2007
DOI: 10.1016/j.supflu.2007.04.007
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Treatment of textile wastewater by SCWO in a tube reactor

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Cited by 58 publications
(17 citation statements)
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“…Figure 10.2 shows that for this set of experiments, excess oxidant concentrations greater than a certain value (here, 400 %) has no significant effect on organics conversion ratio, which is already brought to 1 here; thus further increasing the excess oxygen results in unnecessary costs without bringing any technical benefits. As expected regarding to excess oxygen use, the rate expressions obtained through kinetic experiments show that the reaction orders for oxidant have positive values close to zero [42][43][44][45].…”
Section: Initial Oxidant Concentrationsupporting
confidence: 76%
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“…Figure 10.2 shows that for this set of experiments, excess oxidant concentrations greater than a certain value (here, 400 %) has no significant effect on organics conversion ratio, which is already brought to 1 here; thus further increasing the excess oxygen results in unnecessary costs without bringing any technical benefits. As expected regarding to excess oxygen use, the rate expressions obtained through kinetic experiments show that the reaction orders for oxidant have positive values close to zero [42][43][44][45].…”
Section: Initial Oxidant Concentrationsupporting
confidence: 76%
“…In which cases, considerable fractions of organic pollutants break down into smaller molecules without being completely oxidized, and leave the reactor system in gas phase instead of remaining in the liquid effluent. The positive effect of temperature is notable for wastewater treatment both oxidation and non-oxidative decomposition reactions in SCWO reactors [42][43][44]. TOC conversions achieved by two different initial oxidant concentrations, and various reactor temperatures at olive mill wastewater treatment with SCWO [42] is shown in Fig.…”
Section: Temperaturementioning
confidence: 96%
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“…2 shows the effect of the O 2 stoichiometric ratio on TOC conversion at a fixed reaction pressure (25 MPa) and TOC concentration of the wastewater storage tank (0.57 mol L −1 ). The initial TOC and O 2 concentrations at the reactor inlet were varied by changing the flow rates of wastewater and H 2 O 2 solution to keep the residence time at a constant value of 15 s. It was found that TOC conversion increased significantly with increasing in reaction temperature [13][14][15][16]. However, as can be seen in Fig.…”
Section: Resultsmentioning
confidence: 99%
“…Conventional dye wastewater treatment methods are gradually becoming inadequate to meet the requirements of a higher environmental quality. In recent years, various advanced oxidation processes such as ozonation [2], wet air oxidation [3,4], supercritical water oxidation [5], photocatalytic oxidation [6,7], electrochemical oxidation [8][9][10][11] and other integrated techniques [12][13][14] have been proposed as substitutes for the conventional treatment techniques. Among these advanced oxidation processes, electrochemical oxidation method which uses electrons as the main reagent, only requiring a little or even no chemical reagent, is a clean and effective wastewater treatment method.…”
Section: Introductionmentioning
confidence: 99%