Vivianite scaling in wastewater treatment plants

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

Prot, T.J.F. (TU Delft BT/Environmental Biotechnology; Wetsus, Centre for Sustainable Water Technology)
Korving, L. (Wetsus, Centre for Sustainable Water Technology)
Dugulan, A.I. (TU Delft RID/TS/Instrumenten groep)
Goubitz, K. (TU Delft RST/Technici Pool)
van Loosdrecht, Mark C.M. (TU Delft BT/Environmental Biotechnology)

2021-06-01

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.

Anaerobic equipment
Centrifuge
Heat exchanger
Iron phosphate
Iron reduction
Wwtp

http://resolver.tudelft.nl/uuid:1f9406ef-b65e-42e8-ab86-711609bae134

https://doi.org/10.1016/j.watres.2021.117045

0043-1354

Water Research, 197

Institutional Repository

journal article

© 2021 T.J.F. Prot, L. Korving, A.I. Dugulan, K. Goubitz, Mark C.M. van Loosdrecht