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2018
DOI: 10.1016/j.cej.2018.04.123
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Disinfection of simulated ballast water by a flow-through electro-peroxone process

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Cited by 55 publications
(8 citation statements)
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“…Figure A depicts a significant increase of log removal with increase in applied voltage or with decrease in flow rate for the two systems. Similar results were also reported that electrochemical disinfection was enhanced at smaller flow rate and higher applied voltage. ,, Obviously, the disinfection performance of red-ox system was much better than that of ox-red system. In ox-red system, less than 3 log removal was obtained at 2.5 V/5–20 mL min –1 and 3.0 or 3.5 V/25–125 mL min –1 .…”
Section: Resultsmentioning
confidence: 99%
“…Figure A depicts a significant increase of log removal with increase in applied voltage or with decrease in flow rate for the two systems. Similar results were also reported that electrochemical disinfection was enhanced at smaller flow rate and higher applied voltage. ,, Obviously, the disinfection performance of red-ox system was much better than that of ox-red system. In ox-red system, less than 3 log removal was obtained at 2.5 V/5–20 mL min –1 and 3.0 or 3.5 V/25–125 mL min –1 .…”
Section: Resultsmentioning
confidence: 99%
“…A flow-through electroperoxone system was developed for the disinfection of two kinds of simulated ballast water, fulfilling the efficient generation of• • OH through the reaction of ozone with in-situ electrochemical generation H2O2. As a result, a higher E. coli inactivation of one order of magnitude was reached, with a very low energy consumption (0.33 and 0.12 kWh m -3 for treating both solutions) compared to ozonation and electrolysis [431]. This process was found also cost-effective and promising for simultaneous tetracycline removal and disinfection of municipal secondary effluents.…”
Section: Electro-peroxonementioning
confidence: 89%
“…Then, they conducted synthetic dye wastewater treatment experiments and discovered that the EP process can significantly improve the degradation efficiency of Orange II (TOC degradation of ≈90–96% in 30–45 min). Zhang et al [ 121 ] used EP to treat simulated ballast water and found that the inactivation of E. coli was an order of magnitude higher than that obtained with ozone oxidation and electrolysis. During the process, the EEC value was 0.33 kWh m −3 for BW1 (initial E. coli concentration: 106–107 CFU mL −1 ) with an effect of log(c/c 0 ) at −5.1, and the EEC decreased to 0.12 kWh m −3 when E. coli < 250 CFU (100 mL) −1 for BW2 (initial E. coli : 0.6 × 104 CFU mL −1 ), which was much better than the results obtained using UV (0.91 kWh m −3 ) and UV/Ag-TiO 2 /O 3 (0.44 kWh m −3 ), if only the cost of ozonation was taken into consideration.…”
Section: Coupling Ms and Cathodic Eaops As An Integrated Technologmentioning
confidence: 99%