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Phong Hamaca Oil Models SRK Peneloux CSP Visc/Thermal Cond Table Format PT aqueous Flash at <No format loaded> Pressure 350.0 Temperature 450.00 Number of phases 2 Total Mol% 100.00 Output Format Weight% 100.00 Fixed pressure Molar Volum 15.16 Volume% 100.00 Code for Missing Property Density 23.9736 Z Factor 0.5436 Molecular W 363.51 Rows per block Enthalpy 137.65 49 Internal En 49056.02 Internal En 134.95 Columns per block Entropy 0.26 16 Heat Capaci 0.64 Heat Capaci 0.62 Blocks per fluid Kappa (Cp/C 1.03 1 JT Coefficient Velocity of Sound Number of fluids Viscosity 1 Thermal Conductivity Interfacial Tension Begin Properties Phong Hamaca Oil Pressure psia 350.0 Temperature Mol% Tot Mol% Vap Mol% Liq °F 120.00 100.00 21.89 78.11 160.00 100.00 23.03 76.97 210.00 100.00 24.02 75.98 250.00 100.00 24.59 75.41 290.00 100.00 25.03 74.97 320.00 100.00 25.30 74.70 450.00 100.00 26.20 73.80

Phong Tran - Summer Research Internship Excel

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Page 1: Phong Tran - Summer Research Internship Excel

Phong Hamaca OilModelsSRK PenelouxCSP Visc/Thermal Cond

Table Format PT aqueous Flash at <No format loaded> Pressure 350.0 psia

Temperatur 450.00 °FNumber of phases

2 Total VaporMol% 100.00 26.20

Output Format Weight% 100.00 1.48Fixed pressure Molar Volum 15.16 27.86

Volume% 100.00 48.13Code for Missing Property Density 23.9736 0.7355

Z Factor 0.5436 0.9988Molecular We 363.51 20.49

Rows per block Enthalpy 137.65 222.0749 Internal Ener 49056.02 2745.73

Internal Ener 134.95 134.01Columns per block Entropy 0.26 0.06

16 Heat Capacity 0.64 0.64Heat Capacity 0.62 0.54

Blocks per fluid Kappa (Cp/Cv 1.03 1.201 JT Coefficient 0.0172

Velocity of Sound 1623.78Number of fluids Viscosity 0.0180

1 Thermal Conductivity 0.04Interfacial Tension 9.60

Begin Properties

Phong Hamaca Oil

Pressurepsia

350.0TemperatureMol% Tot Mol% Vap Mol% LiqWeight% Tot

°F120.00 100.00 21.89 78.11 100.00160.00 100.00 23.03 76.97 100.00210.00 100.00 24.02 75.98 100.00250.00 100.00 24.59 75.41 100.00290.00 100.00 25.03 74.97 100.00320.00 100.00 25.30 74.70 100.00450.00 100.00 26.20 73.80 100.00

Original Simulated

Page 2: Phong Tran - Summer Research Internship Excel

120.00 25000 28854.109160.00 6430 5802.690210.00 945 933.856250.00 245 248.457290.00 79 73.945320.00 35 31.754450.00 3 1.597

100 150 200 250 300 350 400 450 5001

10

100

1000

10000

100000

Real ViscositySimulated Viscosity

Temperature, oF

Visc

osity

, cp

Page 3: Phong Tran - Summer Research Internship Excel

Composition (mol%) at Pressure 350.0 psia

Temperature 450.00 °F

Total Vapor

N2 0.030 0.101CO2 1.920 5.670C1 29.040 90.788C2 0.290 0.774

Liquid C3 0.150 0.33673.80 iC4 0.070 0.13398.52 nC4 0.120 0.21310.66 ft³/lb-mol iC5 0.080 0.11551.87 nC5 0.080 0.108

45.5397 lb/ft³ C6 0.310 0.3070.3820 C7 0.720 0.564485.28 C8 0.110 0.067136.39 BTU/lb C9 0.060 0.026

65495.27 BTU/lb-mol C10-C22 18.680 0.783134.97 BTU/lb C23-C31 10.795 0.014

0.26 BTU/lb °F C32-C39 8.350 0.0010.64 BTU/lb °F C40-C46 6.462 0.0000.62 BTU/lb °F C47-C53 5.764 0.0001.03 C54-C60 5.141 0.000

-0.0047 °F/psi C61-C67 4.586 0.0002506.38 ft/s C68-C74 4.090 0.000

1.4565 cP C75-C80 3.152 0.0000.06 BTU/(hr ft ºF)9.60 dyn/cm C10+ 67.020 0.797

C10+ mol wgt 531.886 219.348

Weight% VapWeight% LiqVolume% TotVolume% VapVolume% LiqDensity Totlb/ft³

1.05 98.95 100.00 33.77 66.23 32.57581.12 98.88 100.00 36.51 63.49 31.07191.18 98.82 100.00 39.34 60.66 29.47341.22 98.78 100.00 41.25 58.75 28.35611.26 98.74 100.00 42.93 57.07 27.34611.28 98.72 100.00 44.06 55.94 26.64451.48 98.52 100.00 48.13 51.87 23.9736

Page 4: Phong Tran - Summer Research Internship Excel

100 150 200 250 300 350 400 450 5001

10

100

1000

10000

100000

Real ViscositySimulated Viscosity

Temperature, oF

Visc

osity

, cp

Page 5: Phong Tran - Summer Research Internship Excel

Liquid

0.005

0.5897.1210.1180.0840.0480.0870.0680.0700.3110.7750.1250.072

25.03314.62211.313

8.7567.8106.9666.2145.5424.271

90.528532.863

Density VapDensity LiqViscosity VapViscosity LiqSurf Ten V/Llb/ft³ lb/ft³ cP cP dyn/cm

1.0172 48.6655 0.0127 28849.1325 12.0710.9520 48.3943 0.0134 5801.9443 11.9050.8836 48.0149 0.0143 933.7786 11.6390.8379 47.6793 0.0149 248.4439 11.3840.7996 47.3147 0.0156 73.9431 11.0940.7759 47.0215 0.0161 31.7564 10.8550.7355 45.5397 0.0180 1.5967 9.604

Page 6: Phong Tran - Summer Research Internship Excel

Phong Hamaca + 0.3 H2OModelsSRK PenelouxCSP Visc/Thermal Cond

Table Format<No format loaded>

Number of phases3

Output FormatFixed pressure

Code for Missing Property

Rows per block49

Columns per block19

Blocks per fluid1

Number of fluids1

Begin Properties

Phong Hamaca + 0.3 H2O

Pressurepsia

1200.0TemperatureMol% Tot Mol% VapMol% Liq Mol% AqWeight% TotWeight% Vap

°F120.00 100.00 76.97 23.03 100.00160.00 100.00 0.62 76.47 22.91 100.00 0.04210.00 100.00 3.43 74.01 22.55 100.00 0.21250.00 100.00 5.23 72.78 21.99 100.00 0.32290.00 100.00 6.94 72.05 21.01 100.00 0.43320.00 100.00 8.38 71.76 19.86 100.00 0.53450.00 100.00 24.43 72.37 3.19 100.00 1.64

Page 7: Phong Tran - Summer Research Internship Excel

Phong Hamaca + 0.3 H2OModelsSRK PenelouxCSP Visc/Thermal Cond

Weight% LiqWeight% AqVolume% TotVolume% VapVolume% LiqVolume% Aq

98.54 1.46 100.00 98.84 1.1698.51 1.46 100.00 0.54 98.29 1.1798.36 1.43 100.00 3.19 95.66 1.1598.28 1.40 100.00 5.07 93.81 1.1398.23 1.33 100.00 6.96 91.96 1.0898.21 1.26 100.00 8.54 90.43 1.0298.16 0.20 100.00 22.62 77.23 0.16

Page 8: Phong Tran - Summer Research Internship Excel

Viscosity VapViscosity LiqViscosity AqSurf Ten V/L Surf Ten V/A Surf Ten L/AcP cP cP dyn/cm dyn/cm dyn/cm

572.7627 0.5597 40.2620.0146 174.8587 0.4017 7.813 55.372 37.9360.0153 51.8891 0.2892 7.962 49.755 34.5080.0159 21.3839 0.2333 8.006 46.691 31.7930.0164 9.5158 0.1944 8.003 45.113 29.1180.0168 5.4506 0.1725 7.979 45.011 27.1190.0179 1.4011 0.1163 7.783 54.741 14.731

Page 9: Phong Tran - Summer Research Internship Excel

Phong Hamaca + 0.3 C3 + H2OModelsSRK PenelouxCSP Visc/Thermal Cond

Table Format PT aqueous Flash at <No format loaded> Pressure 1200.0

Temperature 450.00Number of phases

3 TotalMol% 100.00

Output Format Weight% 100.00Fixed pressure Molar Volume 7.96

Volume% 100.00Code for Missing Property Density 36.1109

Z Factor 0.9787Molecular Weight 287.51

Rows per block Enthalpy 139.6749 Internal Energy 38389.11

Internal Energy (Mass) 133.52Columns per block Entropy 0.25

19 Heat Capacity (Cp) 0.64Heat Capacity (Cv) 0.62

Blocks per fluid Kappa (Cp/Cv) 1.041 JT Coefficient

Velocity of SoundNumber of fluids Viscosity

1 Thermal ConductivityInterfacial Tension

Begin Properties

Phong Hamaca + 0.3 C3 + H2O

Pressurepsia

1200.0TemperatureMol% Tot Mol% Vap Mol% Liq Mol% Aq

°F120.00 100.00 91.32 8.68160.00 100.00 91.47 8.53210.00 100.00 1.50 90.38 8.12250.00 100.00 4.67 87.88 7.45290.00 100.00 7.84 85.89 6.27320.00 100.00 10.51 84.65 4.84450.00 100.00 19.88 80.12

Page 10: Phong Tran - Summer Research Internship Excel

Composition (mol%) at Pressure

Temperature

H2Opsia N2°F CO2

C1Vapor Liquid C219.88 80.12 C3

1.69 98.31 iC47.78 8.01 ft³/lb-mol nC4

19.43 80.57 iC53.1396 44.0599 lb/ft³ nC50.9563 0.9842 C6

24.43 352.79 C7194.09 138.74 BTU/lb C8

3013.22 47166.72 BTU/lb-mol C9123.36 133.70 BTU/lb C10-C22

0.03 0.26 BTU/lb °F C23-C310.67 0.64 BTU/lb °F C32-C390.54 0.62 BTU/lb °F C40-C461.23 1.04 C47-C53

0.0255 -0.0045 °F/psi C54-C601454.23 2350.51 ft/s C61-C67

0.0182 1.5310 cP C68-C740.03 0.17 BTU/(hr ft ºF) C75-C806.47 6.47 dyn/cm

C10+C10+ mol wgt

Weight% TotWeight% VapWeight% LiqWeight% Aq Volume% Tot

100.00 99.46 0.54 100.00100.00 99.47 0.53 100.00100.00 0.11 99.39 0.51 100.00100.00 0.34 99.19 0.47 100.00100.00 0.59 99.01 0.39 100.00100.00 0.81 98.88 0.30 100.00100.00 1.69 98.31 100.00

Page 11: Phong Tran - Summer Research Internship Excel

Composition (mol%) at 1200.0 psia Pressure 1200.0

450.00 °F Temperature 160.00

Total Vapor Liquid Total

8.769 18.968 6.239 H2O 8.769

0.023 0.071 0.011 N2 0.0231.477 3.317 1.020 CO2 1.477

22.338 56.458 13.873 C1 22.3380.223 0.407 0.177 C2 0.223

14.423 19.613 13.135 C3 14.4230.054 0.059 0.053 iC4 0.0540.092 0.092 0.092 nC4 0.0920.062 0.047 0.065 iC5 0.0620.062 0.045 0.066 nC5 0.0620.238 0.124 0.267 C6 0.2380.554 0.230 0.634 C7 0.5540.085 0.028 0.099 C8 0.0850.046 0.011 0.055 C9 0.046

14.369 0.510 17.808 C10-C22 14.3698.304 0.017 10.360 C23-C31 8.3046.423 0.001 8.016 C32-C39 6.4234.971 0.000 6.204 C40-C46 4.9714.434 0.000 5.534 C47-C53 4.4343.955 0.000 4.936 C54-C60 3.9553.527 0.000 4.403 C61-C67 3.5273.146 0.000 3.927 C68-C74 3.1462.425 0.000 3.026 C75-C80 2.425

51.554 0.529 64.214 C10+ 51.554

531.886 222.295 532.519 C10+ mol wgt 531.886

Volume% VapVolume% LiqVolume% AqViscosity VapViscosity LiqViscosity AqcP cP cP

99.57 0.43 307.5776 0.559799.57 0.43 100.7295 0.4017

1.33 98.26 0.41 0.0154 31.0797 0.28924.27 95.36 0.37 0.0159 14.1276 0.23337.34 92.34 0.31 0.0164 6.8217 0.19449.93 89.83 0.24 0.0167 4.1311 0.1725

19.43 80.57 0.0182 1.5310

Page 12: Phong Tran - Summer Research Internship Excel

Composition (mol%) at Composition (mol%) at psia Pressure 1200.0 psia

°F Temperat 210.00 °F

Liquid Aqueous Total Vapor LiquidAqueous

0.275 99.865 H2O 8.769 1.429 0.707 99.868

0.025 0.000 N2 0.023 0.170 0.023 0.0001.610 0.046 CO2 1.477 3.372 1.574 0.043

24.413 0.085 C1 22.338 83.608 23.320 0.0840.244 0.000 C2 0.223 0.332 0.241 0.000

15.768 0.004 C3 14.423 10.931 15.776 0.0050.059 0.000 iC4 0.054 0.026 0.059 0.0000.101 0.000 nC4 0.092 0.036 0.102 0.0000.067 0.000 iC5 0.062 0.015 0.068 0.0000.067 0.000 nC5 0.062 0.013 0.068 0.0000.261 0.000 C6 0.238 0.026 0.263 0.0000.605 0.000 C7 0.554 0.031 0.612 0.0000.093 0.000 C8 0.085 0.003 0.094 0.0000.050 0.000 C9 0.046 0.001 0.051 0.000

15.709 0.000 C10-C22 14.369 0.009 15.899 0.0009.078 0.000 C23-C31 8.304 0.000 9.188 0.0007.022 0.000 C32-C39 6.423 0.000 7.107 0.0005.435 0.000 C40-C46 4.971 0.000 5.500 0.0004.847 0.000 C47-C53 4.434 0.000 4.906 0.0004.324 0.000 C54-C60 3.955 0.000 4.376 0.0003.856 0.000 C61-C67 3.527 0.000 3.903 0.0003.440 0.000 C68-C74 3.146 0.000 3.481 0.0002.651 0.000 C75-C80 2.425 0.000 2.683 0.000

56.361 0.000 C10+ 51.554 0.009 57.042 0.000

531.886 216.479 C10+ mol 531.886 217.133 531.887 216.479

Surf Ten V/L Surf Ten V/A Surf Ten L/Adyn/cm dyn/cm dyn/cm

38.30334.822

7.114 54.614 31.2407.089 51.966 29.0837.040 50.561 26.9716.999 50.417 25.3996.472

Page 13: Phong Tran - Summer Research Internship Excel

Phong Hamaca + 0.3 C4 + H2OModelsSRK PenelouxCSP Visc/Thermal Cond

Table Format PT aqueous Flash at <No format loaded> Pressure 1200.0

Temperature 450.00Number of phases

3 Total

Mol% 100.00

Output Format Weight% 100.00Fixed pressure Molar Volume 7.77

Volume% 100.00

Code for Missing Property Density 37.2416Z Factor 0.9556Molecular Weight 289.52

Rows per block Enthalpy 139.1749 Internal Energy 38565.81

Internal Energy (Mass) 133.21Columns per block Entropy 0.25

19 Heat Capacity (Cp) 0.64Heat Capacity (Cv) 0.62

Blocks per fluid Kappa (Cp/Cv) 1.041 JT Coefficient

Velocity of SoundNumber of fluids Viscosity

1 Thermal ConductivityInterfacial Tension

Begin Properties

Phong Hamaca + 0.3 C4 + H2O

Pressurepsia

1200.0TemperatureMol% Tot Mol% Vap Mol% Liq Mol% Aq

°F120.00 100.00 91.32 8.68160.00 100.00 91.47 8.53210.00 100.00 91.86 8.14250.00 100.00 2.10 90.39 7.50290.00 100.00 4.85 88.77 6.38320.00 100.00 7.19 87.77 5.04450.00 100.00 16.38 83.62

Page 14: Phong Tran - Summer Research Internship Excel

Composition (mol%) at Pressure

Temperature

H2Opsia N2°F CO2

C1Vapor Liquid C216.38 83.62 C3

1.41 98.59 iC47.72 7.79 ft³/lb-mol nC4

16.26 83.74 iC53.2397 43.8455 lb/ft³ nC50.9485 0.9570 C6

25.00 341.35 C7193.14 138.39 BTU/lb C8

3115.05 45512.17 BTU/lb-mol C9124.60 133.33 BTU/lb C10-C22

0.03 0.26 BTU/lb °F C23-C310.67 0.64 BTU/lb °F C32-C390.54 0.62 BTU/lb °F C40-C461.23 1.04 C47-C53

0.0268 -0.0044 °F/psi C54-C601426.31 2309.66 ft/s C61-C67

0.0183 1.4831 cP C68-C740.03 0.17 BTU/(hr ft ºF) C75-C806.35 6.35 dyn/cm

C10+C10+ mol wgt

Weight% TotWeight% VapWeight% LiqWeight% Aq Volume% Tot

100.00 99.46 0.54 100.00100.00 99.47 0.53 100.00100.00 99.49 0.51 100.00100.00 0.15 99.39 0.47 100.00100.00 0.35 99.25 0.40 100.00100.00 0.54 99.14 0.31 100.00100.00 1.41 98.59 100.00

Page 15: Phong Tran - Summer Research Internship Excel

Composition (mol%) at 1200.0 psia Pressure 1200.0

450.00 °F Temperature 250.00

Total Vapor Liquid Total

8.769 20.197 6.530 H2O 8.769

0.023 0.078 0.012 N2 0.0231.477 3.486 1.083 CO2 1.477

22.338 60.174 14.925 C1 22.3380.223 0.420 0.184 C2 0.223

0.115 0.159 0.107 C3 0.115

0.054 0.059 0.053 iC4 0.05414.400 14.463 14.388 nC4 14.400

0.062 0.047 0.064 iC5 0.062

0.062 0.045 0.065 nC5 0.062

0.238 0.124 0.261 C6 0.2380.554 0.221 0.619 C7 0.5540.085 0.026 0.096 C8 0.0850.046 0.011 0.053 C9 0.046

14.369 0.473 17.092 C10-C22 14.3698.304 0.016 9.928 C23-C31 8.3046.423 0.001 7.681 C32-C39 6.4234.971 0.000 5.945 C40-C46 4.9714.434 0.000 5.303 C47-C53 4.4343.955 0.000 4.730 C54-C60 3.9553.527 0.000 4.219 C61-C67 3.5273.146 0.000 3.763 C68-C74 3.1462.425 0.000 2.900 C75-C80 2.425

51.554 0.490 61.560 C10+ 51.554

531.886 222.184 532.369 C10+ mol wgt 531.886

Volume% VapVolume% LiqVolume% AqViscosity VapViscosity LiqViscosity AqcP cP cP

99.58 0.42 314.7047 0.559799.58 0.42 102.6220 0.401799.59 0.41 30.2883 0.2892

1.96 97.66 0.38 0.0159 13.4339 0.23334.64 95.03 0.32 0.0164 6.4359 0.19446.95 92.79 0.25 0.0168 3.8815 0.1725

16.26 83.74 0.0183 1.4831

Page 16: Phong Tran - Summer Research Internship Excel

Composition (mol%) at Composition (mol%) at psia Pressure 1200.0 psia

°F Temperat 210.00 °F

Vapor Liquid Aqueous Total LiquidAqueous

3.105 1.338 99.865 H2O 8.769 0.699 99.867

0.162 0.022 0.000 N2 0.023 0.025 0.0003.695 1.544 0.043 CO2 1.477 1.604 0.044

85.457 22.719 0.090 C1 22.338 24.310 0.0870.370 0.238 0.000 C2 0.223 0.243 0.000

0.103 0.125 0.000 C3 0.115 0.126 0.000

0.031 0.059 0.000 iC4 0.054 0.059 0.0006.936 15.769 0.002 nC4 14.400 15.676 0.0020.019 0.068 0.000 iC5 0.062 0.067 0.000

0.016 0.068 0.000 nC5 0.062 0.067 0.000

0.036 0.263 0.000 C6 0.238 0.260 0.0000.046 0.612 0.000 C7 0.554 0.603 0.0000.005 0.093 0.000 C8 0.085 0.092 0.0000.002 0.051 0.000 C9 0.046 0.050 0.0000.019 15.896 0.000 C10-C22 14.369 15.642 0.0000.000 9.186 0.000 C23-C31 8.304 9.039 0.0000.000 7.105 0.000 C32-C39 6.423 6.992 0.0000.000 5.499 0.000 C40-C46 4.971 5.411 0.0000.000 4.905 0.000 C47-C53 4.434 4.827 0.0000.000 4.375 0.000 C54-C60 3.955 4.305 0.0000.000 3.902 0.000 C61-C67 3.527 3.840 0.0000.000 3.481 0.000 C68-C74 3.146 3.425 0.0000.000 2.682 0.000 C75-C80 2.425 2.640 0.000

0.019 57.031 0.000 C10+ 51.554 56.121 0.000

217.428 531.888 216.479 C10+ mol 531.886 531.886 216.479

Surf Ten V/L Surf Ten V/A Surf Ten L/Adyn/cm dyn/cm dyn/cm

38.78535.38831.370

7.231 50.302 28.9807.125 49.203 26.8217.034 49.363 25.2356.347

Page 17: Phong Tran - Summer Research Internship Excel

Vapor Liquid210 F 15.676250 F 6.936 15.769

450 F 14.463 14.388

210 F 250 F 450 F0%

10%

20%

30%

40%

50%

60%

70%

80%

90%

100%

Solvent Composition

Vapor Liquid

Page 18: Phong Tran - Summer Research Internship Excel

210 F 250 F 450 F0%

10%

20%

30%

40%

50%

60%

70%

80%

90%

100%

Solvent Composition

Vapor Liquid

Page 19: Phong Tran - Summer Research Internship Excel

Phong Hamaca + 0.3 C6 + H20ModelsSRK PenelouxCSP Visc/Thermal Cond

Table Format PT aqueous Flash at <No format loaded> Pressure 1200.0

Temperature 450.00Number of phases

3 TotalMol% 100.00

Output Format Weight% 100.00Fixed pressure Molar Volume 7.61

Volume% 100.00Code for Missing Property Density 38.5733

Z Factor 0.9352Molecular Weight 293.49

Rows per block Enthalpy 138.1949 Internal Energy 38866.47

Internal Energy (Mass) 132.43Columns per block Entropy 0.25

19 Heat Capacity (Cp) 0.64Heat Capacity (Cv) 0.62

Blocks per fluid Kappa (Cp/Cv) 1.041 JT Coefficient

Velocity of SoundNumber of fluids Viscosity

1 Thermal ConductivityInterfacial Tension

Begin Properties

Phong Hamaca + 0.3 C6 + H20

Pressurepsia

1200.0TemperatureMol% Tot Mol% Vap Mol% Liq Mol% Aq

°F120.00 100.00 91.26 8.74160.00 100.00 91.41 8.59210.00 100.00 91.80 8.20250.00 100.00 0.36 92.04 7.60290.00 100.00 2.58 90.88 6.54320.00 100.00 4.43 90.28 5.29450.00 100.00 12.29 87.71

Page 20: Phong Tran - Summer Research Internship Excel

Composition (mol%) at Pressure

Temperature

H2Opsia N2°F CO2

C1Vapor Liquid C212.29 87.71 C3

1.00 99.00 iC47.74 7.59 ft³/lb-mol nC4

12.50 87.50 iC53.0840 43.6440 lb/ft³ nC50.9517 0.9329 C6

23.88 331.25 C7194.02 137.62 BTU/lb C8

2913.47 43902.09 BTU/lb-mol C9122.01 132.53 BTU/lb C10-C22

0.01 0.25 BTU/lb °F C23-C310.67 0.64 BTU/lb °F C32-C390.54 0.62 BTU/lb °F C40-C461.24 1.04 C47-C53

0.0266 -0.0043 °F/psi C54-C601467.87 2273.12 ft/s C61-C67

0.0184 1.4143 cP C68-C740.03 0.17 BTU/(hr ft ºF) C75-C806.46 6.46 dyn/cm

C10+C10+ mol wgt

Weight% TotWeight% VapWeight% LiqWeight% Aq Volume% Tot

100.00 99.46 0.54 100.00100.00 99.47 0.53 100.00100.00 99.50 0.50 100.00100.00 0.02 99.51 0.47 100.00100.00 0.17 99.43 0.40 100.00100.00 0.31 99.37 0.32 100.00100.00 1.00 99.00 100.00

Page 21: Phong Tran - Summer Research Internship Excel

1200.0 psia

450.00 °F

Total Vapor Liquid

8.832 21.946 6.995

0.023 0.088 0.0141.477 3.731 1.161

22.338 65.528 16.2890.223 0.436 0.1930.115 0.160 0.1090.054 0.059 0.0530.092 0.091 0.0920.062 0.046 0.0640.062 0.043 0.064

14.483 7.202 15.5030.554 0.207 0.6020.085 0.025 0.0930.046 0.010 0.051

14.369 0.413 16.3248.304 0.013 9.4656.423 0.001 7.3224.971 0.000 5.6674.434 0.000 5.0553.955 0.000 4.5093.527 0.000 4.0223.146 0.000 3.5872.425 0.000 2.764

51.554 0.427 58.715531.886 221.841 532.202

Volume% VapVolume% LiqVolume% AqViscosity VapViscosity LiqViscosity AqcP cP cP

99.58 0.42 330.7435 0.559799.58 0.42 106.8553 0.401799.59 0.41 31.2788 0.2892

0.35 99.27 0.39 0.0159 13.2529 0.23332.52 97.14 0.33 0.0164 6.2655 0.19444.39 95.34 0.27 0.0168 3.7362 0.1725

12.50 87.50 0.0184 1.4143

Page 22: Phong Tran - Summer Research Internship Excel

Surf Ten V/L Surf Ten V/A Surf Ten L/Adyn/cm dyn/cm dyn/cm

39.53736.24332.112

7.572 47.965 29.2687.448 46.782 27.0057.330 46.981 25.3536.461

Page 23: Phong Tran - Summer Research Internship Excel

Phong Hamaca + 0.3 C7 + H2OModelsSRK PenelouxCSP Visc/Thermal Cond

Table Format PT aqueous Flash at <No format loaded> Pressure 1200.0

Temperature 450.00Number of phases

3 TotalMol% 100.00

Output Format Weight% 100.00Fixed pressure Molar Volume 7.57

Volume% 100.00Code for Missing Property Density 38.9827

Z Factor 0.9300Molecular Weight 294.94

Rows per block Enthalpy 136.7349 Internal Energy 38646.50

Internal Energy (Mass) 131.03Columns per block Entropy 0.25

19 Heat Capacity (Cp) 0.64Heat Capacity (Cv) 0.62

Blocks per fluid Kappa (Cp/Cv) 1.041 JT Coefficient

Velocity of SoundNumber of fluids Viscosity

1 Thermal ConductivityInterfacial Tension

Begin Properties

Phong Hamaca + 0.3 C7 + H2O

Pressurepsia

1200.0TemperatureMol% Tot Mol% Vap Mol% Liq Mol% Aq

°F120.00 100.00 91.32 8.68160.00 100.00 91.46 8.54210.00 100.00 91.85 8.15250.00 100.00 0.31 92.13 7.55290.00 100.00 2.38 91.12 6.50320.00 100.00 4.09 90.64 5.26450.00 100.00 11.32 88.68

Page 24: Phong Tran - Summer Research Internship Excel

Composition (mol%) at Pressure

Temperature

H2Opsia N2°F CO2

C1Vapor Liquid C211.32 88.68 C3

0.89 99.11 iC47.79 7.54 ft³/lb-mol nC4

11.66 88.34 iC52.9737 43.7339 lb/ft³ nC50.9576 0.9265 C6

23.17 329.63 C7193.26 136.22 BTU/lb C8

2747.37 43228.94 BTU/lb-mol C9118.58 131.14 BTU/lb C10-C22

0.00 0.25 BTU/lb °F C23-C310.65 0.64 BTU/lb °F C32-C390.53 0.62 BTU/lb °F C40-C461.24 1.04 C47-C53

0.0248 -0.0043 °F/psi C54-C601499.37 2275.34 ft/s C61-C67

0.0186 1.4190 cP C68-C740.03 0.17 BTU/(hr ft ºF) C75-C806.57 6.57 dyn/cm

C10+C10+ mol wgt

Weight% TotWeight% VapWeight% LiqWeight% Aq Volume% Tot

100.00 99.47 0.53 100.00100.00 99.48 0.52 100.00100.00 99.50 0.50 100.00100.00 0.02 99.52 0.46 100.00100.00 0.15 99.45 0.40 100.00100.00 0.27 99.41 0.32 100.00100.00 0.89 99.11 100.00

Page 25: Phong Tran - Summer Research Internship Excel

1200.0 psia

450.00 °F

Total Vapor Liquid

8.769 21.807 7.105

0.023 0.092 0.0141.477 3.803 1.180

22.338 67.355 16.5920.223 0.444 0.1950.115 0.163 0.1090.054 0.059 0.0530.092 0.092 0.0920.062 0.046 0.0630.062 0.043 0.0640.238 0.118 0.254

14.862 5.519 16.0540.085 0.024 0.0920.046 0.010 0.051

14.369 0.409 16.1518.304 0.013 9.3626.423 0.001 7.2434.971 0.000 5.6064.434 0.000 5.0003.955 0.000 4.4603.527 0.000 3.9783.146 0.000 3.5482.425 0.000 2.734

51.554 0.423 58.081531.886 221.822 532.174

Volume% VapVolume% LiqVolume% AqViscosity VapViscosity LiqViscosity AqcP cP cP

99.58 0.42 335.9459 0.559799.58 0.42 108.2286 0.401799.59 0.41 31.6121 0.2892

0.30 99.32 0.38 0.0159 13.3734 0.23332.34 97.32 0.33 0.0165 6.3145 0.19444.08 95.65 0.27 0.0169 3.7628 0.1725

11.66 88.34 0.0186 1.4190

Page 26: Phong Tran - Summer Research Internship Excel

Surf Ten V/L Surf Ten V/A Surf Ten L/Adyn/cm dyn/cm dyn/cm

39.41536.44232.274

7.717 47.333 29.3917.604 46.040 27.0767.491 46.154 25.3856.573

Page 27: Phong Tran - Summer Research Internship Excel

Table 3 - Viscosity of Hamaca Oil in Different CasesViscosity (cp)

Temp (F) Original H20 (SAGD) (C3 + H2O) (C4 + H2O) (C6 + H2O)120 28849 572.76 307.58 314.70 330.74160 5802 174.86 100.73 102.62 106.86210 934 51.89 31.08 30.29 31.28250 248 21.38 14.13 13.43 13.25290 74 9.52 6.82 6.44 6.27320 32 5.45 4.13 3.88 3.74

450 2 1.40 1.53 1.48 1.41

100 150 200 250 300 350 400 450 5001

10

100

1000

10000

100000Visc. vs Temperature

Original Viscosity

SAGD

C3

C4

C6

C7

Temperature (F)

Visc

osity

(cp)

100 150 200 250 300 350 400 450 5000

100

200

300

400

500

600Visc. vs Temperature

SAGD

C3 + H2O

C4 + H20

C6 + H20

C7 + H20

Temperature (F)

Visc

osity

(cp)

Page 28: Phong Tran - Summer Research Internship Excel

100 150 200 250 300 350 400 450 5000

100

200

300

400

500

600Visc. vs Temperature

SAGD

C3 + H2O

C4 + H20

C6 + H20

C7 + H20

Temperature (F)

Visc

osity

(cp)

100 150 200 250 300 350 400 450 5000

50

100

150

200

250

300

350

400

Visc. vs Temperature

C3

C4

C6

C7

Temperature, F

Visc

osity

, cp

Page 29: Phong Tran - Summer Research Internship Excel

Table 3 - Viscosity of Hamaca Oil in Different CasesViscosity (cp)

(C7 + H2O)335.95108.23

31.6113.37

6.313.76

1.42

100 150 200 250 300 350 400 450 5001

10

100

1000

10000

100000Visc. vs Temperature

Original Viscosity

SAGD

C3

C4

C6

C7

Temperature (F)

Visc

osity

(cp)

100 150 200 250 300 350 400 450 5000

100

200

300

400

500

600Visc. vs Temperature

SAGD

C3 + H2O

C4 + H20

C6 + H20

C7 + H20

Temperature (F)

Visc

osity

(cp)

Page 30: Phong Tran - Summer Research Internship Excel

100 150 200 250 300 350 400 450 5000

100

200

300

400

500

600Visc. vs Temperature

SAGD

C3 + H2O

C4 + H20

C6 + H20

C7 + H20

Temperature (F)

Visc

osity

(cp)

100 150 200 250 300 350 400 450 5000

50

100

150

200

250

300

350

400

Visc. vs Temperature

C3

C4

C6

C7

Temperature, F

Visc

osity

, cp

Page 31: Phong Tran - Summer Research Internship Excel
Page 32: Phong Tran - Summer Research Internship Excel

Interfacial Tension (dyne/cm)Temp (F) Pressure (psi) Original SAGD C3 C4 C6 C7

120 1200 12.071160 1200 11.905 7.813210 1200 11.639 7.962 7.114250 1200 11.384 8.006 7.089 7.231 7.572 7.717290 1200 11.094 8.003 7.040 7.125 7.448 7.604320 1200 10.855 7.979 6.999 7.034 7.330 7.491

450 1200 9.604 7.783 6.472 6.347 6.461 6.573

100 150 200 250 300 350 400 450 5000.000

2.000

4.000

6.000

8.000

10.000

12.000

14.000

Interfacial Tension vs. Temperature

OriginalSAGDC4C6C7C3

Temperature (F)

Inte

rfac

ial T

ensio

n (d

yne/

cm)

Page 33: Phong Tran - Summer Research Internship Excel

100 150 200 250 300 350 400 450 5000.000

2.000

4.000

6.000

8.000

10.000

12.000

14.000

Interfacial Tension vs. Temperature

OriginalSAGDC4C6C7C3

Temperature (F)

Inte

rfac

ial T

ensio

n (d

yne/

cm)

Page 34: Phong Tran - Summer Research Internship Excel

Viscosity at different C6 concentrations, cpTemperature, F 5% 10% 15% 30% Volume percentage

120.00 ### ### ### ###160.00 393.6005 304.0240 ### ###210.00 93.6216 74.9647 61.3182 31.2788250.00 33.9320 28.3077 24.0046 13.2529290.00 13.5934 11.6906 10.2144 6.2655320.00 7.2365 6.3442 5.6353 3.7362

450.00 1.4558 1.4518 1.4456 1.4143

100 150 200 250 300 350 400 450 5000

200

400

600

800

1000

1200

1400

1600

1800

Viscosity Reduction Comparison

5% C6 10% C6 15% C6 30% C6

Temperature (F)

Visc

osity

(cp)

Page 35: Phong Tran - Summer Research Internship Excel

100 150 200 250 300 350 400 450 5000

200

400

600

800

1000

1200

1400

1600

1800

Viscosity Reduction Comparison

5% C6 10% C6 15% C6 30% C6

Temperature (F)

Visc

osity

(cp)

Page 36: Phong Tran - Summer Research Internship Excel

Viscosity at different pressures, cpTemperature, F 350 psia 700 psia 1200 psia

120.00 1507.7590 1074.0944 875.3197160.00 392.8530 305.1227 242.2216210.00 90.4805 75.8222 61.3182250.00 32.3482 28.2327 24.0046290.00 12.9421 11.6296 10.2144320.00 6.9621 6.3635 5.6353

450.00 1.1450 1.3627 1.4456

100 150 200 250 300 350 400 450 5000

200

400

600

800

1000

1200

1400

1600

Viscosity of Hamaca oil at Various Pressure

350 psia700 psia1200 psia

Temperature, F

Visc

osity

, cp

Page 37: Phong Tran - Summer Research Internship Excel

100 150 200 250 300 350 400 450 5000

200

400

600

800

1000

1200

1400

1600

Viscosity of Hamaca oil at Various Pressure

350 psia700 psia1200 psia

Temperature, F

Visc

osity

, cp

Page 38: Phong Tran - Summer Research Internship Excel

Composition (mol%) at Pressure 1200.0 psiaTemperat 450.00 °F

C3 C6 C7Total Vapor Liquid Vapor Liquid Vapor

H2O 8.769 18.968 6.239 21.946 6.995 21.807N2 0.023 0.071 0.011 0.088 0.014 0.092CO2 1.477 3.317 1.020 3.731 1.161 3.803C1 22.338 56.458 13.873 65.528 16.289 67.355C2 0.223 0.407 0.177 0.436 0.193 0.444C3 14.423 19.613 13.135 0.160 0.109 0.163iC4 0.054 0.059 0.053 0.059 0.053 0.059nC4 0.092 0.092 0.092 0.091 0.092 0.092iC5 0.062 0.047 0.065 0.046 0.064 0.046nC5 0.062 0.045 0.066 0.043 0.064 0.043C6 0.238 0.124 0.267 7.202 15.503 0.118C7 0.554 0.230 0.634 0.207 0.602 5.519C8 0.085 0.028 0.099 0.025 0.093 0.024C9 0.046 0.011 0.055 0.010 0.051 0.010C10-C22 14.369 0.510 17.808 0.413 16.324 0.409C23-C31 8.304 0.017 10.360 0.013 9.465 0.013C32-C39 6.423 0.001 8.016 0.001 7.322 0.001C40-C46 4.971 0.000 6.204 0.000 5.667 0.000C47-C53 4.434 0.000 5.534 0.000 5.055 0.000C54-C60 3.955 0.000 4.936 0.000 4.509 0.000C61-C67 3.527 0.000 4.403 0.000 4.022 0.000C68-C74 3.146 0.000 3.927 0.000 3.587 0.000C75-C80 2.425 0.000 3.026 0.000 2.764 0.000

C10+ 51.554 0.529 64.214 0.427 58.715 0.423C10+ mol 531.886 222.295 532.519 221.841 532.202 221.822

C3 C4 C6 C70.000

5.000

10.000

15.000

20.000

25.000

Solvent Composition at 450 oF and 1200 psi

Vapor

Liquid

Solvents

Perc

enta

ge, %

Page 39: Phong Tran - Summer Research Internship Excel

C4Liquid Vapor Liquid7.105 20.197 6.5300.014 0.078 0.0121.180 3.486 1.083 Vapor Liquid

16.592 60.174 14.925 C3 19.613 13.1350.195 0.420 0.184 C4 14.463 14.3880.109 0.159 0.107 C6 7.202 15.5030.053 0.059 0.053 C7 5.519 16.0540.092 14.463 14.3880.063 0.047 0.0640.064 0.045 0.0650.254 0.124 0.261

16.054 0.221 0.6190.092 0.026 0.0960.051 0.011 0.053

16.151 0.473 17.0929.362 0.016 9.9287.243 0.001 7.6815.606 0.000 5.9455.000 0.000 5.3034.460 0.000 4.7303.978 0.000 4.2193.548 0.000 3.7632.734 0.000 2.900

58.081 0.490 61.560532.174 222.184 532.369

C3 C4 C6 C70.000

5.000

10.000

15.000

20.000

25.000

Solvent Composition at 450 oF and 1200 psi

Vapor

Liquid

Solvents

Perc

enta

ge, %

Page 40: Phong Tran - Summer Research Internship Excel

Phong Hamaca + 0.1 H20ModelsSRK PenelouxCSP Visc/Thermal Cond

Table Format PT aqueous Flash at <No format loaded> Pressure 1200.0 psia

Temperatu 450.00 °FNumber of phases

3 Total Vapor LiquidMol% 100.00 19.03 80.97

Output Format Weight% 100.00 1.14 98.86Fixed pressure Molar Volu 8.51 7.76 8.68

Volume% 100.00 17.36 82.64Code for Missing Property Density 37.4285 2.4548 44.7762

Z Factor 1.0458 0.9543 1.0673Molecular 318.45 19.06 388.79

Rows per block Enthalpy 139.78 194.62 139.1549 Internal En 42623.09 1985.33 52171.58

Internal En 133.85 104.17 134.19Columns per block Entropy 0.26 -0.07 0.26

19 Heat Capaci 0.64 0.66 0.64Heat Capaci 0.62 0.51 0.62

Blocks per fluid Kappa (Cp/C 1.04 1.29 1.031 JT Coefficient 0.0283 -0.0046

Velocity of Sound 1677.84 2481.76Number of fluids Viscosity 0.0183 1.4818

1 Thermal Conductivity 0.03 0.17Interfacial Tension 7.56 7.56

Begin Properties

Phong Hamaca + 0.15 H20

Pressurepsia

350.0TemperatureMol% Tot Mol% VapMol% Liq Mol% AqWeight% TotWeight% Vap

°F120.00 100.00 19.14 67.96 12.89 100.00 1.05160.00 100.00 20.36 67.04 12.60 100.00 1.13210.00 100.00 22.01 66.31 11.68 100.00 1.24250.00 100.00 23.99 66.00 10.01 100.00 1.36290.00 100.00 27.48 65.88 6.64 100.00 1.58320.00 100.00 32.28 65.89 1.84 100.00 1.87450.00 100.00 35.24 64.76 100.00 2.25

Phong Hamaca + 0.15 H20

Pressure

Page 41: Phong Tran - Summer Research Internship Excel

psia700.0

TemperatureMol% Tot Mol% VapMol% Liq Mol% AqWeight% TotWeight% Vap°F

120.00 100.00 10.41 76.64 12.95 100.00 0.56160.00 100.00 12.50 74.74 12.76 100.00 0.68210.00 100.00 14.58 73.21 12.22 100.00 0.81250.00 100.00 16.23 72.48 11.30 100.00 0.91290.00 100.00 18.31 72.09 9.60 100.00 1.03320.00 100.00 20.54 71.98 7.48 100.00 1.17450.00 100.00 28.65 71.35 100.00 1.75

Phong Hamaca + 0.15 H20

Pressurepsia

1200.0TemperatureMol% Tot Mol% VapMol% Liq Mol% AqWeight% TotWeight% Vap

°F120.00 100.00 87.03 12.97 100.00160.00 100.00 0.72 86.45 12.83 100.00 0.04210.00 100.00 3.90 83.67 12.43 100.00 0.21250.00 100.00 5.92 82.28 11.79 100.00 0.33290.00 100.00 7.87 81.45 10.69 100.00 0.44320.00 100.00 9.50 81.12 9.38 100.00 0.53450.00 100.00 19.03 80.97 100.00 1.14

Page 42: Phong Tran - Summer Research Internship Excel

Composition (mol%) at Pressure 1200.0 psia

Temperature 450.00 °F

Total Vapor Liquid

H2O 13.043 29.339 9.214N2 0.026 0.083 0.013CO2 1.670 3.798 1.169C1 25.252 65.088 15.892C2 0.252 0.459 0.204C3 0.130 0.174 0.120iC4 0.061 0.065 0.060

ft³/lb-mol nC4 0.104 0.101 0.105iC5 0.070 0.052 0.074

lb/ft³ nC5 0.070 0.048 0.075C6 0.270 0.133 0.302C7 0.626 0.223 0.721

BTU/lb C8 0.096 0.026 0.112BTU/lb-mol C9 0.052 0.010 0.062BTU/lb C10-C22 16.243 0.389 19.969BTU/lb °F C23-C31 9.387 0.010 11.590BTU/lb °F C32-C39 7.261 0.001 8.966BTU/lb °F C40-C46 5.619 0.000 6.940

C47-C53 5.012 0.000 6.190°F/psi C54-C60 4.471 0.000 5.521ft/s C61-C67 3.988 0.000 4.924cP C68-C74 3.557 0.000 4.392BTU/(hr ft ºF) C75-C80 2.741 0.000 3.385dyn/cm

C10+ 58.278 0.400 71.878C10+ mol wgt 531.886 220.954 532.293

Weight% LiqWeight% AqVolume% TotVolume% VapVolume% LiqVolume% Aq

98.22 0.73 100.00 33.75 65.86 0.3998.16 0.71 100.00 36.74 62.88 0.3798.10 0.66 100.00 40.39 59.27 0.3498.07 0.57 100.00 43.78 55.94 0.2898.05 0.38 100.00 48.30 51.53 0.1798.02 0.10 100.00 53.04 46.92 0.0497.75 100.00 58.55 41.45

Page 43: Phong Tran - Summer Research Internship Excel

Weight% LiqWeight% AqVolume% TotVolume% VapVolume% LiqVolume% Aq

98.70 0.73 100.00 11.75 87.73 0.5298.60 0.72 100.00 14.74 84.76 0.5198.50 0.69 100.00 17.98 81.54 0.4898.46 0.64 100.00 20.55 79.01 0.4498.42 0.54 100.00 23.47 76.17 0.3798.41 0.42 100.00 26.18 73.53 0.2898.25 100.00 35.89 64.11

Weight% LiqWeight% AqVolume% TotVolume% VapVolume% LiqVolume% Aq

99.27 0.73 100.00 99.42 0.5899.23 0.73 100.00 0.56 98.86 0.5899.08 0.70 100.00 3.22 96.21 0.5699.01 0.67 100.00 5.11 94.35 0.5498.96 0.60 100.00 7.02 92.49 0.4998.93 0.53 100.00 8.61 90.96 0.4398.86 100.00 17.36 82.64

Page 44: Phong Tran - Summer Research Internship Excel

Viscosity VapViscosity LiqViscosity AqSurf Ten V/L Surf Ten V/A Surf Ten L/AcP cP cP dyn/cm dyn/cm dyn/cm

0.0127 2849.5627 0.5587 12.075 66.776 51.5570.0134 735.0901 0.4003 11.916 61.109 47.0830.0142 158.1271 0.2876 11.674 57.246 41.9210.0147 52.2602 0.2317 11.457 57.621 38.0870.0151 19.1193 0.1929 11.232 62.038 34.4360.0153 9.5737 0.1710 11.064 68.511 31.7460.0172 1.0738 9.793

Page 45: Phong Tran - Summer Research Internship Excel

Viscosity VapViscosity LiqViscosity AqSurf Ten V/L Surf Ten V/A Surf Ten L/AcP cP cP dyn/cm dyn/cm dyn/cm

0.0132 1552.3254 0.5591 10.086 64.144 46.4280.0138 420.4354 0.4009 10.097 58.197 42.8520.0146 98.5336 0.2882 10.029 52.868 38.5350.0152 35.1876 0.2323 9.929 50.665 35.2330.0157 13.9152 0.1935 9.804 50.704 32.0390.0160 7.3881 0.1717 9.700 52.418 29.6690.0176 1.1777 8.826

Viscosity VapViscosity LiqViscosity AqSurf Ten V/L Surf Ten V/A Surf Ten L/AcP cP cP dyn/cm dyn/cm dyn/cm

1076.1268 0.5597 40.2550.0146 294.9084 0.4017 7.813 55.376 37.9350.0153 76.8028 0.2892 7.962 49.759 34.5070.0159 29.1581 0.2333 8.005 46.695 31.7920.0164 12.1273 0.1944 8.002 45.117 29.1180.0168 6.6414 0.1725 7.979 45.014 27.1190.0183 1.4818 7.564

Page 46: Phong Tran - Summer Research Internship Excel

Phong Hamaca + 0.4 C6 + H2OModelsSRK PenelouxCSP Visc/Thermal Cond

Table Format PT aqueous Flash at <No format loaded> Pressure

TemperatureNumber of phases

3Mol%

Output Format Weight%Fixed pressure Molar Volume

Volume%Code for Missing Property Density

Z FactorMolecular Weight

Rows per block Enthalpy49 Internal Energy

Internal Energy (Mass)Columns per block Entropy

19 Heat Capacity (Cp)Heat Capacity (Cv)

Blocks per fluid Kappa (Cp/Cv)1 JT Coefficient

Velocity of SoundNumber of fluids Viscosity

1 Thermal ConductivityInterfacial Tension

Begin Properties

Phong Hamaca + 0.4 C6 + H2O

Pressurepsia

1200.0TemperatureMol% Tot Mol% Vap Mol% Liq

°F120.00 100.00 89.15160.00 100.00 89.30210.00 100.00 89.68250.00 100.00 90.27290.00 100.00 0.95 90.31320.00 100.00 2.78 89.66450.00 100.00 13.20 86.80

Page 47: Phong Tran - Summer Research Internship Excel

1200.0 psia450.00 °F

Total Vapor Liquid100.00 13.20 86.80100.00 1.20 98.80

7.32 7.60 7.28 ft³/lb-mol100.00 13.69 86.31

37.8131 3.3122 43.2864 lb/ft³0.8999 0.9336 0.8947276.82 25.16 315.08137.66 187.80 137.05 BTU/lb

36480.17 3037.75 41564.80 BTU/lb-mol131.78 120.76 131.92 BTU/lb

0.25 0.03 0.25 BTU/lb °F0.65 0.67 0.65 BTU/lb °F0.62 0.54 0.62 BTU/lb °F1.05 1.25 1.04

0.0314 -0.0042 °F/psi1408.44 2211.83 ft/s

0.0183 1.3888 cP0.03 0.17 BTU/(hr ft ºF)6.25 6.25 dyn/cm

Mol% AqWeight% TotWeight% VapWeight% LiqWeight% AqVolume% Tot

10.85 100.00 99.29 0.71 100.0010.70 100.00 99.30 0.70 100.0010.32 100.00 99.33 0.67 100.00

9.73 100.00 99.37 0.63 100.008.75 100.00 0.07 99.36 0.57 100.007.56 100.00 0.21 99.30 0.49 100.00

100.00 1.20 98.80 100.00

Page 48: Phong Tran - Summer Research Internship Excel

Composition (mol%) at Pressure 1200.0 psia

Temperature 450.00 °F

Total Vapor Liquid

H2O 10.935 26.988 8.494N2 0.021 0.079 0.013CO2 1.371 3.394 1.064C1 20.743 59.044 14.920C2 0.207 0.398 0.178C3 0.107 0.147 0.101iC4 0.050 0.055 0.049nC4 0.086 0.085 0.086iC5 0.057 0.043 0.059nC5 0.057 0.041 0.060C6 17.858 9.078 19.193C7 0.514 0.196 0.563C8 0.079 0.023 0.087C9 0.043 0.009 0.048C10-C22 13.343 0.406 15.310C23-C31 7.710 0.013 8.881C32-C39 5.964 0.001 6.871C40-C46 4.616 0.000 5.318C47-C53 4.117 0.000 4.743C54-C60 3.672 0.000 4.231C61-C67 3.275 0.000 3.774C68-C74 2.922 0.000 3.366C75-C80 2.252 0.000 2.594

C10+ 47.871 0.420 55.086C10+ mol wgt 531.886 222.071 532.245

Volume% VapVolume% LiqVolume% AqViscosity VapViscosity LiqcP cP

99.44 0.56 242.898999.44 0.56 82.372299.45 0.55 25.364299.48 0.52 11.0211

0.99 98.54 0.48 0.0164 5.18622.93 96.66 0.41 0.0168 3.1800

13.69 86.31 0.0183 1.3888

Page 49: Phong Tran - Summer Research Internship Excel

Viscosity AqSurf Ten V/L Surf Ten V/A Surf Ten L/AcP dyn/cm dyn/cm dyn/cm

0.5597 39.3780.4017 35.8690.2892 31.8040.2333 28.9310.1944 7.287 47.222 26.4910.1725 7.142 47.503 24.921

6.247

Page 50: Phong Tran - Summer Research Internship Excel

Phong Hamaca + 0.05 H20ModelsSRK PenelouxCSP Visc/Thermal Cond

Table Format PT aqueous Flash at <No format loaded> Pressure 1200.0 psia

Temperatu 450.00 °FNumber of phases

3 Total Vapor LiquidMol% 100.00 12.85 87.15

Output Format Weight% 100.00 0.71 99.29Fixed pressure Molar Volu 8.72 8.06 8.82

Volume% 100.00 11.87 88.13Code for Missing Property Density 39.7783 2.3631 44.8191

Z Factor 1.0724 0.9906 1.0845Molecular 347.06 19.04 395.44

Rows per block Enthalpy 139.86 210.83 139.3649 Internal En 46603.49 2225.47 53149.32

Internal En 134.28 116.86 134.41Columns per block Entropy 0.26 -0.08 0.26

19 Heat Capaci 0.64 0.66 0.64Heat Capaci 0.62 0.53 0.62

Blocks per fluid Kappa (Cp/C 1.03 1.25 1.031 JT Coefficient 0.0163 -0.0047

Velocity of Sound 1715.71 2502.85Number of fluids Viscosity 0.0186 1.4834

1 Thermal Conductivity 0.03 0.14Interfacial Tension 7.29 7.29

Begin Properties

Phong Hamaca + 0.05 H20

Pressurepsia

350.0TemperatureMol% Tot Mol% VapMol% Liq Mol% AqWeight% TotWeight% Vap

°F120.00 100.00 20.97 74.44 4.59 100.00 1.06160.00 100.00 22.31 73.42 4.27 100.00 1.14210.00 100.00 24.11 72.63 3.26 100.00 1.24250.00 100.00 26.28 72.28 1.44 100.00 1.37290.00 100.00 28.06 71.94 100.00 1.48320.00 100.00 28.37 71.63 100.00 1.51450.00 100.00 29.42 70.58 100.00 1.73

Phong Hamaca + 0.05 H20

Pressure

Page 51: Phong Tran - Summer Research Internship Excel

psia700.0

TemperatureMol% Tot Mol% VapMol% Liq Mol% AqWeight% TotWeight% Vap°F

120.00 100.00 11.42 83.94 4.65 100.00 0.57160.00 100.00 13.70 81.85 4.44 100.00 0.69210.00 100.00 15.97 80.18 3.85 100.00 0.81250.00 100.00 17.78 79.38 2.84 100.00 0.91290.00 100.00 20.07 78.95 0.98 100.00 1.04320.00 100.00 21.38 78.62 100.00 1.12450.00 100.00 22.74 77.26 100.00 1.28

Phong Hamaca + 0.05 H20

Pressurepsia

1200.0TemperatureMol% Tot Mol% VapMol% Liq Mol% AqWeight% TotWeight% Vap

°F120.00 100.00 95.33 4.67 100.00160.00 100.00 0.80 94.68 4.51 100.00 0.04210.00 100.00 4.28 91.64 4.08 100.00 0.21250.00 100.00 6.50 90.12 3.38 100.00 0.33290.00 100.00 8.63 89.20 2.17 100.00 0.44320.00 100.00 10.42 88.85 0.74 100.00 0.54450.00 100.00 12.85 87.15 100.00 0.71

Page 52: Phong Tran - Summer Research Internship Excel

Composition (mol%) at Pressure 1200.0 psia

Temperature 450.00 °F

Total Vapor Liquid

H2O 4.762 11.480 3.771N2 0.029 0.111 0.016CO2 1.829 4.612 1.418C1 27.657 81.927 19.652C2 0.276 0.542 0.237C3 0.143 0.198 0.135iC4 0.067 0.071 0.066

ft³/lb-mol nC4 0.114 0.110 0.115iC5 0.076 0.055 0.079

lb/ft³ nC5 0.076 0.051 0.080C6 0.295 0.137 0.319C7 0.686 0.239 0.752

BTU/lb C8 0.105 0.028 0.116BTU/lb-mol C9 0.057 0.011 0.064BTU/lb C10-C22 17.790 0.417 20.353BTU/lb °F C23-C31 10.281 0.011 11.795BTU/lb °F C32-C39 7.952 0.001 9.125BTU/lb °F C40-C46 6.155 0.000 7.062

C47-C53 5.490 0.000 6.299°F/psi C54-C60 4.896 0.000 5.619ft/s C61-C67 4.367 0.000 5.012cP C68-C74 3.895 0.000 4.470BTU/(hr ft ºF) C75-C80 3.002 0.000 3.445dyn/cm

C10+ 63.829 0.429 73.180C10+ mol wgt 531.886 221.028 532.155

Weight% LiqWeight% AqVolume% TotVolume% VapVolume% LiqVolume% Aq

98.70 0.24 100.00 33.85 66.02 0.1398.64 0.22 100.00 36.84 63.04 0.1298.59 0.17 100.00 40.50 59.42 0.0998.56 0.07 100.00 43.89 56.07 0.0498.52 100.00 46.74 53.2698.49 100.00 47.92 52.0898.27 100.00 52.12 47.88

Page 53: Phong Tran - Summer Research Internship Excel

Weight% LiqWeight% AqVolume% TotVolume% VapVolume% LiqVolume% Aq

99.19 0.24 100.00 11.80 88.03 0.1799.08 0.23 100.00 14.80 85.04 0.1698.99 0.20 100.00 18.05 81.81 0.1498.94 0.15 100.00 20.63 79.27 0.1098.91 0.05 100.00 23.55 76.41 0.0398.88 100.00 25.38 74.6298.72 100.00 29.32 70.68

Weight% LiqWeight% AqVolume% TotVolume% VapVolume% LiqVolume% Aq

99.76 0.24 100.00 99.81 0.1999.73 0.23 100.00 0.57 99.24 0.1999.57 0.21 100.00 3.24 96.59 0.1799.50 0.18 100.00 5.14 94.72 0.1499.45 0.11 100.00 7.06 92.85 0.0999.42 0.04 100.00 8.66 91.31 0.0399.29 100.00 11.87 88.13

Page 54: Phong Tran - Summer Research Internship Excel

Viscosity VapViscosity LiqViscosity AqSurf Ten V/L Surf Ten V/A Surf Ten L/AcP cP cP dyn/cm dyn/cm dyn/cm

0.0127 3776.2622 0.5587 12.075 66.780 51.5560.0134 931.8868 0.4003 11.916 61.112 47.0830.0142 190.8456 0.2876 11.674 57.248 41.9210.0147 60.9331 0.2317 11.457 57.623 38.0860.0152 21.9728 11.1930.0157 10.9851 10.9500.0177 1.1337 9.681

Page 55: Phong Tran - Summer Research Internship Excel

Viscosity VapViscosity LiqViscosity AqSurf Ten V/L Surf Ten V/A Surf Ten L/AcP cP cP dyn/cm dyn/cm dyn/cm

0.0132 2168.0508 0.5591 10.085 64.147 46.4270.0138 546.7265 0.4009 10.097 58.200 42.8520.0146 119.8496 0.2882 10.029 52.871 38.5350.0152 41.0847 0.2323 9.929 50.667 35.2330.0157 15.7065 0.1935 9.804 50.706 32.0390.0161 8.1873 9.6620.0181 1.2446 8.635

Viscosity VapViscosity LiqViscosity AqSurf Ten V/L Surf Ten V/A Surf Ten L/AcP cP cP dyn/cm dyn/cm dyn/cm

1638.2316 0.5597 40.2510.0146 417.5138 0.4017 7.813 55.379 37.9340.0153 99.5781 0.2892 7.962 49.761 34.5070.0159 35.7641 0.2333 8.005 46.697 31.7920.0164 14.2066 0.1944 8.002 45.119 29.1180.0168 7.5399 0.1725 7.979 45.017 27.1190.0186 1.4834 7.294

Page 56: Phong Tran - Summer Research Internship Excel

Phong Hamaca + 0.1 H20ModelsSRK PenelouxCSP Visc/Thermal Cond

Table Format PT aqueous Flash at <No format loaded> Pressure 1200.0 psia

Temperatu 450.00 °FNumber of phases

3 Total Vapor LiquidMol% 100.00 15.97 84.03

Output Format Weight% 100.00 0.92 99.08Fixed pressure Molar Volu 8.61 7.91 8.74

Volume% 100.00 14.68 85.32Code for Missing Property Density 38.5705 2.4079 44.7928

Z Factor 1.0584 0.9727 1.0746Molecular 332.10 19.05 391.61

Rows per block Enthalpy 139.83 202.72 139.2549 Internal En 44524.73 2105.48 52588.65

Internal En 134.07 110.50 134.29Columns per block Entropy 0.26 -0.07 0.26

19 Heat Capaci 0.64 0.66 0.64Heat Capaci 0.62 0.52 0.62

Blocks per fluid Kappa (Cp/C 1.04 1.27 1.031 JT Coefficient 0.0218 -0.0046

Velocity of Sound 1696.32 2490.60Number of fluids Viscosity 0.0184 1.4905

1 Thermal Conductivity 0.03 0.16Interfacial Tension 7.44 7.44

Begin Properties

Phong Hamaca + 0.1 H20

Pressurepsia

350.0TemperatureMol% Tot Mol% VapMol% Liq Mol% AqWeight% TotWeight% Vap

°F120.00 100.00 20.02 71.05 8.93 100.00 1.06160.00 100.00 21.29 70.08 8.62 100.00 1.13210.00 100.00 23.01 69.33 7.66 100.00 1.24250.00 100.00 25.08 69.00 5.92 100.00 1.36290.00 100.00 28.74 68.87 2.39 100.00 1.58320.00 100.00 31.28 68.72 100.00 1.74450.00 100.00 32.44 67.56 100.00 1.99

Phong Hamaca + 0.1 H20

Pressure

Page 57: Phong Tran - Summer Research Internship Excel

psia700.0

TemperatureMol% Tot Mol% VapMol% Liq Mol% AqWeight% TotWeight% Vap°F

120.00 100.00 10.89 80.12 8.99 100.00 0.56160.00 100.00 13.07 78.13 8.79 100.00 0.68210.00 100.00 15.24 76.53 8.22 100.00 0.81250.00 100.00 16.97 75.77 7.26 100.00 0.91290.00 100.00 19.15 75.36 5.49 100.00 1.04320.00 100.00 21.48 75.26 3.27 100.00 1.17450.00 100.00 25.77 74.23 100.00 1.51

Phong Hamaca + 0.1 H20

Pressurepsia

1200.0TemperatureMol% Tot Mol% VapMol% Liq Mol% AqWeight% TotWeight% Vap

°F120.00 100.00 90.99 9.01 100.00160.00 100.00 0.76 90.38 8.86 100.00 0.04210.00 100.00 4.08 87.48 8.44 100.00 0.21250.00 100.00 6.20 86.02 7.78 100.00 0.33290.00 100.00 8.23 85.15 6.62 100.00 0.44320.00 100.00 9.94 84.81 5.26 100.00 0.54450.00 100.00 15.97 84.03 100.00 0.92

Page 58: Phong Tran - Summer Research Internship Excel

Composition (mol%) at Pressure 1200.0 psia

Temperature 450.00 °F

Total Vapor Liquid

H2O 9.091 21.207 6.788N2 0.027 0.095 0.014CO2 1.745 4.177 1.283C1 26.400 72.745 17.590C2 0.264 0.498 0.219C3 0.136 0.185 0.127iC4 0.064 0.068 0.063

ft³/lb-mol nC4 0.109 0.105 0.110iC5 0.073 0.053 0.076

lb/ft³ nC5 0.073 0.050 0.077C6 0.282 0.135 0.310C7 0.655 0.231 0.735

BTU/lb C8 0.100 0.027 0.114BTU/lb-mol C9 0.055 0.011 0.063BTU/lb C10-C22 16.982 0.402 20.134BTU/lb °F C23-C31 9.813 0.011 11.677BTU/lb °F C32-C39 7.591 0.001 9.033BTU/lb °F C40-C46 5.875 0.000 6.992

C47-C53 5.240 0.000 6.236°F/psi C54-C60 4.674 0.000 5.562ft/s C61-C67 4.169 0.000 4.961cP C68-C74 3.718 0.000 4.425BTU/(hr ft ºF) C75-C80 2.866 0.000 3.410dyn/cm

C10+ 60.927 0.413 72.431C10+ mol wgt 531.886 220.982 532.223

Weight% LiqWeight% AqVolume% TotVolume% VapVolume% LiqVolume% Aq

98.46 0.48 100.00 33.80 65.94 0.2698.40 0.47 100.00 36.79 62.96 0.2598.35 0.42 100.00 40.44 59.34 0.2198.32 0.32 100.00 43.84 56.00 0.1698.29 0.13 100.00 48.35 51.59 0.0698.26 100.00 51.30 48.7098.01 100.00 55.56 44.44

Page 59: Phong Tran - Summer Research Internship Excel

Weight% LiqWeight% AqVolume% TotVolume% VapVolume% LiqVolume% Aq

98.95 0.49 100.00 11.78 87.88 0.3598.84 0.48 100.00 14.77 84.90 0.3398.75 0.45 100.00 18.02 81.67 0.3198.70 0.39 100.00 20.59 79.14 0.2798.67 0.30 100.00 23.51 76.29 0.2098.65 0.18 100.00 26.23 73.65 0.1298.49 100.00 32.75 67.25

Weight% LiqWeight% AqVolume% TotVolume% VapVolume% LiqVolume% Aq

99.51 0.49 100.00 99.61 0.3999.48 0.48 100.00 0.56 99.05 0.3999.33 0.46 100.00 3.23 96.40 0.3799.25 0.42 100.00 5.13 94.53 0.3499.20 0.36 100.00 7.04 92.67 0.2999.18 0.29 100.00 8.64 91.13 0.2399.08 100.00 14.68 85.32

Page 60: Phong Tran - Summer Research Internship Excel

Viscosity VapViscosity LiqViscosity AqSurf Ten V/L Surf Ten V/A Surf Ten L/AcP cP cP dyn/cm dyn/cm dyn/cm

0.0127 3227.3203 0.5587 12.075 66.778 51.5570.0134 816.3857 0.4003 11.916 61.110 47.0830.0142 171.8417 0.2876 11.674 57.247 41.9210.0147 55.9328 0.2317 11.457 57.622 38.0860.0151 20.1883 0.1929 11.232 62.039 34.4360.0154 10.1271 11.0260.0174 1.1008 9.742

Page 61: Phong Tran - Summer Research Internship Excel

Viscosity VapViscosity LiqViscosity AqSurf Ten V/L Surf Ten V/A Surf Ten L/AcP cP cP dyn/cm dyn/cm dyn/cm

0.0132 1798.8991 0.5591 10.086 64.145 46.4270.0138 472.1425 0.4009 10.097 58.198 42.8520.0146 107.4407 0.2882 10.029 52.870 38.5350.0152 37.6823 0.2323 9.929 50.666 35.2330.0157 14.6807 0.1935 9.804 50.705 32.0390.0160 7.7208 0.1717 9.700 52.419 29.6690.0178 1.2104 8.739

Viscosity VapViscosity LiqViscosity AqSurf Ten V/L Surf Ten V/A Surf Ten L/AcP cP cP dyn/cm dyn/cm dyn/cm

1294.6638 0.5597 40.2530.0146 343.6738 0.4017 7.813 55.378 37.9350.0153 86.1132 0.2892 7.962 49.760 34.5070.0159 31.9052 0.2333 8.005 46.696 31.7920.0164 13.0047 0.1944 8.002 45.118 29.1180.0168 7.0248 0.1725 7.979 45.016 27.1190.0184 1.4905 7.438

Page 62: Phong Tran - Summer Research Internship Excel

Phong Hamaca + 0.1 C6+H2O(wt)ModelsSRK PenelouxCSP Visc/Thermal Cond

Table Format PT aqueous Flash at <No format loaded> Pressure

TemperatureNumber of phases

3Mol%

Output Format Weight%Fixed pressure Molar Volume

Volume%Code for Missing Property Density

Z FactorMolecular Weight

Rows per block Enthalpy49 Internal Energy

Internal Energy (Mass)Columns per block Entropy

19 Heat Capacity (Cp)Heat Capacity (Cv)

Blocks per fluid Kappa (Cp/Cv)1 JT Coefficient

Velocity of SoundNumber of fluids Viscosity

1 Thermal ConductivityInterfacial Tension

Begin Properties

Phong Hamaca + 0.1 C6+H2O(wt)

Pressurepsia

1200.0TemperatureMol% Tot Mol% Vap

°F120.00 100.00160.00 100.00 0.67210.00 100.00 4.01250.00 100.00 6.13290.00 100.00 8.17320.00 100.00 9.88450.00 100.00 15.77

Page 63: Phong Tran - Summer Research Internship Excel

Composition (mol%) at Pressure

Temperature

H2O1200.0 psia N2450.00 °F CO2

C1Total Vapor Liquid C2

100.00 15.77 84.23 C3100.00 0.91 99.09 iC4

8.60 7.92 8.73 ft³/lb-mol nC4100.00 14.52 85.48 iC5

38.6278 2.4147 44.7793 lb/ft³ nC51.0572 0.9733 1.0730 C6332.24 19.12 390.88 C7139.81 202.99 139.23 BTU/lb C8

44540.31 2122.95 52483.18 BTU/lb-mol C9134.06 111.03 134.27 BTU/lb C10-C22

0.26 -0.07 0.26 BTU/lb °F C23-C310.64 0.66 0.64 BTU/lb °F C32-C390.62 0.52 0.62 BTU/lb °F C40-C461.04 1.27 1.03 C47-C53

0.0216 -0.0046 °F/psi C54-C601693.44 2488.02 ft/s C61-C67

0.0184 1.4797 cP C68-C740.03 0.16 BTU/(hr ft ºF) C75-C807.42 7.42 dyn/cm

C10+C10+ mol wgt

Mol% Liq Mol% AqWeight% TotWeight% VapWeight% LiqWeight% Aq

91.20 8.80 100.00 99.52 0.4890.67 8.65 100.00 0.03 99.50 0.4787.76 8.24 100.00 0.21 99.34 0.4586.30 7.57 100.00 0.32 99.27 0.4185.42 6.41 100.00 0.44 99.22 0.3585.07 5.04 100.00 0.53 99.19 0.2784.23 100.00 0.91 99.09

Page 64: Phong Tran - Summer Research Internship Excel

Composition (mol%) at 1200.0 psia

450.00 °F

Total Vapor Liquid

8.885 20.780 6.657

0.027 0.096 0.0141.745 4.191 1.288

26.400 73.058 17.6630.264 0.499 0.2200.136 0.185 0.1270.064 0.068 0.0630.109 0.105 0.1100.073 0.053 0.0760.073 0.049 0.0770.488 0.233 0.5360.655 0.231 0.7340.100 0.027 0.1140.055 0.011 0.063

16.982 0.403 20.0869.813 0.011 11.6497.591 0.001 9.0125.875 0.000 6.9755.240 0.000 6.2214.674 0.000 5.5494.169 0.000 4.9493.718 0.000 4.4152.866 0.000 3.402

60.927 0.414 72.259531.886 220.994 532.219

Volume% TotVolume% VapVolume% LiqVolume% AqViscosity VapcP

100.00 99.62 0.38100.00 0.50 99.13 0.38 0.0146100.00 3.17 96.47 0.36 0.0153100.00 5.07 94.60 0.33 0.0159100.00 6.98 92.73 0.28 0.0164100.00 8.59 91.19 0.22 0.0168100.00 14.52 85.48 0.0184

Page 65: Phong Tran - Summer Research Internship Excel

Composition (mol%) at

Viscosity LiqViscosity AqSurf Ten V/L Surf Ten V/A Surf Ten L/AcP cP dyn/cm dyn/cm dyn/cm

872.4905 0.5597 40.242247.2095 0.4017 7.810 55.386 37.883

67.2522 0.2892 7.957 49.774 34.46226.2173 0.2333 8.000 46.715 31.75311.1410 0.1944 7.995 45.142 29.085

6.1849 0.1725 7.970 45.044 27.0921.4797 7.418

Page 66: Phong Tran - Summer Research Internship Excel

Phong Hamaca + 0.1 C3+H2O(wt)ModelsSRK PenelouxCSP Visc/Thermal Cond

Table Format PT aqueous Flash at <No format loaded> Pressure

TemperatureNumber of phases

3Mol%

Output Format Weight%Fixed pressure Molar Volume

Volume%Code for Missing Property Density

Z FactorMolecular Weight

Rows per block Enthalpy49 Internal Energy

Internal Energy (Mass)Columns per block Entropy

19 Heat Capacity (Cp)Heat Capacity (Cv)

Blocks per fluid Kappa (Cp/Cv)1 JT Coefficient

Velocity of SoundNumber of fluids Viscosity

1 Thermal ConductivityInterfacial Tension

Begin Properties

Phong Hamaca + 0.1 C3+H2O(wt)

Pressurepsia

1200.0TemperatureMol% Tot Mol% Vap

°F120.00 100.00160.00 100.00 0.67210.00 100.00 4.03250.00 100.00 6.19290.00 100.00 8.25320.00 100.00 9.99450.00 100.00 15.77

Page 67: Phong Tran - Summer Research Internship Excel

Composition (mol%) at Pressure

Temperature

H2O1200.0 psia N2450.00 °F CO2

C1Total Vapor Liquid C2

100.00 15.77 84.23 C3100.00 0.91 99.09 iC4

8.60 7.92 8.73 ft³/lb-mol nC4100.00 14.53 85.47 iC5

38.6225 2.4231 44.7758 lb/ft³ nC51.0573 0.9740 1.0729 C6332.20 19.20 390.81 C7139.82 203.21 139.24 BTU/lb C8

44540.44 2142.25 52478.96 BTU/lb-mol C9134.08 111.57 134.28 BTU/lb C10-C22

0.26 -0.07 0.26 BTU/lb °F C23-C310.64 0.66 0.64 BTU/lb °F C32-C390.62 0.52 0.62 BTU/lb °F C40-C461.04 1.27 1.03 C47-C53

0.0213 -0.0046 °F/psi C54-C601689.94 2487.68 ft/s C61-C67

0.0184 1.4806 cP C68-C740.03 0.16 BTU/(hr ft ºF) C75-C807.40 7.40 dyn/cm

C10+C10+ mol wgt

Mol% Liq Mol% AqWeight% TotWeight% VapWeight% LiqWeight% Aq

91.39 8.61 100.00 99.53 0.4790.87 8.46 100.00 0.03 99.51 0.4687.92 8.05 100.00 0.21 99.35 0.4486.44 7.38 100.00 0.33 99.27 0.4085.53 6.21 100.00 0.44 99.22 0.3485.17 4.84 100.00 0.54 99.20 0.2684.23 100.00 0.91 99.09

Page 68: Phong Tran - Summer Research Internship Excel

Composition (mol%) at 1200.0 psia

450.00 °F

Total Vapor Liquid

8.696 20.320 6.520

0.027 0.096 0.0141.745 4.192 1.287

26.400 73.074 17.6610.264 0.499 0.2200.531 0.723 0.4950.064 0.068 0.0630.109 0.105 0.1100.073 0.053 0.0760.073 0.049 0.0770.282 0.135 0.3090.655 0.231 0.7340.100 0.027 0.1140.055 0.011 0.063

16.982 0.406 20.0859.813 0.011 11.6497.591 0.001 9.0125.875 0.000 6.9755.240 0.000 6.2214.674 0.000 5.5494.169 0.000 4.9493.718 0.000 4.4152.866 0.000 3.402

60.927 0.417 72.257531.886 221.015 532.222

Volume% TotVolume% VapVolume% LiqVolume% AqViscosity VapcP

100.00 99.63 0.37100.00 0.49 99.14 0.37 0.0146100.00 3.19 96.46 0.35 0.0153100.00 5.11 94.57 0.32 0.0159100.00 7.05 92.68 0.27 0.0164100.00 8.67 91.12 0.21 0.0168100.00 14.53 85.47 0.0184

Page 69: Phong Tran - Summer Research Internship Excel

Viscosity LiqViscosity AqSurf Ten V/L Surf Ten V/A Surf Ten L/AcP cP dyn/cm dyn/cm dyn/cm

865.7259 0.5597 40.197245.5490 0.4017 7.794 55.487 37.821

66.9335 0.2892 7.940 49.890 34.41426.1249 0.2333 7.982 46.837 31.71511.1127 0.1944 7.978 45.264 29.057

6.1728 0.1725 7.953 45.163 27.0701.4806 7.399

Page 70: Phong Tran - Summer Research Internship Excel

Phong Hamaca + 0.05 C6ModelsSRK PenelouxCSP Visc/Thermal Cond

Table Format Component Mol %<No format loaded> N2 0.029

CO2 1.829Number of phases C1 27.657

2 C2 0.276C3 0.143

Output Format iC4 0.067Fixed pressure nC4 0.114

iC5 0.076Code for Missing Property nC5 0.076

C6 5.057C7 0.686

Rows per block C8 0.10549 C9 0.057

C10-C22 17.790Columns per block C23-C31 10.281

16 C32-C39 7.952C40-C46 6.155

Blocks per fluid C47-C53 5.4901 C54-C60 4.896

C61-C67 4.367Number of fluids C68-C74 3.895

1 C75-C80 3.002

Begin Properties

Phong Hamaca + 0.05 C6

Pressurepsia

350.0TemperatureMol% Tot Mol% VapMol% LiqWeight% TotWeight% Vap

°F120.00 100.00 20.27 79.73 100.00 1.02160.00 100.00 21.48 78.52 100.00 1.10210.00 100.00 22.61 77.39 100.00 1.18250.00 100.00 23.33 76.67 100.00 1.25290.00 100.00 23.96 76.04 100.00 1.33320.00 100.00 24.40 75.60 100.00 1.39450.00 100.00 26.19 73.81 100.00 1.77

Phong Hamaca + 0.05 C6

Pressure

Page 71: Phong Tran - Summer Research Internship Excel

psia700.0

TemperatureMol% Tot Mol% VapMol% LiqWeight% TotWeight% Vap°F

120.00 100.00 10.09 89.91 100.00 0.50160.00 100.00 12.43 87.57 100.00 0.62210.00 100.00 14.47 85.53 100.00 0.74250.00 100.00 15.66 84.34 100.00 0.81290.00 100.00 16.58 83.42 100.00 0.88320.00 100.00 17.15 82.85 100.00 0.93450.00 100.00 18.85 81.15 100.00 1.16

Phong Hamaca + 0.05 C6

Pressurepsia

1200.0TemperatureMol% Tot Mol% VapMol% LiqWeight% TotWeight% Vap

°F120.00 100.00 100.00 100.00160.00 100.00 100.00 100.00210.00 100.00 2.20 97.80 100.00 0.11250.00 100.00 4.17 95.83 100.00 0.21290.00 100.00 5.63 94.37 100.00 0.29320.00 100.00 6.47 93.53 100.00 0.34450.00 100.00 8.46 91.54 100.00 0.50

Page 72: Phong Tran - Summer Research Internship Excel

Phong Hamaca + 0.05 C6ModelsSRK PenelouxCSP Visc/Thermal Cond

Weight% LiqVolume% TotVolume% VapVolume% LiqDensity TotDensity VapDensity Liqlb/ft³ lb/ft³ lb/ft³

98.98 100.00 32.79 67.21 32.9412 1.0244 48.509698.90 100.00 35.65 64.35 31.3771 0.9663 48.224698.82 100.00 38.65 61.35 29.6961 0.9104 47.828098.75 100.00 40.73 59.27 28.5007 0.8777 47.479698.67 100.00 42.61 57.39 27.3992 0.8545 47.103798.61 100.00 43.91 56.09 26.6209 0.8431 46.803498.23 100.00 48.89 51.11 23.5757 0.8551 45.3059

Page 73: Phong Tran - Summer Research Internship Excel

Weight% LiqVolume% TotVolume% VapVolume% LiqDensity TotDensity VapDensity Liqlb/ft³ lb/ft³ lb/ft³

99.50 100.00 10.44 89.56 43.3531 2.0678 48.164399.38 100.00 13.44 86.56 41.7273 1.9313 47.905099.26 100.00 16.45 83.55 40.0061 1.7977 47.526999.19 100.00 18.44 81.56 38.8002 1.7146 47.185499.12 100.00 20.17 79.83 37.7023 1.6495 46.810699.07 100.00 21.33 78.67 36.9332 1.6116 46.507898.84 100.00 25.38 74.62 33.9510 1.5531 44.9701

Weight% LiqVolume% TotVolume% VapVolume% LiqDensity TotDensity VapDensity Liqlb/ft³ lb/ft³ lb/ft³

100.00 100.00 100.00 47.8728 47.8728100.00 100.00 100.00 47.4927 47.4927

99.89 100.00 1.67 98.33 46.3532 3.0724 47.088399.79 100.00 3.32 96.68 45.3053 2.9073 46.761499.71 100.00 4.68 95.32 44.3528 2.7755 46.394299.66 100.00 5.54 94.46 43.6876 2.6956 46.093199.50 100.00 8.10 91.90 41.1298 2.5190 44.5308

Page 74: Phong Tran - Summer Research Internship Excel

0.0127 2613.2797 0.5587 Emulsion Forming between oil and water.0.0134 672.2509 0.4003

0.0141 146.9857 0.2876

Viscosity VapViscosity LiqSurf Ten V/LcP cP dyn/cm

0.0127 2442.5038 12.067 0.0127050.0134 584.2279 11.876 0.0133790.0142 129.8319 11.573 0.0141420.0149 45.3329 11.287 0.0147650.0155 17.4627 10.965 0.0153890.0159 9.0674 10.703 0.0158450.0177 1.1673 9.376 0.017703

Page 75: Phong Tran - Summer Research Internship Excel

Viscosity VapViscosity LiqSurf Ten V/LcP cP dyn/cm

0.0132 1852.9644 10.0650.0138 476.9327 10.0450.0146 107.4805 9.9200.0153 37.5874 9.7530.0159 14.6761 9.5360.0163 7.7263 9.3420.0182 1.3374 8.244

Viscosity VapViscosity LiqSurf Ten V/LcP cP dyn/cm

1524.4858387.0831

0.0154 91.2487 7.8430.0159 33.2604 7.8260.0165 13.3250 7.7400.0169 7.0514 7.6360.0188 1.4196 6.849

Page 76: Phong Tran - Summer Research Internship Excel

Phong Hamaca + 0.1 C6ModelsSRK PenelouxCSP Visc/Thermal Cond

Table Format Component Mol %<No format loaded> N2 0.027

CO2 1.745Number of phases C1 26.400

2 C2 0.264C3 0.136

Output Format iC4 0.064Fixed pressure nC4 0.109

iC5 0.073Code for Missing Property nC5 0.073

C6 9.373C7 0.655

Rows per block C8 0.10049 C9 0.055

C10-C22 16.982Columns per block C23-C31 9.813

16 C32-C39 7.591C40-C46 5.875

Blocks per fluid C47-C53 5.2401 C54-C60 4.674

C61-C67 4.169Number of fluids C68-C74 3.718

1 C75-C80 2.866

Begin Properties

Phong Hamaca + 0.1 C6

Pressurepsia

350.0TemperatureMol% Tot Mol% VapMol% LiqWeight% TotWeight% Vap Weight% Liq

°F120.00 100.00 18.79 81.21 100.00 0.98 99.02160.00 100.00 20.06 79.94 100.00 1.07 98.93210.00 100.00 21.30 78.70 100.00 1.18 98.82250.00 100.00 22.15 77.85 100.00 1.28 98.72290.00 100.00 22.95 77.05 100.00 1.39 98.61320.00 100.00 23.55 76.45 100.00 1.49 98.51450.00 100.00 26.22 73.78 100.00 2.07 97.93

Phong Hamaca + 0.1 C6

Pressure

Page 77: Phong Tran - Summer Research Internship Excel

psia700.0

TemperatureMol% Tot Mol% VapMol% LiqWeight% TotWeight% Vap Weight% Liq°F

120.00 100.00 8.41 91.59 100.00 0.43 99.57160.00 100.00 10.81 89.19 100.00 0.56 99.44210.00 100.00 12.94 87.06 100.00 0.70 99.30250.00 100.00 14.21 85.79 100.00 0.78 99.22290.00 100.00 15.24 84.76 100.00 0.87 99.13320.00 100.00 15.90 84.10 100.00 0.93 99.07450.00 100.00 18.16 81.84 100.00 1.26 98.74

Phong Hamaca + 0.1 C6

Pressurepsia

1200.0TemperatureMol% Tot Mol% VapMol% LiqWeight% TotWeight% Vap Weight% Liq

°F120.00 100.00 100.00 100.00 100.00160.00 100.00 100.00 100.00 100.00210.00 100.00 0.40 99.60 100.00 0.02 99.98250.00 100.00 2.44 97.56 100.00 0.13 99.87290.00 100.00 3.98 96.02 100.00 0.22 99.78320.00 100.00 4.89 95.11 100.00 0.28 99.72450.00 100.00 7.26 92.74 100.00 0.47 99.53

Page 78: Phong Tran - Summer Research Internship Excel

Phong Hamaca + 0.1 C6ModelsSRK PenelouxCSP Visc/Thermal Cond

Volume% TotVolume% Vap Volume% Liq Viscosity VapViscosity Liq Surf Ten V/LcP cP dyn/cm

100.00 31.80 68.20 0.0127 1715.5214 12.065100.00 34.78 65.22 0.0134 436.0264 11.849100.00 37.93 62.07 0.0142 98.2121 11.512100.00 40.17 59.83 0.0148 34.6454 11.195100.00 42.25 57.75 0.0154 13.6512 10.843100.00 43.73 56.27 0.0158 7.2525 10.558100.00 49.61 50.39 0.0174 1.1865 9.161

Page 79: Phong Tran - Summer Research Internship Excel

Volume% TotVolume% Vap Volume% Liq Viscosity VapViscosity Liq Surf Ten V/LcP cP dyn/cm

100.00 9.10 90.90 0.0132 1278.2287 10.050100.00 12.20 87.80 0.0138 350.6812 10.006100.00 15.33 84.67 0.0146 84.4780 9.846100.00 17.42 82.58 0.0153 30.8654 9.649100.00 19.26 80.74 0.0159 12.5135 9.400100.00 20.51 79.49 0.0163 6.7525 9.182100.00 25.14 74.86 0.0181 1.3724 7.992

Volume% TotVolume% Vap Volume% Liq Viscosity VapViscosity Liq Surf Ten V/LcP cP dyn/cm

100.00 100.00 1084.1376100.00 100.00 290.7765100.00 0.31 99.69 0.0154 70.5382 7.756100.00 2.02 97.98 0.0159 26.8584 7.710100.00 3.44 96.56 0.0165 11.1127 7.593100.00 4.35 95.65 0.0169 5.9543 7.465100.00 7.17 92.83 0.0188 1.3636 6.583

Page 80: Phong Tran - Summer Research Internship Excel

Phong Hamaca + 0.1 C6ModelsSRK PenelouxCSP Visc/Thermal Cond

Table Format Component Mol %<No format loaded> N2 0.026

CO2 1.670Number of phases C1 25.252

2 C2 0.252C3 0.130

Output Format iC4 0.061Fixed pressure nC4 0.104

iC5 0.070Code for Missing Property nC5 0.070

C6 13.313C7 0.626

Rows per block C8 0.09649 C9 0.052

C10-C22 16.243Columns per block C23-C31 9.387

16 C32-C39 7.261C40-C46 5.619

Blocks per fluid C47-C53 5.0121 C54-C60 4.471

C61-C67 3.988Number of fluids C68-C74 3.557

1 C75-C80 2.741

Begin Properties

Phong Hamaca + 0.15 C6

Pressurepsia

350.0TemperatureMol% Tot Mol% VapMol% LiqWeight% TotWeight% VapWeight% Liq

°F120.00 100.00 17.43 82.57 100.00 0.95 99.05160.00 100.00 18.75 81.25 100.00 1.05 98.95210.00 100.00 20.09 79.91 100.00 1.18 98.82250.00 100.00 21.05 78.95 100.00 1.30 98.70290.00 100.00 22.00 78.00 100.00 1.45 98.55320.00 100.00 22.74 77.26 100.00 1.57 98.43450.00 100.00 26.27 73.73 100.00 2.37 97.63

Phong Hamaca + 0.15 C6

Pressure

Page 81: Phong Tran - Summer Research Internship Excel

psia700.0

TemperatureMol% Tot Mol% VapMol% LiqWeight% TotWeight% VapWeight% Liq°F

120.00 100.00 6.88 93.12 100.00 0.37 99.63160.00 100.00 9.32 90.68 100.00 0.51 99.49210.00 100.00 11.52 88.48 100.00 0.65 99.35250.00 100.00 12.87 87.13 100.00 0.75 99.25290.00 100.00 13.99 86.01 100.00 0.85 99.15320.00 100.00 14.74 85.26 100.00 0.93 99.07450.00 100.00 17.52 82.48 100.00 1.36 98.64

Phong Hamaca + 0.15 C6

Pressurepsia

1200.0TemperatureMol% Tot Mol% VapMol% LiqWeight% TotWeight% VapWeight% Liq

°F120.00 100.00 100.00 100.00 100.00160.00 100.00 100.00 100.00 100.00210.00 100.00 100.00 100.00 100.00250.00 100.00 0.83 99.17 100.00 0.05 99.95290.00 100.00 2.44 97.56 100.00 0.14 99.86320.00 100.00 3.41 96.59 100.00 0.21 99.79450.00 100.00 6.10 93.90 100.00 0.43 99.57

Page 82: Phong Tran - Summer Research Internship Excel

Phong Hamaca + 0.1 C6ModelsSRK PenelouxCSP Visc/Thermal Cond

Volume% TotVolume% VapVolume% LiqViscosity VapViscosity LiqSurf Ten V/LcP cP dyn/cm

100.00 30.81 69.19 0.0127 1231.8601 12.063100.00 33.90 66.10 0.0134 331.0340 11.824100.00 37.21 62.79 0.0142 79.1352 11.454100.00 39.60 60.40 0.0148 29.0292 11.108100.00 41.86 58.14 0.0153 11.8682 10.727100.00 43.51 56.49 0.0157 6.4586 10.421100.00 50.30 49.70 0.0171 1.2268 8.957

Page 83: Phong Tran - Summer Research Internship Excel

Volume% TotVolume% VapVolume% LiqViscosity VapViscosity LiqSurf Ten V/LcP cP dyn/cm

100.00 7.76 92.24 0.0132 907.5432 10.036100.00 10.97 89.03 0.0138 263.7012 9.969100.00 14.21 85.79 0.0146 67.3326 9.777100.00 16.39 83.61 0.0152 25.6499 9.551100.00 18.33 81.67 0.0158 10.7572 9.271100.00 19.68 80.32 0.0163 5.9283 9.030100.00 24.88 75.12 0.0179 1.3786 7.751

Volume% TotVolume% VapVolume% LiqViscosity VapViscosity LiqSurf Ten V/LcP cP dyn/cm

100.00 100.00 797.3697100.00 100.00 224.6305100.00 100.00 56.9419100.00 0.72 99.28 0.0159 21.9921 7.600100.00 2.19 97.81 0.0165 9.3013 7.454100.00 3.14 96.86 0.0169 5.0158 7.304100.00 6.21 93.79 0.0187 1.3024 6.332

Page 84: Phong Tran - Summer Research Internship Excel

Phong Hamaca + 0.5C6+H20(10%V)ModelsSRK PenelouxCSP Visc/Thermal Cond

Table Format PT aqueous Flash at <No format loaded> Pressure 1200.0 psia

Temperat 450.00 °FNumber of phases

3 Total VaporMol% 100.00 10.12

Output Format Weight% 100.00 0.58Fixed pressure Molar Vol 8.60 8.12

Volume% 100.00 9.56Code for Missing Property Density 40.6077 2.4587

Z Factor 1.0566 0.9977Molecular 349.06 19.96

Rows per block Enthalpy 139.60 213.4549 Internal En 46818.99 2457.34

Internal En 134.13 123.13Columns per block Entropy 0.26 -0.07

23 Heat Capaci 0.64 0.67Heat Capaci 0.62 0.54

Blocks per fluid Kappa (Cp/ 1.04 1.241 JT Coefficient 0.0147

Velocity of Sound 1677.57Number of fluids Viscosity 0.0187

1 Thermal Conductivity 0.04Interfacial Tension 7.02

Begin Properties

Phong Hamaca + 0.5C6+H20(10%V)

Pressurepsia

350.0TemperatureMol% Tot ol% VapMol% LiqMol% AqWeight% TotWeight% Vap

°F120.00 100.00 20.62 77.74 1.64 100.00 1.04160.00 100.00 22.03 76.64 1.32 100.00 1.13210.00 100.00 23.96 75.74 0.30 100.00 1.25250.00 100.00 24.93 75.07 100.00 1.32290.00 100.00 25.52 74.48 100.00 1.39320.00 100.00 25.92 74.08 100.00 1.44450.00 100.00 27.45 72.55 100.00 1.77

Phong Hamaca + 0.05 C6 + H20

Pressure

Page 85: Phong Tran - Summer Research Internship Excel

psia700.0

TemperatureMol% Tot ol% VapMol% LiqMol% AqWeight% TotWeight% Vap°F

120.00 100.00 10.63 87.67 1.70 100.00 0.53160.00 100.00 13.03 85.47 1.50 100.00 0.65210.00 100.00 15.43 83.68 0.89 100.00 0.79250.00 100.00 17.25 82.75 100.00 0.89290.00 100.00 18.18 81.82 100.00 0.96320.00 100.00 18.74 81.26 100.00 1.00450.00 100.00 20.34 79.66 100.00 1.21

Phong Hamaca + 0.05 C6 + H20

Pressurepsia

1200.0TemperatureMol% Tot ol% VapMol% LiqMol% AqWeight% TotWeight% Vap

°F120.00 100.00 98.28 1.72 100.00160.00 100.00 98.44 1.56 100.00210.00 100.00 3.19 95.69 1.12 100.00 0.16250.00 100.00 5.53 94.06 0.41 100.00 0.28290.00 100.00 7.25 92.75 100.00 0.38320.00 100.00 8.11 91.89 100.00 0.43450.00 100.00 10.12 89.88 100.00 0.58

120.00 1560.3615 1147.1955160.00 393.6005 304.0240210.00 93.6216 74.9647250.00 33.9320 28.3077290.00 13.5934 11.6906320.00 7.2365 6.3442450.00 1.4558 1.4518

Page 86: Phong Tran - Summer Research Internship Excel

Phong Hamaca + 0.5C6+H20(10%V) Composition (mol%) at Models Pressure 1200.0 psia

SRK Peneloux Temperat 450.00 °FCSP Visc/Thermal Cond

Total Vapor Liquid

PT aqueous Flash at H2O 1.822 4.525 1.518N2 0.029 0.122 0.018CO2 1.829 4.824 1.491C1 27.657 87.261 20.944

Liquid C2 0.276 0.560 0.24489.88 C3 0.143 0.202 0.13699.42 iC4 0.067 0.072 0.066

8.65 ft³/lb-mol nC4 0.114 0.110 0.11590.44 iC5 0.076 0.055 0.079

44.6397 lb/ft³ nC5 0.076 0.051 0.0791.0632 C6 3.235 1.493 3.431386.13 C7 0.686 0.241 0.736139.17 BTU/lb C8 0.105 0.028 0.113

51815.45 BTU/lb-mol C9 0.057 0.011 0.062134.19 BTU/lb C10-C22 17.790 0.432 19.745

0.26 BTU/lb °F C23-C31 10.281 0.012 11.4370.64 BTU/lb °F C32-C39 7.952 0.001 8.8480.62 BTU/lb °F C40-C46 6.155 0.000 6.8481.03 C47-C53 5.490 0.000 6.108

-0.0046 °F/psi C54-C60 4.896 0.000 5.4482470.15 ft/s C61-C67 4.367 0.000 4.859

1.4558 cP C68-C74 3.895 0.000 4.3340.14 BTU/(hr ft ºF) C75-C80 3.002 0.000 3.3407.02 dyn/cm

C10+ 63.829 0.445 70.967C10+ mol 531.886 221.220 532.105

Weight% LiqWeight% Aqme% Totme% Vapme% Liqume% Aq sity Tot sity Vapnsity Liqlb/ft³ lb/ft³ lb/ft³

98.88 0.08 100.00 33.27 66.68 0.05 32.7537 1.0223 48.567998.81 0.07 100.00 36.35 63.62 0.04 31.0900 0.9624 48.286998.74 0.02 100.00 40.12 59.87 0.01 29.0418 0.9041 47.893498.68 100.00 42.42 57.58 27.7462 0.8664 47.549698.61 100.00 44.26 55.74 26.6683 0.8368 47.178798.56 100.00 45.52 54.48 25.9141 0.8201 46.881698.23 100.00 50.19 49.81 23.0143 0.8097 45.3922

Page 87: Phong Tran - Summer Research Internship Excel

Weight% LiqWeight% Aqme% Totme% Vapme% Liqume% Aq sity Tot sity Vapnsity Liqlb/ft³ lb/ft³ lb/ft³

99.39 0.09 100.00 10.99 88.95 0.06 43.1635 2.0652 48.229399.27 0.08 100.00 14.06 85.89 0.05 41.5065 1.9268 47.973599.17 0.05 100.00 17.40 82.57 0.03 39.6326 1.7915 47.598299.11 100.00 19.96 80.04 38.1648 1.7077 47.257499.04 100.00 21.73 78.27 37.0548 1.6337 46.888899.00 100.00 22.91 77.09 36.2822 1.5886 46.590598.79 100.00 26.94 73.06 33.3318 1.4979 45.0704

Weight% LiqWeight% Aqme% Totme% Vapme% Liqume% Aq sity Tot sity Vapnsity Liqlb/ft³ lb/ft³ lb/ft³

99.91 0.09 100.00 99.93 0.07 47.9206 47.911799.92 0.08 100.00 99.94 0.06 47.5396 47.532099.78 0.06 100.00 2.41 97.54 0.05 46.1084 3.0654 47.167599.70 0.02 100.00 4.36 95.63 0.02 44.9269 2.9037 46.839999.62 100.00 5.95 94.05 43.8743 2.7669 46.475799.57 100.00 6.86 93.14 43.1949 2.6774 46.179799.42 100.00 9.56 90.44 40.6077 2.4587 44.6397

875.3197 330.7435242.2216 106.8553

61.3182 31.278824.0046 13.252910.2144 6.2655

5.6353 3.73621.4456 1.4143

Page 88: Phong Tran - Summer Research Internship Excel

Composition (mol%) at

Density AqViscosity VapViscosity LiqViscosity AqSurf Ten V/L Surf Ten V/A Surf Ten L/Alb/ft³ cP cP cP dyn/cm dyn/cm dyn/cm

60.4309 0.0127 2613.2797 0.5587 12.072 66.907 50.53459.0402 0.0134 672.2509 0.4003 11.898 61.360 46.17457.1610 0.0141 146.9857 0.2876 11.632 57.704 41.159

0.0148 50.1758 11.3640.0154 18.9923 11.0530.0158 9.7343 10.7980.0177 1.1513 9.494

Page 89: Phong Tran - Summer Research Internship Excel

Density AqViscosity VapViscosity LiqViscosity AqSurf Ten V/L Surf Ten V/A Surf Ten L/Alb/ft³ cP cP cP dyn/cm dyn/cm dyn/cm

60.4468 0.0132 1955.9407 0.5591 10.075 64.219 45.54359.0655 0.0138 499.3507 0.4009 10.070 58.343 42.05057.1970 0.0146 111.2277 0.2882 9.980 53.131 37.847

0.0152 38.5653 9.8550.0158 15.0170 9.6490.0163 7.8907 9.4640.0181 1.3074 8.394

Density AqViscosity VapViscosity LiqViscosity AqSurf Ten V/L Surf Ten V/A Surf Ten L/Alb/ft³ cP cP cP dyn/cm dyn/cm dyn/cm

60.4769 1560.3615 0.5597 40.10059.1021 393.6005 0.4017 37.39757.2483 0.0153 93.6216 0.2892 7.902 49.940 33.91755.6419 0.0159 33.9320 0.2333 7.926 46.945 31.278

0.0164 13.5934 7.8700.0169 7.2365 7.7750.0187 1.4558 7.018

Page 90: Phong Tran - Summer Research Internship Excel

Phong Hamaca + 0.1 C6 + H20ModelsSRK PenelouxCSP Visc/Thermal Cond

Table Format PT aqueous Flash at <No format loaded> Pressure 1200.0 psia

Temperat 450.00 °FNumber of phases

3 Total Vapor LiquidMol% 100.00 10.53 89.47

Output Format Weight% 100.00 0.65 99.35Fixed pressure Molar Vol 8.36 8.04 8.40 ft³/lb-mol

Volume% 100.00 10.13 89.87Code for Missing Property Density 40.1883 2.5903 44.4275 lb/ft³

Z Factor 1.0275 0.9888 1.0320Molecular 335.93 20.84 373.01

Rows per block Enthalpy 139.30 209.09 138.85 BTU/lb49 Internal En ### 2570.53 ### BTU/lb-mol

Internal En 133.78 123.36 133.85 BTU/lbColumns per block Entropy 0.26 -0.04 0.26 BTU/lb °F

23 Heat Capaci 0.64 0.67 0.64 BTU/lb °FHeat Capaci 0.62 0.54 0.62 BTU/lb °F

Blocks per fluid Kappa (Cp/ 1.04 1.23 1.041 JT Coefficient 0.0169 -0.0046 °F/psi

Velocity of Sound 1626.26 2424.43 ft/sNumber of fluids Viscosity 0.0186 1.4518 cP

1 Thermal Conductivity 0.04 0.15 BTU/(hr ft ºF)Interfacial Tension 6.90 6.90 dyn/cm

Begin Properties

Phong Hamaca + 0.1 C6 + H20

Pressurepsia

350.0TemperatureMol% Tot ol% VapMol% LiqMol% Aqght% Totht% Vapght% Liqght% Aq

°F120.00 100.00 19.34 77.36 3.31 100.00 1.02 98.81 0.18160.00 100.00 20.76 76.24 3.00 100.00 1.11 98.73 0.16210.00 100.00 22.72 75.27 2.01 100.00 1.25 98.64 0.11250.00 100.00 25.06 74.72 0.22 100.00 1.42 98.57 0.01290.00 100.00 26.00 74.00 100.00 1.52 98.48320.00 100.00 26.53 73.47 100.00 1.60 98.40450.00 100.00 28.68 71.32 100.00 2.07 97.93

Phong Hamaca + 0.1 C6 + H20

Pressure

Page 91: Phong Tran - Summer Research Internship Excel

psia700.0

TemperatureMol% Tot ol% VapMol% LiqMol% Aqght% Totht% Vapght% Liqght% Aq°F

120.00 100.00 9.40 87.24 3.36 100.00 0.48 99.34 0.18160.00 100.00 11.79 85.05 3.16 100.00 0.62 99.21 0.17210.00 100.00 14.19 83.23 2.57 100.00 0.76 99.10 0.14250.00 100.00 16.12 82.30 1.59 100.00 0.88 99.03 0.09290.00 100.00 18.36 81.64 100.00 1.03 98.97320.00 100.00 19.02 80.98 100.00 1.09 98.91450.00 100.00 21.10 78.90 100.00 1.38 98.62

Phong Hamaca + 0.1 C6 + H20

Pressurepsia

1200.0TemperatureMol% Tot ol% VapMol% LiqMol% Aqght% Totht% Vapght% Liqght% Aq

°F120.00 100.00 96.62 3.38 100.00 99.82 0.18160.00 100.00 96.78 3.22 100.00 99.83 0.17210.00 100.00 2.00 95.21 2.80 100.00 0.11 99.74 0.15250.00 100.00 4.33 93.56 2.11 100.00 0.23 99.65 0.11290.00 100.00 6.57 92.51 0.92 100.00 0.36 99.59 0.05320.00 100.00 8.11 91.89 100.00 0.45 99.55450.00 100.00 10.53 89.47 100.00 0.65 99.35

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Composition (mol%) at Pressure 1200.0 psia

Temperat 450.00 °F

Total Vapor Liquid

H2O 3.479 8.664 2.869N2 0.027 0.114 0.017CO2 1.745 4.572 1.413C1 26.400 82.166 19.838C2 0.264 0.532 0.232C3 0.136 0.192 0.130iC4 0.064 0.069 0.063nC4 0.109 0.106 0.109iC5 0.073 0.053 0.075nC5 0.073 0.049 0.075C6 5.893 2.769 6.261C7 0.655 0.233 0.704C8 0.100 0.027 0.109C9 0.055 0.011 0.060C10-C22 16.982 0.429 18.930C23-C31 9.813 0.012 10.967C32-C39 7.591 0.001 8.484C40-C46 5.875 0.000 6.566C47-C53 5.240 0.000 5.857C54-C60 4.674 0.000 5.224C61-C67 4.169 0.000 4.659C68-C74 3.718 0.000 4.156C75-C80 2.866 0.000 3.203

C10+ 60.927 0.442 68.045C10+ mol 531.886 221.351 532.123

me% Totme% Vapme% Liqume% Aq sity Tot sity Vapnsity Liq nsity AqViscosity Vaplb/ft³ lb/ft³ lb/ft³ lb/ft³ cP

100.00 32.65 67.25 0.10 32.9938 1.0265 48.4727 60.4308 0.0127100.00 35.80 64.12 0.09 31.2920 0.9708 48.1832 59.0401 0.0134100.00 39.68 60.26 0.06 29.1893 0.9199 47.7792 57.1610 0.0141100.00 43.34 56.66 0.01 27.2582 0.8933 47.4235 55.5334 0.0146100.00 45.51 54.49 26.0316 0.8723 47.0462 0.0152100.00 46.90 53.10 25.2276 0.8622 46.7457 0.0156100.00 52.14 47.86 22.1166 0.8789 45.2529 0.0174

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me% Totme% Vapme% Liqume% Aq sity Tot sity Vapnsity Liq nsity AqViscosity Vaplb/ft³ lb/ft³ lb/ft³ lb/ft³ cP

100.00 10.16 89.71 0.13 43.4619 2.0712 48.1229 60.4465 0.0132100.00 13.29 86.59 0.12 41.7705 1.9384 47.8590 59.0653 0.0138100.00 16.70 83.20 0.10 39.8559 1.8127 47.4726 57.1970 0.0146100.00 19.42 80.52 0.06 38.3128 1.7396 47.1218 55.5781 0.0152100.00 22.38 77.62 36.6539 1.6875 46.7362 0.0157100.00 23.68 76.32 35.8295 1.6498 46.4318 0.0161100.00 28.26 71.74 32.6548 1.5952 44.8901 0.0180

me% Totme% Vapme% Liqume% Aq sity Tot sity Vapnsity Liq nsity AqViscosity Vaplb/ft³ lb/ft³ lb/ft³ lb/ft³ cP

100.00 99.86 0.14 47.8634 47.8453 60.4785100.00 99.86 0.14 47.4737 47.4576 59.1037100.00 1.57 98.31 0.12 46.3491 3.0968 47.0274 57.2481 0.0153100.00 3.56 96.35 0.09 45.1429 2.9468 46.6904 55.6419 0.0159100.00 5.57 94.39 0.04 43.8910 2.8373 46.3097 53.9133 0.0164100.00 7.02 92.98 42.9667 2.7718 45.9996 0.0168100.00 10.13 89.87 40.1883 2.5903 44.4275 0.0186

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Viscosity LiqViscosity AqSurf Ten V/L Surf Ten V/A Surf Ten L/AcP cP dyn/cm dyn/cm dyn/cm

1966.6497 0.5587 12.070 67.022 49.600489.2065 0.4003 11.880 61.588 45.342107.3079 0.2876 11.592 58.127 40.460

37.2427 0.2317 11.336 58.905 36.86114.9678 11.010

8.0010 10.7401.1431 9.388

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Viscosity LiqViscosity AqSurf Ten V/L Surf Ten V/A Surf Ten L/AcP cP dyn/cm dyn/cm dyn/cm

1429.8621 0.5591 10.064 64.282 44.736386.2940 0.4009 10.045 58.473 41.318

91.1470 0.2882 9.932 53.371 37.21732.7972 0.2323 9.791 51.387 34.10213.1248 9.615

7.0591 9.4141.3360 8.279

Viscosity LiqViscosity AqSurf Ten V/L Surf Ten V/A Surf Ten L/AcP cP dyn/cm dyn/cm dyn/cm

1147.1955 0.5597 39.965304.0240 0.4017 37.137

74.9647 0.2892 7.846 50.104 33.37728.3077 0.2333 7.850 47.176 30.80811.6906 0.1944 7.804 45.742 28.296

6.3442 7.7291.4518 6.905

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Phong Hamaca+0.15 C6+H20ModelsSRK PenelouxCSP Visc/Thermal Cond

Table Format PT aqueous Flash at <No format loaded> Pressure 1200.0 psia

Temperatu 450.00 °FNumber of phases

3 Total Vapor LiquidMol% 100.00 10.95 89.05

Output Format Weight% 100.00 0.73 99.27Fixed pressure Molar Volu 8.14 7.97 8.17

Volume% 100.00 10.72 89.28Code for Missing Property Density 39.7742 2.7186 44.2222

Z Factor 1.0011 0.9796 1.0037Molecular 323.93 21.67 361.11

Rows per block Enthalpy 139.02 204.97 138.5349 Internal En 43223.56 2671.11 48211.10

Internal En 133.43 123.29 133.51Columns per block Entropy 0.26 -0.02 0.26

19 Heat Capaci 0.64 0.66 0.64Heat Capaci 0.62 0.54 0.62

Blocks per fluid Kappa (Cp/C 1.04 1.23 1.041 JT Coefficient 0.0192 -0.0045

Velocity of Sound 1580.41 2382.27Number of fluids Viscosity 0.0186 1.4456

1 Thermal Conductivity 0.03 0.16Interfacial Tension 6.79 6.79

Begin Properties

Phong Hamaca + 0.15 C6 + H20

Pressurepsia

350.0TemperatureMol% Tot Mol% VapMol% Liq Mol% AqWeight% TotWeight% Vap

°F120.00 100.00 18.16 77.01 4.83 100.00 0.99160.00 100.00 19.60 75.88 4.53 100.00 1.09210.00 100.00 21.57 74.86 3.57 100.00 1.25250.00 100.00 23.94 74.23 1.84 100.00 1.44290.00 100.00 26.47 73.53 100.00 1.66320.00 100.00 27.12 72.88 100.00 1.77450.00 100.00 29.90 70.10 100.00 2.39

Phong Hamaca + 0.15 C6 + H20

Pressure

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psia700.0

TemperatureMol% Tot Mol% VapMol% Liq Mol% AqWeight% TotWeight% Vap°F

120.00 100.00 8.27 86.85 4.88 100.00 0.44160.00 100.00 10.65 84.66 4.69 100.00 0.58210.00 100.00 13.06 82.83 4.11 100.00 0.73250.00 100.00 14.99 81.85 3.16 100.00 0.86290.00 100.00 17.42 81.19 1.39 100.00 1.04320.00 100.00 19.30 80.70 100.00 1.18450.00 100.00 21.85 78.15 100.00 1.56

Phong Hamaca + 0.15 C6 + H20

Pressurepsia

1200.0TemperatureMol% Tot Mol% VapMol% Liq Mol% AqWeight% TotWeight% Vap

°F120.00 100.00 95.11 4.89 100.00160.00 100.00 95.26 4.74 100.00210.00 100.00 0.89 94.78 4.33 100.00 0.05250.00 100.00 3.22 93.11 3.66 100.00 0.18290.00 100.00 5.46 92.03 2.50 100.00 0.32320.00 100.00 7.34 91.52 1.14 100.00 0.43450.00 100.00 10.95 89.05 100.00 0.73

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Composition (mol%) at Pressure 1200.0 psia

Temperature 450.00 °F

Total Vapor Liquid

H2O 4.992 12.448 4.075N2 0.026 0.107 0.016CO2 1.670 4.338 1.341C1 25.252 77.477 18.829C2 0.252 0.505 0.221C3 0.130 0.183 0.124iC4 0.061 0.066 0.060

ft³/lb-mol nC4 0.104 0.102 0.105iC5 0.070 0.051 0.072

lb/ft³ nC5 0.070 0.048 0.072C6 8.321 3.973 8.856C7 0.626 0.226 0.675

BTU/lb C8 0.096 0.027 0.104BTU/lb-mol C9 0.052 0.011 0.057BTU/lb C10-C22 16.243 0.425 18.189BTU/lb °F C23-C31 9.387 0.012 10.540BTU/lb °F C32-C39 7.261 0.001 8.153BTU/lb °F C40-C46 5.619 0.000 6.311

C47-C53 5.012 0.000 5.629°F/psi C54-C60 4.471 0.000 5.020ft/s C61-C67 3.988 0.000 4.478cP C68-C74 3.557 0.000 3.994BTU/(hr ft ºF) C75-C80 2.741 0.000 3.078dyn/cm

C10+ 58.278 0.438 65.392C10+ mol wgt 531.886 221.478 532.142

Weight% LiqWeight% AqVolume% TotVolume% VapVolume% LiqVolume% Aq

98.74 0.27 100.00 32.02 67.83 0.1598.65 0.25 100.00 35.24 64.62 0.1398.55 0.20 100.00 39.24 60.66 0.1098.46 0.10 100.00 43.02 56.93 0.0598.34 100.00 46.69 53.3198.23 100.00 48.20 51.8097.61 100.00 53.97 46.03

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Weight% LiqWeight% AqVolume% TotVolume% VapVolume% LiqVolume% Aq

99.29 0.27 100.00 9.32 90.48 0.2099.16 0.26 100.00 12.52 87.30 0.1999.04 0.23 100.00 16.01 83.83 0.1698.96 0.18 100.00 18.79 81.09 0.1298.89 0.08 100.00 22.01 77.94 0.0598.82 100.00 24.42 75.5898.44 100.00 29.55 70.45

Weight% LiqWeight% AqVolume% TotVolume% VapVolume% LiqVolume% Aq

99.73 0.27 100.00 99.78 0.2299.74 0.26 100.00 99.79 0.2199.71 0.24 100.00 0.73 99.07 0.2099.61 0.20 100.00 2.75 97.08 0.1799.54 0.14 100.00 4.81 95.07 0.1199.50 0.06 100.00 6.56 93.39 0.0599.27 100.00 10.72 89.28

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Viscosity VapViscosity LiqViscosity AqSurf Ten V/L Surf Ten V/A Surf Ten L/AcP cP cP dyn/cm dyn/cm dyn/cm

0.0127 1507.7590 0.5587 12.069 67.127 48.7440.0134 392.8530 0.4003 11.863 61.799 44.5790.0141 90.4805 0.2876 11.553 58.523 39.8160.0146 32.3482 0.2317 11.278 59.488 36.3180.0150 12.9421 10.9640.0155 6.9621 10.6810.0171 1.1450 9.287

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Viscosity VapViscosity LiqViscosity AqSurf Ten V/L Surf Ten V/A Surf Ten L/AcP cP cP dyn/cm dyn/cm dyn/cm

0.0132 1074.0944 0.5591 10.055 64.340 43.9970.0138 305.1227 0.4009 10.020 58.593 40.6460.0146 75.8222 0.2882 9.886 53.595 36.6380.0151 28.2327 0.2323 9.725 51.712 33.6040.0156 11.6296 0.1935 9.536 52.108 30.7020.0160 6.3635 9.3600.0178 1.3627 8.165

Viscosity VapViscosity LiqViscosity AqSurf Ten V/L Surf Ten V/A Surf Ten L/AcP cP cP dyn/cm dyn/cm dyn/cm

875.3197 0.5597 39.842242.2216 0.4017 36.893

0.0153 61.3182 0.2892 7.791 50.258 32.8820.0159 24.0046 0.2333 7.777 47.392 30.3750.0164 10.2144 0.1944 7.711 46.025 27.9340.0168 5.6353 0.1725 7.638 46.085 26.1310.0186 1.4456 6.793

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Phong TranSummer Internship Hours

Date HoursWeek 1 1-Jun 4Week 2 8-Jun 13Week 3 15-Jun 18Week 4 22-Jun 20Week 5 29-Jun 20Week 6 6-Jul 20Week 7 13-Jul 20Week 8 20-Jul 20Week 9 27-Jul 15

Total 150