2004
DOI: 10.1016/j.jhazmat.2004.04.004
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Unhairing effluents treated by an activated sludge system

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Cited by 41 publications
(23 citation statements)
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References 16 publications
(24 reference statements)
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“…7) in the COD values (a = 0.05; P \ 0.001). The effluents derived from the dyeing processes contain non-biodegradable and dissolved compounds which must be removed via a tertiary treatment because previous biological and physicochemical processes are not able to reach effluent standards (Tabrizi and Mehrvar 2004;Vidal et al 2004;Rajkumar and Kim 2006;Vilaseca et al 2010). The results for total color removal with coagulant and DFJ (92 %) are similar to those reported by Fan et al (2007) who achieved a removal rate of 94 % using a flocculation aid along with coagulant salt.…”
Section: Resultssupporting
confidence: 79%
“…7) in the COD values (a = 0.05; P \ 0.001). The effluents derived from the dyeing processes contain non-biodegradable and dissolved compounds which must be removed via a tertiary treatment because previous biological and physicochemical processes are not able to reach effluent standards (Tabrizi and Mehrvar 2004;Vidal et al 2004;Rajkumar and Kim 2006;Vilaseca et al 2010). The results for total color removal with coagulant and DFJ (92 %) are similar to those reported by Fan et al (2007) who achieved a removal rate of 94 % using a flocculation aid along with coagulant salt.…”
Section: Resultssupporting
confidence: 79%
“…This efficiency was slightly lower than total biodegradable COD of the raw wastewater (57.4%); however, the performance of the biological treatment in the SBR was adequate (92.0% of biodegradable fraction). These results agree with those obtained by other researchers who reported COD removals from 80 to 95% when using a SBR to treat tannery effluents [11,14,30,31]. Results of the tertiary treatment showed the efficiency of the coagulation-flocculation process during COD removal (Figure 3).…”
Section: Efficiency Of Cod Removalsupporting
confidence: 91%
“…Según estos resultados, no sería viable ni recomendable aplicar un sistema de tratamiento biológico en las aguas residuales de tenerías. Sin embargo, investigadores como Vidal et al [4] y Lefebvre et al [5], lograron aplicar con éxito, tratamientos biológicos a efluentes de tenerías con relaciones DBO/DQO de 0,3, lo cual indica que la relación de biodegradabilidad mencionada no es adecuada para estos efluentes industriales. Una de las razones por las cuales la relación DBO 5,20 /DQO total no es precisa, es porque la DBO 5,20 no es un buen parámetro de referencia cuando se emplean aguas residuales de tenerías, debido a que la compleja matriz de compuestos tóxicos y no tóxicos que la conforman, son inhibitorios para la prueba de DBO 5,20 [4] y [5].…”
Section: Materiales Y Métodosunclassified
“…La relación convencional de biodegradabilidad, que relaciona la DBO 5,20 /DQO total (Tabla 1) es inferior al contenido de material biodegradable (DQOBT) obtenido mediante la prueba del fraccionamiento de la DQO (Tabla 2), especialmente para el efluente almacenado en la laguna y para la mezcla C-T. Estos resultados reforzaron que la DBO 5,20 tampoco fue un buen parámetro de referencia cuando se emplearon los efluentes de tenerías estudiados en esta investigación, coincidiendo con lo señalado por Vidal et al [4] y Lefebvre et al [5].…”
Section: Fraccionamiento De La Demanda Química De Oxígenounclassified
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