A lab-scale reactor with a fixed-bed hematite catalyst for the effective decomposition of HO and bacteria inactivation was designed. The bactericidal effect is the largest at a low initial bacterial count of 2·10 CFU/L, which is typical for natural surface waters. When using a 5 mM HO solution and a residence time of 104 min, the reduction in the number of E. coli bacteria is about 3.5-log. At a higher initial bacterial count of 1-2·10 CFU/L, a 5 mM HO solution reduces the bacteria number by about 4-log. The HO decomposition follows the log-linear kinetics of a first-order reaction while the bacterial inactivation does not. The kinetics of bacterial inactivation was described using the Weibull model in the modified form: log(N/N) = b · t. The values of the non-linearity parameter n were found to be lower than 1, indicating that bacterial inactivation slows down over time. With increasing initial HO concentration, the rate parameter b increases while the non-linearity parameter n decreases. With increasing temperature, both parameters increase. The stability of the catalyst has been proved by XRD, FTIR, SEM, and ICP-OES. The concentration of iron leaching into water during disinfection is much lower than the limit declared by WHO for iron in drinking water. The results show that technical-grade hematite is a promising Fenton-like catalyst for water disinfection. The fixed-bed reactor can be the basis of the mobile installations for water purification in emergencies.

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http://dx.doi.org/10.1007/s11356-024-32794-0DOI Listing

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