SK82994A3 - Method of electro-chemical reduction of nitrates - Google Patents

Method of electro-chemical reduction of nitrates Download PDF

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Publication number
SK82994A3
SK82994A3 SK82994A SK82994A SK82994A3 SK 82994 A3 SK82994 A3 SK 82994A3 SK 82994 A SK82994 A SK 82994A SK 82994 A SK82994 A SK 82994A SK 82994 A3 SK82994 A3 SK 82994A3
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Slovakia
Prior art keywords
cathode
nitrate
nitrates
compartment
solution
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Application number
SK82994A
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Slovak (sk)
Inventor
Bernd Fenk
Peter Haftendorn
Dieter Hahnewald
Klaus Fischwasser
Johannes Reichert
Dietmar Rahner
Katrin Isberner
Katrin Otter
Frieder Seibt
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Hahnewald Gmbh
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Publication date
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Publication of SK82994A3 publication Critical patent/SK82994A3/en

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    • 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
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/467Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction
    • C02F1/4676Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction by electroreduction
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B1/00Electrolytic production of inorganic compounds or non-metals
    • 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
    • C02F1/42Treatment of water, waste water, or sewage by ion-exchange
    • C02F2001/422Treatment of water, waste water, or sewage by ion-exchange using anionic exchangers
    • 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
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104Devices therefor; Their operating or servicing
    • C02F1/46109Electrodes
    • C02F2001/46133Electrodes characterised by the material
    • C02F2001/46138Electrodes comprising a substrate and a coating
    • C02F2001/46142Catalytic coating
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/10Inorganic compounds
    • C02F2101/16Nitrogen compounds, e.g. ammonia
    • C02F2101/163Nitrates
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/46Apparatus for electrochemical processes
    • C02F2201/461Electrolysis apparatus
    • C02F2201/46105Details relating to the electrolytic devices
    • C02F2201/46115Electrolytic cell with membranes or diaphragms

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Metallurgy (AREA)
  • Materials Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)
  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)

Abstract

The invention relates to a process for the catalytic electrochemical reduction of nitrate, principally to give elemental nitrogen in aqueous solutions at a cathode. The aim of the invention is to denitrify even concentrated salt-containing aqueous solutions by these nitrate reductions. The aqueous solution is introduced into the cathode compartment of an electrolysis cell, in which the cathode compartment and anode compartment are separated from each other by a cation exchange membrane, and is subjected to a voltage in the same.

Description

SPÔSOB ELEKTROCHEMICKEJ REDUKCIE DUSIČNANOVMETHOD OF ELECTROCHEMICAL REDUCTION OF NITRATES

Oblasť technikyTechnical field

Vynález sa týka spôsobu katalytickej elektrochemickej redukcie dusičnanov, predovšetkým na elementárny dusík vo vodnom roztoku na katóde.The invention relates to a method of catalytic electrochemical reduction of nitrates, in particular to elemental nitrogen in an aqueous solution on the cathode.

Doterajší stav technikyBACKGROUND OF THE INVENTION

Vodné roztoky obsahujúce dusičitany sú napríklad regeneráty z iónovej výmeny, ktoré sa používajú na elimináciu dusičnanov z pitnej vody, alebo odpadové roztoky z priemyslu.Aqueous solutions containing nitrates are, for example, ion exchange regenerates, which are used to eliminate nitrates from drinking water, or waste solutions from industry.

Bežná až doteraz známa enzymatická biologická denitrifikácia pracuje často nespoľahlivo, hlavne pri vyšších koncentráciách solí. Tak až doteraz napríklad nebolo možné regeneráty z iónovej výmeny obsahujúcej dusičnany spracovať tak, aby sa mohol uskutočniť obeh regeneračného prostriedku.Conventional enzymatic biological denitrification, known hitherto, often works unreliable, especially at higher salt concentrations. So far, for example, it has not been possible to process nitrate-containing ion exchange regenerates so that the regeneration medium can be circulated.

Podstata vynálezuSUMMARY OF THE INVENTION

Cieľom vynálezu je denitrifikácia koncentrovaných vodných roztokov solí katalytickou, katódovou redukciou dusičnanov.It is an object of the invention to denitrify concentrated aqueous salt solutions by catalytic, cathodic reduction of nitrates.

Podstata vynálezu spočíva vo vytvorení kombinácie elektrolýzy so spôsobmi zvýšenia koncentrácie ako je iónová výmena, reverzná osmóza, elektrodialýza, predpoklady na vytvorenie postupových kombinácií prínosných eliminácií dusičnanov z vody a vodných roztokov kvôli ochrane životného prostredia.SUMMARY OF THE INVENTION The object of the present invention is to provide a combination of electrolysis with concentration-increasing methods such as ion exchange, reverse osmosis, electrodialysis, the prerequisites for creating process combinations of beneficial nitrate elimination from water and aqueous solutions for environmental protection.

Táto úloha sa vyrieši poznatkami podľa patentových nárokov, a to tým, že sa vodný roztok obsahujúci dusičnany uloží do katódového priestoru elektrolyzéra a zavedie sa vhodné elektrické napätie.This object is solved by the teachings of the claims by placing an aqueous solution containing nitrates in the cathode space of the electrolyzer and introducing a suitable electrical voltage.

V elektrolyzéri sú katódový a anódový priestor navzájom oddelené katexovou membránou, katóda je dotovaná katalyzátorom a v priestore anódy sa nachádza ďalší vodný roztok, napríklad kyseliny sírovej, ktorá cirkuluje.In the electrolyser, the cathode and anode compartments are separated from each other by a cation exchange membrane, the cathode is doped with a catalyst, and in the anode compartment there is another aqueous solution, such as sulfuric acid, that circulates.

Na katóde nastáva chemická redukcia dusičnanov podlá prvej z uvedených rovníc, pričom naAt the cathode there is a chemical reduction of nitrates according to the first of the above equations, whereby at

eden mól dusičnanu sa spotrebuje molov protónov.one mole of nitrate consumes moles of protons.

NO^ + 6H+ + 5e <--> 0,5 N2 + 3H2ONO 2 + 6H + + 5e <--> 0.5 N 2 + 3H 2 O

2,5H2O - 5e <----> 1,25 O2 + 5H+ 2.5H 2 O - 5e <----> 1.25 O 2 + 5H +

Na anóde prebieha podlá druhej rovnice rozpad vody za vzniku 5 molov protónov, ktoré prechádzajú z anódového priestoru katexovou membránou do katódového priestoru. S rozpadom vody je spojené zvýšenie koncentrácie roztoku v anódovom priestore, takže sa musí doplniť voda. Deficit minimálne 1 mólu protónov na jeden mól dusičnanov zostávajúci v katódovom priestore sa musí vyrovnať prídavkom kyseliny, napríklad kyseliny chlorovodíkovej do i spracovávaného roztoku obsahujúceho dusičnany.At the anode, according to the second equation, water breaks down to form 5 moles of protons that pass from the anode space through the cation exchange membrane to the cathode space. Water decay is associated with increasing the concentration of the solution in the anode compartment, so water must be added. A deficiency of at least 1 mole of protons per mole of nitrates remaining in the cathode compartment must be compensated by the addition of an acid, for example hydrochloric acid, to the nitrate-treated solution.

S ohľadom na skutočnosť, že elektrochemická redukcia dusičnanov je kinetický silne brzdená a môžu ju rušiť vedľajšie reakcie sprevádzajúce celý proces, napríklad vznik amónia, hrá okrem zloženia roztoku obsahujúceho dusičnany a potenciálu, významnú úlohu hlavne spojenie katóda/katalyzátor, pričom ako nosič pre katalyzátor slúži elektróda.Due to the fact that the electrochemical reduction of nitrates is strongly kinetic and can be disturbed by side reactions accompanying the whole process, such as the formation of ammonium, in addition to the composition of the nitrate-containing solution and potential, electrode.

Podľa vynálezu umožňuje katalytickú katódovú redukciu dusičnanov podľa prvej vyššie uvedenej rovnice elektróda napríklad z častíc aktívneho uhlia dotovaná rôznymi ťažkými kovmi napríklad medi s paládiom. Variáciou nosného materiálu a tiež obsahom ťažkých kovov v nosnom materiáli sa môže dosiahnuť ovplyvnenie kinetiky redukcie dusičnanov, a tým vznik vedľajších produktov.According to the invention, the catalytic cathode reduction of nitrates according to the above-mentioned equation allows an electrode of, for example, activated carbon particles doped with various heavy metals, for example copper with palladium. By varying the carrier material and also the heavy metal content of the carrier material, it is possible to influence the nitrate reduction kinetics and thereby the formation of by-products.

Príklady CLS/M/vite/irOs vynálezuExamples of CLS / M / vite / iOs of the invention

V nasledujúcom je bližšie popísaný príklad vyhotovenia postupu podlá vynálezu.The following is an example of an embodiment of the process according to the invention.

V elektrolyzéri, v ktorom sú oddelené katódový a anódový priestor katexovou membránou, je v katódovom priestore roztok dusičnanu, asi 10 g dusičnanu vil roztoku a v anódovom priestore je cca 5 % kyselina sírová. Ako katóda slúži elektróda z častíc aktívneho uhlia dotovaná meďou s paládiom, pričom podiel medi je menší ako 10 % a podiel paládia je menší ako 1 %. Pri potenciáli 1 000 až 1 400 mV sa cca 90 % dusičnanu prevedie na dusík. Hodnota pH sa udržiava prídavkom kyseliny chlorovodíkovej v katódovom priestore konštantná. Plná redukcia dusičnanu nie je žiaduca, pretože roztok spracovávaný v katódovom priestore slúži ako regeneračné činidlo pre menič aniónov znečistený dusičnanom.In an electrolyzer in which the cathode and anode compartments are separated by a cation exchange membrane, there is a nitrate solution in the cathode compartment, about 10 g of a nitrate vial of solution and about 5% sulfuric acid in the anode compartment. The electrode made of activated carbon particles doped with copper with palladium serves as a cathode, the copper content being less than 10% and the palladium content being less than 1%. At a potential of 1,000 to 1,400 mV, about 90% of the nitrate is converted to nitrogen. The pH is kept constant by the addition of hydrochloric acid in the cathode space. Full reduction of nitrate is not desirable because the solution treated in the cathode space serves as a regenerating agent for the anion exchanger contaminated with nitrate.

Claims (4)

PATENTOVÉ NÁROKYPATENT CLAIMS 1. Spôsob elektrochemickej redukcie dusičnanov katalýzou, hlavne na elementárny dusík vo vodnom roztoku, vyznačujúci sa tým, že sa na vodný roztok dusičnanov umiestnený v katódovom priestore pôsobí elektrickým napätím, pričom katódový priestor a anódový priestor sú navzájom oddelené katexovou membránou.A method for the electrochemical reduction of nitrates by catalysis, in particular elemental nitrogen in an aqueous solution, characterized in that an aqueous nitrate solution located in the cathode compartment is subjected to an electrical voltage, the cathode compartment and the anode compartment being separated from each other by a cation exchange membrane. 2. Spôsob podlá nároku 1, vyznačujúci sa tým, že katóda pozostáva z nosného materiálu, ktorý sa dotuje katalyzátorom.Method according to claim 1, characterized in that the cathode consists of a support material which is doped with a catalyst. 3. Spôsob podlá nárokov 1 alebo 2, vyznačujúci sa tým, že nosný materiál je tvorený katalytickou zmesou ťažkých kovov.Method according to claim 1 or 2, characterized in that the support material is a catalytic mixture of heavy metals. 4. Spôsob podlá jedného z nárokov 1 až 3, vyznačujúci sa tým, že sa roztokom obsahujúcim dusičnany elektrolyticky spracovaným v priestore katódy pôsobí po spracovaní na iónový menič.Method according to one of Claims 1 to 3, characterized in that, after treatment, the nitrate-containing solution electrolytically treated in the cathode space is treated with an ion exchanger.
SK82994A 1993-12-24 1994-07-11 Method of electro-chemical reduction of nitrates SK82994A3 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE19934344613 DE4344613C2 (en) 1993-12-24 1993-12-24 Process for the catalytic-electrochemical reduction of nitrate-containing solutions and use of the treated aqueous solutions as regeneration agents for ion exchangers

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SK82994A3 true SK82994A3 (en) 1995-07-11

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EP (1) EP0659692A1 (en)
CZ (1) CZ134094A3 (en)
DE (1) DE4344613C2 (en)
HU (1) HUT71990A (en)
PL (1) PL306397A1 (en)
RU (1) RU94045266A (en)
SK (1) SK82994A3 (en)

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Publication number Priority date Publication date Assignee Title
DE19512955C2 (en) * 1995-04-10 1998-09-10 Ernst A Prof Dr Stadlbauer Water treatment process for the reductive conversion of nitrate and nitrite into elemental nitrogen
DE19517652A1 (en) * 1995-05-17 1996-11-21 Grundfos As Reducing nitrate or nitrite content in water by electrolytic and catalytic treatment
GB9603741D0 (en) * 1996-02-22 1996-04-24 Lin Mei Treatment of water by electrolysis
DE19624023B9 (en) * 1996-06-17 2009-05-20 Verein für Kernverfahrenstechnik und Analytik Rossendorf e.V. Process for the remediation of acidic, iron-containing open cast mining water
FR2754251B1 (en) * 1996-10-03 1998-11-27 Step PLANT AND PROCESS FOR THE TREATMENT OF AQUEOUS FLUIDS
AU4398399A (en) * 1998-11-09 2000-05-29 Hee Jung Kim Electrochemical treatment system for hard-resoluble waste water
GB2348209B (en) * 1999-03-24 2001-05-09 Ionex Ltd Water purification process
US6645366B2 (en) * 2000-11-01 2003-11-11 Sanyo Electric Co., Ltd. Waste water treatment device
FI115904B (en) 2002-01-25 2005-08-15 Bcde Group Waste Man Ltd Oy Method and apparatus for removing contaminants from waste water by electroplating
JP3691461B2 (en) * 2002-02-13 2005-09-07 三洋電機株式会社 Water purification system and water purification method
US7300591B2 (en) 2002-04-18 2007-11-27 Sanyo Electronic Co., Ltd. Wastewater treating method and wastewater treating apparatus
GB2449655A (en) * 2007-05-30 2008-12-03 Jlj Engineering Sercices Ltd An electrochemical reactor for aqueous solutions with high electrical resistance
DE102009026179A1 (en) * 2009-07-15 2011-01-27 Haas, Rüdiger, Dipl.-Geol. Bioelectrolytic denitrification
DK2902368T3 (en) 2010-11-17 2016-10-03 Technion Res & Dev Foundation PHYSICAL AND CHEMICAL PROCEDURE FOR THE REMOVAL OF NITROGENIC COMPOUNDS FROM RECYCLED AQUACULTURE SYSTEMS
CA3016844C (en) 2016-03-08 2023-09-26 Technion Research & Development Foundation Limited Disinfection and removal of nitrogen species from saline aquaculture systems

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CH675715A5 (en) * 1988-10-21 1990-10-31 Asea Brown Boveri
DE3838181A1 (en) * 1988-11-10 1990-05-23 Linde Ag Process and apparatus for removing nitrogen compounds from aqueous solutions
GB2267290A (en) * 1992-05-27 1993-12-01 Electricity Ass Tech A Process for the electrolytic destruction of nitrate in aqueous liquids

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EP0659692A1 (en) 1995-06-28
HU9403756D0 (en) 1995-03-28
HUT71990A (en) 1996-03-28
CZ134094A3 (en) 1995-08-16
DE4344613C2 (en) 1997-07-17
DE4344613A1 (en) 1995-06-29
PL306397A1 (en) 1995-06-26
RU94045266A (en) 1996-09-27

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