Suncor Energy Inc.
APPENDIX 8 PROCESS FLOW DIAGRAMS AND HEAT
AND MATERIAL BALANCE
SUNCOR MEADOW CREEK WESTHEAT 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 0.003 0.000 0.000 0.001 0.009 0.000 1.000 1.000 0.000 0.000 0.265 0.000 0.062 1.000 1.000 1.000 0.101 0.021 0.000 1.000Operating Temperature °C 193.0 194.1 141.1 136.0 135.3 136.0 180.5 127.1 135.3 136.0 121.9 55.0 53.0 127.2 120.3 122.1 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 1,089,507 1,102,616 1,102,616 1,166,211 362,003 801,786 4,704 2,422 34,453 836,239 326,020 304,516 304,516 1,531 22,567 30,875 30,875 30,875 30,471 404
Mass Density kg/m3 716.4 870.8 918.2 837.5 753.6 914.7 2.2 7.1 917.7 914.8 133.0 970.5 128.2 7.2 8.0 8.0 75.8 266.7 660.9 5.1Molecular Weight kg/kgmole 23.58 23.48 23.48 24.29 102.69 18.04 19.40 48.90 18.02 18.04 206.04 261.22 261.22 49.83 53.83 53.99 53.99 53.99 54.44 33.14
Mass Heat Capacity kJ/kg‐C 4.20 4.23 3.95 3.86 2.45 4.50 1.95 2.07 4.50 4.50 2.13 1.88 1.86 2.08 2.09 2.09 2.52 2.33 2.34 1.51Thermal Conductivity W/m‐K ‐ 0.477 0.482 ‐ ‐ 0.686 0.036 0.026 0.688 0.686 ‐ 0.115 ‐ 0.026 0.024 0.024 ‐ ‐ 0.114 0.022
Combined LiquidMass Flow kg/h 1,086,577 1,102,616 1,102,616 1,163,789 360,472 801,742 0 0 34,453 836,195 303,413 304,516 300,161 0 0 0 27,961 30,471 30,471 0
Std Ideal Liq Vol Flow m3/h 1,086 1,102 1,102 1,194 388 803 ‐ ‐ 35 838 319 320 313 ‐ ‐ ‐ 43 47 47 ‐Actual Volume Flow m3/h 1,246 1,266 1,201 1,287 410 874 ‐ ‐ 38 912 330 314 308 ‐ ‐ ‐ 45 46 46 ‐
Mass Density kg/m3 871.6 870.2 917.5 899.7 862.9 917.0 ‐ ‐ 917.7 917.0 856.3 933.6 934.8 ‐ ‐ ‐ 619.2 660.4 660.9 ‐Molecular Weight kg/kgmole 23.59 23.48 23.48 24.26 103.16 18.04 ‐ ‐ 18.02 18.04 261.00 261.22 274.54 ‐ ‐ ‐ 54.41 54.44 54.44 ‐
Viscosity cP 2.55 2.51 9.66 1.24 3.71 0.21 ‐ ‐ 0.20 0.21 4.00 127.81 175.75 ‐ ‐ ‐ 0.21 0.29 0.28 ‐Thermal Conductivity W/m‐K 0.474 0.477 0.482 0.422 0.113 0.686 ‐ ‐ 0.688 0.686 0.104 0.115 0.118 ‐ ‐ ‐ 0.104 0.114 0.114 ‐
OilMass Flow kg/h 268,377 268,256 267,779 327,006 324,390 1,166 0 0 0 1,166 303,413 304,324 144,261 0 0 0 25,520 27,980 27,980 0
Std Ideal Liq Vol Flow m3/h 266 266 266 356 352 1 ‐ ‐ ‐ 1 319 320 143 ‐ ‐ ‐ 40 44 44 ‐Actual Volume Flow m3/h 296 297 286 374 370 1 ‐ ‐ ‐ 1 330 314 141 ‐ ‐ ‐ 43 44 44 ‐
Mass Density (Note 3) kg/m3 901.1 900.5 932.6 854.7 856.8 856.3 ‐ ‐ ‐ 856.3 856.3 933.6 934.8 ‐ ‐ ‐ 597.9 640.4 640.9 ‐API Gravity (STD) °API 10.0 9.8 9.8 13.7 21.0 10.2 ‐ ‐ ‐ 10.17 21.87 17.15 17.15 ‐ ‐ ‐ 86.63 86.63 85.87 ‐ Molecular Weight kg/kgmole 412.94 415.19 432.61 214.89 217.44 232.07 ‐ ‐ ‐ 231.97 261.00 263.46 374.44 ‐ ‐ ‐ 67.43 66.36 66.36 ‐Viscosity (Note 4) cP 9.91 9.91 39.17 3.90 4.10 4.04 ‐ ‐ ‐ 4.00 4.00 127.89 175.75 ‐ ‐ ‐ 0.17 0.24 0.24 ‐
Thermal Conductivity W/m‐K 0.129 0.129 0.124 0.094 0.095 0.097 ‐ ‐ ‐ 0.097 0.104 0.115 0.122 ‐ ‐ ‐ 0.095 0.105 0.105 ‐Water
Mass Flow kg/h 818,199 834,359 834,837 836,784 36,083 800,576 0 0 34,453 835,029 0 192 0 0 0 0 2,440 2,491 2,491 0Std Ideal Liq Vol Flow m3/h 820 836 837 839 36 802 0 0 35 837 0 0.2 0 0 0 0 2 2 2 ‐Actual Volume Flow m3/h 949 970 915 912 39 873 ‐ ‐ 38 910 ‐ 0.2 ‐ ‐ ‐ ‐ 2 2 2 ‐
Mass Density kg/m3 861.8 860.4 912.6 917.2 917.8 917.1 ‐ ‐ 917.7 917.1 ‐ 984.5 ‐ ‐ ‐ ‐ 985.3 1,017.4 1,017.3 ‐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 0.669 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 2,930 0 0 2,422 1,531 44 4,704 2,422 0 44 22,606 0 4,355 1,531 22,567 30,875 2,914 404 0 404Std Gas Flow STD_m3/h 3,548 ‐ ‐ 1,171 727 21 5,734 1,171 ‐ 21 9,926 ‐ 1,713 727 9,913 13,523 1,372 288 ‐ 288
Molecular Weight kg/kgmole 19.53 ‐ ‐ 48.90 49.83 49.58 19.40 48.90 ‐ 49.58 53.85 ‐ 60.13 49.83 53.83 53.99 50.21 33.14 ‐ 33.14Mass Density kg/m3 10.7 ‐ ‐ 22.9 21.6 19.3 2.2 7.1 ‐ 19.3 10.7 ‐ 2.1 7.2 8.0 8.0 8.0 5.8 ‐ 5.1
Viscosity cP 0.014 ‐ ‐ 0.011 0.011 0.011 0.013 0.011 ‐ 0.011 0.010 ‐ 0.007 0.011 0.010 0.010 0.010 0.011 ‐ 0.011Cp/(Cp‐R) (Ideal Gamma) 1.092 ‐ ‐ 1.097 1.034 1.114 1.281 1.090 ‐ 1.114 1.019 ‐ 1.017 1.087 1.080 1.080 1.065 1.071 ‐ 1.200
Z Factor 0.946 ‐ ‐ 0.876 0.878 0.890 0.985 0.958 ‐ 0.890 0.923 ‐ 0.977 0.956 0.941 0.943 0.941 0.971 ‐ 0.975Thermal Conductivity W/m‐K 0.041 ‐ ‐ 0.028 0.028 0.027 0.036 0.026 ‐ 0.027 0.024 ‐ 0.017 0.026 0.024 0.024 0.021 0.022 ‐ 0.022
H2O 0.9856 0.9870 0.9870 0.9680 0.5788 0.9997 0.7766 0.2291 0.9999 0.9997 0.0765 0.0108 0.0108 0.2412 0.2587 0.2416 0.2416 0.2416 0.2468 0.0035H2S 0.00001 0.00001 0.00001 0.00001 0.0001 0.00001 0.0007 0.0009 0.00001 0.00001 0.0001 0.00003 0.00003 0.0009 0.0004 0.0004 0.0004 0.0004 0.0004 0.0027CO2 0.0005 0.0002 0.0002 0.0004 0.0023 0.0001 0.0535 0.0627 0.0001 0.0001 0.0039 0.0005 0.0005 0.0540 0.0132 0.0189 0.0189 0.0189 0.0134 0.2723
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 0.0010 0.0001 0.0001 0.0002 0.0018 0.0000 0.1674 0.0897 0.0000 0.0000 0.0026 0.0002 0.0002 0.0659 0.0094 0.0185 0.0185 0.0185 0.0086 0.4768Ethane 0.0000 0.0000 0.0000 0.0001 0.0007 0.0000 0.0000 0.0153 0.0000 0.0000 0.0014 0.0002 0.0002 0.0139 0.0045 0.0058 0.0058 0.0058 0.0050 0.0428
Propane 0.0000 0.0000 0.0000 0.0004 0.0047 0.0000 0.0000 0.0485 0.0000 0.0000 0.0095 0.0031 0.0031 0.0478 0.0272 0.0305 0.0305 0.0305 0.0297 0.0643C4+ 0.0129 0.0127 0.0127 0.0309 0.4117 0.0001 0.0018 0.5539 0.0000 0.0001 0.9061 0.9852 0.9852 0.5763 0.6865 0.6843 0.6843 0.6843 0.6962 0.1376
NOTES:SUNCOR MEADOW CREEK WEST
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 - Page 1 of 6
SUNCOR MEADOW CREEK WESTHEAT 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 0.166 0.000 0.000 1.000 1.000 0.000 0.000 1.000 0.375 0.000 1.000 1.000 1.000 0.001 0.000 0.000 0.000 1.000 1.000Operating Temperature °C 135.7 120.9 134.9 123.2 176.1 129.0 129.5 129.7 149.2 60.0 60.0 59.8 112.2 112.5 60.0 60.0 115.6 111.6 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 868,565 30,413 840,773 947,307 2,730 6,583 1,064 32,327 11,287 11,287 6,803 4,484 28,516 28,607 28,607 28,523 890,658 28,049 84 1,684
Mass Density kg/m3 915.2 16.9 917.3 928.1 3.0 2.4 929.1 922.8 2.3 7.4 976.4 2.6 0.9 0.9 314.7 980.6 946.1 985.5 1.4 2.6Molecular Weight kg/kgmole 18.04 18.72 18.02 18.02 18.05 18.92 395.25 18.02 19.12 19.12 18.45 20.23 18.02 18.05 18.05 18.02 18.02 18.02 37.23 18.14
Mass Heat Capacity kJ/kg‐C 4.50 4.00 4.50 4.46 1.99 2.12 2.11 4.48 2.06 3.36 4.27 1.99 1.92 1.92 4.32 4.33 4.24 4.18 1.02 2.09Thermal Conductivity W/m‐K 0.686 ‐ 0.688 0.687 0.032 0.036 0.123 0.688 0.036 ‐ 0.626 0.035 0.026 0.025 ‐ 0.654 0.686 0.649 0.020 0.031
Combined LiquidMass Flow kg/h 868,523 25,335 840,770 947,307 0 0 1,064 32,327 0 6,803 6,803 0 0 0 28,523 28,523 890,658 28,049 0 0
Std Ideal Liq Vol Flow m3/h 870 25 842 949 ‐ ‐ 1 32 ‐ 7 7 ‐ ‐ ‐ 29 29 892 28 ‐ ‐Actual Volume Flow m3/h 947 27 916 1,021 ‐ ‐ 1 35 ‐ 7 7 ‐ ‐ ‐ 29 29 941 28 ‐ ‐
Mass Density kg/m3 917.3 930.9 917.8 928.1 ‐ ‐ 929.1 922.8 ‐ 976.4 976.4 ‐ ‐ ‐ 980.5 980.6 946.1 985.5 ‐ ‐Molecular Weight kg/kgmole 18.04 18.69 18.02 18.02 ‐ ‐ 395.25 18.02 ‐ 18.5 18.45 ‐ ‐ ‐ 18.02 18.02 18.02 18.02 ‐ ‐
Viscosity cP 0.20 0.25 0.20 0.22 ‐ ‐ 39.10 0.21 ‐ 0.5 0.50 ‐ ‐ ‐ 0.46 0.46 0.24 0.50 ‐ ‐Thermal Conductivity W/m‐K 0.686 0.652 0.688 0.687 ‐ ‐ 0.123 0.688 ‐ 0.6 0.626 ‐ ‐ ‐ 0.653 0.654 0.686 0.649 ‐ ‐
OilMass Flow kg/h 1,168 951 26 0 0 0 1,064 0 0 179 179 0 0 0 0 0 0 0 0 0
Std Ideal Liq Vol Flow m3/h 1 1 0.03 ‐ ‐ ‐ 1 ‐ ‐ 0.2 0.2 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ Actual Volume Flow m3/h 1 1 0.03 ‐ ‐ ‐ 1 ‐ ‐ 0.2 0.2 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐
Mass Density (Note 3) kg/m3 888.5 948.8 943.2 ‐ ‐ ‐ 929.1 ‐ ‐ 842.8 842.9 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐API Gravity (STD) °API 10.17 37.12 10.15 ‐ ‐ ‐ 10.30 ‐ ‐ 104.2 10.7 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐Molecular Weight kg/kgmole 231.22 437.83 446.30 ‐ ‐ ‐ 395.26 ‐ ‐ 169.6 169.6 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐Viscosity (Note 4) cP 7.57 85.68 61.00 ‐ ‐ ‐ 39.10 ‐ ‐ 10.7 10.7 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐
Thermal Conductivity W/m‐K 0.097 0.125 0.125 ‐ ‐ ‐ 0.123 ‐ ‐ 0.1 0.1 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐Water
Mass Flow kg/h 867,356 24,383 840,745 947,307 0 0 0 32,327 0 6,624 6,624 0 0 0 28,523 28,523 890,658 28,049 0 0Std Ideal Liq Vol Flow m3/h 869 24 842 949 0 0 0 32 0 7 7 0 0 0 29 29 892 28 0 0Actual Volume Flow m3/h 946 26 916 1,021 ‐ ‐ ‐ 35 ‐ 7 7 ‐ ‐ ‐ 29 29 941 28 ‐ ‐
Mass Density kg/m3 917.3 930.2 917.8 928.1 ‐ ‐ ‐ 922.8 ‐ 980.6 980.6 ‐ ‐ ‐ 980.5 980.6 946.1 985.5 ‐ ‐Viscosity cP 0.20 0.23 0.20 0.22 ‐ ‐ ‐ 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 ‐ 0.653 0.654 ‐ ‐ ‐ 0.653 0.654 0.686 0.649 ‐ ‐Vapour
Mass Flow kg/h 42 5,079 2 0 2,730 6,583 0 0 11,287 4,484 0 4,484 28,516 28,607 84 0 0 0 84 1,684Std Gas Flow STD_m3/h 20 6,364 3 ‐ 3,576 8,226 ‐ ‐ 13,959 5,241 ‐ 5,241 37,426 37,477 53 ‐ ‐ ‐ 53 2,195
Molecular Weight kg/kgmole 49.59 18.87 18.02 ‐ 18.05 18.92 ‐ ‐ 19.1 20.2 ‐ 20.2 18.02 18.05 37.23 ‐ ‐ ‐ 37.23 18.14Mass Density kg/m3 19.3 2.9 4.2 ‐ 3.0 2.4 ‐ ‐ 2.3 3.0 ‐ 2.6 0.9 0.9 1.4 ‐ ‐ ‐ 1.4 2.6
Viscosity cP 0.011 0.013 0.013 ‐ 0.011 0.012 ‐ ‐ 0.012 0.013 ‐ 0.013 0.013 0.010 0.014 ‐ ‐ ‐ 0.014 0.011Cp/(Cp‐R) (Ideal Gamma) 1.114 1.125 1.114 ‐ 1.301 1.261 ‐ ‐ 1.3 1.1 ‐ 1.3 1.317 1.317 1.119 ‐ ‐ ‐ 1.280 1.280
Z Factor 0.890 0.988 0.985 ‐ 0.969 0.987 ‐ ‐ 1.0 1.0 ‐ 1.0 0.988 0.988 0.995 ‐ ‐ ‐ 0.995 0.990Thermal Conductivity W/m‐K 0.027 0.037 0.040 ‐ 0.032 0.036 ‐ ‐ 0.04 0.03 ‐ 0.03 0.026 0.025 0.020 ‐ ‐ ‐ 0.020 0.031
H2O 0.9998 0.9027 1.0000 1.0000 0.9954 0.5473 0.0170 1.0000 0.6415 0.6415 0.9971 0.0501 1.0000 0.9986 0.9986 0.9998 1.0000 1.0000 0.2001 0.0039H2S 0.00001 0.0001 0.000003 0.000004 0.00003 0.0004 0.00003 0.000001 0.000525 0.000525 0.000005 0.001390 0.0000 0.0001 0.0001 0.000054 0.0000 0.0000 0.0632 0.0012CO2 0.0001 0.0033 0.0000 0.0000 0.0015 0.0160 0.0004 0.0000 0.0314 0.0314 0.0001 0.0835 0.0000 0.0012 0.0012 0.0002 0.0000 0.0000 0.7007 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 0.0000 0.0000 0.0009 0.0001Nitrogen 0.0000 0.0004 0.0000 0.0000 0.0000 0.0019 0.0000 0.0000 0.0011 0.0011 0.0000 0.0030 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0055 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 0.0000 0.0000 0.0000 0.0000Methane 0.0000 0.0837 0.0000 0.0000 0.0031 0.3928 0.0055 0.0000 0.3002 0.3002 0.0000 0.8000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0295 0.9010Ethane 0.0000 0.0047 0.0000 0.0000 0.0000 0.0218 0.0008 0.0000 0.0128 0.0128 0.0000 0.0342 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0500
Propane 0.0000 0.0013 0.0000 0.0000 0.0000 0.0062 0.0005 0.0000 0.0037 0.0037 0.0000 0.0098 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0139C4+ 0.0001 0.0039 0.0000 0.0000 0.0000 0.0134 0.9757 0.0000 0.0087 0.0087 0.0028 0.0180 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0059
NOTES:SUNCOR MEADOW CREEK WEST
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 - Page 2 of 6
SUNCOR MEADOW CREEK WESTHEAT 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 (Grand Rapids)
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 115.9 178.4 180.1 180.1 180.1 286.7 286.7 286.7 286.7 286.7 286.7 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 890,658 890,658 890,658 529,414 361,245 518,825 872,845 10,588 17,813 7,225 354,020 381,399 18,965 362,434 362,434 28,049 28,049 78,043 78,043
Mass Density kg/m3 946.8 889.0 891.0 891.0 891.0 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 0.677 0.677 0.677 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 LiquidMass Flow kg/h 890,658 890,658 890,658 529,414 361,245 0 0 10,588 17,813 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 892 892 892 530 362 ‐ ‐ 11 18 7 ‐ 362 18 344 344 28 28 78 78Actual Volume Flow m3/h 941 1,002 1,000 594 405 ‐ ‐ 14 24 10 ‐ 363 18 345 347 28 28 77 77
Mass Density kg/m3 946.8 889.0 891.0 891.0 891.0 ‐ ‐ 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 0.677 0.677 0.677 ‐ ‐ 0.564 0.564 0.564 ‐ 0.413 0.413 0.413 0.416 0.649 0.649 0.596 0.596
OilMass 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
Mass Flow kg/h 890,658 890,658 890,658 529,414 361,245 0 0 10,588 17,813 7,225 0 0 0 0 0 28,049 28,049 78,043 78,043Std Ideal Liq Vol Flow m3/h 892 892 892 530 362 0 0 11 18 7 0 0 0 0 0 28 28 78 78Actual Volume Flow m3/h 941 1,002 1,000 594 405 ‐ ‐ 14 24 10 ‐ ‐ ‐ ‐ ‐ 28 28 77 77
Mass Density kg/m3 946.8 889.0 891.0 891.0 891.0 ‐ ‐ 738.2 738.2 738.2 ‐ ‐ ‐ ‐ ‐ 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 ‐ ‐ ‐ ‐ ‐ 0.50 0.50 1.12 1.12
Thermal Conductivity W/m‐K 0.686 0.677 0.677 0.677 0.677 ‐ ‐ 0.564 0.564 0.564 ‐ ‐ ‐ ‐ ‐ 0.649 0.649 0.596 0.596Vapour
Mass Flow kg/h 0 0 0 0 0 518,825 872,845 0 0 0 354,020 0 0 0 0 0 0 0 0Std Gas Flow STD_m3/h ‐ ‐ ‐ ‐ ‐ 680,947 1,145,591 ‐ ‐ ‐ 464,643 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐
Molecular Weight kg/kgmole ‐ ‐ ‐ ‐ ‐ 18.02 18.02 ‐ ‐ ‐ 18.02 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐Mass Density kg/m3 ‐ ‐ ‐ ‐ ‐ 37.1 37.1 ‐ ‐ ‐ 37.1 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐
Viscosity cP ‐ ‐ ‐ ‐ ‐ 0.019 0.019 ‐ ‐ ‐ 0.019 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐Cp/(Cp‐R) (Ideal Gamma) ‐ ‐ ‐ ‐ ‐ 1.100 1.100 ‐ ‐ ‐ 1.100 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐
Z Factor ‐ ‐ ‐ ‐ ‐ 0.741 0.741 ‐ ‐ ‐ 0.741 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐Thermal Conductivity W/m‐K ‐ ‐ ‐ ‐ ‐ 0.042 0.042 ‐ ‐ ‐ 0.042 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐
H2O 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:SUNCOR MEADOW CREEK WEST
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 - Page 3 of 6
SUNCOR MEADOW CREEK WESTHEAT 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 71.5 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 517,034 48,953 48,953 250,871 250,871 54,750 54,750 407,534 212,750 183,369 183,369 11,415 11,415 183,369 450,869 450,869 54,750 107,710 107,710
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 1,053.2 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 3.32 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 0.351 0.348 0.342 0.351 0.351 0.351 0.336
Combined LiquidMass Flow kg/h 517,034 48,953 48,953 250,871 250,871 54,750 54,750 407,534 212,750 183,369 183,369 11,415 11,415 183,369 450,869 450,869 54,750 107,710 107,710
Std Ideal Liq Vol Flow m3/h 472 45 45 229 229 50 50 372 194 167 167 10 10 167 412 412 50 98 98Actual Volume Flow m3/h 481 46 47 233 242 51 52 393 205 177 172 11 11 172 428 420 51 100 104
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 1,053.2 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 2.09 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 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
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 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0Actual 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:SUNCOR MEADOW CREEK WESTAREA 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 - Page 4 of 6
SUNCOR MEADOW CREEK WESTHEAT 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 36.2 50.0 34.2 34.2 30.8 24.4 24.4 24.4 24.4 7.0 19.1 19.8 19.8 26.1 48.9
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 49,897 49,721 49,721 49,721 1,600 19,205 19,205 32,623 32,621 25,178 7,444 156 21 93 151 2,621 6,572
Mass Density kg/m3 67.5 67.5 55.7 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 2.7Molecular Weight kg/kgmole 17.67 17.67 17.67 17.67 17.67 17.67 17.67 18.11 18.11 18.11 18.11 17.67 17.67 17.67 17.67 17.67 20.12
Mass Heat Capacity kJ/kg‐C 2.88 2.88 2.68 2.64 2.38 2.38 2.32 2.12 2.12 2.12 2.12 2.88 2.15 2.16 2.16 2.25 2.00Thermal Conductivity W/m‐K 0.038 0.038 0.041 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
Combined LiquidMass Flow kg/h 0 0 0 0 0 0 0 2 0 0 0 0 0 0 0 0 13.5
Std Ideal Liq Vol Flow m3/h ‐ ‐ ‐ ‐ ‐ ‐ ‐ 0.0 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ 0Actual Volume Flow m3/h ‐ ‐ ‐ ‐ ‐ ‐ ‐ 0.0 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ 0
Mass Density kg/m3 ‐ ‐ ‐ ‐ ‐ ‐ ‐ 857.2 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ 977Molecular Weight kg/kgmole ‐ ‐ ‐ ‐ ‐ ‐ ‐ 163.36 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ 19.2
Viscosity cP ‐ ‐ ‐ ‐ ‐ ‐ ‐ 33.00 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ 0.7Thermal Conductivity W/m‐K ‐ ‐ ‐ ‐ ‐ ‐ ‐ 0.118 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ 0.6
OilMass Flow kg/h 0 0 0 0 0 0 0 2 0 0 0 0 0 0 0 0 0.9
Std Ideal Liq Vol Flow m3/h ‐ ‐ ‐ ‐ ‐ ‐ ‐ 0.002 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ 0.001Actual Volume Flow m3/h ‐ ‐ ‐ ‐ ‐ ‐ ‐ 0.002 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ 0.001
Mass Density (Note 3) kg/m3 ‐ ‐ ‐ ‐ ‐ ‐ ‐ 857.2 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ 841.9API Gravity (STD) °API ‐ ‐ ‐ ‐ ‐ ‐ ‐ 303.23 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ 254.07Molecular Weight kg/kgmole ‐ ‐ ‐ ‐ ‐ ‐ ‐ 163.36 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ 161.22Viscosity (Note 4) cP ‐ ‐ ‐ ‐ ‐ ‐ ‐ 33.00 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ 12.64
Thermal Conductivity W/m‐K ‐ ‐ ‐ ‐ ‐ ‐ ‐ 0.118 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ 0.115Water
Mass Flow kg/h 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 12.5Std Ideal Liq Vol Flow m3/h 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0Actual Volume Flow m3/h ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ 0.013
Mass Density kg/m3 ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ 989.2Viscosity cP ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ 0.554
Thermal Conductivity W/m‐K ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐ 0.642Vapour
Mass Flow kg/h 49,897 49,721 49,721 49,721 1,600 19,205 19,205 32,621 32,621 25,178 7,444 156 21 93 151 2,621 6,558Std Gas Flow STD_m3/h 66,784 66,548 66,548 66,548 2,141 25,704 25,704 42,592 42,592 32,873 9,719 208 28 124 202 3,508 7,707
Molecular Weight kg/kgmole 17.67 17.67 17.67 17.67 17.67 17.67 17.67 18.11 18.11 18.11 18.11 17.67 17.67 17.67 17.67 17.67 20.12Mass Density kg/m3 67.5 67.5 55.7 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 2.7
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 1.213 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 1.261
Z Factor 0.795 0.795 0.860 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 0.041 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 0.0064 0.0064 0.0064 0.0064 0.0000 0.0000 0.0000 0.0000 0.0000 0.0332H2S 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0003 0.0003 0.0003 0.0003 0.0000 0.0000 0.0000 0.0000 0.0000 0.0014CO2 0.0058 0.0058 0.0058 0.0058 0.0058 0.0058 0.0058 0.0180 0.0180 0.0180 0.0180 0.0058 0.0058 0.0058 0.0058 0.0058 0.0689
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 0.0044 0.0044 0.0044 0.0044 0.0046 0.0046 0.0046 0.0046 0.0046 0.0034
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 0.8994 0.8994 0.8994 0.8994 0.9180 0.9180 0.9180 0.9180 0.9180 0.8218Ethane 0.0510 0.0510 0.0510 0.0510 0.0510 0.0510 0.0510 0.0488 0.0488 0.0488 0.0488 0.0510 0.0510 0.0510 0.0510 0.0510 0.0397
Propane 0.0142 0.0142 0.0142 0.0142 0.0142 0.0142 0.0142 0.0140 0.0140 0.0140 0.0140 0.0142 0.0142 0.0142 0.0142 0.0142 0.0130C4+ 0.0063 0.0063 0.0063 0.0063 0.0063 0.0063 0.0063 0.0086 0.0086 0.0086 0.0086 0.0063 0.0063 0.0063 0.0063 0.0063 0.0185
NOTES:SUNCOR MEADOW CREEK WESTAREA 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 - Page 5 of 6
SUNCOR MEADOW CREEK WESTHEAT 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:• Diluent operating and design conditions are based on Battery Limti Table (SC850‐L‐9000‐1 Rev 1B). SUNCOR MEADOW CREEK WEST• Trim diluent flow rate is based on meeting 350 cSt dilbit viscosity at 7.5 °C pipeline winter reference temperature. AREA 4000 ‐ HC TANK FARM
HEAT AND MATERIAL BALANCE
PROJECT # DRAWING NUMBER REVISION
40,000 BPSD
Stream Number
Stream Name
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To
Overall
Overall Composition Mole Fraction
Area 4000 HMB - Page 6 of 6