A laboratory-scale fixed bed reactor of five stages running serially, with
free working volume of 61, and up- and down-flow successively, was used for
treating low-strength wastewater. With this design was sought a greater pa
ssage of the liquid over the support of the biofilm, constituted of waste t
yre rubber (disposable material). The objective was to demonstrate the effi
ciency of this system to purify domestic wastewaters of 1000 mg COD/1 of hi
gh microbiological load. Different hydraulic retention times (HRTs), 4, 2 a
nd 1 days, and 12 and 8 h, were studied. For HRTs from 4 to 1 days, the eff
iciency of organic matter removal in the first stage reached the maximum va
lue, and was maintained after passing the liquid through the rest of the st
ages. For 12 and 8 h, a greater variation of the removal efficiency was obs
erved among all the stages; fundamentally, in the first three. BOD removal
efficiencies greater than 60% were achieved: acceptable values for this pri
mary treatment. The variations during the process in GOD, total and suspend
ed solids, minerals and volatiles, volatile fatty acids, alkalinity, ammoni
a nitrogen and phosphorus, and faecal coliforms were determined. Good resul
ts were achieved for short HRTs, therefore, it would be possible to try a g
reater wastewater flow. The total and faecal coliform removal efficiencies
varied from 99% for 4 days to 70% for 8 h HRT. This was considered acceptab
le taking into account the high microorganisms concentration of the wastewa
ter used (1.4 x 10(10) MPN/100 ml). (C) 1999 Elsevier Science Ltd. All righ
ts reserved.