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Comparison between Industrial and Simulated Textile Wastewater Treatment by AOPs—Biodegradability, Toxicity and Cost Assessment

Bilińska, Lucyna, Gmurek, Marta, Ledakowicz, Stanisław·2016·Chemical Engineering Journal
DOI 10.1016/j.cej.2016.07.100
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CC-BY-NC-ND · From the PDF
Fig. 1 Chemical structure and UV-vis spectrum of Reactive Black 5 (RB5).
Fig. 1 Chemical structure and UV-vis spectrum of Reactive Black 5 (RB5).CC-BY-NC-ND · From the PDF
Fig. 2 H2O2 effect on RB5 decomposition pseudo-first order constant in the case of the O3/H2O2 and O3/UV/H2O2 processes; O3 concentration in the inlet gas mixture C G O3 = 42.3 g/Nm 3 ; the gas flow Qin = 40 L/h. C H2O2 0 = 0-0.01 M, pH = 12, UVC lamp (15 W).
Fig. 2 H2O2 effect on RB5 decomposition pseudo-first order constant in the case of the O3/H2O2 and O3/UV/H2O2 processes; O3 concentration in the inlet gas mixture C G O3 = 42.3 g/Nm 3 ; the gas flow Qin = 40 L/h. C H2O2 0 = 0-0.01 M, pH = 12, UVC lamp (15 W).CC-BY-NC-ND · From the PDF
Fig. 3 O3, O3/H2O2, O3/UV/H2O2 and UV/H2O2 processes for: A) RB5 solution 125 mg/L, B) diluted industrial wastewater (Setazol Black DPT approx. 125 mg/L), C) textile wastewater without dilution (Setazol Black DPT approx. 730 mg/L); ozone concentration C G O3 =42,3 gO3/Nm 3 , gas flow Qin = 40 L/h, C H2O2 0 = 0.005 M, pH = 12, UVC lamp (15 W).
Fig. 3 O3, O3/H2O2, O3/UV/H2O2 and UV/H2O2 processes for: A) RB5 solution 125 mg/L, B) diluted industrial wastewater (Setazol Black DPT approx. 125 mg/L), C) textile wastewater without dilution (Setazol Black DPT approx. 730 mg/L); ozone concentration C G O3 =42,3 gO3/Nm 3 , gas flow Qin = 40 L/h, C H2O2 0 = 0.005 M, pH = 12, UVC lamp (15 W).CC-BY-NC-ND · From the PDF
Fig. 4 TOC and COD removal for the decolorization of RB5 aqueous solutions A) and textile wastewater containing Setazol Black DPT: diluted one B) and not diluted one C) by ozonation, UV/H2O2, O3/H2O2, UV/O3/H2O2 (C RB5 0 = 125 mg/L, C O 3 in = 42.3 g/Nm 3 , Qin = 40 L/h, pH = 12, UVC lamp 15 W, C H2O2 0 = 0.005 and 0.01 M) and H2O2/UV process (for dye aqueous solution: C RB5 0 = 125 mg/L, C H2O2 0 = 0.2 M, pH = 6.28; for wastewater C H2O2 0 = 0.2 M, pH = 11.23).
Fig. 4 TOC and COD removal for the decolorization of RB5 aqueous solutions A) and textile wastewater containing Setazol Black DPT: diluted one B) and not diluted one C) by ozonation, UV/H2O2, O3/H2O2, UV/O3/H2O2 (C RB5 0 = 125 mg/L, C O 3 in = 42.3 g/Nm 3 , Qin = 40 L/h, pH = 12, UVC lamp 15 W, C H2O2 0 = 0.005 and 0.01 M) and H2O2/UV process (for dye aqueous solution: C RB5 0 = 125 mg/L, C H2O2 0 = 0.2 M, pH = 6.28; for wastewater C H2O2 0 = 0.2 M, pH = 11.23).CC-BY-NC-ND · From the PDF
Fig. 5 COD/TOC A), AOS B), BOD5/COD values obtained for the decomposition of RB5 aqueous solutions and COD/TOC D) AOS E), BOD5/COD F) values obtained for the decomposition of diluted wastewater by ozonation, O3/H2O2, UV/O3/H2O2 (C RB5 0 = 125 mg/L, C G O3 = 42.3 g/Nm 3 , Qin = 40 L/h, pH = 12, UVC lamp 15 W, C H2O2 0 = 0.005 and 0.01 M).
Fig. 5 COD/TOC A), AOS B), BOD5/COD values obtained for the decomposition of RB5 aqueous solutions and COD/TOC D) AOS E), BOD5/COD F) values obtained for the decomposition of diluted wastewater by ozonation, O3/H2O2, UV/O3/H2O2 (C RB5 0 = 125 mg/L, C G O3 = 42.3 g/Nm 3 , Qin = 40 L/h, pH = 12, UVC lamp 15 W, C H2O2 0 = 0.005 and 0.01 M).CC-BY-NC-ND · From the PDF
Fig. 6 Toxicity assessment for the oxidation of RB5 aqueous solutions by ozonation, O3/H2O2, UV/O3/H2O2 (C RB5 0 = 125 mg/L, C G O3 = 42.3 g/Nm 3 , Qin = 40 L/h, pH = 12, UVC lamp 15 W, C H2O2 0 = 0.005 and 0.01 M).
Fig. 6 Toxicity assessment for the oxidation of RB5 aqueous solutions by ozonation, O3/H2O2, UV/O3/H2O2 (C RB5 0 = 125 mg/L, C G O3 = 42.3 g/Nm 3 , Qin = 40 L/h, pH = 12, UVC lamp 15 W, C H2O2 0 = 0.005 and 0.01 M).CC-BY-NC-ND · From the PDF
Fig. 7 The investment A) and operating B) costs of ozone-based AOPs.
Fig. 7 The investment A) and operating B) costs of ozone-based AOPs.CC-BY-NC-ND · From the PDF

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Research works printed but not linked: 32

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Metadata

Authors
Bilińska, L., Gmurek, M., & Ledakowicz, S.
Venue
Chemical Engineering Journal
Publisher
Elsevier BV
Published
2016-12
Volume
306
Pages
550-559
ISSN
1385-8947
DOI
10.1016/j.cej.2016.07.100
Cited by
296
References
0
Language
en
Licence
Funders
  • National Center for Research and Development (PBS2/A9/22/2013)
  • Textile Company Biliński, Konstantynów Łódzki, Poland
  • Foundation for Polish Science

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