the conductivity of the liquid in which the electrodes are immersed changes, the on/off ratio will be adjusted automatically.
Fig. 2 shows an arrangement similar to Fig. 1 and in which like parts are indicated by like reference numbers. Here, the current detection in the feedback loop is achieved by an inductive loop 21.
Fig. 3 shows the relationship between current flowing in the electrodes sensed by the feedback device and the on time or pulse width for both the arrangements shown in Figs. 1 and 2. If the conductivity of the water changes the on/off ratio will automatically adjust ie. if current drops, the 'on' time or pulse width will be lengthened to maintain the average current and the desired level. Conversely, if the current increases the unit will produce a shorter pulse of current.
The voltages and times specified above are by way of example of typical values which may be encountered in practice. However, variations in voltage, current and time as well as number and spacing of electrodes are permissible depending on the exact use to which the system is being put.
The level of currents output from the power supply can very depending on a number of factors such as the conductivity of the liquid. Typically, currents of the order of hundreds of milliamps will be used but it is possible for currents of 1 amp or more to occur. The power supply should be chosen to have a sufficient capacity to allow the supply of power at an appropriate current level for the application to which the apparatus is put.

Claims

CLAIMS :
1. An ionic disinfection system comprising a chamber through which liquid to be disinfected is arranged to pass, electrodes disposed within the chamber and containing a proportion of copper and a DC power supply connected to the electrodes for causing copper ions to be discharged, in use into the liquid, characterised in that a voltage source of the power supply is fixed at a level high enough to cause cupric ions to be discharged and means are provided for producing pulses of said voltage to cause periodic discharge of cupric ions.
2. A system according to claim 1, wherein the pulse producing means is a switching circuit for periodically connecting the voltage source to the electrodes.
3. A system according to claim 2, wherein the on/off ratio of the switching circuit is changeable.
4. A system according to claim 3, wherein the switching means is provided with manual means for changing the on/off ratio.
5. A system according to claim 2 or 3, wherein the switching means is provided with a means for sensing output current to the electrodes and for automatically changing the on/off ratio.
6. A system according to any one of the preceding claims wherein means are provided for reversing the polarity of the voltage applied to the electrodes.
7. A system according to any one of the preceding claims wherein the voltage is set at a level between 15 and 50 volts.
8. A system according to claim 7, wherein the voltage is set at a level between 20 and 40 volts.
PCT/GB1994/000488 1993-03-12 1994-03-11 Improvements to ionic disinfection systems WO1994020420A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
EP94909194A EP0691936A1 (en) 1993-03-12 1994-03-11 Improvements to ionic disinfection systems

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB9305122.5 1993-03-12
GB939305122A GB9305122D0 (en) 1993-03-12 1993-03-12 Improvements to ionic disinfection systems

Publications (1)

Publication Number Publication Date
WO1994020420A1 true WO1994020420A1 (en) 1994-09-15

Family

ID=10731955

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/GB1994/000488 WO1994020420A1 (en) 1993-03-12 1994-03-11 Improvements to ionic disinfection systems

Country Status (3)

Country Link
EP (1) EP0691936A1 (en)
GB (1) GB9305122D0 (en)
WO (1) WO1994020420A1 (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5543040A (en) * 1994-12-12 1996-08-06 Fi-Tek Purification Systems, Inc. Apparatus for purification of water-based fluids in closed-loop flow systems
WO1997041072A1 (en) * 1996-04-29 1997-11-06 Valery Grigorievich Daniljuk Domestic and autonomous ioniser 'sylva' and variants
US5753100A (en) * 1996-12-27 1998-05-19 Lumsden; Dennis L. Ionization-type water purification system
WO2001089997A2 (en) * 2000-05-11 2001-11-29 Megaton Systems As Means for electrochemical treatment of water
ES2229921A1 (en) * 2003-09-04 2005-04-16 Sofia Vinageras Supervia Waste hot water recirculation ions dosing system includes electronic controller and ionization tank for dispensing via a pump serving the water
US20120329121A1 (en) * 2011-03-18 2012-12-27 Green Michael P Enhancing algae growth by reducing competing microorganisms in a growth medium
DE102012007236A1 (en) * 2012-04-07 2013-10-10 Necon Gmbh Device for electro-physical water treatment, comprises electrodes arranged at different poles of electrical power source, control device which adjusts the power source at electrodes, and current pulse generator for generating current pulses
US9085745B2 (en) 2010-10-18 2015-07-21 Originoil, Inc. Systems and methods for extracting non-polar lipids from an aqueous algae slurry and lipids produced therefrom

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2067724A5 (en) * 1969-11-14 1971-08-20 Etu Diff Procedes Brevet
DE2619725A1 (en) * 1976-05-04 1977-11-17 Adriano Squazzin Swimming pool water sterilisation - by direct current passage through immersed copper electrodes
EP0128782A1 (en) * 1983-06-14 1984-12-19 Tarn-Pure Limited Water purification apparatus
EP0226284A1 (en) * 1985-10-01 1987-06-24 Safety First Limited Water recirculating apparatus and method
US5234563A (en) * 1992-06-01 1993-08-10 Janix Kabushiki Kaisha Electrolytic ionized water producer of a continuous type

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2067724A5 (en) * 1969-11-14 1971-08-20 Etu Diff Procedes Brevet
DE2619725A1 (en) * 1976-05-04 1977-11-17 Adriano Squazzin Swimming pool water sterilisation - by direct current passage through immersed copper electrodes
EP0128782A1 (en) * 1983-06-14 1984-12-19 Tarn-Pure Limited Water purification apparatus
EP0226284A1 (en) * 1985-10-01 1987-06-24 Safety First Limited Water recirculating apparatus and method
US5234563A (en) * 1992-06-01 1993-08-10 Janix Kabushiki Kaisha Electrolytic ionized water producer of a continuous type

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5543040A (en) * 1994-12-12 1996-08-06 Fi-Tek Purification Systems, Inc. Apparatus for purification of water-based fluids in closed-loop flow systems
WO1997041072A1 (en) * 1996-04-29 1997-11-06 Valery Grigorievich Daniljuk Domestic and autonomous ioniser 'sylva' and variants
US5753100A (en) * 1996-12-27 1998-05-19 Lumsden; Dennis L. Ionization-type water purification system
WO2001089997A2 (en) * 2000-05-11 2001-11-29 Megaton Systems As Means for electrochemical treatment of water
WO2001089997A3 (en) * 2000-05-11 2002-05-02 Megaton Systems As Means for electrochemical treatment of water
ES2229921A1 (en) * 2003-09-04 2005-04-16 Sofia Vinageras Supervia Waste hot water recirculation ions dosing system includes electronic controller and ionization tank for dispensing via a pump serving the water
US9085745B2 (en) 2010-10-18 2015-07-21 Originoil, Inc. Systems and methods for extracting non-polar lipids from an aqueous algae slurry and lipids produced therefrom
US20120329121A1 (en) * 2011-03-18 2012-12-27 Green Michael P Enhancing algae growth by reducing competing microorganisms in a growth medium
DE102012007236A1 (en) * 2012-04-07 2013-10-10 Necon Gmbh Device for electro-physical water treatment, comprises electrodes arranged at different poles of electrical power source, control device which adjusts the power source at electrodes, and current pulse generator for generating current pulses

Also Published As

Publication number Publication date
EP0691936A1 (en) 1996-01-17
GB9305122D0 (en) 1993-04-28

Similar Documents

Publication Publication Date Title
US4525272A (en) Electrochemical ionization system for purifying water
US4680114A (en) Water purification apparatus
US6800206B2 (en) Electrolysis based water treatment
US6284293B1 (en) Method for generating oxygenated water
US4936979A (en) Swimming pool bacteria and algae control system and method
KR100803113B1 (en) Metal ion elution unit and apparatus equipped with it
US4525253A (en) Method and apparatus for purification of water
US5314589A (en) Ion generator and method of generating ions
US4986906A (en) Swimming pool water purification system
US5324398A (en) Capacitive discharge control circuit for use with electrolytic fluid treatment systems
USRE36402E (en) Electrolytic cell assembly and process for production of bromine
AU733841B2 (en) Water purification systems
US4769119A (en) Water treatment
EP0691936A1 (en) Improvements to ionic disinfection systems
US9181111B2 (en) Method and apparatus for processing fluids
JPH0771670B2 (en) Beverage dispenser
WO1999050185A1 (en) Method and apparatus for sterilising liquids
JP3773520B1 (en) Fixed electric water purifier
KR100883259B1 (en) Metal ion elution unit and apparatus comprising same
CN213950688U (en) Water purification equipment
JPH0515998Y2 (en)
RU2076073C1 (en) Apparatus for electrochemical treatment of liquid
JPH03181389A (en) Potable water sterilizer in automatic vending machine
AU2001239004B2 (en) Electrolysis based water treatment
KR20020071255A (en) Control apparatus for sterilization and disinfection system by metal ion under water diffusion by electric method

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A1

Designated state(s): US

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): AT BE CH DE DK ES FR GB GR IE IT LU MC NL PT SE

121 Ep: the epo has been informed by wipo that ep was designated in this application
DFPE Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101)
WWE Wipo information: entry into national phase

Ref document number: 1994909194

Country of ref document: EP

ENP Entry into the national phase

Ref country code: US

Ref document number: 1995 513962

Date of ref document: 19951006

Kind code of ref document: A

Format of ref document f/p: F

WWP Wipo information: published in national office

Ref document number: 1994909194

Country of ref document: EP

WWW Wipo information: withdrawn in national office

Ref document number: 1994909194

Country of ref document: EP