Combined biological and chemical treatment of highly concentrated residual dyehouse liquors

1998 ◽  
Vol 38 (4-5) ◽  
pp. 339-346 ◽  
Author(s):  
R. Krull ◽  
M. Hemmi ◽  
P. Otto ◽  
D. C. Hempel

The combined biological and chemical treatment of highly concentrated reactive azo dye-containing residual dyehouse liquors with recalcitrant compounds was investigated in a sequencing batch reactor (SBR). The plant consists of a batch reactor in which the anoxic and aerobic phases are carried out by sequenced steps. Water-soluble reactive dyes were reductively cleft and decolorized by a facultative anaerobic bacterial mixed culture under anoxic conditions. Complete decolorization was observed up to concentrations of nearly 20 g dye/L without addition of an external auxiliar substrate. Mineralization of the cleavage products occurs with the same bacterial mixed culture in the same reactor under aerobic conditions. The biomass used for the anoxic treatment is grown in this aerobic phase by the use of split flows with readily biodegradable compounds. Because of the recalcitrant toxic character of some remaining substances, further aerobic mineralization was initiated by partial oxidation with ozone. Partial ozonization in a circulated stream with biological post-treatment of the transformed substances led to an increased reaction selectivity, to a better biological degradation and not least to a lower consumption of ozone. Due to this purification procedure involving highly concentrated residual dyehouse liquors a total decolorization and an overvall degradation of nearly 90% in DOC was achieved.

2018 ◽  
Vol 16 (2) ◽  
pp. 159-170 ◽  
Author(s):  
Ensiyeh Taheri ◽  
Mohammad Mehdi Amin ◽  
Ali Fatehizadeh ◽  
Hamidreza Pourzamani ◽  
Bijan Bina ◽  
...  

2018 ◽  
Vol 35 (12) ◽  
pp. 1322-1328
Author(s):  
Luis Enrique Lemus-Gómez ◽  
Maria Aurora Martínez-Trujillo ◽  
Isabel Membrillo-Venegas ◽  
Mayola García-Rivero

2001 ◽  
Vol 44 (5) ◽  
pp. 85-92 ◽  
Author(s):  
R. Krull ◽  
D.C. Hempel

A new developed sequencing batch process for the purification of residual water containing concentrated azo dye was investigated. Within a treatment cycle the biological anoxic decolorization, followed by an aerobic mineralization of organic metabolites in combination with the biodegradability-achieving partial oxidation with ozone are carried out sequentially. The split flow can be destructively purified to 90% with respect to the parameter DOC. It was decolorized to an extent of 98% and the toxicity measured by the bioluminescence test decreased up to 99%. With an unspecific facultative anaerobic bacterial mixed culture anoxic decolorization of the residual liquor (20 gdye/L) without addition of an external auxiliary substrate was observed. In the first phase of the treatment cycle, the azo dye-molecules are cleft at the azo bond by biochemical reduction which leads to the corresponding sulfonated aromatic amines. In the following aerobic phase the cleft products were mineralized by the same microorganisms in the same reactor. Because of the recalcitrant and respectively toxic character of a part of the remaining metabolites, further aerobic mineralization was initialized by partial oxidation with ozone. The recursive ozonization in a recircled stream with biological post-treatment of the transformed substances led to an increased reaction selectivity and lower consumption of ozone. The results have shown that the chosen sequencing batch reactor with the ozonization bypass is suitable for an effective treatment of high concentrated dyehouse liquors.


2004 ◽  
Vol 4 (5-6) ◽  
pp. 65-72
Author(s):  
G. Farabegoli ◽  
L. Pietrelli ◽  
E. Rolle ◽  
A. Sabene

The main aim of this research is to compare the efficiency of biological and chemical–physical treatments for the removal of organic azo dyes in the textile wastewater. Regarding the biological reduction of the wastewater colour the anaerobic/aerobic (ANA/AER) sequential step-treatment provides the best reductions in colour and COD. A lab-scale Sequencing Batch Reactor (SBR) fed with synthetic wastewater and mono-azo dye (at the initial concentration of 25 mg/l) was used achieving 84% colour reduction and 82% COD removal. Chemical–physical treatments were performed using the oxidative method with Fenton's reagent and adsorption on the activated carbon achieving respectively colour reduction over 90% (from the initial concentration of 250 mg/l) and 155 mg col/g GAC total adsorption capacity (from the initial concentration of 1 g/l).


2015 ◽  
Vol 85 ◽  
pp. 327-336 ◽  
Author(s):  
Rita D.G. Franca ◽  
Anabela Vieira ◽  
Ana M.T. Mata ◽  
Gilda S. Carvalho ◽  
Helena M. Pinheiro ◽  
...  

2018 ◽  
Vol 5 (4) ◽  
pp. 907-917 ◽  
Author(s):  
Hassan Khorsandi ◽  
Nahid Ghochlavi ◽  
Ali Ahmad Aghapour

2004 ◽  
Vol 50 (6) ◽  
pp. 241-250 ◽  
Author(s):  
N. Yagci ◽  
G. Insel ◽  
N. Artan ◽  
D. Orhon

This paper improves the modeling of enhanced biological phosphate removal, by introducing the mechanistic description of a mixed culture of glycogen and phosphate accumulating organisms competing for acetate, and glycogen metabolism of the latter. A new process stoichiometry is defined for the mixed culture based upon previously developed metabolic concepts and models. The proposed model is tested with and used for the calibration of experimental data generated by a sequencing batch reactor operated with acetate feeding at a P/Ac ratio of 0.05 mgP mg-1COD. The calibration yielded acceptable numerical results for all the model coefficients tested and supported the validity of selected metabolic relationships for process stoichiometry. It also defined conditions that allow the system to sustain glycogen accumulating organisms with significant impact on process behaviour and performance.


Author(s):  
Marta Cerruti ◽  
Berber Stevens ◽  
Sirous Ebrahimi ◽  
Abbas Alloul ◽  
Siegfried E. Vlaeminck ◽  
...  

Graphical AbstractSequencing batch reactor enrichment and aggregation of purple non-sulfur bacteria.


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