RAMOS, J. B. E.; http://lattes.cnpq.br/8890576479043752; RAMOS, José Beldson Elias.
Resumo:
CETREL - a Company of Environmental Protection is responsible for the
treatment of the organic and inorganic liquid effluents dischargeds from the petrochemical
complexai Camaçari-Bahia. The organic part is treated at the Central Treatment Plant by
means ofan activated sludge, process which resultsinthe generation of 30 t/d of excess
sludge. Presently aerobic digestion is applied for sludge stabilisation, before its final
destination at land farms. Although the aerobic mechanism associated to the land farms has
proved its efflciency, it has become unsuitable because of the high energy costs. In an
attempt to reduce operational costs, an experimental investigation was carried out with the
objective to establish the technical and economical feasibility of excess sludge stabilisation
by anaerobic digestion. Pilot and bench scale units were used in the investigation. On the
basis of experimental data, it was verified that the application of anaerobic digestion is
technically feasible for CETREL sludge. The existing main aerobic digester can be
converted into an anaerobic unit and operated at environmental temperature (25 to 35°C)
with a minimum retention timeof lOdays. The removal efflciency of suspended solids
varied from 30 to 40 per cent for retention times of 10 to lódays. The latter retention time
was identified as the optimal one. The methane production was estimated at 82m3 (10 d) to
134m3 (16 d) per ton of applied volatile sludge. The results show that there is a generation
potentialof 3,8 t/d of methane from which a electric power of 800kW can be produced.
At the same time the power required in the aerobic reactor (800kW) is strongly
reduced. The total energy savings of reducing the consumption and having internai
power generation represent a total of 1600kW which at current cost of 0,07 US$/kWh
result in an economy of approximately US$1.200.000 per annum. The required
investment is estimated at US$2.000.000 so that the conversion of aerobic to anaerobic
digestion is vexy attractive from the economical point of view having a pay-back time of
less than 2 years. It was also established that anaerobic sludge, after aperiod of
settling, can be processed more easily on drying beds than aerobic sludge.