CH605421A5 - Disinfecting water using hydrogen peroxide - Google Patents
Disinfecting water using hydrogen peroxideInfo
- Publication number
- CH605421A5 CH605421A5 CH416076A CH416076A CH605421A5 CH 605421 A5 CH605421 A5 CH 605421A5 CH 416076 A CH416076 A CH 416076A CH 416076 A CH416076 A CH 416076A CH 605421 A5 CH605421 A5 CH 605421A5
- Authority
- CH
- Switzerland
- Prior art keywords
- water
- hydrogen peroxide
- pref
- catalyzes
- drinking
- Prior art date
Links
Classifications
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L2/00—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor
- A61L2/16—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor using chemical substances
- A61L2/18—Liquid substances or solutions comprising solids or dissolved gases
-
- 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
- C02F1/467—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction
- C02F1/4672—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction by electrooxydation
-
- 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
- C02F1/505—Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment 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
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/722—Oxidation by peroxides
Abstract
Bath-, drinking and industrial water is disinfected by (i) adding H2O2 and (ii) activating the H2O2 or catalysing its decompsn. H2O2 can be added before or after filtration. Catalysis usually takes place before filtering, e.g. with the opt. addn. of flocculants. The catalysts may be metals metal ions or metal cpds., pref. of Cu, Pd, Fe, ni, Co, Pb, Cd or Ag. Organic cpds. e.g. aldehydes may also be used.Good catalytic activity can be achieved by incorporating an electrolytic cell in cycle of water processing plant. The cell electrodes are pref. of Cu, graphite, Fe, Ni, Pt or Ag. H2O2 has high oxidising power and can reduce coli-bacteria count to 0.
Description
Die vorliegende Erfindung bezieht sich auf ein Verfahren zur Desinfektion von Bade-, Trink- und Industriewasser mit Wasserstoffperoxid.
Die wichtigsten Anforderungen, die an die Aufbereitung von Bade- und Trinkwasser gestellt werden, sind erstens eine sofortige Desinfektion und zweitens eine möglichst gute Depotwirkung. Im weiteren werden auch Desodorierung und Schönung des behandelten Wassers angestrebt.
Bei der Industriewasseraufbereitung wird eine gute bakterizide und algizide Wirkung ohne störende Rückstände verlangt, wie z. B. in der Lebensmittelindustrie, bei Kühlwässern, Ionenaustauschern usw.
Die gebräuchlichen Desinfektionsmittel sind Oxidationssubstanzen, die auf die Zellmembran der Bakterien keimtötend wirken und daneben auch mit im Wasser vorhandenen organischen Substanzen (Schmutz) reagieren. Die bisher zur Aufbereitung von Wasser hauptsächlich verwendeten Desinfektionsmittel umfassen Chlorgas, Chlordioxid, Di-Halo (Chlor-brom-dimethylhydantoin) Brom, Elektrochlor, Javelwasser (Natriumhypochlorit) Ozon und Ozon mit Chlor.
Alle bisher eingesetzten Desinfektionsmittel weisen neben Vorteilen entscheidende Nachteile auf, wie z. B. Chlorgeruch des Wassers und der sich darüber befindenden Luft, pH-Anstieg des Wassers, Chloraminbildung im Badewasser, hohe Investitionskosten, schlechte Depotwirkung, Unfallgefahr durch Giftigkeit, schwierige Lagerung oder schlechte Oxydationskraft usw.
Die vorliegende Erfindung schlägt nun für die Aufbereitung von Bade-, Trink- und Industriewasser die Verwendung von Wasserstoffperoxid als Desinfektionsmittel mit ausgezeichneter Oxydationskraft und wenigen Nachteilen der oben beschriebenen Art vor.
Das erfindungsgemässe Verfahren zur Desinfektion von Bade-, Trink- und Industriewasser mit Wasserstoffperoxid ist dadurch gekennzeichnet, dass man dem Wasser Wasserstoffperoxid zusetzt und dieses aktiviert bzw. dessen Zersetzung katalysiert.
Die Wasserstoffperoxid-Zugabe kann je nach der Aufbereitungsart vor oder nach der Filtration erfolgen.
Die Katalyse erfolgt in der Regel vor dem Filter, z. B.
gleichzeitig mit einer eventuellen Zugabe von Flockungsmitteln. Als Katalysator können Metalle, Metallionen oder Metallverbindungen von z. B. Kupfer, Palladium, Eisen, Nickel, Kobalt, Blei, Cadmium, Silber usw. verwendet werden.
Es können aber auch organische Stoffe, z. B. Aldehyde, verwendet werden.
Eine sehr gute Katalysewirkung kann auch durch den Einbau einer Stromquelle in den Wasserkreislauf einer Wasseraufbereitungsanlage erzielt werden. Als Elektrodenmaterialien kommen dabei Stoffe wie z. B. Kupfer, Graphit, Eisen, Nickel, Platin, Silber usw. in Frage.
Die folgenden Versuche zeigen die gute Wirkung von Wasserstoffperoxid als Desinfektionsmittel bei der Wasseraufbereitung, wo z. B. bei Badewasser der Wert 0 für die Menge der coliformen Keime verlangt wird.
Laborversuche
Diese Versuche wurden mit einem Kunststoffbassin von 40 1 Inhalt mit Rheinwasser (Entnahme oberhalb des Kraftwerkes Mellikon) durchgeführt.
Das Wasser wies eine Temperatur von 200 C auf und wurde mit Förderpumpen umgewälzt (Umwälzzeit 1 bis 4 Std.
und über einen Sandfilter geführt. Die Katalyse erfolgte mittelt einer Stromzelle vor dem Sandfilter. Die Stromzelle wies Kupferelektroden auf, die Spannung betrug #24 V und der Strom ' 80 mA. Die Ergebnisse sind in den folgenden Tabellen zusammengestellt.
Tabelle I
Versuche ohne 11202 ohne Stromzelle Probenahme H202 Bakterien Datum Zeit 100% coliforme übrige mg/l Keime Keime in 100 ml in 100 ml Versuch 1:
4.11.75 0800 0 650 500
5.11.75 0800 0 850 280 Versuch 2: 24.11.75 1600 0 2900 1500 25.11.75 0800 0 2400 1800
1600 0 1800 1700 26.11.75 0800 0 1450 1500
Tabelle II
Versuch mit 11202 ohne Stromzelle Probenahme H202 Bakterien Datum Zeit 100% coliforme übrige mg/l Keime Keime in 100 ml in 100 ml Versuch 3:
12.11.75 0930 0 2825 3150
1000 10 nicht nicht bestimmt bestimmt
1400 7 1275 1550 13.11.75 0800 0 740 830
Tabelle III
Versuch mit 11202 mit Stromzelle Probenahme H202 Bakterien Datum Zeit 100% coliforme übrige mg/l Keime Keime in 100 ml in 100 ml Versuch 4: 5.11.75 0900 10 1110 15780
1000 4 2 1710 Versuch 5:
8.12.75 1200 10 600 3440
1300 5 6 174
1400 6 3 63 Versuch 6: 17.12.75 0900 10 900 8100
1000 6 10 20
1400 4 0 6 Versuch 7: 29.12.75 1100 10 500 4600
1300 5 0 120
1600 0 0 10 Versuch 8:
6.1.76 0800 10 875 1440
0900 10 0 280
Versuch im Schwimmbad Schauenberg
In der Schwimmanlage Schauenberg wurde ein Desinfektionsversuch durchgeführt, wobei die Infektion und Bestimmung der Keimzahlen durch das chemische Laboratorium der Stadt Zürich erfolgten.
Beim Schwimmbad Schauenberg gelangt das Wasser vom Hauptbecken (160 m3) in ein Zwischengefäss (40 m3) und von hier mir Umwälzpumpe über den Drucksandfilter wieder ins Hauptbecken. Die Umwälzung beträgt etwa 40 m3 pro Std.
Die Stromzelle war vor der Umwälzpumpe angebracht, während das Wasserstoffperoxid dem Zwischengefäss zugegeben wurde.
Die Angaben und Daten des Desinfektionsversuches sind in der Tabelle IV und die entsprechenden durch das chemische Laboratorium der Stadt Zürich ermittelten Keimzahlen in der Tabelle V zusammengestellt.
Tabelle IV Datum Zeit Bassin H202 E. Zelle Bassin H202 ab 1976 mg/l i. Betrieb Cu mg/l Hahn 12.2. 0800 - 0,025 0 Do 0830 - Bakterien
1030 - 0 Zugabe
1100 x
1200 2,7 x 6,3
1300 4,3 x 12,0
1400 7,1 x 12,2
1500 9,0 x 13,0
1600 10,5 x 13,0
1700 10,9 x 0,065 10,3
1800 10,3 10,0
2000 9,9
2200 9,0 13.2. 0800 3,9 0,08 3,4
0830 0,08 7,3
0900 4,8 11,5
0930 10,0
1000 6,3 9,5
1100 7,7 13,8
1200 8,8 12,2
1300 9,7 12,4
1400 9,9 12,4
1500 9,9 x 0,07 ¯ 11,5
1600 9,9 x 11,5
Tabelle V 12.2.1976 Zeit Colif. Keime Enterokokken pro 100 ml pro 100 ml auf a.
Endogar Enterokokkusagar Vor Versuch 0800 0 0 Nach Infektion des Bades mit Coliund Enterokokken Bakterien 1000 636 000 650 000 Desinfektions- 1100 532 000 464 000 Anlage 1200 180000 295000 in Betrieb 1300 95000 234000
1400 76 000 155 000
1500 51000 98 000
1600 5800 42000
1800 230 11 000
2000 40 8 700
2200 10 110 13.2.1976 0800 0 0
1000 0 0
1200 0 0
1400 0 0
1600 0 0
The present invention relates to a method for disinfecting bathing, drinking and industrial water with hydrogen peroxide.
The most important requirements placed on the treatment of bathing and drinking water are firstly an immediate disinfection and secondly the best possible depot effect. Furthermore, deodorization and fining of the treated water are aimed for.
In industrial water treatment, a good bactericidal and algicidal effect without disturbing residues is required, such as B. in the food industry, with cooling water, ion exchangers, etc.
The common disinfectants are oxidizing substances that have a germicidal effect on the cell membrane of the bacteria and also react with organic substances (dirt) in the water. The main disinfectants used to date for treating water include chlorine gas, chlorine dioxide, di-halo (chlorobromo-dimethylhydantoin) bromine, electrochlor, javel water (sodium hypochlorite) ozone and ozone with chlorine.
All disinfectants used so far have advantages, as well as decisive disadvantages, such as: B. The smell of chlorine in the water and the air above it, pH rise in the water, chloramine formation in the pool water, high investment costs, poor depot effect, risk of accidents due to toxicity, difficult storage or poor oxidative power, etc.
The present invention now proposes the use of hydrogen peroxide as a disinfectant with excellent oxidizing power and few disadvantages of the type described above for the treatment of bathing, drinking and industrial water.
The method according to the invention for disinfecting bathing, drinking and industrial water with hydrogen peroxide is characterized in that hydrogen peroxide is added to the water and this is activated or its decomposition is catalyzed.
The addition of hydrogen peroxide can take place before or after the filtration, depending on the type of preparation.
The catalysis usually takes place upstream of the filter, e.g. B.
at the same time with a possible addition of flocculants. As a catalyst, metals, metal ions or metal compounds of z. B. copper, palladium, iron, nickel, cobalt, lead, cadmium, silver, etc. can be used.
But it can also organic substances such. B. aldehydes can be used.
A very good catalytic effect can also be achieved by installing a power source in the water cycle of a water treatment plant. As electrode materials, substances such as B. copper, graphite, iron, nickel, platinum, silver, etc. in question.
The following experiments show the good effect of hydrogen peroxide as a disinfectant in water treatment, where z. B. in bath water the value 0 is required for the amount of coliforms.
Laboratory tests
These tests were carried out with a plastic basin with a volume of 40 l with Rhine water (taken from above the Mellikon power station).
The water had a temperature of 200 ° C. and was circulated with feed pumps (circulation time 1 to 4 hours.
and passed through a sand filter. The catalysis took place by means of a power cell in front of the sand filter. The current cell had copper electrodes, the voltage was 24 V and the current was 80 mA. The results are compiled in the following tables.
Table I.
Experiments without 11202 without electricity cell Sampling H202 bacteria Date Time 100% coliforms remaining mg / l germs Germs in 100 ml in 100 ml Experiment 1:
11/4/75 0800 0 650 500
11/5/75 0800 0 850 280 Trial 2: 11/24/75 1600 0 2900 1500 11/25/75 0800 0 2400 1800
1600 0 1800 1700 11/26/75 0800 0 1450 1500
Table II
Experiment with 11202 without current cell Sampling H202 bacteria Date Time 100% coliforms remaining mg / l germs Germs in 100 ml in 100 ml Experiment 3:
11/12/75 0930 0 2825 3150
1000 10 not determined not determined
1400 7 1275 1550 11/13/75 0800 0 740 830
Table III
Experiment with 11202 with current cell sampling H202 bacteria date time 100% coliforms remaining mg / l germs germs in 100 ml in 100 ml experiment 4: 5.11.75 0900 10 1110 15780
1000 4 2 1710 Trial 5:
12/8/75 1200 10 600 3440
1300 5 6 174
1400 6 3 63 Experiment 6: 17.12.75 0900 10 900 8100
1000 6 10 20
1400 4 0 6 Trial 7: 29.12.75 1100 10 500 4600
1300 5 0 120
1600 0 0 10 Try 8:
6.1.76 0800 10 875 1440
0900 10 0 280
Try in the Schauenberg swimming pool
A disinfection test was carried out in the Schauenberg swimming area, the infection and determination of the germ counts being carried out by the chemical laboratory of the City of Zurich.
At the Schauenberg swimming pool, the water flows from the main pool (160 m3) into an intermediate tank (40 m3) and from here with a circulation pump via the pressure sand filter back into the main pool. The circulation is around 40 m3 per hour.
The power cell was installed in front of the circulation pump while the hydrogen peroxide was added to the intermediate vessel.
The details and data of the disinfection test are compiled in Table IV and the corresponding bacterial counts determined by the chemical laboratory of the City of Zurich in Table V.
Table IV Date Time Basin H202 E. Cell Basin H202 from 1976 mg / l i. Operation Cu mg / l stopcock 12.2. 0800 - 0.025 0 Do 0830 - bacteria
1030 - 0 addition
1100 x
1200 2.7 x 6.3
1300 4.3 x 12.0
1400 7.1 x 12.2
1500 9.0 x 13.0
1600 10.5 x 13.0
1700 10.9 x 0.065 10.3
1800 10.3 10.0
2000 9.9
2200 9.0 13.2. 0800 3.9 0.08 3.4
0830 0.08 7.3
0900 4.8 11.5
0930 10.0
1000 6.3 9.5
1100 7.7 13.8
1200 8.8 12.2
1300 9.7 12.4
1400 9.9 12.4
1500 9.9 x 0.07 ¯ 11.5
1600 9.9 x 11.5
Table V 02.12.1976 Time Colif. Enterococci germs per 100 ml per 100 ml on a.
Endogenous enterococcus agar Before the experiment 0800 0 0 After infection of the bath with coliform and enterococcal bacteria 1000 636 000 650 000 Disinfection 1100 532 000 464 000 System 1200 180000 295000 in operation 1300 95000 234000
1400 76 000 155 000
1500 51000 98000
1600 5800 42000
1800 230 11 000
2000 40 8 700
2200 10 110 02/13/1976 0800 0 0
1000 0 0
1200 0 0
1400 0 0
1600 0 0
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CH416076A CH605421A5 (en) | 1976-04-02 | 1976-04-02 | Disinfecting water using hydrogen peroxide |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CH416076A CH605421A5 (en) | 1976-04-02 | 1976-04-02 | Disinfecting water using hydrogen peroxide |
Publications (1)
Publication Number | Publication Date |
---|---|
CH605421A5 true CH605421A5 (en) | 1978-09-29 |
Family
ID=4270918
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CH416076A CH605421A5 (en) | 1976-04-02 | 1976-04-02 | Disinfecting water using hydrogen peroxide |
Country Status (1)
Country | Link |
---|---|
CH (1) | CH605421A5 (en) |
Cited By (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1980001457A1 (en) * | 1979-01-11 | 1980-07-24 | J Peel | Method of sterilisation |
FR2464229A1 (en) * | 1979-09-04 | 1981-03-06 | Interox Chemicals Ltd | PROCESS AND COMPOSITIONS FOR THE DISINFECTION OF AQUEOUS MEDIA |
US4370241A (en) * | 1977-01-27 | 1983-01-25 | Degussa Ag | Process for the detoxification of waste water containing phenol, phenol derivative or phenol and formaldehyde |
EP0086592A1 (en) * | 1982-02-08 | 1983-08-24 | Interox America | Abatement of hydrogen sulfide in aqueous media using hydrogen peroxide and transition metal catalyst |
EP0238975A1 (en) * | 1986-03-25 | 1987-09-30 | Peroxid-Chemie GmbH | Process for activating hydrogen peroxide for the oxidation of non-biodegradable toxic substances |
WO1997019025A1 (en) * | 1995-11-23 | 1997-05-29 | Lennart Olausson | Method of disinfecting water |
WO1997019896A1 (en) * | 1995-11-28 | 1997-06-05 | Austech Limited | Liquid sterilisation apparatus |
DE19607390A1 (en) * | 1996-02-28 | 1997-09-11 | Krupp Vdm Gmbh | Simple, ecologically compatible sterilisation of water, e.g. cooling tower water |
US5928481A (en) * | 1994-05-13 | 1999-07-27 | Austech Limited | Apparatus for sterilising water by the process of heavy metal sterilisation using silver |
US6022459A (en) * | 1997-02-10 | 2000-02-08 | Austech Pty Ltd. | Liquid purification apparatus |
FR2784979A1 (en) * | 1998-10-26 | 2000-04-28 | Pour Le Traitement De L Eau Ci | Long term electrochemical disinfection of water or waste water is effected by anodic oxidation combined with cathodic peroxidation |
WO2001016031A2 (en) * | 1999-09-01 | 2001-03-08 | University Of Abertay Dundee | Method of producing hydroxyl radicals for chemical reactions |
DE10128129A1 (en) * | 2001-06-09 | 2002-12-19 | Mol Katalysatortechnik Gmbh | Degradation of biological and/or organic substances in liquid phase used for sterilizing liquids comprises reacting solid metal catalyst |
WO2006064135A1 (en) | 2004-12-16 | 2006-06-22 | Analyses Mesures Pollutions (A.M.P.) | Method for treating water |
DE102019004242A1 (en) * | 2019-06-18 | 2020-12-24 | Joachim Thielemann | Device and method for catalytic disinfection |
-
1976
- 1976-04-02 CH CH416076A patent/CH605421A5/en not_active IP Right Cessation
Cited By (22)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4370241A (en) * | 1977-01-27 | 1983-01-25 | Degussa Ag | Process for the detoxification of waste water containing phenol, phenol derivative or phenol and formaldehyde |
WO1980001457A1 (en) * | 1979-01-11 | 1980-07-24 | J Peel | Method of sterilisation |
US4289728A (en) | 1979-01-11 | 1981-09-15 | National Research Development Corp. | Improvements in methods of sterilization |
FR2464229A1 (en) * | 1979-09-04 | 1981-03-06 | Interox Chemicals Ltd | PROCESS AND COMPOSITIONS FOR THE DISINFECTION OF AQUEOUS MEDIA |
EP0086592A1 (en) * | 1982-02-08 | 1983-08-24 | Interox America | Abatement of hydrogen sulfide in aqueous media using hydrogen peroxide and transition metal catalyst |
EP0238975A1 (en) * | 1986-03-25 | 1987-09-30 | Peroxid-Chemie GmbH | Process for activating hydrogen peroxide for the oxidation of non-biodegradable toxic substances |
US5928481A (en) * | 1994-05-13 | 1999-07-27 | Austech Limited | Apparatus for sterilising water by the process of heavy metal sterilisation using silver |
WO1997019025A1 (en) * | 1995-11-23 | 1997-05-29 | Lennart Olausson | Method of disinfecting water |
US6267885B1 (en) | 1995-11-28 | 2001-07-31 | Austech Pty., Ltd. | Liquid sterilization apparatus |
AU702918B2 (en) * | 1995-11-28 | 1999-03-11 | Austech Limited | Liquid sterilisation apparatus |
WO1997019896A1 (en) * | 1995-11-28 | 1997-06-05 | Austech Limited | Liquid sterilisation apparatus |
DE19607390A1 (en) * | 1996-02-28 | 1997-09-11 | Krupp Vdm Gmbh | Simple, ecologically compatible sterilisation of water, e.g. cooling tower water |
US6022459A (en) * | 1997-02-10 | 2000-02-08 | Austech Pty Ltd. | Liquid purification apparatus |
FR2784979A1 (en) * | 1998-10-26 | 2000-04-28 | Pour Le Traitement De L Eau Ci | Long term electrochemical disinfection of water or waste water is effected by anodic oxidation combined with cathodic peroxidation |
WO2001016031A2 (en) * | 1999-09-01 | 2001-03-08 | University Of Abertay Dundee | Method of producing hydroxyl radicals for chemical reactions |
WO2001016031A3 (en) * | 1999-09-01 | 2001-09-20 | Univ Abertay Dundee | Method of producing hydroxyl radicals for chemical reactions |
US6692632B1 (en) | 1999-09-01 | 2004-02-17 | University Of Abertay Dundee | Method of producing hydroxyl radicals for chemical reactions |
DE10128129A1 (en) * | 2001-06-09 | 2002-12-19 | Mol Katalysatortechnik Gmbh | Degradation of biological and/or organic substances in liquid phase used for sterilizing liquids comprises reacting solid metal catalyst |
DE10128129B4 (en) * | 2001-06-09 | 2012-07-19 | Mol Katalysatortechnik Gmbh | Process for the degradation of biological and / or organic substances and full metal catalyst |
WO2006064135A1 (en) | 2004-12-16 | 2006-06-22 | Analyses Mesures Pollutions (A.M.P.) | Method for treating water |
FR2879590A1 (en) * | 2004-12-16 | 2006-06-23 | Analyses Mesures Pollutions A | PROCESS FOR TREATING WATER |
DE102019004242A1 (en) * | 2019-06-18 | 2020-12-24 | Joachim Thielemann | Device and method for catalytic disinfection |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP2139817B1 (en) | Use of electrochemically treated water as a disinfection agent | |
CH605421A5 (en) | Disinfecting water using hydrogen peroxide | |
DE60131747T2 (en) | PROCESS FOR SYNTHESIS OF AN OXIDIZING AGENT AND THE APPLICATION THEREOF | |
US7235169B2 (en) | Method and apparatus for purging and disinfecting water | |
DE602004009136T2 (en) | Electrochemical sterilization and bacteriostatic process | |
DE2911288C2 (en) | Method for disinfecting water, in particular swimming pool water | |
WO2009067838A2 (en) | Method and technical design for cleaning laundry, crockery, vehicles and floor surfaces with electrolysed water by means of oxidative radicals produced by diamond electrodes | |
DE4318628A1 (en) | Water treatment processes | |
EP1468151B1 (en) | Method for sterilisation and cleaning of water supply systems, in particular in swimming and bathing pool units and device for carrying out the same | |
CA3003308A1 (en) | Apparatus and method for electrodisinfection | |
DE102015006706A1 (en) | Continuous process for removal of micro-contaminants from biologically clarified municipal wastewater | |
DE102008004663B4 (en) | Process for the electrochemical sanitation and germ reduction of biologically treated wastewater, in particular domestic wastewater, and of wastewater streams and apparatus therefor | |
DE602004008584T2 (en) | METHOD AND DEVICE FOR ELECTROCHEMICAL WATER DISINFECTION | |
DE10128129B4 (en) | Process for the degradation of biological and / or organic substances and full metal catalyst | |
EP0008074A1 (en) | Process for the chemical and biological treatment of waste water | |
DE19903649A1 (en) | Process for the production of drinking water | |
Denisova et al. | Electrochemical/granular activated carbon hybrid system for drinking water disinfection at flow conditions | |
DE2847339C2 (en) | Method for disinfecting water, in particular swimming pool water | |
EP1858810B1 (en) | Device and method for the electrolytic treatment of water and aqueous solutions | |
KR100323337B1 (en) | Purification equipment for swimming pools and baths | |
DE102017007440A1 (en) | Process for removing organic compounds from biologically clarified, prefiltered wastewater | |
EP4019476A2 (en) | Method for the preparation of electrochemically modified water | |
DE104438C (en) | ||
Tay | Silver Ion as Disinfectant for Swimming Pool Application | |
Esterhuyse et al. | STUDIES OF ALTERNATIVE DISINFECTANTS FOR WASTEWATER EFFLUENT |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PL | Patent ceased |