Vivianite scaling in wastewater treatment plants: Occurrence, formation mechanisms and mitigation solutions.

Anaerobic equipment Centrifuge Heat exchanger Iron phosphate Iron reduction Wwtp

Journal

Water research
ISSN: 1879-2448
Titre abrégé: Water Res
Pays: England
ID NLM: 0105072

Informations de publication

Date de publication:
01 Jun 2021
Historique:
received: 15 01 2021
revised: 03 03 2021
accepted: 11 03 2021
pubmed: 13 4 2021
medline: 30 4 2021
entrez: 12 4 2021
Statut: ppublish

Résumé

The presence of soluble iron and phosphorus in wastewater sludge can lead to vivianite scaling. This problem is not often reported in literature, most likely due to the difficult identification and quantification of this mineral. It is usually present as a hard and blue deposit that can also be brown or black depending on its composition and location. From samples and information gathered in 14 wastewater treatment plants worldwide, it became clear that vivianite scaling is common and can cause operational issues. Vivianite scaling mainly occurred in 3 zones, for which formation hypotheses were discussed. Firstly, iron reduction seems to be the trigger for scaling in anaerobic zones like sludge pipes, mainly after sludge thickening. Secondly, pH increase was evaluated to be the major cause for the formation of a mixed scaling (a majority of oxidized vivianite with some iron hydroxides) around dewatering centrifuges of undigested sludge. Thirdly, the temperature dependence of vivianite solubility appears to be the driver for vivianite deposition in heat exchanger around mesophilic digesters (37 °C), while higher temperatures potentially aggravate the phenomenon, for instance in thermophilic digesters. Mitigation solutions like the use of buffer tanks or steam injections are discussed. Finally, best practices for safe mixing of sludges with each other are proposed, since poor admixing can contribute to scaling aggravation. The relevance of this study lays in the occurrence of ironphosphate scaling, while the use of iron coagulants will probably increase in the future to meet more stringent phosphorus discharge limits.

Identifiants

pubmed: 33845278
pii: S0043-1354(21)00243-8
doi: 10.1016/j.watres.2021.117045
pii:
doi:

Substances chimiques

Ferrous Compounds 0
Phosphates 0
Sewage 0
ferrous phosphate D07L04MRWI

Types de publication

Journal Article

Langues

eng

Sous-ensembles de citation

IM

Pagination

117045

Informations de copyright

Copyright © 2021 The Authors. Published by Elsevier Ltd.. All rights reserved.

Déclaration de conflit d'intérêts

Declaration of Competing Interest The authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper.

Auteurs

T Prot (T)

Wetsus, European Centre Of Excellence for Sustainable Water Technology, Oostergoweg 9, 8911 MA, Leeuwarden, Netherlands; Dept. Biotechnology, Delft University of Technology, Van der Maasweg 9, 2629 HZ Delft, Netherlands. Electronic address: thomas.prot@hotmail.fr.

L Korving (L)

Wetsus, European Centre Of Excellence for Sustainable Water Technology, Oostergoweg 9, 8911 MA, Leeuwarden, Netherlands.

A I Dugulan (AI)

Fundamental Aspects Mat & Energy Group, Delft University of Technology, Mekelweg 15, 2629 JB Delft, Netherlands.

K Goubitz (K)

Fundamental Aspects Mat & Energy Group, Delft University of Technology, Mekelweg 15, 2629 JB Delft, Netherlands.

M C M van Loosdrecht (MCM)

Dept. Biotechnology, Delft University of Technology, Van der Maasweg 9, 2629 HZ Delft, Netherlands.

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Classifications MeSH