dave stropky, paul nowak, suqin dong process simulations ltd. konstantin pougatch, martha salcudean...
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Dave Stropky, Paul Nowak, Suqin DongProcess Simulations Ltd.
Konstantin Pougatch, Martha SalcudeanUniversity of British Columbia
P.S. Pagoria, W.A. Barkley, C.W. BryantWeyerhaeuser Paper Company
CFD Predictions CFD Predictions in Largein Large
Mechanically Aerated LagoonsMechanically Aerated Lagoons
ContentsContents
Introduction
Aerated Lagoon CFD Model Lagoon Hydraulics RTD Predictions Biological Model
Application Weyerhaeuser Grande Prairie
Industrial Application
Conclusions
Introduction
IntroductionIntroductionMotivation: Improvement of lagoon performance through a deeper understanding of the hydraulics. Development of Residence Time Distribution (RTD) curves without dye studies.
Goal: Develop a 3-D Computational Fluid Dynamics (CFD) hydraulic model of a large aerated industrial lagoon.
IntroductionIntroduction
Performance FactorsIncorporated in Model
Basin shape
Inflow rate and position
Aerators: Number, position, HP
Baffles/Curtains
Sludge accumulation profile
Biology
Aerated LagoonCFD Model
Aerated Lagoon GeometryAerated Lagoon Geometry
Aerators
Inlets
Baffles
Outlet
CFD Grid
Bottom Sludge ProfilesBottom Sludge Profiles
Aerators #13 and #16
y = 5.118E-11x6 - 2.591E-08x5 + 4.587E-06x4 - 3.219E-04x3 + 6.469E-03x2 + 1.046E-01x
0.0
3.0
6.0
9.0
12.0
15.0
18.0
0 25 50 75 100 125 150
R (ft)
Slu
dg
e D
ep
th (
ft)
All Data Except 13 SW
Poly. (All Data Except 13 SW)
MeasurementData
Surface GenerationAlgorithm
RTD Prediction MethodsRTD Prediction Methods
days164.8meanT
Case Tmean Tpeak TmedianAge Equation
(exit)TCPU
Particle 8.244 4.336 6.969 0.92Dye 8.364 4.502 7.086
8.37757.0
Particlevs.Dye
0
0.03
0.06
0.09
0.12
0.15
0 0.25 0.5 0.75 1 1.25 1.5 1.75 2t / tmean
E(t)
Dye
Particle
Gxvx Ddt2dt)(d
cD)c(t
c 2
v
t
tDVMean
Age
)0(SBOD
)0(LBOD
)0(4PO
)0(DO
)0(ZX
DO
SBOD
LBOD
4PO
XZ
dt
Xd
dt
POd
dt
LBODd
dt
SBODd
dt
DOd
Z
4
SBOD
4PO
ZX Ben
thal
Pha
se
Aeration
Biological ModelBiological Model
LBODLignin based BOD. LBOD, specific to pulp and paper, converts to SBOD at a given rate. It needs to be accounted for to correlate with measured SBOD concentrations in the effluent.
SBOD Soluble BOD
XZ Active biomass (viable bacteria)
DO Dissolved oxygen
PO4 Nutrient phosphorus
Biological ModelBiological Model
Rate Equations
LBODLBOD
Lkd t
d
feedbac kbenthalLBODXZ
SBOD
SBODXZOBRY
SBOD
SBODXZOBR
SBOD
conversion LBODfrom Production
XZ of deathfrom Production
Growth) ( nConsumptioEnergy) ( nConsumptio
)()(
1
LLdeath
SS
kYOBRk
Kk
KkY
d t
d
DepositionDeath
Growth
Equation SBOD
XZXZ(Grow th) nC ons umptioOBR
XZ depos itiondeath kk
d t
d 1
feedbac kbenthalD eathGrow thPO
Eq.XZEq.XZ
PXYd t
d )4(
AerationGrow th)(Energy nC ons umptioD O
EquationSBOD
d t
d )(
Throttled by DO (both) and PO4 (growth)
Applications
Weyerhaeuser Grande PrairieWeyerhaeuser Grande Prairie
Grande Prairie is a >850,000 m3, two cell lagoon 5.29m deep (18ft) with an operating water depth of 4.57m (15ft) when clean. Cell 1 is 326m x 323m, and cell 2 is 326m x 312m. Cell 2 has two flow baffles. The 1997 volume flow rate is 622 l/s from the south inlet, and the 2005 flow is 632 l/s from the north inlet. Each floating aerator is 75HP and circulates 1286 l/s of liquid. The 1997 configuration has 25 aerators (18 in cell1 and 7 in cell2). The 2005 configuration has 27 aerators (19 in cell 1 and 8 in cell 2).
2005 Hydraulic Flowfield2005 Hydraulic Flowfield
Vertical magnification x10
1997 Grande Prairie Field Study Comparison1997 Grande Prairie Field Study Comparison
0
0.01
0.02
0.03
0.04
0.05
0.06
0.07
0.08
0.09
0 5 10 15 20 25 30 35 40
T(days)
E(t)
Measurement
Computation
T0 Tpeak Tmean Tmedian Theory Tmean
Measurement 1.1 5.7 11.3 9.5 11.6
Computation 1.3 7.9 12.0 10.3 11.6
Model sludge profile estimated.Unknown at time of dye study.
Grande Prairie Aerator OptimizationGrande Prairie Aerator Optimization
0.00
0.01
0.02
0.03
0.04
0.05
0.06
0.07
0 5 10 15 20 25 30 35 40
T(Days)
E(T
)
Optimized Layout
Initial Layout
T0 Tpeak Tmean Tmedian Theory Tmean
Initial 1.3 8.0 16.6 13.7 16.6
Optimized 3.4 12.4 17.1 15.9 16.6
Initial
Optimized
Biological ModelBiological Model
Biological ModelBiological Model
LBOD SBOD XZ DO PO4
Inlet Measurement 267 297 5.5 0 1
Mid Channel Measurement 25 128 4.3 0.7
Mid Channel CFD Prediction 186 33 102 1.1 0.1
Outlet Measurement 13 21 4.2 1.2
Outlet CFD Prediction 126 28 49 0.1 1.6
A three dimensional CFD model has been developed for predicting detailed hydraulic performance (including RTD curve prediction) in large mechanically aerated lagoons.
Using this model, wastewater engineers can combine their existing knowledge and expertise with the established power of CFD. The operation of an existing aerated lagoon can be fully analyzed over a range of operational parameters (aerator numbers, positions, and capacities; baffle installation; influent flowrate and location; bottom sludge profile, etc.) without running field dye studies. The method constitutes an efficient and powerful tool for improving lagoon performance and optimizing lagoon
ConclusionsConclusions
A simplified aerobic biological model has been developed and coupled into the hydraulic CFD model. Through this coupling, three dimensional variation and evolution of the biological processes can be predicted within the lagoon. Prediction of BOD removal is a natural consequence of the three dimensional interplay (including deposition and feedback) between bacteria solids, BOD, and nutrients, and also of the dissolved oxygen supplied through individual aerators.
Initial results show promise and provide a pathway towards a deeper understanding of the wastewater treatment in these lagoons.
ConclusionsConclusions