542
J. Lohmann
Fig. 8
Specific BOD reduction costs of the combined trickling filter/activated sludge process
C s = f (Th, Tfc , C B 0 D ) at F = 1000 kg/h, η 0 = 95 %
?2
·*
Efficiency[%]
-*
?i
Fig. 9
Specific BOD reduction costs of the combined trickling filter/activated sludge process
C s = f ( Vi, Tfc, r? 0 ) at F = 1000 kg/h, C ί O D = 5000 mg/1
J. Lohmann
Fig. 8
Specific BOD reduction costs of the combined trickling filter/activated sludge process
C s = f (Th, Tfc , C B 0 D ) at F = 1000 kg/h, η 0 = 95 %
?2
·*
Efficiency[%]
-*
?i
Fig. 9
Specific BOD reduction costs of the combined trickling filter/activated sludge process
C s = f ( Vi, Tfc, r? 0 ) at F = 1000 kg/h, C ί O D = 5000 mg/1