E-Andrew Sindt Creative Component S11.pdf

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AOB and NOB maximum specific growth rateTable AII.6- Expansion of best run from Table AII.3. Sumabsolute value of percent error for regular mode.Heterotrophic Yield (OHO)-24 -23 -22 -21 -20 -19 -18 -17 -16-26 226 224 223 221 220 218 216 213 211-27 216 214 213 211 209 207 204 202 199-28 205 204 202 200 198 195 193 190 193-29 194 192 190 188 185 183 181 185 190-30 188 185 182 178 174 173 177 181 187-31 181 177 173 170 170 174 177 181 185-32 171 167 163 166 170 173 177 181 186-33 158 157 160 164 167 171 175 180 185-34 172 174 176 179 181 184 187 191 19525020015010050-100-34500-50-320-30-24 AOB and NOB-23 -22 -28 maximum specific-21 -20 growth rate-19 -18 -26OHO Yield -17 -16Figure AII.4- Regular mode calibration progression for best run in Table AII.3200-250150-200100-15092
AOB and NOBmaximumspecific growthrateSum absolute value of percent errorsTable AII.7- Sum absolute value of percent error for BNR-S1 modeOHO yield-30 -25 -20 -15 -10 -5 0 5-20 250.3 507.4 473.1 441 378 303 250 313-25 515.8 414.7 401.2 366 303 231 251 315-30 464.3 382.0 356.5 299 219 171 251 310-35 471.3 430.5 379.2 299 232 208 248 295-40 479.7 431.7 384.9 325 255 209 226 267Grey values were omitted from plot500400-500400300-400300200-3002001000-15-10-50Percent adjustment from default OHO yield5-20-25-30-35-40Percent adjustmentfrom default AOBand NOB maximumspecific growth rate100-2000-100Figure AII.5- BNR-S1 mode calibration progression93
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Prediction of nutrient removal with
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Table of ContentsList of Figures ..
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3.9 Effect of COD Fractions .......
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List of FiguresFigure 2.1- Biomass
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Figure AI.14- D.O. set point itiner
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Table AI.1- Influent specifier inpu
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Chapter 1: Introduction1.1 Importan
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Chapter 2: Literature Review2.1 Nut
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has a very low cBOD concentration a
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dissolved oxygen (D.O.) at a suffic
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Denitrification using biomass decay
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Figure 2.7- Phoredox process (Rittm
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increased the mean volatile fatty a
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used model is the Activated Sludge
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conditions included a discrete fill
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3.1 Wastewater Treatment Plant Desc
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BNR-S2 operated with 1.5 hours simu
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Effluent 7.2 35 7.8 3.5 0.8 0.8 1.9
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constant width of 12.6 m over this
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Table 3.5- Sensitivity Parameters f
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3.6.2 Calibration of BNR-S1 ModeThe
Page 44 and 45: Chapter 4 Results and Discussion4.1
Page 46 and 47: include 24-hour composite samples t
Page 48 and 49: Perecent deviation (predicted - obs
Page 50 and 51: Percent deviation (predicted-observ
Page 52 and 53: Percent deviaton in value (model-ob
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Page 56 and 57: 4.2.2.2 Aerobic P/PHA uptake and P/
Page 58 and 59: Calibrated simulator parameters for
Page 60 and 61: Sum absolute value of percent devia
Page 62 and 63: Absolute value of percent deviation
Page 64 and 65: Table 4.10- BNR-S2 colder (15.7 o C
Page 66 and 67: Table 4.13- Width adjustment effect
Page 68 and 69: Percent removala linear trend from
Page 70 and 71: Chapter 5: Conclusion5.1 SummaryBio
Page 72 and 73: Chapter 6: ReferencesAlleman, J.E.,
Page 74 and 75: Libra, R. D., Wolter, C. F., and La
Page 76 and 77: Appendix IBioWin Simulation Setup74
Page 78 and 79: Figure AI.2 - Influent specifier fr
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Page 82 and 83: Figure AI.9 - SBR operation page fo
Page 84 and 85: Figure AI.13 - SBR operation page f
Page 86 and 87: Appendix IISelected BioWin Simulati
Page 88 and 89: Table AII.1- Percent deviation from
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Page 92 and 93: Sum absolute value of percent devia
Page 96 and 97: Appendix IIIMonthly Monitoring Repo
Page 98 and 99: DAYIrrig.1000'sGPDInfluentNH3-Nmg/L
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