APPENDIX 8 PROCESS FLOW DIAGRAMS AND HEAT AND … · 2017. 11. 8. · HEAT AND MATERIAL BALANCE PROJECT #DRAWING NUMBER REVISION 40,000 BPSD Stream Number To Overall Composition Mole

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


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


AREA 2000/3000 ‐ OIL REMOVAL, WATER TREATMENTHEAT AND MATERIAL BALANCE



40,000 BPSD

Overall

Stream Number

Stream Name

From

To



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


AREA 5000 & 5700 ‐ BFW & STEAM GENERATIONAREA 7000 & 9000 ‐ DISPOSAL & RAW WATER SYSTEMS

HEAT AND MATERIAL BALANCE


Overall

Stream Number

Stream Name

From

To

40,000 BPSD

Area 5000-5700 HMB - Page 3 of 6


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


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


Produced Gas Condenser


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



40,000 BPSD

Overall

Stream Number

Stream Name

From

To



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


40,000 BPSD


Overall

Stream Number

Stream Name

From

To



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


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APPENDIX 8 PROCESS FLOW DIAGRAMS AND HEAT AND … · 2017. 11. 8. · HEAT AND MATERIAL BALANCE PROJECT #DRAWING NUMBER REVISION 40,000 BPSD Stream Number To Overall Composition Mole