Biodegradation of 2-chlorophenol (2CP) in an anaerobic sequencing batch reactor (ASBR)

2012 ◽  
Vol 65 (10) ◽  
pp. 1721-1728 ◽  
Author(s):  
Lizeth Beristain-Montiel ◽  
Jorge Gómez ◽  
Oscar Monroy ◽  
Flor de Maria Cuervo-López ◽  
Florina Ramírez-Vives

The aim of this study is to contribute to the knowledge about anaerobic digestion of 2-chlorophenol (2CP) in an anaerobic sequencing batch reactor (ASBR). Two reactors were set up (ASBRA and ASBRB). The ASBRA was fed with 2-chlorophenol (28–196 mg 2CP-C/L) and no other exogenous electron donor. The ASBRB was fed with a mixture of 2CP (28–196 mg 2CP-C/L) and phenol (28–196 mg phenol-C/L) as an electron donor. The process evaluation was conducted by three means: first by substrate consumption efficiency (E2CP), second, by biogas yield (Ybiogas-C/2CP-C) and third, by the specific consumption rates (q2CP) as response variables. The 2CP consumption efficiency (90 ± 0.4%) was not influenced by the increase in the concentrations tested. In both reactors ASBRA and ASBRB, both concentration as well as speed increased. Concentration increased from 28 to 114 mg 2CP-C/L. The specific consumption rate (q2CP) values were fivefold higher. However, a decrease of 37% was observed at 140 mg 2CP-C/L and one of 72% at 196 mg 2CP-C/L. The biogas yields (0.80 ± 0.06) remained stable in both reactors. In both reactors the biogas yield decreased to 78 ± 3% at 196 mg 2CP-C/L. We might assume this decrease was due to the accumulation of VFA. Finally, poor sludge settleability was determined only in the SBRB reactor at 140 and 196 mg 2CP-C/L. An increase was observed in both SVI ≤ 140 ± 5 mL/g and over exopolymeric protein ≤120 mg EP/L.

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

1992 ◽  
Vol 26 (9-11) ◽  
pp. 2429-2432 ◽  
Author(s):  
R. R. Dague ◽  
C. E. Habben ◽  
S. R. Pidaparti

This research focuses on an evaluation of the performance of a new process being called the “anaerobic sequencing batch reactor” (ASBR). The ASBR operates on an intermittent, fill and draw regimen. This results in alternating high substrate/low substrate (feast/famine) conditions. The high substrate conditions right after feeding results in high rates of substrate conversion to biogas. The low substrate concentration near the end of the react sequence results in efficient bioflocculation and solids separation.


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