DD253353A3 - METHOD FOR ELECTROCHEMICAL WASTEWATER CLEANING - Google Patents

METHOD FOR ELECTROCHEMICAL WASTEWATER CLEANING Download PDF

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Publication number
DD253353A3
DD253353A3 DD24981983A DD24981983A DD253353A3 DD 253353 A3 DD253353 A3 DD 253353A3 DD 24981983 A DD24981983 A DD 24981983A DD 24981983 A DD24981983 A DD 24981983A DD 253353 A3 DD253353 A3 DD 253353A3
Authority
DD
German Democratic Republic
Prior art keywords
soluble electrodes
anode
electrolysis cell
wastewater treatment
value
Prior art date
Application number
DD24981983A
Other languages
German (de)
Inventor
Gennadij S Zenin
Semen A Bogatych
Anatolij T Solovev
Aleksandr A Daniljuk
Raisa A Sokolskaja
Vladimir P Ivlev
Valentin A Sulimov
Original Assignee
Le Technolog I Cholodilnoj Pro
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
Priority claimed from SU823414564A external-priority patent/SU1318535A1/en
Application filed by Le Technolog I Cholodilnoj Pro filed Critical Le Technolog I Cholodilnoj Pro
Priority to DD24981983A priority Critical patent/DD253353A3/en
Publication of DD253353A3 publication Critical patent/DD253353A3/en

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Abstract

Die Erfindung bezieht sich auf das Gebiet der Abwasserreinigung unter Verwendung loeslicher Elektroden und kann zur Abwasserreinigung auf Schiffen angewendet werden. Das Verfahren umfasst die Zufuhr der Abwaesser als Parallelstroeme in den Anoden- und Katodenraum der Diaphragmaelektrolysezelle unter Verwendung loeslicher Elektroden unter nachfolgender Durchmischung. Vor der Zufuhr in den Anoden- und Katodenraum der Elektrolysezelle mit den loeslichen Elektroden wird der Strom im Anodenraum bzw. Katodenraum der Diaphragmaelektrolysezelle mit den unloeslichen Elektroden behandelt, bis der p H-Wert des Anolyten 3,0...3,5 und der p H-Wert des Katolyten 10,1...10,6 erreicht.The invention relates to the field of wastewater treatment using soluble electrodes and can be applied to wastewater treatment on ships. The method comprises supplying the effluents as parallel streams into the anode and cathode compartments of the diaphragm electrolysis cell using soluble electrodes with subsequent mixing. Before being fed into the anode and cathode compartments of the electrolysis cell with the soluble electrodes, the current in the anode compartment or cathode compartment of the diaphragm electrolysis cell is treated with the non-soluble electrodes until the p H value of the anolyte reaches 3.0 p H value of the catholyte reaches 10.1 ... 10.6.

Description

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OHMCAHME M30EPETEHM K ABTOPCKOMy CBHKETEJLbCTBy 3aHBJieHo: 13.04.82 3aüBKa: Jg 3414564/23-26 MKM3 C02F 1/46 Abtoph: Γ.CSeHHH, C.A.BoraTHX, Α.Τ.Οολοββθβ, A.A.OHMCAHME M30EPETEHM K ABTOPCKOMy CBHKETEJLbCTBy 3aHBJieHo: 13.04.82 3aüBKa: Jg 3414564 / 23-26 MKM 3 C02F 1/46 Abtoph: Γ.CSeHHH, CABoraTHX, Α.Τ.Οολοββθβ, AA

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-aiaβ5- 287.81 ε-aiaβ5- 287.81 ε

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pH=4,3-4,5, a H3 KaTOjmoro npocTpaHCTBa - pH=9,I-9,3. IlepenojnocoBKa npon3BOÄHJiacL KajK^He 30 MHHyT. ΠρΗ stom Ha nOBepXHOCTH BJieKTpOÄOB 0Öpa30BHBaJICfl pHXJIHH OCaflOK.pH = 4.3-4.5, a H3 KaTOjmoro npocTpaHCTBa - pH = 9, I-9.3. Ilepenojnoco BKa npon3BOÄHJiacL KajK ^ He 30 MHHyT. ΠρΗ stom Ha nOBepXHOCTH BJieKTpOÄOB 0Öpa30BHBaJICfl pHXJIHH OCaflOK.

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H3 aHOßHoro npocTpaHCTBa, HwieJHi pH=2,9 H H3 npocTpaHCTBa pH=II,I.. Πρκ 3tom Ha KaTOfle oöpa30BHBajicH OeJMH ocaflOK, aHaJiH3 κοτοροΓΟ noKa3aji, ύγο oh coctoht iipeHMyiiiecTBeHHO H3 MgCOH)2» Πρκ ηώμθηθηηη nOJIHpHOCTH OCaHOK C ΠΟΒβρΧΗΟΟΤΗ SJieKTpOiia paCTBOpHJICH.H3 aHOßHoro npocTpaHCTBa, HwieJHi pH = 2.9 pH = H H3 npocTpaHCTBa II, I .. Πρκ 3tom Ha KaTOfle oöpa30BHBajicH OeJMH ocaflOK, aHaJiH3 κοτοροΓΟ noKa3aji, ύγο oh coctoht iipeHMyiiiecTBeHHO MgCOH H3) 2 »Πρκ ηώμθηθηηη nOJIHpHOCTH OCaHOK C ΠΟΒβρΧΗΟΟΤΗ SJieKTpOiia paCTBOpHJICH.

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ΤρΟ^ΟΒ H ΑΗβφρείΓΜΘΗΗΟΜ 3JIeKTpOJIH3epe C paCTBOpHMHMH 3jieKTpo,n;aMH Ha noBepxHocTH 3JieKTpoÄOB oopasoBBmajicH ocanoK, npeiiHTCTByKinHH sjieKTpoxHMH^ecKoS o^HCTKe HHX BO1H;, a Ha noBepxHocTii γρεΦητοβηχ sjieKTpojOB npn 3jieKTpojiH3e 6e3 nepenojnocoBKH Taicate oöpasyeTCH oca^oK KOTOpHH y^aJIHeTCH ΠρΗ H3MeHeHHH nOJIHpHOCTH 3JIeKTpOJ[OB.ΤρΟ ^ ΟΒ H ΑΗβφρείΓΜΘΗΗΟΜ 3JIeKTpOJIH3epe C paCTBOpHMHMH 3jieKTpo, n; AMH Ha noBepxHocTH 3JieKTpoÄOB oopasoBBmajicH ocanoK, npeiiHTCTByKinHH sjieKTpoxHMH Eckos ^ o ^ HCTKe HHX BO 1 H ;, a Ha noBepxHocTii γρεΦητοβηχ sjieKTpojOB npn 3jieKTpojiH3e 6e3 nepenojnocoBKH Taicate oöpasyeTCH oca ^ oK KOTOpHH y ^ aJIHeTCH ΠρΗ H3MeHeHHH nOJIHpHOCTH 3JIektpOJ [OB.

JIaHHHe, nojiy^eHHHe npH nonane β κβ.το%ηυώ KaMepy iPsa$paiMeHHoro 3JieKTpojni3epa nojmiejioHeHHHx η β aHOÄHyiJIaHHHe, nojiy ^ eHHHe npH nonane β κβ.το% ηυώ KaMepy iPsa $ paiMeHHoro 3JieKTpojni3epa nojmiejioHeHHHx η β aHOÄHyi

- nOÄKHCJieHHHX CTO^HHX BOJi; ΠρΗΒβίζβΗΗ B TaOJfflliax 1,2. HcOHTaHHH ΠρΗ KaS1ITOM 3Ha^eHHH pH npOBOÄHJIHCL B- nOÄKHCJieHHHX CTO ^ HHX BOJi; ΠρΗΒβίζβΗΗ B TaOJfflliax 1,2. HcOHTaHHH ΠρΗ KaS 1 ITOM 3Ha ^ eHHH pH npOBOÄHJIHCL B

20 "qacoB, nocjie HcnHTaHHfi οπτιγίθοκημ HajiH"qHe cjioh γελροκοηηοβ Ha20 "qacoB, nocjie HcnHTaHHfi οπτιγίθοκημ HajiH" qHe cjioh γελροκοηηοβ Ha

(+)(+) KaTOAHOKaTOAHO - 3 -- 3 - Taöjnma I.Taojnma I. npocTpaHCTBOnpocTpaHCTBO (-)(-) .y,i«y,o,y, • · ·.y, i «y, o, y, • · · e προcTpaHCTBOe προcTpaHCTBO is,9:3,7:3,5:3,3:3,i:2,9:2,7:2,5 ·'* · * · ·.· ·is, 9: 3.7: 3.5: 3.3: 3, i: 2.9: 2.7: 2.5 · '* · * · · · · · 5:9,7:9,9:io,i:io,3:io,7:io,9;n,i • · ♦ · a · ·5: 9.7: 9.9: io, i: io, 3: io, 7: io, 9; n, i • · ♦ · a · · ι ι ^- _^ ^- ^- ^- . ^ι ι ^ - _ ^ ^ - ^ - ^ - . ^ pHpH Ha eHa e + + - - - -+ + - - - - HaniraaeHaniraae "Q "MO"Q" MO CJIOH THJC-CJIOH THJC- • • • •• • • • POKCHÄOB 9ΛβΚΤρθίίPOKCHÄOB 9ΛβΚΤρθίί (+)(+) ÄHOflHOeÄHOflHOe TaojDma 2. ,TaojDma 2., 4,5:4,3:4,14.5: 4.3: 4.1 (-)(-) + + ++ + + pHpH - Hajffl^ieHajffl ^ ie ee OTcyTCT-OTcyTCT- BHeBHe CJIOH ΓΗΑCJIOH ΓΗΑ POKCHBOB BjieKTpoÄPOKCHBOB BjieKTpoÄ

noKa3HBaioT, ^το πρπ noÄa^e β KaMepy cto-ίηηχ boä c pH> 10,1, a b aHOjmyio pH < 3,5 npHBOjiHT κ HCKMHeHHK) oopa3OBaHHH ocaitKa Ha BjieKTpoflax, ·ίτο oc5ecne^HBaeT cTaoHJiBnyio paooTy annapa-Ta - HCKJiK)-q;aeT noBHmemie HanpHaceHHfl Ha Hewi, το ecTB cHHMaeT pacxoA BHeprna Ha npoBefleHne npoiiecca.noKa3HBaioT, ^ το πρπ noÄa ^ e β KaMepy cto-ηηηχ boä c pH> 10,1, ab aHOjmyio pH <3,5 npHBOjiHT κ HCKMHeHHK) oopa3OBaHHH ocaitKa Ha BjieKTpoflax, · οτο oc5ecne ^ HBaeT cTaoHJiBnyio paoooyy annapa-Ta - HCKJiK) -q; aeT noBHmemie HanpHaceHHfl Ha Hewi, το ecTB cHHMaeT pacxoA BHeprna Ha npoBefleHne npoiiecca.

Claims (1)

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DD24981983A 1982-04-13 1983-04-14 METHOD FOR ELECTROCHEMICAL WASTEWATER CLEANING DD253353A3 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
DD24981983A DD253353A3 (en) 1982-04-13 1983-04-14 METHOD FOR ELECTROCHEMICAL WASTEWATER CLEANING

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
SU823414564A SU1318535A1 (en) 1982-04-13 1982-04-13 Method for electrochemical treatment of waste water
DD24981983A DD253353A3 (en) 1982-04-13 1983-04-14 METHOD FOR ELECTROCHEMICAL WASTEWATER CLEANING

Publications (1)

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DD253353A3 true DD253353A3 (en) 1988-01-20

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