Temperature, pH and dissolved oxygen strongly influence the aqueous Cr(VI) removal process using Fe(II). Reaction rate was increased by increasing pH from 6 to 8. At 25 oC and pH values higher than 7, maximum Cr(VI) removal was achieved at a reaction time equal or less than 5min, which in turn resulted in a second–order rate {d[Cr(VI)]/dt = kobs[Fe(II)][Cr(VI)]} coefficient kobs > 1x104 M-1s-1.
Dissolved oxygen strongly competed with Cr(VI) in Fe(II) oxidation increasing reaction ratio [Fe(II)]/[Cr(VI)] from an almost stoichiometric value 3.1 at pH 6 to 25 at pH 8. Reaction rate was also increased by increasing temperature from 10oC to 40oC, confirming the endothermic character of the reaction. Pilot scale experiments proved that the sand bed contributed to Fe(II) oxidation, improving in turn the removal of chromium recipitates. This was attributed to ferric oxy-hydroxides retained on the sand bed, whose surface hydroxyl groups coordinated with Fe(II) increasing its oxidation rate and removal.
Copyright: | © Aristotle University of Thessaloniki | |
Quelle: | 2nd International Conference 2009 (Juni 2009) | |
Seiten: | 6 | |
Preis inkl. MwSt.: | € 5,00 | |
Autor: | M. Mitrakas A. Pantazatou Roxani Tzimou-Tsitouridou C. Sikalidis | |
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Probenahme- und Analyseverfahren zur kostengünstigen Überwachung von Arzneimittelwirkstoffen im Abwasser
© DIV Deutscher Industrieverlag GmbH (6/2011)
Fachbeitrag zum vom BMWi geförderten Forschungsprojekt der GBA Gesellschaft für Bioanalytik Hamburg mbH
Behandlung von Arzneimittel(rückständen) in Krankenhaus- und kommunalem Abwasser
© Lehrstuhl für Abfallverwertungstechnik und Abfallwirtschaft der Montanuniversität Leoben (11/2010)
Einschlägige Studien zeigten in den letzten Jahren, daß kommunale Kläranlagen Arzneimittel – und deren Rückstände – sowie Komplexbildner (wie etwa EDTA und NTA) teilweise nur sehr unvollständig mit konventionellen Anlagen behandeln können. Eine Haupteintragsquelle dieser anthropogenen Stoffe stellen menschliche und tierische Fäkalien dar, welche über die Kanalisation in die Kläranlagen und dann weiter in die aquatische Umwelt gelangen. Für Komplexbildner existieren bereits einschlägige Grenzwerte, EDTA (Ethylendiamintetraessigsäure) und NTA (Nitrilotriessigsäure) werden etwa in der Wasserrahmenrichtlinie als prioritäre Substanzen definiert.
Treatability studies for an organized industrial district (OID) effluent in Bursa, Turkiye for agricultural irrigation purposes
© Aristotle University of Thessaloniki (6/2009)
The reusability of the effluent from the wastewater treatment plant of an organized industrial district in the northwest of Turkiye was investigated in this study. Chemical precipitation and ion exchange methods were used to obtain a water reusable for agricultural irrigation purposes.
Assessment of wastewater effluent quality in Thessaly region, Greece
© Aristotle University of Thessaloniki (6/2009)
The objective of the present study was to assess wastewater effluent quality in Thessaly region, Greece in order to determine whether this kind of water could be used as an alternative water resource for beneficial uses. Such uses may include agricultural as well as landscape irrigation.
Treatment of the textile effluents in a cottonseed batch reactor: Determination of optimum process conditions
© Aristotle University of Thessaloniki (6/2009)
The adsorption of Reactive Black 5 on cottonseed (CS) has been investigated in a series of batch adsorption experiments. Adsorption tests were carried out as a function of solids concentrations, conditioning time, temparature and dye dosage. The adsorption density increases with increasing the mixing time until about 30 min, and then reaches a plateau value.