Journal
WATER RESEARCH
Volume 197, Issue -, Pages -Publisher
PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.watres.2021.117045
Keywords
Wwtp; Iron phosphate; Iron reduction; Centrifuge; Anaerobic equipment; Heat exchanger
Funding
- Dutch Ministry of Economic Affairs
- European Union Regional Development Fund
- Province of Fryslan
- Ministry of Infrastructure and Environment
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The article highlights the issue of vivianite scaling in wastewater sludge, caused by the presence of soluble iron and phosphorus. Vivianite scaling was found to be common in wastewater treatment plants worldwide, with identified formations occurring in anaerobic zones, dewatering centrifuges of undigested sludge, and heat exchangers around mesophilic digesters. Mitigation solutions and best practices for safe sludge mixing were discussed in the study, emphasizing the relevance of ironphosphate scaling and the potential increase in the use of iron coagulants in the future to meet stricter phosphorus discharge limits.
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.& nbsp; & nbsp;(C)& nbsp;& nbsp;2021 The Authors. Published by Elsevier Ltd. This is an open access article under the CC BY license ( http://creativecommons.org/licenses/by/4.0/ )
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