Design of Kinetics and Constants1. BASIC ASSUMPTION AND DEFINITION
qc = XVR /(QW XW + QE XE) V ¾ volume of aeration tank, ft3 Qw ¾ sludge wastage rate, gal/day Xw ¾ wastage sludge conc., mg/l XE ¾ MLVSS in effluent, mg/l 2. MICROORGANISM IN SYSTEM AND EFFLUENT QUALITYqc = {Y(So-SE)/(q X)} - kdX = qcY(So - S)/[q (1+kdqc)] S = KS(1+kdqc)/[qc(YK-kd)-1] Y ¾ maximum yield coefficient, mg VSS/mg BOD5 q ¾ V/Q, hydraulic detention time K ¾ maximum substrate utilization rate, mg BOD5/mg VSS× time, K=mmax /Y kd ¾ endogenous decay coefficient, 1/time Ks ¾ half-velocity constant, substrate concentration at one-half the maximum growth rate, mg BOD5/l S ¾ effluent BOD5, mg/l 3. PROCESS DESIGN AND CONTROL RELATIONSHIPRemoval efficiency: E = (So-S)/SoFood-microorganism ratio: F/M = QSo/(VX) Specific utilization rate: U = Q(So-S)/(VX) 1/time Relationship between U and qc: 1/qc= YU - kd = Y(F/M)E - kd Process control: qc= VX/(Qw XW) Operation phase: Most activated sludge treatment systems operate in the range between the declining growth phase and the endogenous phase of microorganisms. In this range, the metabolism of organic is nearly complete and sludge exhibited well settling characteristics: Use qc to control the growth rate of microorganisms and hence their degree of waste stabilization, qc = 5 ~ 15 days. | Previous Page | Main Page | Next Page|
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