Performance of staged and non-staged up-flow anaerobic sludge bed (USSB and UASB) reactors treating low strength complex wastewater.
The use of anaerobic processes to treat low-strength wastewater has been increasing in recent years due to their favourable performance-costs balance. For optimal results, it is necessary to identify reactor configurations that are best suited for this kind of application. This paper reports on the comparative study carried out with two high-rate anaerobic reactor systems with the objective of evaluating their performances when used for the treatment of low-strength, complex wastewater. One of the systems is the commonly used up-flow anaerobic sludge blanket (UASB) reactor. The other is the up-flow staged sludge bed (USSB) system in which the reactor was divided longitudinally into 3, 5 and 7 compartments by the use of baffles. The reactors (9 l) were fed with a synthetic, soluble and colloidal waste (chemical oxygen demand (COD) < 1000 mg/l) and operated at 28 degrees C and 24 h hydraulic retention time. Intermediate flow hydraulics, between plug-flow and completely-mixed, in the UASB and 7 stages USSB reactors allowed efficient degradation of substrates with minimum effluent concentrations. Low number of compartments in the USSB reactors increased the levels of short-circuiting thus reducing substrate removal efficiencies. All reactors showed high COD removal efficiencies (93-98%) and thus can be regarded as suitable for the treatment of low strength, complex wastewater. Staged anaerobic reactors can be a good alternative for this kind of application provided they are fitted with a large enough (> or =7) number of compartments to fully take advantage of their strengths. Scale factors seem to have influenced importantly on the comparison between one and multi staged sludge-bed reactors and, therefore, observations made here could change at larger reactor volumes.
Sevilla-Espinosa
Susana
S
El Colegio de la Frontera Sur, Carretera Antiguo Aeropuerto Tapachula, Chiapas, Mexico.
Solórzano-Campo
Maricela
M
Bello-Mendoza
Ricardo
R
D000693:Anaerobiosis; D001419:Bacteria / Q000378:metabolism / Q000648:ultrastructure; D019149:Bioreactors / Q000592:standards*; D005232:Fatty Acids, Volatile / Q000032:analysis; D008697:Methane / Q000378:metabolism; D010100:Oxygen / Q000032:analysis; D012212:Rheology; D012722:Sewage / Q000382:microbiology*; D012995:Solubility; D013997:Time Factors; D014865:Waste Disposal, Fluid / Q000295:instrumentation*; D018508:Water Purification / Q000295:instrumentation*
D005232:Fatty Acids, Volatile; D012722:Sewage; D008697:Methane; D010100:Oxygen