Abstract

Aircraft de-icing fluid at 7 000 mg COD/ℓ was successfully treated in an anaerobic baffled reactor operated with and without recycle at volumetric organic loading rate of between 4 and 11 g COD/ℓreactor·d. Reactor recycle was found to improve reactor performance. The anaerobic baffled reactor operated with a 6:1 recycle ratio achieved a minimum hydraulic retention time of 17 h with an acceptable COD removal efficiency of 93% at a volumetric organic loading rate of 9.9 g COD/ℓreactor·d. This corresponded to a specific organic loading rate of 0.35 g COD/g VSS·d and specific organic removal rate of 0.32 g CODrem/g VSS·d. Without recycle similar removal efficiency was achieved; however, the loading rates were about 40% less. Due to biomass growth specific organic loading rate was not found to vary significantly through most of the experimental period despite loading rate increases. Hydrodynamically, an anaerobic baffled reactor may be characterised as an in-series continuously stirred tank reactor where the number of continuously stirred tank reactors corresponded to the number of actual compartments. Volatile fatty acid profiles tend to indicate that anaerobic baffled reactor compartmentalisation served to separate acidogenic and methanogenic activities longitudinally through the reactor, with the highest proportion of acidogenic activity in the first compartments. The net accumulated yield within the anaerobic baffled reactor was found to be of 0.007 g VSS/g CODrem when the ABR was operated without recycle and of 0.016 g VSS/g CODrem for the ABR operated with recycle. Water SA Vol.31 (3) 2005: pp.377-384

Highlights

  • Successful treatment of ADF has already been achieved using high-rate anaerobic reactors

  • Given the results of the mixing study and in consideration of the results reported by Grobicki and Stuckey (1992) it was reasonable to assume that the ABRs in this study could be represented by 4-CSTRs-in-series where a single sample would be representative of the soluble concentration within an entire compartment

  • A 1% v/v (7 000 mg COD/l) ADF wastewater was successfully treated in ABRs operated with and without recycle at OLRs varying between 4 and 11 g COD/lreactor·d

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Summary

Introduction

Successful treatment of ADF has already been achieved using high-rate anaerobic reactors. Albany International Airport (Albany, NY), achieved 95% removal efficiencies for propylene glycol based ADF using a 700 l anaerobic fluidised bed reactor (Switzenbaum et al, 2001) at an OLR of 15 kg COD/ m3reactor·d. Mulligan et al (1997) successfully treated 90% COD removal of ethylene glycol based ADF in an anaerobic multiplate reactor at an OLR of 16.5 kg COD/m3reactor·d. The complex multi-plate arrangement resulted in high capital costs as well as operational problems. Darlington and Kennedy (1998) and Pham and Kennedy (2004) reported treatment of ethylene glycol-based ADF wastewaters

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