Attachment 14
Heat and Material Balance
SUNCOR LEWIS PH 1 2HEAT MATERIAL BALANCE TABLE
1000 1001 1002 1003 1004 1005 1006 1007 1008 1009 1010 1011 1012 1013 1014 1015 1016 1017 1018 1019Produced emulsion
De‐gassed Emulsion
Cooled Emulsion Cooled Emulsion Wet dilbit Produced Water Produced Gas Produced Gas Produced Water Produced Water Dilbit Dilbit Dilbit Produced Gas Produced Gas Produced Gas DiluentRecovered Diluent
Recovered Diluent
Produced Gas
CPF B/L Inlet Separator Emul./BFW HE Static Mixer FWKO FWKO Inlet Separator FWKO Treater FWKO / Treater Treater Dilbit Cooler Dilbit Header Treater Gas Boot PG HeaderDiluent Rec.
Cooler Diluent Rec. Trim Cooler
Diluent Rec. Pumps
Diluent Rec. Separator
Inlet Separator Emul./BFW HE Static Mixer FWKO Treaters PW HeaderEvap. Vent Condenser
PG Header PW Header CFU Gas Boot Dilbit Header HC Tank farm PG Header PG HeaderDiluent Rec.
CoolerDiluent Rec. Trim Cooler
Diluent Rec. Separator
FWKO Feed Header
MFG Drum
Vapour Fraction 0.000 0.000 0.000 0.001 0.008 0.000 1.000 1.000 0.000 0.000 0.265 0.000 0.062 1.000 1.000 1.000 0.087 0.019 0.000 1.000Operating Temperature °C 193.0 194.6 141.1 136.1 135.5 136.1 181.3 127.3 135.5 136.1 122.1 55.0 53.0 127.4 120.5 122.1 54.0 12.0 12.6 11.5
Operating Pressure kPaa 2,000 1,794 1,494 1,394 1,294 1,179 423 460 1,179 1,179 600 530 93 460 460 460 410 403 1,394 353Mass Flow kg/h 1,088,173 1,105,337 1,105,337 1,168,296 361,942 804,523 651 1,831 34,454 838,977 326,071 304,526 304,526 1,417 22,546 30,138 30,138 30,138 29,835 303
Mass Density kg/m3 862.0 870.2 918.1 851.8 759.7 915.0 2.1 6.9 917.5 915.2 133.0 970.4 128.4 7.1 8.0 8.0 86.1 284.6 657.8 4.4Molecular Weight kg/kgmole 23.58 23.46 23.46 24.26 102.70 18.04 18.49 48.02 18.02 18.04 206.00 261.20 261.20 49.15 53.77 53.96 53.96 53.96 54.44 28.68
Mass Heat Capacity kJ/kg‐C 4.21 4.23 3.95 3.87 2.45 4.50 2.05 2.11 4.51 4.50 2.14 1.88 1.86 2.11 2.09 2.10 2.54 2.34 2.35 1.73Thermal Conductivity W/m‐K 0.000 0.477 0.483 0.000 0.000 0.686 0.037 0.027 0.688 0.686 0.000 0.115 0.000 0.026 0.024 0.024 0.000 0.000 0.114 0.025
Combined Liquid 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0Mass Flow kg/h 1,088,024 1,105,337 1,105,337 1,166,465 360,525 804,487 0 0 34,454 838,942 303,494 304,526 300,182 0 0 0 27,782 29,835 29,835 0
Std Ideal Liq Vol Flow m3/h 1,088 1,105 1,105 1,197 388 806 0 0 35 841 319 320 313 0 ‐ 0 42 46 46 ‐Actual Volume Flow m3/h 1,248 1,270 1,204 1,290 410 877 0 0 38 915 331 314 308 0 ‐ 0 45 45 45 ‐
Mass Density kg/m3 872.2 870.2 918.1 904.3 879.5 916.9 940.8 915.3 917.5 917.0 917.9 970.4 974.3 917.4 ‐ 976.3 617.6 657.4 657.8 ‐Molecular Weight kg/kgmole 23.58 23.46 23.46 24.24 103.15 18.04 535.10 322.88 18.02 18.04 260.94 261.20 274.49 323.53 ‐ 392.08 54.50 54.44 54.44 ‐
Viscosity cP 2.55 2.51 9.64 1.24 3.71 0.20 55.90 17.81 0.20 0.21 4.00 127.81 175.75 18.37 ‐ 83.16 0.21 0.28 0.28 ‐Thermal Conductivity W/m‐K 0.47 0.48 0.48 0.42 0.11 0.69 0.12 0.11 0.69 0.69 0.10 0.12 0.12 0.11 ‐ 0.11 0.10 0.11 0.11 ‐
OilMass Flow kg/h 268,337 268,274 267,779 326,955 324,440 1,176 0 0 0 1,176 303,494 304,334 144,259 0 0 0 25,388 27,399 27,400 0
Std Ideal Liq Vol Flow m3/h 266 266 266 356 352 1 0 0 ‐ 1 319 320 143 0 ‐ 0 40 44 44 ‐Actual Volume Flow m3/h 296 297 286 375 371 1 0 0 ‐ 1 331 314 141 0 ‐ 0 43 43 43 ‐
Mass Density (Note 3) kg/m3 901.1 900.2 932.6 854.7 856.8 856.3 941 915 ‐ 856.3 856.3 933.6 934.8 917 ‐ 976 597 637 638 ‐API Gravity (STD) °API 10 10 10 14 21 10 68 98 ‐ 10 22 17 17 95 ‐ 88 88 88 87 ‐Molecular Weight kg/kgmole 413.35 415.31 433.10 214.99 217.40 229.26 535.10 322.88 ‐ 229.23 260.94 263.44 374.40 323.53 ‐ 392.08 67.36 66.37 66.36 ‐Viscosity (Note 4) cP 9.91 9.90 39.17 3.90 4.10 4.04 55.90 17.81 ‐ 4.00 4.00 127.89 175.75 18.37 ‐ 83.16 0.17 0.24 0.23 ‐
Thermal Conductivity W/m‐K 0.129 0.130 0.124 0.094 0.095 0.097 0.121 0.109 ‐ 0.097 0.103 0.115 0.122 0.109 ‐ 0.111 0.095 0.106 0.105 ‐Water
Mass Flow kg/h 819,687 837,063 837,558 839,510 36,085 803,311 0 0 34,454 837,766 0 192 0 0 0 0 2,393 2,436 2,435 0Std Ideal Liq Vol Flow m3/h 821 839 839 841 36 805 ‐ ‐ 35 839 ‐ 0 ‐ ‐ ‐ ‐ 2 2 2 ‐Actual Volume Flow m3/h 951 973 918 915 39 876 ‐ ‐ 38 914 ‐ 0 ‐ ‐ ‐ ‐ 2 2 2 ‐
Mass Density kg/m3 861.8 859.9 912.6 917.1 917.6 917.0 ‐ ‐ 917.5 917.0 ‐ 984.5 ‐ ‐ ‐ ‐ 985.3 1,017.2 1,017.1 ‐Viscosity cP 0.14 0.14 0.19 0.20 0.20 0.20 ‐ ‐ 0.20 0.20 ‐ 0.50 ‐ ‐ ‐ ‐ 0.51 1.23 1.21 ‐
Thermal Conductivity W/m‐K 0.669 0.668 0.688 0.688 0.688 0.688 ‐ ‐ 0.688 0.688 ‐ 0.649 ‐ ‐ ‐ ‐ 0.648 0.590 0.591 ‐Vapour
Mass Flow kg/h 149 0 0 1,831 1,417 36 651 1,831 0 35 22,577 0 4,344 1,417 22,546 30,138 2,356 303 0 303Std Gas Flow STD_m3/h 192 ‐ ‐ 901 682 17 832 901 ‐ 17 9,925 ‐ 1,709 682 9,915 13,207 1,155 250 ‐ 250
Molecular Weight kg/kgmole 18.3 ‐ ‐ 48.0 49.1 49.3 18.5 48.0 ‐ 49.2 53.8 ‐ 60.1 49.1 53.8 54.0 48.2 28.7 ‐ 28.7Mass Density kg/m3 9.9 ‐ ‐ 22.4 21.3 19.2 2.1 6.9 ‐ 19.2 10.6 ‐ 2.1 7.1 8.0 8.0 7.7 5.0 ‐ 4.4
Viscosity cP 0.014 ‐ ‐ 0.011 0.011 0.011 0.013 0.011 ‐ 0.011 0.010 ‐ 0.007 0.010 0.009 0.010 0.010 0.011 ‐ 0.011Cp/(Cp‐R) (Ideal Gamma) 1.1 ‐ ‐ 1.1 1.0 1.1 1.3 1.1 ‐ 1.1 1.0 ‐ 1.0 1.1 1.1 1.1 1.1 1.1 ‐ 1.2
Z Factor 0.9 ‐ ‐ 0.9 0.9 0.9 1.0 1.0 ‐ 0.9 0.9 ‐ 1.0 1.0 0.9 0.9 0.9 1.0 ‐ 1.0Thermal Conductivity W/m‐K 0.0 ‐ ‐ 0.0 0.0 0.0 0.0 0.0 ‐ 0.0 0.0 ‐ 0.0 0.0 0.0 0.0 0.0 0.0 ‐ 0.0
H2O 0.9867 0.9871 0.9871 0.9684 0.5790 0.9998 0.7838 0.2293 1.0000 0.9998 0.0766 0.0109 0.0109 0.2418 0.2590 0.2421 0.2421 0.2421 0.2467 0.0035H2S 0.00000 0.00000 0.00000 0.00001 0.00003 0.00000 0.00032 0.00043 0.00000 0.00000 0.00006 0.00001 0.00001 0.00042 0.00019 0.00021 0.00021 0.00021 0.00019 0.00131CO2 0.0001 0.0001 0.0001 0.0001 0.0009 0.0001 0.0204 0.0251 0.0000 0.0001 0.0016 0.0002 0.0002 0.0219 0.0054 0.0072 0.0072 0.0072 0.0053 0.1078
Helium 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000Nitrogen 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
Air 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000Methane 0.0003 0.0001 0.0001 0.0003 0.0024 0.0000 0.1937 0.1214 0.0000 0.0000 0.0036 0.0002 0.0002 0.0908 0.0129 0.0232 0.0232 0.0232 0.0114 0.6345Ethane 0.0000 0.0000 0.0000 0.0001 0.0008 0.0000 0.0000 0.0176 0.0000 0.0000 0.0016 0.0003 0.0003 0.0161 0.0052 0.0064 0.0064 0.0064 0.0056 0.0483
Propane 0.0000 0.0000 0.0000 0.0004 0.0049 0.0000 0.0000 0.0507 0.0000 0.0000 0.0099 0.0032 0.0032 0.0501 0.0285 0.0315 0.0315 0.0315 0.0308 0.0666C4+ 0.0129 0.0127 0.0127 0.0307 0.4120 0.0001 0.0018 0.5555 0.0000 0.0001 0.9067 0.9852 0.9852 0.5788 0.6888 0.6893 0.6893 0.6893 0.7000 0.1380
NOTES:1. Values are for each 40,000 bpd phase for Phases 1 & 2. SUNCOR LEWIS PH 1 & 2
AREA 1000 ‐ OIL TREATINGHEAT AND MATERIAL BALANCE
PROJECT # DRAWING NUMBER REVISION
40,000 BPSD
Stream Number
To
Overall Composition Mole Fraction
Overall
Stream Name
From
Area 1000 HMB (1,2) - Page 1 of 12
SUNCOR LEWIS PH 1 2HEAT MATERIAL BALANCE TABLE
2000 2001 2002 2003 2004 2005 2006 2007 2008 2009 2010 2011 3000 3001 3002 3003 3004 3005 3006 3007
Produced water CFU froth De‐oiled waterDe‐oiled /
makeup waterCasing gas Slop vapours Slop oil Slop water Produced Gas Produced Gas PG Condensate Produced Gas Evap vapors
Combined vapors
Condensate Condensate Distillate Evaporator BD Vapors Ejector gas
Produced water header
CFU CFUProducedWater Surge Drum
B/L Pipeline Slop Vessel Slop Vessel Slop VesselProduced Gas
HeaderProduced Gas Condenser
PG Condensate Pump
PG Condenser Separator
Evaporator HeaderEvap Vent Condenser
Evap Cond. Pumps
Evaporator Evaporator Evap Vent Cond
Separator Fuel gas header
CFU Slop VesselProducedWater Surge Drum
Evaporator Slop vesselProduced Gas
HeaderGas Boot CFU
Produced Gas Condenser
PG Condenser Separator
Slop VesselProduced Gas
HeaderEvap. Vent Condenser
Evap. Vent Condenser
Evap Vent Cond Separator
PW Surge DrumBFW Surge
DrumDisposal Water Treatment
Produced Gas header
Produced gas header
Vapour Fraction 0.000 0.163 0.000 0.000 1.000 1.000 0.000 0.000 1.000 0.430 0.000 1.000 1.000 1.000 0.001 0.000 0.000 0.000 1.000 1.000Operating Temperature °C 135.9 121.1 135.1 123.3 176.3 130.4 131.0 131.1 134.7 60.0 60.0 59.8 112.2 112.4 60.0 60.0 115.6 55.0 60.0 20.3
Operating Pressure kPaa 1,179 493 779 507 594 423 600 1,200 423 403 493 353 151 151 100 507 172 150 100 353Mass Flow kg/h 868,631 30,458 840,794 947,591 2,716 6,664 1,002 29,654 7,315 7,315 4,104 3,211 28,786 28,838 28,838 28,786 890,736 28,049 41 1,684
Mass Density kg/m3 915.4 17.2 917.1 928.0 3.0 2.4 938.6 921.5 2.3 6.3 978.1 2.4 0.9 0.9 473.9 980.6 946.1 985.5 1.3 2.6Molecular Weight kg/kgmole 18.04 18.67 18.02 18.02 18.02 18.56 426.02 18.02 18.55 18.55 18.26 18.94 18.02 18.03 18.03 18.02 18.02 18.02 36.27 18.14
Mass Heat Capacity kJ/kg‐C 4.50 4.01 4.51 4.46 1.99 2.14 2.11 4.49 2.14 3.36 4.29 2.16 1.92 1.92 4.32 4.33 4.24 4.18 1.05 2.09Thermal Conductivity W/m‐K 0.686 0.000 0.688 0.687 0.032 0.036 0.124 0.688 0.036 0.000 0.638 0.036 0.026 0.026 0.000 0.654 0.686 0.649 0.021 0.031
Combined LiquidMass Flow kg/h 868,597 25,516 840,792 947,591 0 0 1,002 29,654 0 4,104 4,104 0 0 0 28,796 28,786 890,736 28,049 0 0
Std Ideal Liq Vol Flow m3/h 870 26 843 950 ‐ ‐ 1 30 0 4 4 ‐ ‐ ‐ 29 29 893 28 ‐ ‐Actual Volume Flow m3/h 947 27 916 1,021 ‐ ‐ 1 32 0 4 4 ‐ ‐ ‐ 29 29 941 28 ‐ ‐
Mass Density kg/m3 917.1 930.7 917.7 928.0 ‐ ‐ 938.6 921.5 876.7 978.1 978.1 ‐ ‐ ‐ 980.5 980.6 946.1 985.5 ‐ ‐Molecular Weight kg/kgmole 18.04 18.69 18.02 18.02 ‐ ‐ 426.02 18.02 314.94 18.26 18.26 ‐ ‐ ‐ 18.02 18.02 18.02 18.02 ‐ ‐
Viscosity cP 0.20 0.25 0.20 0.22 ‐ ‐ 53.63 0.21 10.26 0.48 0.48 ‐ ‐ ‐ 0.46 0.46 0.24 0.50 ‐ ‐Thermal Conductivity W/m‐K 0.686 0.652 0.688 0.687 ‐ ‐ 0.124 0.688 0.119 0.638 0.638 ‐ ‐ ‐ 0.653 0.654 0.686 0.649 ‐ ‐
OilMass Flow kg/h 1,177 955 26 0 0 0 1,001 0 0 61 61 0 0 0 0 0 0 0 0 0
Std Ideal Liq Vol Flow m3/h 1 1 0 ‐ ‐ ‐ 1 ‐ 0 0 0 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ Actual Volume Flow m3/h 1 1 0 ‐ ‐ ‐ 1 ‐ 0 0 0 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐
Mass Density (Note 3) kg/m3 885.8 948.6 943.0 ‐ ‐ ‐ 938.6 ‐ 876.7 840.6 840.7 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐API Gravity (STD) °API 10.16 36.96 10.15 ‐ ‐ ‐ 9.00 ‐ 127.48 127.48 10.48 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐Molecular Weight kg/kgmole 228.88 437.69 446.34 ‐ ‐ ‐ 426.03 ‐ 314.94 161.84 161.84 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐Viscosity (Note 4) cP 7.33 84.85 60.66 ‐ ‐ ‐ 53.63 ‐ 10.26 8.96 8.95 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐
Thermal Conductivity W/m‐K 0.097 0.125 0.125 ‐ ‐ ‐ 0.124 ‐ 0.119 0.115 0.115 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐Water
Mass Flow kg/h 867,420 24,561 840,766 947,591 0 0 0 29,654 0 4,043 4,043 0 0 0 28,796 28,786 890,736 28,049 0 0Std Ideal Liq Vol Flow m3/h 869 25 842 950 ‐ ‐ 0 30 ‐ 4 4 ‐ ‐ ‐ 29 29 893 28 ‐ 0Actual Volume Flow m3/h 946 26 916 1,021 ‐ ‐ 0 32 ‐ 4 4 ‐ ‐ ‐ 29 29 941 28 ‐ ‐
Mass Density kg/m3 917.2 930.0 917.7 928.0 ‐ ‐ 921.3 921.5 ‐ 980.5 980.5 ‐ ‐ ‐ 980.5 980.6 946.1 985.5 ‐ ‐Viscosity cP 0.20 0.23 0.20 0.22 ‐ ‐ 0.21 0.21 ‐ 0.46 0.46 ‐ ‐ ‐ 0.46 0.46 0.24 0.50 ‐ ‐
Thermal Conductivity W/m‐K 0.688 0.687 0.688 0.687 ‐ ‐ 0.688 0.688 ‐ 0.653 0.654 ‐ ‐ ‐ 0.653 0.654 0.686 0.649 ‐ ‐Vapour
Mass Flow kg/h 35 4,942 2 0 2,716 6,664 0 0 7,314 3,211 0 3,211 28,786 28,838 41 0 0 0 41 1,684Std Gas Flow STD_m3/h 17 6,280 3 ‐ 3,564 8,490 ‐ ‐ 9,323 4,008 ‐ 4,008 37,781 37,811 27 ‐ ‐ ‐ 27 2,195
Molecular Weight kg/kgmole 49.23 18.61 17.60 ‐ 18.02 18.56 ‐ ‐ 18.55 18.94 ‐ 18.94 18.02 18.03 36.27 ‐ ‐ ‐ 36.27 18.14Mass Density kg/m3 19.2 2.8 4.1 ‐ 3.0 2.4 ‐ ‐ 2.3 2.8 ‐ 2.4 0.9 0.9 1.3 ‐ ‐ ‐ 1.3 2.6
Viscosity cP 0.011 0.013 0.013 ‐ 0.011 0.012 ‐ ‐ 0.012 0.012 ‐ 0.012 0.013 0.013 0.014 ‐ ‐ ‐ 0.014 0.011Cp/(Cp‐R) (Ideal Gamma) 1.114 1.125 1.114 ‐ 1.301 1.264 ‐ ‐ 1.265 1.154 ‐ 1.255 1.317 1.317 1.119 ‐ ‐ ‐ 1.281 1.280
Z Factor 0.888 0.988 0.985 ‐ 0.969 0.987 ‐ ‐ 0.987 0.992 ‐ 0.993 0.988 0.988 0.995 ‐ ‐ ‐ 0.995 0.990Thermal Conductivity W/m‐K 0.028 0.038 0.041 ‐ 0.032 0.036 ‐ ‐ 0.036 0.036 ‐ 0.036 0.026 0.026 0.021 ‐ ‐ ‐ 0.021 0.031
H2O 0.9998 0.9048 1.0000 1.0000 0.9988 0.5717 0.0176 1.0000 0.5906 0.5906 0.9983 0.0500 1.0000 0.9992 0.9992 0.9998 1.0000 1.0000 0.2001 0.0039H2S 0.0000 0.0000 0.0000 0.0000 0.0000 0.0002 0.0000 0.0000 0.0002 0.0002 0.0000 0.0005 0.0000 0.0001 0.0001 0.0001 <hidden> <hidden> 0.0605 0.0012CO2 0.0001 0.0015 0.0000 0.0000 0.0003 0.0071 0.0002 0.0000 0.0083 0.0083 0.0000 0.0193 0.0000 0.0006 0.0006 0.0002 <hidden> <hidden> 0.6661 0.0193
Helium 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0001 0.0000 0.0000 0.0000 0.0000 <hidden> <hidden> 0.0018 0.0001Nitrogen 0.0000 0.0004 0.0000 0.0000 0.0000 0.0019 0.0000 0.0000 0.0017 0.0017 0.0000 0.0040 0.0000 0.0000 0.0000 0.0000 <hidden> <hidden> 0.0110 0.0046
Air 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 <hidden> <hidden> 0.0000 0.0000Methane 0.0000 0.0834 0.0000 0.0000 0.0009 0.3797 0.0053 0.0000 0.3631 0.3631 0.0000 0.8446 0.0000 0.0000 0.0000 0.0000 <hidden> <hidden> 0.0604 0.9010Ethane 0.0000 0.0046 0.0000 0.0000 0.0000 0.0211 0.0008 0.0000 0.0192 0.0192 0.0000 0.0447 0.0000 0.0000 0.0000 0.0000 <hidden> <hidden> 0.0001 0.0500
Propane 0.0000 0.0013 0.0000 0.0000 0.0000 0.0060 0.0005 0.0000 0.0055 0.0055 0.0000 0.0128 0.0000 0.0000 0.0000 0.0000 <hidden> <hidden> 0.0000 0.0139C4+ 0.0001 0.0038 0.0000 0.0000 0.0000 0.0123 0.9756 0.0000 0.0113 0.0113 0.0016 0.0242 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0059
NOTES:1. Values are for each 40,000 bpd phase for Phases 1 & 2. SUNCOR LEWIS PH 1 & 2
AREA 2000/3000 ‐ OIL REMOVAL, WATER TREATMENTHEAT AND MATERIAL BALANCE
PROJECT # DRAWING NUMBER REVISION
Overall Composition Mole Fraction
40,000 BPSD
Overall
Stream Number
Stream Name
From
To
Area 2000 HMB (1,2) - Page 2 of 12
SUNCOR LEWIS PH 1 2HEAT MATERIAL BALANCE TABLE
5000 5001 5002 5003 5004 5005 5006 5007 5008 5700 5701 5702 5703 5704 5705 7000 7001 9000 9001
LP BFW LP BFW HP BFW HP BFW HP BFW HP Steam HP Steam CBD Combined CBD CBD HP Steam Cold glycol Cold glycol Cold glycol Hot glycol Disposal water Disposal water Raw water Raw water
LP BFW PumpsEmulsion / BFW
exchangerHP BFW pumps HP BFW header HP BFW header
HP Steam generator
HP Steam header
HP Steam generators
HRSG/ HP Steam Gen.
HRSG HRSGCogen Glycol
Pumps Cogen Glycol
HeaderCogen Glycol
HeaderGTG
Disposal water treatment
Disposal Water Pumps
Source water Raw water pumps
Emulsion / BFW exchanger
HP BFW pumps HP BFW headerSteam
GeneratorHRSG
HP Steam header
B/L Well padsBlowdown header
Inlet SeparatorBlowdown header
HP Steam header
Cogen Glycol Header
Cogen Glycol Filter
GTGCogen Glycol
CoolersDisposal Water
TankDisposal wells CPF B/L PW Surge Drum
Vapour Fraction 0.000 0.000 0.000 0.000 0.000 1.000 1.000 0.000 0.000 0.000 1.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000Operating Temperature °C 115.9 179.2 180.8 180.8 180.8 286.7 286.7 286.7 286.7 286.7 286.7 50.0 50.0 50.0 56.3 55.0 55.6 15.5 15.7
Operating Pressure kPaa 2,009 1,909 7,493 7,493 7,493 7,093 7,093 7,093 7,093 7,093 7,093 793 793 793 490 150 5,022 363 1,670Mass Flow kg/h 890,736 890,736 890,736 529,491 361,245 518,902 872,921 10,590 17,815 7,225 354,020 381,399 18,965 362,434 362,434 28,049 28,049 78,043 78,043
Mass Density kg/m3 946.8 888.2 890.2 890.2 890.2 37.1 37.1 738.2 738.2 738.2 37.1 1,050.8 1,050.8 1,050.8 1,045.5 985.5 987.3 1,014.5 1,014.7Molecular Weight kg/kgmole 18.02 18.02 18.02 18.02 18.02 18.02 18.02 18.02 18.02 18.02 18.02 28.55 28.55 28.55 28.55 18.02 18.02 18.02 18.02
Mass Heat Capacity kJ/kg‐C 4.23 4.40 4.38 4.38 4.38 5.08 5.08 5.43 5.43 5.43 5.08 3.45 3.45 3.45 3.46 4.18 4.17 4.32 4.31Thermal Conductivity W/m‐K 0.686 0.677 0.676 0.676 0.676 0.042 0.042 0.564 0.564 0.564 0.042 0.413 0.413 0.413 0.416 0.649 0.649 0.596 0.596
Combined Liquid 0 0 0 0Mass Flow kg/h 890,736 890,736 890,736 529,491 361,245 0 0 10,590 17,815 7,225 0 381,399 18,965 362,434 362,434 28,049 28,049 78,043 78,043
Std Ideal Liq Vol Flow m3/h 893 893 893 531 362 ‐ ‐ 11 18 7 ‐ 362 18 344 344 28 28 78 78Actual Volume Flow m3/h 941 1,003 1,001 595 406 ‐ ‐ 14 24 10 ‐ 363 18 345 347 28 28 77 77
Mass Density kg/m3 946.8 888.2 890.2 890.2 890.2 ‐ ‐ 738.2 738.2 738.2 ‐ 1,050.8 1,050.8 1,050.8 1,045.5 985.5 987.3 1,014.5 1,014.7Molecular Weight kg/kgmole 18.02 18.02 18.02 18.02 18.02 ‐ ‐ 18.02 18.02 18.02 ‐ 28.55 28.55 28.55 28.55 18.02 18.02 18.02 18.02
Viscosity cP 0.24 0.15 0.15 0.15 0.15 ‐ ‐ 0.09 0.09 0.09 ‐ 1.54 1.54 1.54 1.36 0.50 0.50 1.12 1.12Thermal Conductivity W/m‐K 0.686 0.677 0.676 0.676 0.676 ‐ ‐ 0.564 0.564 0.564 ‐ 0.413 0.413 0.413 0.416 0.649 0.649 0.596 0.596
Oil 0 0 0 0Mass Flow kg/h 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
Std Ideal Liq Vol Flow m3/h ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐Actual Volume Flow m3/h ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐
Mass Density (Note 3) kg/m3 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐API Gravity (STD) °API ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐Molecular Weight kg/kgmole ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐Viscosity (Note 4) cP ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐
Thermal Conductivity W/m‐K ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐Water 0 0 0 0
Mass Flow kg/h 890,736 890,736 890,736 529,491 361,245 0 0 10,590 17,815 7,225 0 381,399 18,965 362,434 362,434 28,049 28,049 78,043 78,043Std Ideal Liq Vol Flow m3/h 893 893 893 531 362 ‐ ‐ 11 18 7 ‐ 362 18 344 344 28 28 78 78Actual Volume Flow m3/h 941 1,003 1,001 595 406 ‐ ‐ 14 24 10 ‐ 363 18 345 347 28 28 77 77
Mass Density kg/m3 946.8 888.2 890.2 890.2 890.2 ‐ ‐ 738.2 738.2 738.2 ‐ 1,050.8 1,050.8 1,050.8 1,045.5 985.5 987.3 1,014.5 1,014.7Viscosity cP 0.24 0.15 0.15 0.15 0.15 ‐ ‐ 0.09 0.09 0.09 ‐ 1.54 1.54 1.54 1.36 0.50 0.50 1.12 1.12
Thermal Conductivity W/m‐K 0.686 0.677 0.676 0.676 0.676 ‐ ‐ 0.564 0.564 0.564 ‐ 0.413 0.413 0.413 0.416 0.649 0.649 0.596 0.596Vapour 0 0 0 0
Mass Flow kg/h 0 0 0 0 0 518,902 872,921 0 0 0 354,020 0 0 0 0 0 0 0 0Std Gas Flow STD_m3/h ‐ ‐ ‐ ‐ ‐ 681,047 1,145,691 ‐ ‐ ‐ 464,643 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐
Molecular Weight kg/kgmole ‐ ‐ ‐ ‐ ‐ 18.0 18.0 ‐ ‐ ‐ 18.0 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐Mass Density kg/m3 ‐ ‐ ‐ ‐ ‐ 37.1 37.1 ‐ ‐ ‐ 37.1 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐
Viscosity cP ‐ ‐ ‐ ‐ ‐ 0.019 0.019 ‐ ‐ ‐ 0.019 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐Cp/(Cp‐R) (Ideal Gamma) ‐ ‐ ‐ ‐ ‐ 1.1 1.1 ‐ ‐ ‐ 1.1 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐
Z Factor ‐ ‐ ‐ ‐ ‐ 0.7 0.7 ‐ ‐ ‐ 0.7 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐Thermal Conductivity W/m‐K ‐ ‐ ‐ ‐ ‐ 0.0 0.0 ‐ ‐ ‐ 0.0 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐
0.00000 0.00000 0.00000 0.00000H2O 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0 (24% EG) 1.0 (24% EG) 1.0 (24% EG) 1.0 (24% EG) 1.0000 1.0000 1.0000 1.0000H2S 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000CO2 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
Helium 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000Nitrogen 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
Air 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000Methane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000Ethane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
Propane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000C4+ 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
NOTES:1. Values are for each 40,000 bpd phase for Phases 1 & 2. SUNCOR LEWIS PH 1 & 2
AREA 5000 & 5700 ‐ BFW & STEAM GENERATIONAREA 7000 & 9000 ‐ DISPOSAL & RAW WATER SYSTEMS
HEAT AND MATERIAL BALANCE
Overall Composition Mole Fraction
Overall
Stream Number
Stream Name
From
To
40,000 BPSD
Area 5000-5700 HMB (1,2) - Page 3 of 12
SUNCOR LEWIS PH 1 2HEAT MATERIAL BALANCE TABLE
6000 6001 6002 6003 6004 6005 6006 6007 6008 6009 6010 6011 6012 6013 6014 6015 6016 6017 6018
Cold glycol Cold glycol Hot glycol Cold Glycol Hot glycol Cold Glycol Warm glycol Hot glycol Hot glycol Hot glycol Hot glycol Hot glycol Cold glycol Cold glycol Hot glycol Cooled glycol Cold Glycol Cold Glycol Hot glycol
Glycol Circ. pump
Cold glycol supply header
Evaporator Cold glycol
supply header Dilbit Coolers
Cold glycol supply header
Sample / seal flush cooling
Dilbit Coolers / Evaporator
bypass lineHot glycol
Supply headerCombustion Air Preheaters
Hot glycol Supply header
Natural gas heater
Heating glycol system
Glycol main return header
Glycol Aerial Coolers
Glycol Circ. Pumps
Cold glycol supply header
Produced Gas Condenser
Cold glycol supply header
EvaporatorHot glycol
Return headerDilbit Coolers
Hot glycol Return header
Sample / seal flush cooling
Warm glycol return header
Hot glycol return header
Glycol Return header
Combustion Air Preheaters
Cold glycol return header
Natural gas heater
Cold glycol return header
Glycol return header
Glycol Aerial Coolers
Expansion Drum Glycol FilterProduced Gas Condenser
Hot glycol Return header
Vapour Fraction 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000Operating Temperature °C 40.0 40.0 90.0 40.0 90.0 40.0 70.0 90.0 90.0 90.0 50.0 90.0 40.0 50.0 69.5 40.0 40.0 40.0 90.0
Operating Pressure kPaa 1,094 1,094 794 1,094 794 1,094 404 794 404 654 404 654 153 404 404 153 153 1,094 794Mass Flow kg/h 475,043 48,953 48,953 251,489 251,489 54,750 54,750 365,543 169,081 183,369 183,369 13,093 13,093 183,369 407,200 407,200 54,750 65,101 65,101
Mass Density kg/m3 1,074.7 1,074.7 1,038.2 1,074.7 1,038.2 1,074.7 1,054.3 1,038.2 1,038.2 1,038.2 1,068.3 1,038.2 1,074.7 1,068.3 1,054.7 1,074.7 1,074.7 1,074.7 1,038.2Molecular Weight kg/kgmole 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17
Mass Heat Capacity kJ/kg‐C 3.19 3.19 3.41 3.19 3.41 3.19 3.32 3.41 3.41 3.41 3.23 3.41 3.19 3.23 3.31 3.19 3.19 3.19 3.41Thermal Conductivity W/m‐K 0.351 0.351 0.336 0.351 0.336 0.351 0.342 0.336 0.336 0.336 0.348 0.336 0.351 0.348 0.342 0.351 0.351 0.351 0.336
Combined LiquidMass Flow kg/h 475,043 48,953 48,953 251,489 251,489 54,750 54,750 365,543 169,081 183,369 183,369 13,093 13,093 183,369 407,200 407,200 54,750 65,101 65,101
Std Ideal Liq Vol Flow m3/h 434 45 45 230 230 50 50 334 154 167 167 12 12 167 372 372 50 59 59Actual Volume Flow m3/h 442 46 47 234 242 51 52 352 163 177 172 13 12 172 386 379 51 61 63
Mass Density kg/m3 1,074.7 1,074.7 1,038.2 1,074.7 1,038.2 1,074.7 1,054.3 1,038.2 1,038.2 1,038.2 1,068.3 1,038.2 1,074.7 1,068.3 1,054.7 1,074.7 1,074.7 1,074.7 1,038.2Molecular Weight kg/kgmole 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17
Viscosity cP 4.82 4.82 1.41 4.82 1.41 4.82 2.16 1.41 1.41 1.41 3.57 1.41 4.82 3.57 2.18 4.82 4.82 4.82 1.41Thermal Conductivity W/m‐K 0.351 0.351 0.336 0.351 0.336 0.351 0.342 0.336 0.336 0.336 0.348 0.336 0.351 0.348 0.342 0.351 0.351 0.351 0.336
OilMass Flow kg/h 475,043 48,953 48,953 251,489 251,489 54,750 54,750 365,543 169,081 183,369 183,369 13,093 13,093 183,369 407,200 407,200 54,750 65,101 65,101
Std Ideal Liq Vol Flow m3/h 434 45 45 230 230 50 50 334 154 167 167 12 12 167 372 372 50 59 59Actual Volume Flow m3/h 442 46 47 234 242 51 52 352 163 177 172 13 12 172 386 379 51 61 63
Mass Density (Note 3) kg/m3 1074.7 1074.7 1038.2 1074.7 1038.2 1074.7 1054.3 1038.2 1038.2 1038.2 1068.3 1038.2 1074.7 1068.3 1054.7 1074.7 1074.7 1074.7 1038.2API Gravity (STD) °API ‐2.41 ‐2.41 ‐2.41 ‐2.41 ‐2.41 ‐2.41 ‐2.41 ‐2.41 ‐2.41 ‐2.41 ‐2.41 ‐2.41 ‐2.41 ‐2.41 ‐2.41 ‐2.41 ‐2.41 ‐2.41 ‐2.41Molecular Weight kg/kgmole 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17Viscosity (Note 4) cP 4.82 4.82 1.41 4.82 1.41 4.82 2.16 1.41 1.41 1.41 3.57 1.41 4.82 3.57 2.18 4.82 4.82 4.82 1.41
Thermal Conductivity W/m‐K 0.351 0.351 0.336 0.351 0.336 0.351 0.342 0.336 0.336 0.336 0.348 0.336 0.351 0.348 0.342 0.351 0.351 0.351 0.336Water 0 0 0 0 0 0 0 0 0
Mass Flow kg/h 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0Std Ideal Liq Vol Flow m3/h ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐Actual Volume Flow m3/h ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐
Mass Density kg/m3 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐Viscosity cP ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐
Thermal Conductivity W/m‐K ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐Vapour
Mass Flow kg/h 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0Std Gas Flow STD_m3/h ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐
Molecular Weight kg/kgmole ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐Mass Density kg/m3 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐
Viscosity cP ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐Cp/(Cp‐R) (Ideal Gamma) ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐
Z Factor ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐Thermal Conductivity W/m‐K ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐
H2O 1.0 (60% TEG) 1.0 (60% TEG) 1.0 (60% TEG) 1.0 (60% TEG) 1.0 (60% TEG) 1.0 (60% TEG) 1.0 (60% TEG) 1.0 (60% TEG) 1.0 (60% TEG) 1.0 (60% TEG) 1.0 (60% TEG) 1.0 (60% TEG) 1.0 (60% TEG) 1.0 (60% TEG) 1.0 (60% TEG) 1.0 ( 60%TEG) 1.0 ( 60%TEG) 1.0 ( 60%TEG) 1.0 ( 60%TEG)H2S 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000CO2 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
Helium 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000Nitrogen 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
Air 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000Methane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000Ethane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
Propane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000C4+ 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
NOTES:1. Values are for each 40,000 bpd phase for Phases 1 & 2. SUNCOR LEWIS PH 1 & 2
AREA 6200 ‐ GLYCOL SYSTEMHEAT AND MATERIAL BALANCE
PROJECT # DRAWING NUMBER REVISION
Overall Composition Mole Fraction
40,000 BPSD
Overall
Stream Number
Stream Name
From
To
Area 6000 HMB (1,2) - Page 4 of 12
SUNCOR LEWIS PH 1 2HEAT MATERIAL BALANCE TABLE
6200 6201 6202 6203 6204 6205 6206 6207 6208 6209 6210 6211 6212 6213 6214 6215 6216
Natural gas Natural gas Natural gas Natural gas HP fuel gas HP fuel gas HP fuel gasCombined Fuel
Gas Mixed fuel gas Mixed fuel gas Mixed fuel gas
Blanketing Natural gas
Purge gas Natural gas Natural gas Bubble gas Mixed Fuel Gas
CPF B/L HeaderDiluent Rec. Trim Cooler
Natural Gas Heater
Header HeaderHP Fuel Gas Coalescer
NG / PG HeaderMixed Fuel Gas
DrumMixed fuel gas
headerMixed fuel gas
headerPipeline
Critical fuel gas header
LP Fuel gas header
LP Fuel gas header
MP fuel gas header
Produced Gas Header
HeaderDiluent Rec. Trim Cooler
Natural Gas Heater
HeaderEvaporator Vent
EjectorHP Fuel Gas Coalescer
GTGMixed Fuel Gas
DrumMixed fuel gas
headerHP Steam Generator
HRSG Wellpads HP Flare headerHRSG pilot burner
Steam Gen. Pilot burner
CFU NG / PG Header
Vapour Fraction 1.000 1.000 1.000 1.000 1.000 1.000 1.000 1.000 1.000 1.000 1.000 1.000 1.000 1.000 1.000 1.000 0.998Operating Temperature °C 7.0 7.0 34.3 50.0 34.2 34.2 30.8 23.3 23.3 23.3 23.3 7.0 19.1 19.8 19.8 26.1 46.9
Operating Pressure kPaa 7,068 7,068 6,968 6,868 3,193 3,193 2,506 353 353 353 353 7,068 443 443 443 1,595 353Mass Flow kg/h 50,467 50,290 50,290 50,290 1,600 19,205 19,205 31,776 31,776 24,528 7,248 156 21 93 151 2,621 5,156
Mass Density kg/m3 67.5 67.5 56.2 51.2 23.8 23.8 18.6 2.6 2.6 2.6 2.6 67.5 3.3 3.3 3.3 11.8 2.5Molecular Weight kg/kgmole 17.67 17.67 17.67 17.67 17.67 17.67 17.67 17.86 17.86 17.86 17.86 17.67 17.67 17.67 17.67 17.67 18.97
Mass Heat Capacity kJ/kg‐C 2.88 2.88 2.69 2.64 2.38 2.38 2.32 2.14 2.14 2.14 2.14 2.88 2.15 2.16 2.16 2.25 2.13Thermal Conductivity W/m‐K 0.038 0.038 0.040 0.042 0.036 0.036 0.035 0.032 0.032 0.032 0.032 0.038 0.032 0.032 0.032 0.034 0.000
Combined LiquidMass Flow kg/h 0 0 0 0 0 0 0 1 0 0 0 0 0 0 0 0 12
Std Ideal Liq Vol Flow m3/h ‐ ‐ ‐ ‐ ‐ ‐ ‐ 0 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ 0Actual Volume Flow m3/h ‐ ‐ ‐ ‐ ‐ ‐ ‐ 0 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ 0
Mass Density kg/m3 ‐ ‐ ‐ ‐ ‐ ‐ ‐ 858.0 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ 976.2Molecular Weight kg/kgmole ‐ ‐ ‐ ‐ ‐ ‐ ‐ 160.2 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ 19.5
Viscosity cP ‐ ‐ ‐ ‐ ‐ ‐ ‐ 30.0 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ 0.7Thermal Conductivity W/m‐K ‐ ‐ ‐ ‐ ‐ ‐ ‐ 0.1 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ 0.6
OilMass Flow kg/h 0 0 0 0 0 0 0 1 0 0 0 0 0 0 0 0 1
Std Ideal Liq Vol Flow m3/h ‐ ‐ ‐ ‐ ‐ ‐ ‐ 0 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ 0Actual Volume Flow m3/h ‐ ‐ ‐ ‐ ‐ ‐ ‐ 0 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ 0
Mass Density (Note 3) kg/m3 ‐ ‐ ‐ ‐ ‐ ‐ ‐ 858.0 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ 841.4API Gravity (STD) °API ‐ ‐ ‐ ‐ ‐ ‐ ‐ 310.2 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ 281.9Molecular Weight kg/kgmole ‐ ‐ ‐ ‐ ‐ ‐ ‐ 160.2 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ 153.9Viscosity (Note 4) cP ‐ ‐ ‐ ‐ ‐ ‐ ‐ 30.0 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ 11.0
Thermal Conductivity W/m‐K ‐ ‐ ‐ ‐ ‐ ‐ ‐ 0.1 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ 0.1Water
Mass Flow kg/h 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 11Std Ideal Liq Vol Flow m3/h ‐ ‐ ‐ ‐ 0 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ 0 ‐ ‐ 0Actual Volume Flow m3/h ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ 0
Mass Density kg/m3 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ 990.8Viscosity cP ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ 0.6
Thermal Conductivity W/m‐K ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ 0.6Vapour
Mass Flow kg/h 50,467 50,290 50,290 50,290 1,600 19,205 19,205 31,776 31,776 24,528 7,248 156 21 93 151 2,621 5,144Std Gas Flow STD_m3/h 67,546 67,310 67,310 67,310 2,141 25,704 25,704 42,056 42,056 32,463 9,593 208 28 124 202 3,508 6,412
Molecular Weight kg/kgmole 17.67 17.67 17.67 17.67 17.67 17.67 17.67 17.86 17.86 17.86 17.86 17.67 17.67 17.67 17.67 17.67 18.97Mass Density kg/m3 67.5 67.5 56.2 51.2 23.8 23.8 18.6 2.6 2.6 2.6 2.6 67.5 3.3 3.3 3.3 11.8 2.5
Viscosity cP 0.013 0.013 0.013 0.014 0.012 0.012 0.012 0.011 0.011 0.011 0.011 0.013 0.011 0.011 0.011 0.012 0.012Cp/(Cp‐R) (Ideal Gamma) 1.195 1.195 1.212 1.217 1.247 1.247 1.254 1.277 1.277 1.277 1.277 1.195 1.280 1.279 1.279 1.265 1.258
Z Factor 0.795 0.795 0.856 0.883 0.928 0.928 0.940 0.990 0.990 0.990 0.990 0.795 0.988 0.988 0.988 0.959 0.992Thermal Conductivity W/m‐K 0.038 0.038 0.040 0.042 0.036 0.036 0.035 0.032 0.032 0.032 0.032 0.038 0.032 0.032 0.032 0.034 0.034
H2O 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0049 0.0049 0.0049 0.0049 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000H2S 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0001 0.0001 0.0001 0.0001 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000CO2 0.0058 0.0058 0.0058 0.0058 0.0058 0.0058 0.0058 0.0081 0.0081 0.0081 0.0081 0.0058 0.0058 0.0058 0.0058 0.0058 0.0058
Helium 0.0001 0.0001 0.0001 0.0001 0.0001 0.0001 0.0001 0.0001 0.0001 0.0001 0.0001 0.0001 0.0001 0.0001 0.0001 0.0001 0.0001Nitrogen 0.0046 0.0046 0.0046 0.0046 0.0046 0.0046 0.0046 0.0045 0.0045 0.0045 0.0045 0.0046 0.0046 0.0046 0.0046 0.0046 0.0046
Air 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000Methane 0.9180 0.9180 0.9180 0.9180 0.9180 0.9180 0.9180 0.9088 0.9088 0.9088 0.9088 0.9180 0.9180 0.9180 0.9180 0.9180 0.9180Ethane 0.0510 0.0510 0.0510 0.0510 0.0510 0.0510 0.0510 0.0504 0.0504 0.0504 0.0504 0.0510 0.0510 0.0510 0.0510 0.0510 0.0510
Propane 0.0142 0.0142 0.0142 0.0142 0.0142 0.0142 0.0142 0.0144 0.0144 0.0144 0.0144 0.0142 0.0142 0.0142 0.0142 0.0142 0.0142C4+ 0.0063 0.0063 0.0063 0.0063 0.0063 0.0063 0.0063 0.0088 0.0088 0.0088 0.0088 0.0063 0.0063 0.0063 0.0063 0.0063 0.0063
NOTES:1. Values are for each 40,000 bpd phase for Phases 1 & 2. SUNCOR LEWIS PH 1 & 2
AREA 6200 ‐ FUEL GAS SYSTEMHEAT AND MATERIAL BALANCE
PROJECT # DRAWING NUMBER REVISION
40,000 BPSD
Overall Composition Mole Fraction
Overall
Stream Number
Stream Name
From
To
Area 6200 HMB (1,2) - Page 5 of 12
SUNCOR LEWIS PH 1-3HEAT MATERIAL BALANCE TABLE
4000 4001 4002 4003 4004 4005 4006 4007
Diluent Diluent Diluent Trim diluent DilbitDilbit / Diluent
vaporsRecovered liquids
VRU Gas
Supply pipeline Diluent pumps Diluent supply
headerDiluent supply
headerDilbit tank
Dilbit/Offspec/ Diluent tanks
VRU package VRU package
CPF B/LDiluent supply
headerFWKO/Treaters
CPF B/L (Trim blending)
CPF B/L (Dilbit product pumps)
VRU package Dilbit headerDiluent Rec.
Cooler
Vapour Fraction 0.000 0.000 0.000 0.000 0.000 1.000 0.000 1.000Operating Temperature °C 15.0 15.8 15.8 15.8 53.0 53.0 53.3 126.6
Operating Pressure kPaa 593 1,613 1,613 1,613 93 93 896 460Mass Flow kg/h 220,646 220,646 33,124 121,274 900,483 13,066 0 4,355
Mass Density kg/m3 676.4 676.5 676.5 676.5 974.3 2.1 934.8 8.9Molecular Weight kg/kgmole 66.12 66.12 66.12 66.12 274.54 60.13 221.30 60.13
Mass Heat Capacity kJ/kg‐C 2.15 2.15 2.15 2.15 1.86 1.79 1.90 2.13Thermal Conductivity W/m‐K 0.109 0.109 0.109 0.109 0.118 0.017 0.114 0.024
Combined LiquidMass Flow kg/h 220,646 220,646 33,124 121,274 900,483 0 0 0
Std Ideal Liq Vol Flow m3/h 326 326 49 179 940 ‐ ‐ ‐
Actual Volume Flow m3/h 326 326 49 179 924 ‐ ‐ ‐
Mass Density kg/m3 676.4 676.5 676.5 676.5 974.3 ‐ ‐ ‐Molecular Weight kg/kgmole 66.12 66.12 66.12 66.12 274.54 ‐ ‐ ‐
Viscosity cP 0.32 0.32 0.32 0.32 183.74 ‐ ‐ ‐Thermal Conductivity W/m‐K 0.109 0.109 0.109 0.109 0.118 ‐ ‐ ‐
OilMass Flow kg/h 220,646 220,646 33,124 121,274 900,483 0 0 0
Std Ideal Liq Vol Flow m3/h 326 326 49 179 940 ‐ ‐ ‐
Actual Volume Flow m3/h 326 326 49 179 924 ‐ ‐ ‐
Mass Density (Note 3) kg/m3 676.4 676.5 676.5 676.5 974.3 ‐ ‐ ‐ API Gravity (STD) °API 77.61 77.61 77.61 77.61 16.10 ‐ ‐ ‐ Molecular Weight kg/kgmole 66.12 66.12 66.12 66.12 274.54 ‐ ‐ ‐ Viscosity (Note 4) cP 0.32 0.32 0.32 0.32 183.74 ‐ ‐ ‐
Thermal Conductivity W/m‐K 0.109 0.109 0.109 0.109 0.118 ‐ ‐ ‐ Water
Mass Flow kg/h 0 0 0 0 0 0 0 0
ndard Ideal Liquid Volume Flow m3/h ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐
Actual Volume Flow m3/h ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐
Mass Density kg/m3 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ Viscosity cP ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐
Thermal Conductivity W/m‐K ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ Vapour
Mass Flow kg/h 0 0 0 0 0 13,066 0 4,355
Std Gas Flow STD_m3/h ‐ ‐ ‐ ‐ ‐ 5,138 ‐ 1,713Molecular Weight kg/kgmole ‐ ‐ ‐ ‐ ‐ 60.13 ‐ 60.13
Mass Density kg/m3 ‐ ‐ ‐ ‐ ‐ 2.1 ‐ 8.9Viscosity cP ‐ ‐ ‐ ‐ ‐ 0.007 ‐ 0.009
Cp/(Cp‐R) (Ideal Gamma) ‐ ‐ ‐ ‐ ‐ 1.084 ‐ 1.069Z Factor ‐ ‐ ‐ ‐ ‐ 0.977 ‐ 0.933
Thermal Conductivity W/m‐K ‐ ‐ ‐ ‐ ‐ 0.017 ‐ 0.024
H2O 0.0000 0.0000 0.0000 0.0000 0.0016 0.1510 0.0016 0.1509
H2S 0.0000 0.0000 0.0000 0.0000 0.00001 0.0004 0.00001 0.0004
CO2 0.0000 0.0000 0.0000 0.0000 0.0001 0.0070 0.0001 0.0070Helium 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
Nitrogen 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000Air 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
Methane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0027 0.0000 0.0027Ethane 0.0012 0.0012 0.0012 0.0012 0.0000 0.0031 0.0000 0.0031
Propane 0.0045 0.0045 0.0045 0.0045 0.0013 0.0297 0.0014 0.0297C4+ 0.9943 0.9943 0.9943 0.9943 0.9970 0.8061 0.9970 0.8062
NOTES:1. Trim diluent flow rate is based on meeting 350 cSt dilbit viscosity at 7.5 °C pipeline winter reference temperature. SUNCOR LEWIS PH 1‐32. Streams 4002, 4006, and 4007 are per 40,000 bpd phase for each of Ph 1 ‐ 3. AREA 4000 ‐ HC TANK FARM
HEAT AND MATERIAL BALANCE
PROJECT # DRAWING NUMBER REVISION
Stream Number
Stream Name
From
To
Overall
Overall Composition Mole Fraction
Area 4000 HMB (1-3) - Page 6 of 12
SUNCOR LEWIS PH 3 4HEAT MATERIAL BALANCE TABLE
1000 1001 1002 1003 1004 1005 1006 1007 1008 1009 1010 1011 1012 1013 1014 1015 1016 1017 1018 1019Produced emulsion
De‐gassed Emulsion
Cooled Emulsion Cooled Emulsion Wet dilbit Produced Water Produced Gas Produced Gas Produced Water Produced Water Dilbit Dilbit Dilbit Produced Gas Produced Gas Produced Gas DiluentRecovered Diluent
Recovered Diluent
Produced Gas
CPF B/L Inlet Separator Emul./BFW HE Static Mixer FWKO FWKO Inlet Separator FWKO Treater FWKO / Treater Treater Dilbit Cooler Dilbit Header Treater Gas Boot PG HeaderDiluent Rec.
Cooler Diluent Rec. Trim Cooler
Diluent Rec. Pumps
Diluent Rec. Separator
Inlet Separator Emul./BFW HE Static Mixer FWKO Treaters PW HeaderEvap. Vent Condenser
PG Header PW Header CFU Gas Boot Dilbit Header HC Tank farm PG Header PG HeaderDiluent Rec.
CoolerDiluent Rec. Trim Cooler
Diluent Rec. Separator
FWKO Feed Header
MFG Drum
Vapour Fraction 0.000 0.000 0.000 0.001 0.008 0.000 1.000 1.000 0.000 0.000 0.265 0.000 0.062 1.000 1.000 1.000 0.087 0.019 0.000 1.000Operating Temperature °C 193.0 194.6 141.1 136.1 135.5 136.1 181.3 127.3 135.5 136.1 122.1 55.0 53.0 127.4 120.5 122.1 54.0 12.0 12.6 11.5
Operating Pressure kPaa 2,000 1,794 1,494 1,394 1,294 1,179 423 460 1,179 1,179 600 530 93 460 460 460 410 403 1,394 353Mass Flow kg/h 1,088,173 1,105,337 1,105,337 1,168,296 361,942 804,523 651 1,831 34,454 838,977 326,071 304,526 304,526 1,417 22,546 30,138 30,138 30,138 29,835 303
Mass Density kg/m3 862.0 870.2 918.1 851.8 759.7 915.0 2.1 6.9 917.5 915.2 133.0 970.4 128.4 7.1 8.0 8.0 86.1 284.6 657.8 4.4Molecular Weight kg/kgmole 23.58 23.46 23.46 24.26 102.70 18.04 18.49 48.02 18.02 18.04 206.00 261.20 261.20 49.15 53.77 53.96 53.96 53.96 54.44 28.68
Mass Heat Capacity kJ/kg‐C 4.21 4.23 3.95 3.87 2.45 4.50 2.05 2.11 4.51 4.50 2.14 1.88 1.86 2.11 2.09 2.10 2.54 2.34 2.35 1.73Thermal Conductivity W/m‐K 0.000 0.477 0.483 0.000 0.000 0.686 0.037 0.027 0.688 0.686 0.000 0.115 0.000 0.026 0.024 0.024 0.000 0.000 0.114 0.025
Combined Liquid 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0Mass Flow kg/h 1,088,024 1,105,337 1,105,337 1,166,465 360,525 804,487 0 0 34,454 838,942 303,494 304,526 300,182 0 0 0 27,782 29,835 29,835 0
Std Ideal Liq Vol Flow m3/h 1,088 1,105 1,105 1,197 388 806 0 0 35 841 319 320 313 0 ‐ 0 42 46 46 ‐Actual Volume Flow m3/h 1,248 1,270 1,204 1,290 410 877 0 0 38 915 331 314 308 0 ‐ 0 45 45 45 ‐
Mass Density kg/m3 872.2 870.2 918.1 904.3 879.5 916.9 940.8 915.3 917.5 917.0 917.9 970.4 974.3 917.4 ‐ 976.3 617.6 657.4 657.8 ‐Molecular Weight kg/kgmole 23.58 23.46 23.46 24.24 103.15 18.04 535.10 322.88 18.02 18.04 260.94 261.20 274.49 323.53 ‐ 392.08 54.50 54.44 54.44 ‐
Viscosity cP 2.55 2.51 9.64 1.24 3.71 0.20 55.90 17.81 0.20 0.21 4.00 127.81 175.75 18.37 ‐ 83.16 0.21 0.28 0.28 ‐Thermal Conductivity W/m‐K 0.47 0.48 0.48 0.42 0.11 0.69 0.12 0.11 0.69 0.69 0.10 0.12 0.12 0.11 ‐ 0.11 0.10 0.11 0.11 ‐
OilMass Flow kg/h 268,337 268,274 267,779 326,955 324,440 1,176 0 0 0 1,176 303,494 304,334 144,259 0 0 0 25,388 27,399 27,400 0
Std Ideal Liq Vol Flow m3/h 266 266 266 356 352 1 0 0 ‐ 1 319 320 143 0 ‐ 0 40 44 44 ‐Actual Volume Flow m3/h 296 297 286 375 371 1 0 0 ‐ 1 331 314 141 0 ‐ 0 43 43 43 ‐
Mass Density (Note 3) kg/m3 901.1 900.2 932.6 854.7 856.8 856.3 941 915 ‐ 856.3 856.3 933.6 934.8 917 ‐ 976 597 637 638 ‐API Gravity (STD) °API 10 10 10 14 21 10 68 98 ‐ 10 22 17 17 95 ‐ 88 88 88 87 ‐Molecular Weight kg/kgmole 413.35 415.31 433.10 214.99 217.40 229.26 535.10 322.88 ‐ 229.23 260.94 263.44 374.40 323.53 ‐ 392.08 67.36 66.37 66.36 ‐Viscosity (Note 4) cP 9.91 9.90 39.17 3.90 4.10 4.04 55.90 17.81 ‐ 4.00 4.00 127.89 175.75 18.37 ‐ 83.16 0.17 0.24 0.23 ‐
Thermal Conductivity W/m‐K 0.129 0.130 0.124 0.094 0.095 0.097 0.121 0.109 ‐ 0.097 0.103 0.115 0.122 0.109 ‐ 0.111 0.095 0.106 0.105 ‐Water
Mass Flow kg/h 819,687 837,063 837,558 839,510 36,085 803,311 0 0 34,454 837,766 0 192 0 0 0 0 2,393 2,436 2,435 0Std Ideal Liq Vol Flow m3/h 821 839 839 841 36 805 ‐ ‐ 35 839 ‐ 0 ‐ ‐ ‐ ‐ 2 2 2 ‐Actual Volume Flow m3/h 951 973 918 915 39 876 ‐ ‐ 38 914 ‐ 0 ‐ ‐ ‐ ‐ 2 2 2 ‐
Mass Density kg/m3 861.8 859.9 912.6 917.1 917.6 917.0 ‐ ‐ 917.5 917.0 ‐ 984.5 ‐ ‐ ‐ ‐ 985.3 1,017.2 1,017.1 ‐Viscosity cP 0.14 0.14 0.19 0.20 0.20 0.20 ‐ ‐ 0.20 0.20 ‐ 0.50 ‐ ‐ ‐ ‐ 0.51 1.23 1.21 ‐
Thermal Conductivity W/m‐K 0.669 0.668 0.688 0.688 0.688 0.688 ‐ ‐ 0.688 0.688 ‐ 0.649 ‐ ‐ ‐ ‐ 0.648 0.590 0.591 ‐Vapour
Mass Flow kg/h 149 0 0 1,831 1,417 36 651 1,831 0 35 22,577 0 4,344 1,417 22,546 30,138 2,356 303 0 303Std Gas Flow STD_m3/h 192 ‐ ‐ 901 682 17 832 901 ‐ 17 9,925 ‐ 1,709 682 9,915 13,207 1,155 250 ‐ 250
Molecular Weight kg/kgmole 18.3 ‐ ‐ 48.0 49.1 49.3 18.5 48.0 ‐ 49.2 53.8 ‐ 60.1 49.1 53.8 54.0 48.2 28.7 ‐ 28.7Mass Density kg/m3 9.9 ‐ ‐ 22.4 21.3 19.2 2.1 6.9 ‐ 19.2 10.6 ‐ 2.1 7.1 8.0 8.0 7.7 5.0 ‐ 4.4
Viscosity cP 0.014 ‐ ‐ 0.011 0.011 0.011 0.013 0.011 ‐ 0.011 0.010 ‐ 0.007 0.010 0.009 0.010 0.010 0.011 ‐ 0.011Cp/(Cp‐R) (Ideal Gamma) 1.1 ‐ ‐ 1.1 1.0 1.1 1.3 1.1 ‐ 1.1 1.0 ‐ 1.0 1.1 1.1 1.1 1.1 1.1 ‐ 1.2
Z Factor 0.9 ‐ ‐ 0.9 0.9 0.9 1.0 1.0 ‐ 0.9 0.9 ‐ 1.0 1.0 0.9 0.9 0.9 1.0 ‐ 1.0Thermal Conductivity W/m‐K 0.0 ‐ ‐ 0.0 0.0 0.0 0.0 0.0 ‐ 0.0 0.0 ‐ 0.0 0.0 0.0 0.0 0.0 0.0 ‐ 0.0
H2O 0.9867 0.9871 0.9871 0.9684 0.5790 0.9998 0.7838 0.2293 1.0000 0.9998 0.0766 0.0109 0.0109 0.2418 0.2590 0.2421 0.2421 0.2421 0.2467 0.0035H2S 0.00000 0.00000 0.00000 0.00001 0.00003 0.00000 0.00032 0.00043 0.00000 0.00000 0.00006 0.00001 0.00001 0.00042 0.00019 0.00021 0.00021 0.00021 0.00019 0.00131CO2 0.0001 0.0001 0.0001 0.0001 0.0009 0.0001 0.0204 0.0251 0.0000 0.0001 0.0016 0.0002 0.0002 0.0219 0.0054 0.0072 0.0072 0.0072 0.0053 0.1078
Helium 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000Nitrogen 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
Air 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000Methane 0.0003 0.0001 0.0001 0.0003 0.0024 0.0000 0.1937 0.1214 0.0000 0.0000 0.0036 0.0002 0.0002 0.0908 0.0129 0.0232 0.0232 0.0232 0.0114 0.6345Ethane 0.0000 0.0000 0.0000 0.0001 0.0008 0.0000 0.0000 0.0176 0.0000 0.0000 0.0016 0.0003 0.0003 0.0161 0.0052 0.0064 0.0064 0.0064 0.0056 0.0483
Propane 0.0000 0.0000 0.0000 0.0004 0.0049 0.0000 0.0000 0.0507 0.0000 0.0000 0.0099 0.0032 0.0032 0.0501 0.0285 0.0315 0.0315 0.0315 0.0308 0.0666C4+ 0.0129 0.0127 0.0127 0.0307 0.4120 0.0001 0.0018 0.5555 0.0000 0.0001 0.9067 0.9852 0.9852 0.5788 0.6888 0.6893 0.6893 0.6893 0.7000 0.1380
NOTES:1. Values are for each 40,000 bpd phase for Phases 3 & 4. SUNCOR LEWIS PH 3 & 4
AREA 1000 ‐ OIL TREATINGHEAT AND MATERIAL BALANCE
PROJECT # DRAWING NUMBER REVISION
40,000 BPSD
Stream Number
Stream Name
From
To
Overall
Overall Composition Mole Fraction
Area 1000 HMB (3,4) - Page 7 of 12
SUNCOR LEWIS PH 3 4HEAT MATERIAL BALANCE TABLE
2000 2001 2002 2003 2004 2005 2006 2007 2008 2009 2010 2011 3000 3001 3002 3003 3004 3005 3006 3007
Produced water CFU froth De‐oiled waterDe‐oiled /
makeup waterCasing gas Slop vapours Slop oil Slop water Produced Gas Produced Gas PG Condensate Produced Gas Evap vapors
Combined vapors
Condensate Condensate Distillate Evaporator BD Vapors Ejector gas
Produced water header
CFU CFUProducedWater Surge Drum
B/L Pipeline Slop Vessel Slop Vessel Slop VesselProduced Gas
HeaderProduced Gas Condenser
PG Condensate Pump
PG Condenser Separator
Evaporator HeaderEvap Vent Condenser
Evap Cond. Pumps
Evaporator Evaporator Evap Vent Cond
Separator Fuel gas header
CFU Slop VesselProducedWater Surge Drum
Evaporator Slop vesselProduced Gas
HeaderGas Boot CFU
Produced Gas Condenser
PG Condenser Separator
Slop VesselProduced Gas
HeaderEvap. Vent Condenser
Evap. Vent Condenser
Evap Vent Cond Separator
PW Surge DrumBFW Surge
DrumDisposal Water Treatment
Produced Gas header
Produced gas header
Vapour Fraction 0.000 0.163 0.000 0.000 1.000 1.000 0.000 0.000 1.000 0.430 0.000 1.000 1.000 1.000 0.001 0.000 0.000 0.000 1.000 1.000Operating Temperature °C 135.9 121.1 135.1 123.3 176.3 130.4 131.0 131.1 134.7 60.0 60.0 59.8 112.2 112.4 60.0 60.0 115.6 55.0 60.0 20.3
Operating Pressure kPaa 1,179 493 779 507 594 423 600 1,200 423 403 493 353 151 151 100 507 172 150 100 353Mass Flow kg/h 868,631 30,458 840,794 947,591 2,716 6,664 1,002 29,654 7,315 7,315 4,104 3,211 28,786 28,838 28,838 28,786 890,736 28,049 41 1,684
Mass Density kg/m3 915.4 17.2 917.1 928.0 3.0 2.4 938.6 921.5 2.3 6.3 978.1 2.4 0.9 0.9 473.9 980.6 946.1 985.5 1.3 2.6Molecular Weight kg/kgmole 18.04 18.67 18.02 18.02 18.02 18.56 426.02 18.02 18.55 18.55 18.26 18.94 18.02 18.03 18.03 18.02 18.02 18.02 36.27 18.14
Mass Heat Capacity kJ/kg‐C 4.50 4.01 4.51 4.46 1.99 2.14 2.11 4.49 2.14 3.36 4.29 2.16 1.92 1.92 4.32 4.33 4.24 4.18 1.05 2.09Thermal Conductivity W/m‐K 0.686 0.000 0.688 0.687 0.032 0.036 0.124 0.688 0.036 0.000 0.638 0.036 0.026 0.026 0.000 0.654 0.686 0.649 0.021 0.031
Combined LiquidMass Flow kg/h 868,597 25,516 840,792 947,591 0 0 1,002 29,654 0 4,104 4,104 0 0 0 28,796 28,786 890,736 28,049 0 0
Std Ideal Liq Vol Flow m3/h 870 26 843 950 ‐ ‐ 1 30 0 4 4 ‐ ‐ ‐ 29 29 893 28 ‐ ‐Actual Volume Flow m3/h 947 27 916 1,021 ‐ ‐ 1 32 0 4 4 ‐ ‐ ‐ 29 29 941 28 ‐ ‐
Mass Density kg/m3 917.1 930.7 917.7 928.0 ‐ ‐ 938.6 921.5 876.7 978.1 978.1 ‐ ‐ ‐ 980.5 980.6 946.1 985.5 ‐ ‐Molecular Weight kg/kgmole 18.04 18.69 18.02 18.02 ‐ ‐ 426.02 18.02 315.04 18.26 18.26 ‐ ‐ ‐ 18.02 18.02 18.02 18.02 ‐ ‐
Viscosity cP 0.20 0.25 0.20 0.22 ‐ ‐ 53.62 0.21 10.27 0.48 0.48 ‐ ‐ ‐ 0.46 0.46 0.24 0.50 ‐ ‐Thermal Conductivity W/m‐K 0.686 0.652 0.688 0.687 ‐ ‐ 0.124 0.688 0.119 0.638 0.638 ‐ ‐ ‐ 0.653 0.654 0.686 0.649 ‐ ‐
OilMass Flow kg/h 1,177 955 26 0 0 0 1,001 0 0 61 61 0 0 0 0 0 0 0 0 0
Std Ideal Liq Vol Flow m3/h 1 1 0 ‐ ‐ ‐ 1 ‐ 0 0 0 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ Actual Volume Flow m3/h 1 1 0 ‐ ‐ ‐ 1 ‐ 0 0 0 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐
Mass Density (Note 3) kg/m3 885.8 948.6 943.0 ‐ ‐ ‐ 938.6 ‐ 876.7 840.6 840.7 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐API Gravity (STD) °API 10.16 36.96 10.15 ‐ ‐ ‐ 9.00 ‐ 127.48 127.48 10.48 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐Molecular Weight kg/kgmole 228.88 437.69 446.34 ‐ ‐ ‐ 426.03 ‐ 315.04 161.84 161.84 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐Viscosity (Note 4) cP 7.33 84.85 60.66 ‐ ‐ ‐ 53.62 ‐ 10.27 8.96 8.95 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐
Thermal Conductivity W/m‐K 0.097 0.125 0.125 ‐ ‐ ‐ 0.124 ‐ 0.119 0.115 0.115 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐Water
Mass Flow kg/h 867,420 24,561 840,766 947,591 0 0 0 29,654 0 4,043 4,043 0 0 0 28,796 28,786 890,736 28,049 0 0Std Ideal Liq Vol Flow m3/h 869 25 842 950 ‐ ‐ 0 30 ‐ 4 4 ‐ ‐ ‐ 29 29 893 28 ‐ 0Actual Volume Flow m3/h 946 26 916 1,021 ‐ ‐ 0 32 ‐ 4 4 ‐ ‐ ‐ 29 29 941 28 ‐ ‐
Mass Density kg/m3 917.2 930.0 917.7 928.0 ‐ ‐ 921.3 921.5 ‐ 980.5 980.5 ‐ ‐ ‐ 980.5 980.6 946.1 985.5 ‐ ‐Viscosity cP 0.20 0.23 0.20 0.22 ‐ ‐ 0.21 0.21 ‐ 0.46 0.46 ‐ ‐ ‐ 0.46 0.46 0.24 0.50 ‐ ‐
Thermal Conductivity W/m‐K 0.688 0.687 0.688 0.687 ‐ ‐ 0.688 0.688 ‐ 0.653 0.654 ‐ ‐ ‐ 0.653 0.654 0.686 0.649 ‐ ‐Vapour
Mass Flow kg/h 35 4,942 2 0 2,716 6,664 0 0 7,315 3,211 0 3,211 28,786 28,838 41 0 0 0 41 1,684Std Gas Flow STD_m3/h 17 6,280 3 ‐ 3,564 8,490 ‐ ‐ 9,323 4,008 ‐ 4,008 37,781 37,811 27 ‐ ‐ ‐ 27 2,195
Molecular Weight kg/kgmole 49.23 18.61 17.60 ‐ 18.02 18.56 ‐ ‐ 18.55 18.94 ‐ 18.94 18.02 18.03 36.27 ‐ ‐ ‐ 36.27 18.14Mass Density kg/m3 19.2 2.8 4.1 ‐ 3.0 2.4 ‐ ‐ 2.3 2.8 ‐ 2.4 0.9 0.9 1.3 ‐ ‐ ‐ 1.3 2.6
Viscosity cP 0.011 0.013 0.013 ‐ 0.011 0.012 ‐ ‐ 0.012 0.012 ‐ 0.012 0.013 0.013 0.014 ‐ ‐ ‐ 0.014 0.011Cp/(Cp‐R) (Ideal Gamma) 1.114 1.125 1.114 ‐ 1.301 1.264 ‐ ‐ 1.265 1.154 ‐ 1.255 1.317 1.317 1.119 ‐ ‐ ‐ 1.281 1.280
Z Factor 0.888 0.988 0.985 ‐ 0.969 0.987 ‐ ‐ 0.987 0.992 ‐ 0.993 0.988 0.988 0.995 ‐ ‐ ‐ 0.995 0.990Thermal Conductivity W/m‐K 0.028 0.038 0.041 ‐ 0.032 0.036 ‐ ‐ 0.036 0.036 ‐ 0.036 0.026 0.026 0.021 ‐ ‐ ‐ 0.021 0.031
H2O 0.9998 0.9048 1.0000 1.0000 0.9988 0.5717 0.0176 1.0000 0.5906 0.5906 0.9983 0.0500 1.0000 0.9992 0.9992 0.9998 1.0000 1.0000 0.2001 0.0039H2S 0.0000 0.0000 0.0000 0.0000 0.0000 0.0002 0.0000 0.0000 0.0002 0.0002 0.0000 0.0005 0.0000 0.0001 0.0001 0.0001 <hidden> <hidden> 0.0605 0.0012CO2 0.0001 0.0015 0.0000 0.0000 0.0003 0.0071 0.0002 0.0000 0.0083 0.0083 0.0000 0.0193 0.0000 0.0006 0.0006 0.0002 <hidden> <hidden> 0.6661 0.0193
Helium 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0001 0.0000 0.0000 0.0000 0.0000 <hidden> <hidden> 0.0018 0.0001Nitrogen 0.0000 0.0004 0.0000 0.0000 0.0000 0.0019 0.0000 0.0000 0.0017 0.0017 0.0000 0.0040 0.0000 0.0000 0.0000 0.0000 <hidden> <hidden> 0.0110 0.0046
Air 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 <hidden> <hidden> 0.0000 0.0000Methane 0.0000 0.0834 0.0000 0.0000 0.0009 0.3797 0.0053 0.0000 0.3631 0.3631 0.0000 0.8446 0.0000 0.0000 0.0000 0.0000 <hidden> <hidden> 0.0604 0.9010Ethane 0.0000 0.0046 0.0000 0.0000 0.0000 0.0211 0.0008 0.0000 0.0192 0.0192 0.0000 0.0447 0.0000 0.0000 0.0000 0.0000 <hidden> <hidden> 0.0001 0.0500
Propane 0.0000 0.0013 0.0000 0.0000 0.0000 0.0060 0.0005 0.0000 0.0055 0.0055 0.0000 0.0128 0.0000 0.0000 0.0000 0.0000 <hidden> <hidden> 0.0000 0.0139C4+ 0.0001 0.0038 0.0000 0.0000 0.0000 0.0123 0.9756 0.0000 0.0113 0.0113 0.0016 0.0242 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0059
NOTES:1. Values are for each 40,000 bpd phase for Phases 3 & 4. SUNCOR LEWIS PH 3 & 4
AREA 2000/3000 ‐ OIL REMOVAL, WATER TREATMENTHEAT AND MATERIAL BALANCE
PROJECT # DRAWING NUMBER REVISION
40,000 BPSD
Stream Number
Stream Name
From
To
Overall
Overall Composition Mole Fraction
Area 2000 HMB (3,4) - Page 8 of 12
SUNCOR LEWIS PH 3 4HEAT MATERIAL BALANCE TABLE
5000 5001 5002 5003 5005 5006 5007 7000 7001 9000 9001
LP BFW LP BFW HP BFW HP BFW HP Steam HP Steam CBD Disposal water Disposal water Raw water Raw water
LP BFW PumpsEmulsion / BFW
exchangerHP BFW pumps HP BFW header
HP Steam generator
HP Steam header
HP Steam generators
Disposal water treatment
Disposal Water Pumps
Source water Raw water pumps
Emulsion / BFW exchanger
HP BFW pumps HP BFW headerSteam
GeneratorHP Steam header
B/L Well padsBlowdown header
Disposal Water Tank
Disposal wells CPF B/L PW Surge Drum
Vapour Fraction 0.000 0.000 0.000 0.000 1.000 1.000 0.000 0.000 0.000 0.000 0.000Operating Temperature °C 115.9 179.2 180.8 180.8 286.7 286.7 286.7 55.0 55.6 15.5 15.7
Operating Pressure kPaa 2,009 1,909 7,493 7,493 7,093 7,093 7,093 150 5,022 363 1,670Mass Flow kg/h 890,736 890,736 890,736 890,736 872,921 872,921 17,815 28,049 28,049 78,043 78,043
Mass Density kg/m3 946.8 888.2 890.2 890.2 37.1 37.1 738.2 985.5 987.3 1,014.5 1,014.7Molecular Weight kg/kgmole 18.02 18.02 18.02 18.02 18.02 18.02 18.02 18.02 18.02 18.02 18.02
Mass Heat Capacity kJ/kg‐C 4.23 4.40 4.38 4.38 5.08 5.08 5.43 4.18 4.17 4.32 4.31Thermal Conductivity W/m‐K 0.686 0.677 0.676 0.676 0.042 0.042 0.564 0.649 0.649 0.596 0.596
Combined Liquid 0 0 0 0Mass Flow kg/h 890,736 890,736 890,736 890,736 0 0 17,815 28,049 28,049 78,043 78,043
Std Ideal Liq Vol Flow m3/h 893 893 893 893 ‐ ‐ 18 28 28 78 78Actual Volume Flow m3/h 941 1,003 1,001 1,001 ‐ ‐ 24 28 28 77 77
Mass Density kg/m3 946.8 888.2 890.2 890.2 ‐ ‐ 738.2 985.5 987.3 1,014.5 1,014.7Molecular Weight kg/kgmole 18.02 18.02 18.02 18.02 ‐ ‐ 18.02 18.02 18.02 18.02 18.02
Viscosity cP 0.24 0.15 0.15 0.15 ‐ ‐ 0.09 0.50 0.50 1.12 1.12Thermal Conductivity W/m‐K 0.686 0.677 0.676 0.676 ‐ ‐ 0.564 0.649 0.649 0.596 0.596
Oil 0 0 0 0Mass Flow kg/h 0 0 0 0 0 0 0 0 0 0 0
Std Ideal Liq Vol Flow m3/h ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐Actual Volume Flow m3/h ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐
Mass Density (Note 3) kg/m3 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐API Gravity (STD) °API ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐Molecular Weight kg/kgmole ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐Viscosity (Note 4) cP ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐
Thermal Conductivity W/m‐K ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐Water 0 0 0 0
Mass Flow kg/h 890,736 890,736 890,736 890,736 0 0 17,815 28,049 28,049 78,043 78,043Std Ideal Liq Vol Flow m3/h 893 893 893 893 ‐ ‐ 18 28 28 78 78Actual Volume Flow m3/h 941 1,003 1,001 1,001 ‐ ‐ 24 28 28 77 77
Mass Density kg/m3 946.8 888.2 890.2 890.2 ‐ ‐ 738.2 985.5 987.3 1,014.5 1,014.7Viscosity cP 0.24 0.15 0.15 0.15 ‐ ‐ 0.09 0.50 0.50 1.12 1.12
Thermal Conductivity W/m‐K 0.686 0.677 0.676 0.676 ‐ ‐ 0.564 0.649 0.649 0.596 0.596Vapour 0 0 0 0
Mass Flow kg/h 0 0 0 0 872,921 872,921 0 0 0 0 0Std Gas Flow STD_m3/h ‐ ‐ ‐ ‐ 1,145,691 1,145,691 ‐ ‐ ‐ ‐ ‐
Molecular Weight kg/kgmole ‐ ‐ ‐ ‐ 18.0 18.0 ‐ ‐ ‐ ‐ ‐Mass Density kg/m3 ‐ ‐ ‐ ‐ 37.1 37.1 ‐ ‐ ‐ ‐ ‐
Viscosity cP ‐ ‐ ‐ ‐ 0.019 0.019 ‐ ‐ ‐ ‐ ‐Cp/(Cp‐R) (Ideal Gamma) ‐ ‐ ‐ ‐ 1.1 1.1 ‐ ‐ ‐ ‐ ‐
Z Factor ‐ ‐ ‐ ‐ 0.7 0.7 ‐ ‐ ‐ ‐ ‐Thermal Conductivity W/m‐K ‐ ‐ ‐ ‐ 0.0 0.0 ‐ ‐ ‐ ‐ ‐
0.00000 0.00000 0.00000 0.00000H2O 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000 1.0000H2S 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000CO2 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
Helium 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000Nitrogen 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
Air 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000Methane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000Ethane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
Propane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000C4+ 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
NOTES:1. Values are for each 40,000 bpd phase for Phases 3 & 4. SUNCOR LEWIS PH 3 & 4
AREA 5000 & 5700 ‐ BFW & STEAM GENERATIONAREA 7000 & 9000 ‐ DISPOSAL & RAW WATER SYSTEMS
HEAT AND MATERIAL BALANCE 40,000 BPSD
Stream Number
Stream Name
From
To
Overall
Overall Composition Mole Fraction
Area 5000-5700 HMB (3,4) - Page 9 of 12
SUNCOR LEWIS PH 3 4HEAT MATERIAL BALANCE TABLE
6000 6001 6002 6003 6004 6005 6006 6007 6008 6009 6010 6011 6012 6013 6014 6015 6016 6017 6018
Cold glycol Cold glycol Hot glycol Cold Glycol Hot glycol Cold Glycol Warm glycol Hot glycol Hot glycol Hot glycol Hot glycol Hot glycol Cold glycol Cold glycol Hot glycol Cooled glycol Cold Glycol Cold Glycol Hot glycol
Glycol Circ. pump
Cold glycol supply header
Evaporator Cold glycol
supply header Dilbit Coolers
Cold glycol supply header
Sample / seal flush cooling
Dilbit Coolers / Evaporator
bypass lineHot glycol
Supply headerCombustion Air Preheaters
Hot glycol Supply header
Natural gas heater
Heating glycol system
Glycol main return header
Glycol Aerial Coolers
Glycol Circ. Pumps
Cold glycol supply header
Produced Gas Condenser
Cold glycol supply header
EvaporatorHot glycol
Return headerDilbit Coolers
Hot glycol Return header
Sample / seal flush cooling
Warm glycol return header
Hot glycol return header
Glycol Return header
Combustion Air Preheaters
Cold glycol return header
Natural gas heater
Cold glycol return header
Glycol return header
Glycol Aerial Coolers
Expansion Drum Glycol FilterProduced Gas Condenser
Hot glycol Return header
Vapour Fraction 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000Operating Temperature °C 40.0 40.0 90.0 40.0 90.0 40.0 70.0 90.0 90.0 90.0 50.0 90.0 45.0 50.0 69.9 40.0 40.0 40.0 90.0
Operating Pressure kPaa 1,094 1,094 794 1,094 794 1,094 404 794 404 654 404 654 153 404 404 153 153 1,094 794Mass Flow kg/h 475,043 48,953 48,953 251,489 251,489 54,750 54,750 365,543 175,668 183,369 183,369 6,506 6,506 183,369 413,786 413,786 54,750 65,101 65,101
Mass Density kg/m3 1,074.7 1,074.7 1,038.2 1,074.7 1,038.2 1,074.7 1,054.3 1,038.2 1,038.2 1,038.2 1,068.3 1,038.2 1,071.5 1,068.3 1,054.4 1,074.7 1,074.7 1,074.7 1,038.2Molecular Weight kg/kgmole 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17
Mass Heat Capacity kJ/kg‐C 3.19 3.19 3.41 3.19 3.41 3.19 3.32 3.41 3.41 3.41 3.23 3.41 3.21 3.23 3.32 3.19 3.19 3.19 3.41Thermal Conductivity W/m‐K 0.351 0.351 0.336 0.351 0.336 0.351 0.342 0.336 0.336 0.336 0.348 0.336 0.349 0.348 0.342 0.351 0.351 0.351 0.336
Combined LiquidMass Flow kg/h 475,043 48,953 48,953 251,489 251,489 54,750 54,750 365,543 175,668 183,369 183,369 6,506 6,506 183,369 413,786 413,786 54,750 65,101 65,101
Std Ideal Liq Vol Flow m3/h 434 45 45 230 230 50 50 334 160 167 167 6 6 167 378 378 50 59 59Actual Volume Flow m3/h 442 46 47 234 242 51 52 352 169 177 172 6 6 172 392 385 51 61 63
Mass Density kg/m3 1,074.7 1,074.7 1,038.2 1,074.7 1,038.2 1,074.7 1,054.3 1,038.2 1,038.2 1,038.2 1,068.3 1,038.2 1,071.5 1,068.3 1,054.4 1,074.7 1,074.7 1,074.7 1,038.2Molecular Weight kg/kgmole 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17
Viscosity cP 4.82 4.82 1.41 4.82 1.41 4.82 2.16 1.41 1.41 1.41 3.57 1.41 4.13 3.57 2.17 4.82 4.82 4.82 1.41Thermal Conductivity W/m‐K 0.351 0.351 0.336 0.351 0.336 0.351 0.342 0.336 0.336 0.336 0.348 0.336 0.349 0.348 0.342 0.351 0.351 0.351 0.336
OilMass Flow kg/h 475,043 48,953 48,953 251,489 251,489 54,750 54,750 365,543 175,668 183,369 183,369 6,506 6,506 183,369 413,786 413,786 54,750 65,101 65,101
Std Ideal Liq Vol Flow m3/h 434 45 45 230 230 50 50 334 160 167 167 6 6 167 378 378 50 59 59Actual Volume Flow m3/h 442 46 47 234 242 51 52 352 169 177 172 6 6 172 392 385 51 61 63
Mass Density (Note 3) kg/m3 1074.7 1074.7 1038.2 1074.7 1038.2 1074.7 1054.3 1038.2 1038.2 1038.2 1068.3 1038.2 1071.5 1068.3 1054.4 1074.7 1074.7 1074.7 1038.2API Gravity (STD) °API ‐2.41 ‐2.41 ‐2.41 ‐2.41 ‐2.41 ‐2.41 ‐2.41 ‐2.41 ‐2.41 ‐2.41 ‐2.41 ‐2.41 ‐2.41 ‐2.41 ‐2.41 ‐2.41 ‐2.41 ‐2.41 ‐2.41Molecular Weight kg/kgmole 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17 38.17Viscosity (Note 4) cP 4.82 4.82 1.41 4.82 1.41 4.82 2.16 1.41 1.41 1.41 3.57 1.41 4.13 3.57 2.17 4.82 4.82 4.82 1.41
Thermal Conductivity W/m‐K 0.351 0.351 0.336 0.351 0.336 0.351 0.342 0.336 0.336 0.336 0.348 0.336 0.349 0.348 0.342 0.351 0.351 0.351 0.336Water 0 0 0 0 0 0 0 0 0
Mass Flow kg/h 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0Std Ideal Liq Vol Flow m3/h ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐Actual Volume Flow m3/h ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐
Mass Density kg/m3 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐Viscosity cP ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐
Thermal Conductivity W/m‐K ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐Vapour
Mass Flow kg/h 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0Std Gas Flow STD_m3/h ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐
Molecular Weight kg/kgmole ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐Mass Density kg/m3 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐
Viscosity cP ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐Cp/(Cp‐R) (Ideal Gamma) ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐
Z Factor ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐Thermal Conductivity W/m‐K ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐
H2O 1.0 (60% TEG) 1.0 (60% TEG) 1.0 (60% TEG) 1.0 (60% TEG) 1.0 (60% TEG) 1.0 (60% TEG) 1.0 (60% TEG) 1.0 (60% TEG) 1.0 (60% TEG) 1.0 (60% TEG) 1.0 (60% TEG) 1.0 (60% TEG) 1.0 (60% TEG) 1.0 (60% TEG) 1.0 (60% TEG) 1.0 ( 60%TEG) 1.0 ( 60%TEG) 1.0 ( 60%TEG) 1.0 ( 60%TEG)H2S 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000CO2 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
Helium 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000Nitrogen 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
Air 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000Methane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000Ethane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
Propane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000C4+ 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
NOTES:1. Values are for each 40,000 bpd phase for Phases 3 & 4. SUNCOR LEWIS PH 3 & 4
AREA 6200 ‐ GLYCOL SYSTEMHEAT AND MATERIAL BALANCE
PROJECT # DRAWING NUMBER REVISION
40,000 BPSD
Stream Number
Stream Name
From
To
Overall
Overall Composition Mole Fraction
Area 6000 HMB (3,4) - Page 10 of 12
SUNCOR LEWIS PH 3 4HEAT MATERIAL BALANCE TABLE
6200 6201 6202 6203 6204 6207 6208 6209 6211 6212 6214 6215 6216
Natural gas Natural gas Natural gas Natural gas HP fuel gasCombined Fuel
Gas Mixed fuel gas Mixed fuel gas
Blanketing Natural gas
Purge gas Natural gas Bubble gas Mixed Fuel Gas
CPF B/L HeaderDiluent Rec. Trim Cooler
Natural Gas Heater
Header NG / PG HeaderMixed Fuel Gas
DrumMixed fuel gas
headerPipeline
Critical fuel gas header
LP Fuel gas header
MP fuel gas header
Produced Gas Header
HeaderDiluent Rec. Trim Cooler
Natural Gas Heater
HeaderEvaporator Vent
EjectorMixed Fuel Gas
DrumMixed fuel gas
headerHP Steam Generator
Wellpads HP Flare headerSteam Gen. Pilot
burnerCFU NG / PG Header
Vapour Fraction 1.000 1.000 1.000 1.000 1.000 1.000 1.000 1.000 1.000 1.000 1.000 1.000 0.998Operating Temperature °C 7.0 7.0 41.4 50.0 34.2 22.4 22.4 22.4 7.0 19.1 19.8 26.1 46.9
Operating Pressure kPaa 7,068 7,068 6,968 6,868 3,193 353 353 353 7,068 443 443 1,595 353Mass Flow kg/h 40,540 40,363 40,363 40,363 1,600 41,055 41,054 41,054 156 21 244 2,621 5,156
Mass Density kg/m3 67.5 67.5 54.2 51.2 23.8 2.6 2.6 2.6 67.5 3.3 3.3 11.8 2.5Molecular Weight kg/kgmole 17.67 17.67 17.67 17.67 17.67 17.82 17.82 17.82 17.67 17.67 17.67 17.67 18.97
Mass Heat Capacity kJ/kg‐C 2.88 2.88 2.67 2.64 2.38 2.14 2.14 2.14 2.88 2.15 2.16 2.25 2.13Thermal Conductivity W/m‐K 0.038 0.038 0.041 0.042 0.036 0.032 0.032 0.032 0.038 0.032 0.032 0.034 0.000
Combined LiquidMass Flow kg/h 0 0 0 0 0 0 0 0 0 0 0 0 12
Std Ideal Liq Vol Flow m3/h ‐ ‐ ‐ ‐ ‐ 0 ‐ ‐ ‐ ‐ ‐ ‐ 0Actual Volume Flow m3/h ‐ ‐ ‐ ‐ ‐ 0 ‐ ‐ ‐ ‐ ‐ ‐ 0
Mass Density kg/m3 ‐ ‐ ‐ ‐ ‐ 862.9 ‐ ‐ ‐ ‐ ‐ ‐ 976.2Molecular Weight kg/kgmole ‐ ‐ ‐ ‐ ‐ 166.2 ‐ ‐ ‐ ‐ ‐ ‐ 19.5
Viscosity cP ‐ ‐ ‐ ‐ ‐ 36.5 ‐ ‐ ‐ ‐ ‐ ‐ 0.7Thermal Conductivity W/m‐K ‐ ‐ ‐ ‐ ‐ 0.1 ‐ ‐ ‐ ‐ ‐ ‐ 0.6
OilMass Flow kg/h 0 0 0 0 0 0 0 0 0 0 0 0 1
Std Ideal Liq Vol Flow m3/h ‐ ‐ ‐ ‐ ‐ 0 ‐ ‐ ‐ ‐ ‐ ‐ 0Actual Volume Flow m3/h ‐ ‐ ‐ ‐ ‐ 0 ‐ ‐ ‐ ‐ ‐ ‐ 0
Mass Density (Note 3) kg/m3 ‐ ‐ ‐ ‐ ‐ 862.9 ‐ ‐ ‐ ‐ ‐ ‐ 841.4API Gravity (STD) °API ‐ ‐ ‐ ‐ ‐ 311.4 ‐ ‐ ‐ ‐ ‐ ‐ 281.9Molecular Weight kg/kgmole ‐ ‐ ‐ ‐ ‐ 166.2 ‐ ‐ ‐ ‐ ‐ ‐ 153.9Viscosity (Note 4) cP ‐ ‐ ‐ ‐ ‐ 36.5 ‐ ‐ ‐ ‐ ‐ ‐ 11.0
Thermal Conductivity W/m‐K ‐ ‐ ‐ ‐ ‐ 0.1 ‐ ‐ ‐ ‐ ‐ ‐ 0.1Water
Mass Flow kg/h 0 0 0 0 0 0 0 0 0 0 0 0 11Std Ideal Liq Vol Flow m3/h ‐ ‐ ‐ ‐ 0 ‐ ‐ ‐ ‐ ‐ ‐ ‐ 0Actual Volume Flow m3/h ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ 0
Mass Density kg/m3 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ 990.8Viscosity cP ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ 0.6
Thermal Conductivity W/m‐K ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ 0.6Vapour
Mass Flow kg/h 40,540 40,363 40,363 40,363 1,600 41,054 41,054 41,054 156 21 244 2,621 5,144Std Gas Flow STD_m3/h 54,260 54,023 54,023 54,023 2,141 54,474 54,474 54,474 208 28 327 3,508 6,412
Molecular Weight kg/kgmole 17.67 17.67 17.67 17.67 17.67 17.82 17.82 17.82 17.67 17.67 17.67 17.67 18.97Mass Density kg/m3 67.5 67.5 54.2 51.2 23.8 2.6 2.6 2.6 67.5 3.3 3.3 11.8 2.5
Viscosity cP 0.013 0.013 0.014 0.014 0.012 0.011 0.011 0.011 0.013 0.011 0.011 0.012 0.012Cp/(Cp‐R) (Ideal Gamma) 1.195 1.195 1.214 1.217 1.247 1.278 1.278 1.278 1.195 1.280 1.279 1.265 1.258
Z Factor 0.795 0.795 0.868 0.883 0.928 0.990 0.990 0.990 0.795 0.988 0.988 0.959 0.992Thermal Conductivity W/m‐K 0.038 0.038 0.041 0.042 0.036 0.032 0.032 0.032 0.038 0.032 0.032 0.034 0.034
H2O 0.0000 0.0000 0.0000 0.0000 0.0000 0.0038 0.0038 0.0038 0.0000 0.0000 0.0000 0.0000 0.0321H2S 0.0000 0.0000 0.0000 0.0000 0.0000 0.0001 0.0001 0.0001 0.0000 0.0000 0.0000 0.0000 0.0006CO2 0.0058 0.0058 0.0058 0.0058 0.0058 0.0076 0.0076 0.0076 0.0058 0.0058 0.0058 0.0058 0.0210
Helium 0.0001 0.0001 0.0001 0.0001 0.0001 0.0001 0.0001 0.0001 0.0001 0.0001 0.0001 0.0001 0.0001Nitrogen 0.0046 0.0046 0.0046 0.0046 0.0046 0.0045 0.0045 0.0045 0.0046 0.0046 0.0046 0.0046 0.0040
Air 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000Methane 0.9180 0.9180 0.9180 0.9180 0.9180 0.9109 0.9109 0.9109 0.9180 0.9180 0.9180 0.9180 0.8576Ethane 0.0510 0.0510 0.0510 0.0510 0.0510 0.0505 0.0505 0.0505 0.0510 0.0510 0.0510 0.0510 0.0468
Propane 0.0142 0.0142 0.0142 0.0142 0.0142 0.0143 0.0143 0.0143 0.0142 0.0142 0.0142 0.0142 0.0153C4+ 0.0063 0.0063 0.0063 0.0063 0.0063 0.0082 0.0082 0.0082 0.0063 0.0063 0.0063 0.0063 0.0225
NOTES:1. Values are for each 40,000 bpd phase for Phases 3 & 4. SUNCOR LEWIS PH 3 & 4
AREA 6200 ‐ FUEL GAS SYSTEMHEAT AND MATERIAL BALANCE
PROJECT # DRAWING NUMBER REVISION
40,000 BPSD
Stream Number
Stream Name
From
To
Overall
Overall Composition Mole Fraction
Area 6200 HMB (3,4) - Page 11 of 12
SUNCOR LEWIS PH 4HEAT MATERIAL BALANCE TABLE
4000 4001 4002 4003 4004 4005 4006 4007
Diluent Diluent Diluent Trim diluent DilbitDilbit / Diluent
vaporsRecovered liquids
VRU Gas
Supply pipeline Diluent pumps Diluent supply
headerDiluent supply
headerDilbit tank
Dilbit/Offspec/ Diluent tanks
VRU package VRU package
CPF B/LDiluent supply
headerFWKO/Treaters
CPF B/L (Trim blending)
CPF B/L (Dilbit product pumps)
VRU package Dilbit headerDiluent Rec.
Cooler
Vapour Fraction 0.000 0.000 0.000 0.000 0.000 1.000 0.000 1.000Operating Temperature °C 15.0 15.8 15.8 15.8 53.0 53.0 53.3 126.6
Operating Pressure kPaa 593 1,613 1,613 1,613 93 93 896 460Mass Flow kg/h 73,549 73,549 33,124 40,425 300,161 4,355 0 4,355
Mass Density kg/m3 676.4 676.5 676.5 676.5 974.3 2.1 934.8 8.9Molecular Weight kg/kgmole 66.12 66.12 66.12 66.12 274.54 60.13 221.30 60.13
Mass Heat Capacity kJ/kg‐C 2.15 2.15 2.15 2.15 1.86 1.79 1.90 2.13Thermal Conductivity W/m‐K 0.109 0.109 0.109 0.109 0.118 0.017 0.114 0.024
Combined LiquidMass Flow kg/h 73,549 73,549 33,124 40,425 300,161 0 0 0
Std Ideal Liq Vol Flow m3/h 109 109 49 60 313 ‐ ‐ ‐
Actual Volume Flow m3/h 109 109 49 60 308 ‐ ‐ ‐
Mass Density kg/m3 676.4 676.5 676.5 676.5 974.3 ‐ ‐ ‐Molecular Weight kg/kgmole 66.12 66.12 66.12 66.12 274.54 ‐ ‐ ‐
Viscosity cP 0.32 0.32 0.32 0.32 183.74 ‐ ‐ ‐Thermal Conductivity W/m‐K 0.109 0.109 0.109 0.109 0.118 ‐ ‐ ‐
OilMass Flow kg/h 73,549 73,549 33,124 40,425 300,161 0 0 0
Std Ideal Liq Vol Flow m3/h 109 109 49 60 313 ‐ ‐ ‐
Actual Volume Flow m3/h 109 109 49 60 308 ‐ ‐ ‐
Mass Density (Note 3) kg/m3 676.4 676.5 676.5 676.5 974.3 ‐ ‐ ‐ API Gravity (STD) °API 77.61 77.61 77.61 77.61 16.10 ‐ ‐ ‐ Molecular Weight kg/kgmole 66.12 66.12 66.12 66.12 274.54 ‐ ‐ ‐ Viscosity (Note 4) cP 0.32 0.32 0.32 0.32 183.74 ‐ ‐ ‐
Thermal Conductivity W/m‐K 0.109 0.109 0.109 0.109 0.118 ‐ ‐ ‐ Water
Mass Flow kg/h 0 0 0 0 0 0 0 0
ndard Ideal Liquid Volume Flow m3/h ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐
Actual Volume Flow m3/h ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐
Mass Density kg/m3 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ Viscosity cP ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐
Thermal Conductivity W/m‐K ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ Vapour
Mass Flow kg/h 0 0 0 0 0 4,355 0 4,355
Std Gas Flow STD_m3/h ‐ ‐ ‐ ‐ ‐ 1,713 ‐ 1,713Molecular Weight kg/kgmole ‐ ‐ ‐ ‐ ‐ 60.13 ‐ 60.13
Mass Density kg/m3 ‐ ‐ ‐ ‐ ‐ 2.1 ‐ 8.9Viscosity cP ‐ ‐ ‐ ‐ ‐ 0.007 ‐ 0.009
Cp/(Cp‐R) (Ideal Gamma) ‐ ‐ ‐ ‐ ‐ 1.084 ‐ 1.069Z Factor ‐ ‐ ‐ ‐ ‐ 0.977 ‐ 0.933
Thermal Conductivity W/m‐K ‐ ‐ ‐ ‐ ‐ 0.017 ‐ 0.024
H2O 0.0000 0.0000 0.0000 0.0000 0.0016 0.1510 0.0016 0.1509
H2S 0.0000 0.0000 0.0000 0.0000 0.00001 0.0004 0.00001 0.0004
CO2 0.0000 0.0000 0.0000 0.0000 0.0001 0.0070 0.0001 0.0070Helium 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
Nitrogen 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000Air 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000
Methane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0027 0.0000 0.0027Ethane 0.0012 0.0012 0.0012 0.0012 0.0000 0.0031 0.0000 0.0031
Propane 0.0045 0.0045 0.0045 0.0045 0.0013 0.0297 0.0014 0.0297C4+ 0.9943 0.9943 0.9943 0.9943 0.9970 0.8061 0.9970 0.8062
NOTES:1. Trim diluent flow rate is based on meeting 350 cSt dilbit viscosity at 7.5 °C pipeline winter reference temperature. SUNCOR LEWIS PH 42. Streams 4002, 4006, and 4007 are per 40,000 bpd phase for each of Ph 1 ‐ 3. AREA 4000 ‐ HC TANK FARM
HEAT AND MATERIAL BALANCE
PROJECT # DRAWING NUMBER REVISION
40,000 BPSD
Stream Number
Stream Name
From
To
Overall
Overall Composition Mole Fraction
Area 4000 HMB (4) - Page 12 of 12