全部 标题 作者
关键词 摘要

OALib Journal期刊
ISSN: 2333-9721
费用:99美元

查看量下载量

相关文章

更多...

The Application of Response Surface Methodology in the Study of Photodegraded Industrial Dairy Effluents by the Photo-Fenton Process: Optimization and Economic Viability

DOI: 10.1155/2014/967534

Full-Text   Cite this paper   Add to My Lib

Abstract:

This study presents results from an application of Photo-Fenton process for organic-load reduction in dairy effluents. Process efficiency was evaluated in terms of percentage dissolved organic carbon, chemical oxygen demand, and biochemical oxygen demand (DOC, COD, and BOD, resp.), whose initial values were ?mg?O2?L?1, ?mg?O2 L?1, and ?mg?O2?L?1, respectively. We applied a statistical design represented by Box-Behnken factorial design inclusive of Fenton's reagent, the power of applied radiation (W), and pH factors. The set temperature value was 30°C with a reaction time of 60?min. The maximum efficiency obtained was at , Fenton reagent in the proportion of 35?g H2O2? ?3.6?g Fe2+, and ultraviolet radiation potency of 28?W. The results obtained for DOC, COD, and BOD were 81%, 90.7%, and 78.8%, respectively. Regarding the cost/benefit evaluation, the variables and their levels should be the following: pH 3.5, 35.0?g H2O2/Fe2+ 3.6?g, and 28?W?UV, obtaining a reduction in concentration of 79.5% DOC. 1. Introduction Dairy industry effluents are characterized by high volumes of water consumption and elevated organic contents and inhibited recalcitrancy for a conventional treatment [1]. The escape into the aqueous environment of such pollutants, defined as industry-relevant organic components and BOD, COD, pH, fats, and phosphates, among others, demands treatment formulas that minimize the devastating impact of effluent pollution inclusive of degraded waterways, harmed environment, and a general detriment to animal and human health [2, 3]. Economically advantageous biological processes are typically used for dairy effluent treatments regardless of a series of practical limitations [4, 5]. A common problem in this methodology is the oscillation of the organic load in the dairy effluent, resulting in expanded sludge volume and compromises to the efficiency of biological processes [5]. POAs are defined as processes with considerable capacity for hydroxyl radical (?OH) production [6, 7]. A high standard reduction potential (see (1)) for this radical is capable of oxidizing a wide variety of organic compounds to CO2, H2O, and inorganic ions from heteroatoms: Among the POAs, the use of Fe2+/Fe3+ in the presence of hydrogen peroxide under irradiation, called a Photo-Fenton reaction, is considered the most promising for remediation of effluents containing a variety of toxic nonbiodegradable organic compounds [8, 9]. Several industrial effluent treatment studies using this process have been made in recent decades [5, 8–11]. Using a process parameter optimization, the

References

[1]  V. B. Bri?o and C. R. G. Tavares, “Effluent generation by the dairy industry: preventive attitudes and opportunities,” Brazilian Journal of Chemical Engineering, vol. 24, no. 4, pp. 487–497, 2007.
[2]  B. Sarkar, P. P. Chakrabarti, A. Vijaykumar, and V. Kale, “Wastewater treatment in dairy industries—possibility of reuse,” Desalination, vol. 195, no. 1–3, pp. 141–152, 2006.
[3]  A. Alturkmani, “Anaerobic treatment of whey in stirred batch reactor,” in Dairy Industry Effluents Treatment, pp. 1–8, Homs Dairy Company Publication, 2006.
[4]  B. Demirel, O. Yenigun, and T. T. Onay, “Anaerobic treatment of dairy wastewaters: a review,” Process Biochemistry, vol. 40, no. 8, pp. 2583–2595, 2005.
[5]  R. Dalla Villa, M. R. A. Silva, F. Raquel, and R. F. Pupo Nogueira, “Potencial de aplica??o do processo foto-fenton/solar como pré-tratamento de efluente da indústria de laticínios,” Química Nova, vol. 30, no. 8, pp. 1799–1803, 2007.
[6]  S. G. Poulopoulos, F. Arvanitakis, and C. J. Philippopoulos, “Photochemical treatment of phenol aqueous solutions using ultraviolet radiation and hydrogen peroxide,” Journal of Hazardous Materials, vol. 129, no. 1–3, pp. 64–68, 2006.
[7]  H. Kusic, N. Koprivanac, and L. Srsan, “Azo dye degradation using Fenton type processes assisted by UV irradiation: a kinetic study,” Journal of Photochemistry and Photobiology A, vol. 181, no. 2-3, pp. 195–202, 2006.
[8]  D. R. Manenti, F. B. Borba, A. N. Módenes et al., “Optimization of photo-Fenton process with UV irradiation in the treatment of effluents from the processing industry by-products of food,” Revista Ciências Exatas e Naturais, vol. 11, no. 1, 2009.
[9]  D. N. Silva, A. A. E. Neto, G. M. A. Cunha, O. C. Filho, and C. A. O. Nascimento, “Processo foto-Fenton aplicado ao tratamento de águas produzidas em campos de petróleo,” Revista Brasileira de Ciências Ambientais, vol. 14, pp. 1–14, 2009.
[10]  R. R. Navarro, H. Ichikawa, and K. Tatsumi, “Ferrite formation from photo-Fenton treated wastewater,” Chemosphere, vol. 80, no. 4, pp. 404–409, 2010.
[11]  Y.-H. Huang, H.-T. Su, and L.-W. Lin, “Removal of citrate and hypophosphite binary components using Fenton, photo-Fenton and electro-Fenton processes,” Journal of Environmental Sciences, vol. 21, no. 1, pp. 35–40, 2009.
[12]  T.-Y. Wang and C.-Y. Huang, “Improving forecasting performance by employing the Taguchi method,” European Journal of Operational Research, vol. 176, no. 2, pp. 1052–1065, 2007.
[13]  L. S. Lima, H. J. Izario Filho, and F. J. M. Chaves, “Determina??o de demanda bioquímica de oxigênio para teores 5?mg?L?1 O2,” Revista Analytica, vol. 25, pp. 52–57, 2006.
[14]  APHA-AWWA, Standard Methods for the Examination of Water and Wasterwater, American Public Health Association, New York, NY, USA, 21st edition, 2005.
[15]  C. C. A. Loures, A. L. C. Peixoto, G. R. Lamas Samanamud et al., “Estudo da aplica??o de UV/Fenton (Fe2+/H2O2) no pré-tratamento de efluentes de laticínios,” in Encontro sobre Aplica??es Ambientais de Processos Oxidativos Avan?ados, vol. 1, pp. 52–53, V EPOA, S?o Paulo, Brazil, 2009.
[16]  W. F. Jaridm and M. C. Canela, “Caderno temático: fundamentos da oxida??o química no tratamento de efluente e remedia??o de solos,” iq/unicamp, uenfirj, Campinas, Brazil, 2004.
[17]  S.-H. Pan, K. V. Lo, P. H. Liao, and H. Schreier, “Microwave pretreatment for enhancement of phosphorus release from dairy manure,” Journal of Environmental Science and Health B, vol. 41, no. 4, pp. 451–458, 2006.
[18]  J.-Y. Jung, Y.-C. Chung, H.-S. Shin, and D.-H. Son, “Enhanced ammonia nitrogen removal using consistent biological regeneration and ammonium exchange of zeolite in modified SBR process,” Water Research, vol. 38, no. 2, pp. 347–354, 2004.
[19]  P. M. Ndegwa, L. Wang, and V. K. Vaddella, “Potential strategies for process control and monitoring of stabilization of dairy wastewaters in batch aerobic treatment systems,” Process Biochemistry, vol. 42, no. 9, pp. 1272–1278, 2007.
[20]  J. R. Banu, S. Anandan, S. Kaliappan, and I.-T. Yeom, “Treatment of dairy wastewater using anaerobic and solar photocatalytic methods,” Solar Energy, vol. 82, no. 9, pp. 812–819, 2008.
[21]  A. A. Mendes, E. B. Pereira, and H. F. Castro, “Biodegrada??o de águas Residuárias do Laticínios Provenientemente Tratadas por Lipases,” Brazilian Journal of Food Technology, vol. 9, no. 2, pp. 143–149, 2006.
[22]  R. F. S. Salazar, A. L. C. Peixoto, and H. J. Izario Filho, “Avalia??o da Metodologia 5220 D. Closed Reflux, Colorimetric Method para Determina??o da Demanda Química de Oxigênio (DQO) em Efluente Lácteo,” Analytica, vol. 44, pp. 55–61, 2010.

Full-Text

Contact Us

service@oalib.com

QQ:3279437679

WhatsApp +8615387084133