COMM Exported from CRANIUM 4.1 Knowledge Base: ChemCAD Export KB.mkskbd COMM Exported on Dec 04, 2020 at 15:03:52 STRC COMM ----- Start: 2,3-Epoxy-1-propanol ----- COMM Descriptive Properties NAME 23Epoxy1propanol FRM C3H6O2 CASNO 556-52-5 SYN (±)-Glycidol SYN Glycidol COMM Structural Groups IDG1 2 NGI1 1 IDG2 15 NGI2 1 IDG3 110 NGI3 1 COMM Constant Properties WM 74.079 TC 1 629.39 PC 7 7.35043e+06 VC 3 0.2005 HGIB 7 -2.34074e+06 LSHF 7 -5.13129e+06 HFOR 7 -4.2749e+06 HVP 7 701229 SOL 0 14.4455 TBOL 1 433.65 MP 1 228.15 DPM 1 4.8e-30 WI 0.777539 COMM Values for Thermal Conductivity, Liquid - f(T) COMM Reference: ThrmCnd,l (T): Missenard + Riedel Method [MKS]: 1,2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20,21 ELTC 1 1 21 2.281500e+02 2.973429e-01 2.384250e+02 2.931033e-01 2.487000e+02 2.888264e-01 2.589750e+02 2.845108e-01 2.692500e+02 2.801551e-01 2.795250e+02 2.757578e-01 2.898000e+02 2.713172e-01 3.000750e+02 2.668316e-01 3.103500e+02 2.622991e-01 3.206250e+02 2.577176e-01 3.309000e+02 2.530851e-01 3.411750e+02 2.483990e-01 3.514500e+02 2.436570e-01 3.617250e+02 2.388561e-01 3.720000e+02 2.339934e-01 3.822750e+02 2.290655e-01 3.925500e+02 2.240689e-01 4.028250e+02 2.189994e-01 4.131000e+02 2.138526e-01 4.233750e+02 2.086237e-01 4.336500e+02 2.033071e-01 COMM Values for Thermal Conductivity, Vapor - f(T) COMM Reference: ThrmCnd,v (T): Stiel + Thodos Method [MKS]: 1,2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20 EVTC 1 1 20 4.336500e+02 2.328436e-02 4.434370e+02 2.421648e-02 4.532240e+02 2.515797e-02 4.630111e+02 2.610829e-02 4.727981e+02 2.706690e-02 4.825851e+02 2.803330e-02 4.923721e+02 2.900698e-02 5.021591e+02 2.998746e-02 5.119462e+02 3.097427e-02 5.217332e+02 3.196697e-02 5.315202e+02 3.296512e-02 5.413072e+02 3.396831e-02 5.510943e+02 3.497614e-02 5.608813e+02 3.598824e-02 5.706683e+02 3.700423e-02 5.804553e+02 3.802378e-02 5.902423e+02 3.904656e-02 6.000294e+02 4.007226e-02 6.098164e+02 4.110059e-02 6.196034e+02 4.213128e-02 COMM Values for Heat Capacity - Isobaric, Liquid - f(T) COMM Reference: Cp,l (T): Poling + Prausnitz + O'Connell CSP Method [MKS]: 1,2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20,21 ECPL 1 7 21 2.281500e+02 2.837165e+03 2.384250e+02 2.817766e+03 2.487000e+02 2.803112e+03 2.589750e+02 2.792585e+03 2.692500e+02 2.785668e+03 2.795250e+02 2.781926e+03 2.898000e+02 2.780992e+03 3.000750e+02 2.782557e+03 3.103500e+02 2.786359e+03 3.206250e+02 2.792181e+03 3.309000e+02 2.799839e+03 3.411750e+02 2.809185e+03 3.514500e+02 2.820099e+03 3.617250e+02 2.832489e+03 3.720000e+02 2.846287e+03 3.822750e+02 2.861455e+03 3.925500e+02 2.877977e+03 4.028250e+02 2.895867e+03 4.131000e+02 2.915167e+03 4.233750e+02 2.935956e+03 4.336500e+02 2.958349e+03 COMM Values for Heat Capacity - Isobaric, Vapor - f(T) COMM Reference: Cp,v (T): Joback Method [MKS]: 1,2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20 ECPV 1 7 20 4.336500e+02 1.567368e+03 4.434370e+02 1.595494e+03 4.532240e+02 1.623078e+03 4.630111e+02 1.650128e+03 4.727981e+02 1.676654e+03 4.825851e+02 1.702666e+03 4.923721e+02 1.728173e+03 5.021591e+02 1.753184e+03 5.119462e+02 1.777709e+03 5.217332e+02 1.801758e+03 5.315202e+02 1.825340e+03 5.413072e+02 1.848464e+03 5.510943e+02 1.871140e+03 5.608813e+02 1.893377e+03 5.706683e+02 1.915186e+03 5.804553e+02 1.936574e+03 5.902423e+02 1.957553e+03 6.000294e+02 1.978130e+03 6.098164e+02 1.998317e+03 6.196034e+02 2.018122e+03 COMM Values for Surface Tension, Liquid - f(T) COMM Reference: SurfTn,l (T): Sastri + Rao Method [MKS]: 1,2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20,21 ESUR 1 2 21 2.281500e+02 5.433792e-02 2.384250e+02 5.264208e-02 2.487000e+02 5.095612e-02 2.589750e+02 4.928024e-02 2.692500e+02 4.761466e-02 2.795250e+02 4.595961e-02 2.898000e+02 4.431532e-02 3.000750e+02 4.268206e-02 3.103500e+02 4.106008e-02 3.206250e+02 3.944967e-02 3.309000e+02 3.785113e-02 3.411750e+02 3.626478e-02 3.514500e+02 3.469094e-02 3.617250e+02 3.312998e-02 3.720000e+02 3.158228e-02 3.822750e+02 3.004826e-02 3.925500e+02 2.852835e-02 4.028250e+02 2.702302e-02 4.131000e+02 2.553280e-02 4.233750e+02 2.405823e-02 4.336500e+02 2.259991e-02 COMM Values for Enthalpy of Vaporization - f(T) COMM Reference: Hv (T): Watson Relation [MKS]: 1,2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20,21 EDHV 1 7 21 2.281500e+02 9.211177e+05 2.384250e+02 9.120821e+05 2.487000e+02 9.028980e+05 2.589750e+02 8.935589e+05 2.692500e+02 8.840578e+05 2.795250e+02 8.743871e+05 2.898000e+02 8.645387e+05 3.000750e+02 8.545037e+05 3.103500e+02 8.442727e+05 3.206250e+02 8.338352e+05 3.309000e+02 8.231802e+05 3.411750e+02 8.122952e+05 3.514500e+02 8.011669e+05 3.617250e+02 7.897805e+05 3.720000e+02 7.781198e+05 3.822750e+02 7.661667e+05 3.925500e+02 7.539014e+05 4.028250e+02 7.413016e+05 4.131000e+02 7.283423e+05 4.233750e+02 7.149954e+05 4.336500e+02 7.012291e+05 COMM Values for Vapor Pressure, Liquid - f(T) COMM Reference: Pvp,l (T): Ambrose + Walton Method [MKS]: 16,17,18,19,20,21 COMM Reference: Pvp,l (T): Gómez-Nieto + Thodos Equation [MKS]: 1,2,3,4,5,6,7,8,9,10,11,12,13,14,15 EVPL 1 7 21 2.281500e+02 2.318020e-03 2.384250e+02 1.653617e-02 2.487000e+02 9.417555e-02 2.589750e+02 4.428183e-01 2.692500e+02 1.767067e+00 2.795250e+02 6.121973e+00 2.898000e+02 1.876505e+01 3.000750e+02 5.170147e+01 3.103500e+02 1.297613e+02 3.206250e+02 3.000476e+02 3.309000e+02 6.453970e+02 3.411750e+02 1.302109e+03 3.514500e+02 2.481681e+03 3.617250e+02 4.495747e+03 3.720000e+02 7.782975e+03 3.822750e+02 1.186577e+04 3.925500e+02 1.914742e+04 4.028250e+02 2.992969e+04 4.131000e+02 4.544665e+04 4.233750e+02 6.720665e+04 4.336500e+02 9.701210e+04 COMM Values for Density, Liquid - f(T) COMM Reference: Den,l (T): Rackett Equation [MKS]: 1,2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20,21 EDY 1 3 21 2.281500e+02 1.125862e+03 2.384250e+02 1.116636e+03 2.487000e+02 1.107314e+03 2.589750e+02 1.097889e+03 2.692500e+02 1.088359e+03 2.795250e+02 1.078718e+03 2.898000e+02 1.068961e+03 3.000750e+02 1.059082e+03 3.103500e+02 1.049074e+03 3.206250e+02 1.038931e+03 3.309000e+02 1.028646e+03 3.411750e+02 1.018210e+03 3.514500e+02 1.007615e+03 3.617250e+02 9.968517e+02 3.720000e+02 9.859085e+02 3.822750e+02 9.747739e+02 3.925500e+02 9.634351e+02 4.028250e+02 9.518775e+02 4.131000e+02 9.400846e+02 4.233750e+02 9.280383e+02 4.336500e+02 9.157177e+02 COMM Values for Viscosity, Liquid - f(T) COMM Reference: Visc,l (T): Przezdziecki + Sridhar Method [MKS]: 1,2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20,21 EVIS 1 6 21 2.281500e+02 -2.102177e-03 2.384250e+02 -4.086867e-03 2.487000e+02 -1.592985e-01 2.589750e+02 4.182802e-03 2.692500e+02 2.036519e-03 2.795250e+02 1.334423e-03 2.898000e+02 9.861519e-04 3.000750e+02 7.781920e-04 3.103500e+02 6.399980e-04 3.206250e+02 5.414923e-04 3.309000e+02 4.676899e-04 3.411750e+02 4.102895e-04 3.514500e+02 3.643228e-04 3.617250e+02 3.266358e-04 3.720000e+02 2.951316e-04 3.822750e+02 2.683625e-04 3.925500e+02 2.452984e-04 4.028250e+02 2.251870e-04 4.131000e+02 2.074670e-04 4.233750e+02 1.917119e-04 4.336500e+02 1.775925e-04 COMM Values for Viscosity, Vapor - f(T) COMM Reference: Visc,v (T): Lucas Method [MKS]: 1,2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20 EVV 1 6 20 4.336500e+02 1.224696e-05 4.434370e+02 1.252415e-05 4.532240e+02 1.280106e-05 4.630111e+02 1.307761e-05 4.727981e+02 1.335373e-05 4.825851e+02 1.362937e-05 4.923721e+02 1.390447e-05 5.021591e+02 1.417897e-05 5.119462e+02 1.445282e-05 5.217332e+02 1.472599e-05 5.315202e+02 1.499843e-05 5.413072e+02 1.527011e-05 5.510943e+02 1.554098e-05 5.608813e+02 1.581103e-05 5.706683e+02 1.608022e-05 5.804553e+02 1.634852e-05 5.902423e+02 1.661592e-05 6.000294e+02 1.688239e-05 6.098164e+02 1.714791e-05 6.196034e+02 1.741247e-05 COMM ----- End: 2,3-Epoxy-1-propanol ----- ENDC STRC COMM ----- Start: Acetic acid ----- COMM Descriptive Properties NAME Acetic acid FRM C2H4O2 CASNO 64-19-7 SYN ASPEN:C2H4O2-1 SYN Ethanoic acid SYN Ethylic acid SYN FEMA Number: 2006 SYN Flavis Number: 8.002 SYN Glacial acetic acid SYN MBDS:Cmp00204 COMM Structural Groups IDG1 1 NGI1 1 IDG2 43 NGI2 1 COMM Constant Properties WM 60.053 TC 1 592.71 PC 7 5.786e+06 VC 3 0.171 LSGF 7 -6.47578e+06 HGIB 7 -6.23635e+06 LSHF 7 -8.06451e+06 HFOR 7 -7.20697e+06 HVP 7 656819 SOL 0 12.9554 TBOL 1 391.05 MP 1 289.49 DPM 1 5.80401e-30 WI 0.447 COMM Values for Thermal Conductivity, Liquid - f(T) COMM Reference: ThrmCnd,l (T): Missenard + Riedel Method [MKS]: 1,21 COMM Reference: ThrmCnd,l (T): Dippr Equation 100 [MKS]: 2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20 ELTC 1 1 21 2.894900e+02 1.900175e-01 2.945680e+02 1.586886e-01 2.996460e+02 1.577644e-01 3.047240e+02 1.568402e-01 3.098020e+02 1.559160e-01 3.148800e+02 1.549918e-01 3.199580e+02 1.540676e-01 3.250360e+02 1.531434e-01 3.301140e+02 1.522193e-01 3.351920e+02 1.512951e-01 3.402700e+02 1.503709e-01 3.453480e+02 1.494467e-01 3.504260e+02 1.485225e-01 3.555040e+02 1.475983e-01 3.605820e+02 1.466741e-01 3.656600e+02 1.457499e-01 3.707380e+02 1.448257e-01 3.758160e+02 1.439015e-01 3.808940e+02 1.429773e-01 3.859720e+02 1.420531e-01 3.910500e+02 1.533713e-01 COMM Values for Thermal Conductivity, Vapor - f(T) COMM Reference: ThrmCnd,v (T): Dippr Equation 102 [MKS]: 1,2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20,21 EVTC 1 1 21 3.910500e+02 1.743752e-02 4.011330e+02 1.829514e-02 4.112160e+02 1.917693e-02 4.212990e+02 2.008281e-02 4.313820e+02 2.101268e-02 4.414650e+02 2.196645e-02 4.515480e+02 2.294405e-02 4.616310e+02 2.394540e-02 4.717140e+02 2.497042e-02 4.817970e+02 2.601903e-02 4.918800e+02 2.709118e-02 5.019630e+02 2.818678e-02 5.120460e+02 2.930577e-02 5.221290e+02 3.044809e-02 5.322120e+02 3.161366e-02 5.422950e+02 3.280242e-02 5.523780e+02 3.401430e-02 5.624610e+02 3.524925e-02 5.725440e+02 3.650719e-02 5.826270e+02 3.778805e-02 5.927100e+02 3.909179e-02 COMM Values for Heat Capacity - Isobaric, Liquid - f(T) COMM Reference: Martin + Andon (1982): 2,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20,21,22,23,24,25,26,27,28,29,30,31,32 COMM Reference: Parks + Kelley (1925): 1,3 ECPL 1 7 32 2.926000e+02 2.041792e+03 2.932000e+02 2.031539e+03 2.947000e+02 2.054344e+03 2.955100e+02 2.039865e+03 2.959000e+02 2.041530e+03 2.985900e+02 2.051521e+03 2.992800e+02 2.054852e+03 3.012600e+02 2.063178e+03 3.030200e+02 2.069838e+03 3.039300e+02 2.073169e+03 3.065800e+02 2.083160e+03 3.067400e+02 2.084825e+03 3.092300e+02 2.093151e+03 3.104500e+02 2.099812e+03 3.125200e+02 2.106473e+03 3.141300e+02 2.113133e+03 3.164500e+02 2.123125e+03 3.177900e+02 2.128120e+03 3.203600e+02 2.139777e+03 3.214300e+02 2.143107e+03 3.242400e+02 2.154763e+03 3.250500e+02 2.158094e+03 3.281100e+02 2.169750e+03 3.286500e+02 2.173080e+03 3.319400e+02 2.186402e+03 3.322300e+02 2.188067e+03 3.357600e+02 2.201389e+03 3.357900e+02 2.203054e+03 3.395600e+02 2.218041e+03 3.433300e+02 2.233027e+03 3.470900e+02 2.249679e+03 3.508200e+02 2.264666e+03 COMM Values for Heat Capacity - Isobaric, Vapor - f(T) COMM Reference: Cp,v (T): Dippr Equation 107 [MKS]: 1,2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20,21 ECPV 1 7 21 3.910500e+02 1.302579e+03 4.011330e+02 1.327375e+03 4.112160e+02 1.351910e+03 4.212990e+02 1.376191e+03 4.313820e+02 1.400221e+03 4.414650e+02 1.424003e+03 4.515480e+02 1.447539e+03 4.616310e+02 1.470829e+03 4.717140e+02 1.493872e+03 4.817970e+02 1.516666e+03 4.918800e+02 1.539210e+03 5.019630e+02 1.561500e+03 5.120460e+02 1.583533e+03 5.221290e+02 1.605305e+03 5.322120e+02 1.626813e+03 5.422950e+02 1.648052e+03 5.523780e+02 1.669020e+03 5.624610e+02 1.689711e+03 5.725440e+02 1.710124e+03 5.826270e+02 1.730254e+03 5.927100e+02 1.750098e+03 COMM Values for Surface Tension, Liquid - f(T) COMM Reference: Vogel (1948): 2,4,6,10,14,21 COMM Reference: SurfTn,l (T): Somayajulu [MKS]: 1,3,5,7,8,9,11,12,13,15,16,17,18,19,20,22,23,24,25,26,27 ESUR 1 2 27 2.894900e+02 2.824088e-02 2.932500e+02 2.757000e-02 2.945680e+02 2.769835e-02 2.962500e+02 2.725000e-02 2.996460e+02 2.716104e-02 3.000500e+02 2.696000e-02 3.047240e+02 2.662867e-02 3.098020e+02 2.610100e-02 3.148800e+02 2.557777e-02 3.154500e+02 2.536000e-02 3.199580e+02 2.505873e-02 3.250360e+02 2.454364e-02 3.301140e+02 2.403225e-02 3.349500e+02 2.346000e-02 3.351920e+02 2.352435e-02 3.402700e+02 2.301968e-02 3.453480e+02 2.251804e-02 3.504260e+02 2.201919e-02 3.555040e+02 2.152293e-02 3.605820e+02 2.102905e-02 3.606500e+02 2.086000e-02 3.656600e+02 2.053733e-02 3.707380e+02 2.004759e-02 3.758160e+02 1.955963e-02 3.808940e+02 1.907327e-02 3.859720e+02 1.858833e-02 3.910500e+02 1.810463e-02 COMM Values for Enthalpy of Vaporization - f(T) COMM Reference: Majer + Svoboda (1985): 3,16,21 COMM Reference: Hv (T): Dippr Equation 106 [MKS]: 2,4,5,6,7,8,9,10,11,12,13,14,15,17,18,19,20,22,23,24 COMM Reference: Hv (T): Watson Relation [MKS]: 1 EDHV 1 7 24 2.894900e+02 7.669347e+05 2.945680e+02 3.627131e+05 2.982000e+02 3.889897e+05 2.996460e+02 3.650406e+05 3.047240e+02 3.672936e+05 3.098020e+02 3.694667e+05 3.148800e+02 3.715546e+05 3.199580e+02 3.735516e+05 3.250360e+02 3.754519e+05 3.301140e+02 3.772497e+05 3.351920e+02 3.789388e+05 3.402700e+02 3.805130e+05 3.453480e+02 3.819659e+05 3.504260e+02 3.832911e+05 3.555040e+02 3.844817e+05 3.586000e+02 3.921536e+05 3.605820e+02 3.855310e+05 3.656600e+02 3.864320e+05 3.707380e+02 3.871776e+05 3.758160e+02 3.877606e+05 3.790000e+02 3.939853e+05 3.808940e+02 3.881736e+05 3.859720e+02 3.884093e+05 3.910500e+02 3.884600e+05 COMM Values for Vapor Pressure, Liquid - f(T) COMM Reference: Pvp,l (T): Antoine Equation - PGL 2001 [MKS]: 3,4,5,6,7,8,11,12,13,15,16,17,18,20,21,22,24,25,30 COMM Reference: McDonald + Shrader + Stull (1959): 9,10,14,19,23,26,27,28,29 COMM Reference: Pvp,l (T): Gómez-Nieto + Thodos Equation [MKS]: 1 COMM Reference: Pvp,l (T): Dippr Equation 101 [MKS]: 2 EVPL 1 7 30 2.894900e+02 8.047034e+02 2.945680e+02 1.707281e+03 2.996460e+02 2.251462e+03 3.047240e+02 2.986642e+03 3.098020e+02 3.918611e+03 3.148800e+02 5.088434e+03 3.199580e+02 6.543222e+03 3.250360e+02 8.336589e+03 3.255100e+02 8.563298e+03 3.287800e+02 9.997847e+03 3.301140e+02 1.052910e+04 3.351920e+02 1.318870e+04 3.402700e+02 1.639111e+04 3.403500e+02 1.651731e+04 3.453480e+02 2.022016e+04 3.504260e+02 2.476817e+04 3.555040e+02 3.013620e+04 3.605820e+02 3.643432e+04 3.646400e+02 4.230186e+04 3.656600e+02 4.378179e+04 3.707380e+02 5.230724e+04 3.758160e+02 6.214879e+04 3.786400e+02 6.821041e+04 3.808940e+02 7.345407e+04 3.859720e+02 8.638030e+04 3.886600e+02 9.415628e+04 3.899800e+02 9.817462e+04 3.904200e+02 9.958383e+04 3.908600e+02 1.009011e+05 3.910500e+02 1.010942e+05 COMM Values for Density, Liquid - f(T) COMM Reference: Yang + Wei + Li (2008): 7,11,15,18,23,24 COMM Reference: Vogel (1948): 2,12,20,26 COMM Reference: Dai + He + Lei + Chen (2008): 1,4,8,9,10,13,16,17,19,21 COMM Reference: Hales + Gundry + Ellender (1983): 3,5,6,14,22,25,27 EDY 1 3 27 2.931500e+02 1.049420e+03 2.931500e+02 1.049200e+03 2.931500e+02 1.049550e+03 2.981500e+02 1.043760e+03 2.981500e+02 1.043920e+03 3.031500e+02 1.038250e+03 3.031500e+02 1.038660e+03 3.031500e+02 1.038100e+03 3.081500e+02 1.032440e+03 3.131500e+02 1.026770e+03 3.131500e+02 1.027370e+03 3.145500e+02 1.026700e+03 3.181500e+02 1.021110e+03 3.200000e+02 1.019190e+03 3.231500e+02 1.016080e+03 3.231500e+02 1.015440e+03 3.281500e+02 1.009770e+03 3.331500e+02 1.005040e+03 3.331500e+02 1.004090e+03 3.345500e+02 1.004400e+03 3.381500e+02 9.983800e+02 3.400000e+02 9.964600e+02 3.431500e+02 9.936900e+02 3.531500e+02 9.829500e+02 3.600000e+02 9.734200e+02 3.602500e+02 9.769000e+02 3.800000e+02 9.499000e+02 COMM Values for Viscosity, Liquid - f(T) COMM Reference: Yang + Wei + Li (2008): 5,11,16,22,26,28 COMM Reference: Dai + He + Lei + Chen (2008): 2,3,6,9,12,14,17,18,21,23 COMM Reference: van Velzen + Cardozo + Langenkamp (1972): 1,4,7,8,10,13,15,19,20,24,25,27,29,30,31,32,33 EVIS 1 6 33 2.911500e+02 1.300000e-03 2.931500e+02 1.204000e-03 2.981500e+02 1.114000e-03 2.983500e+02 1.155000e-03 3.031500e+02 1.059000e-03 3.031500e+02 1.037000e-03 3.031500e+02 1.040000e-03 3.040500e+02 1.025000e-03 3.081500e+02 9.640000e-04 3.130500e+02 9.030000e-04 3.131500e+02 9.200000e-04 3.131500e+02 9.020000e-04 3.141500e+02 1.000000e-03 3.181500e+02 8.410000e-04 3.216500e+02 8.060000e-04 3.231500e+02 8.040000e-04 3.231500e+02 7.870000e-04 3.281500e+02 7.410000e-04 3.306500e+02 7.210000e-04 3.321500e+02 7.000000e-04 3.331500e+02 6.970000e-04 3.331500e+02 7.090000e-04 3.381500e+02 6.570000e-04 3.412500e+02 6.380000e-04 3.431500e+02 6.000000e-04 3.431500e+02 6.320000e-04 3.498500e+02 5.800000e-04 3.531500e+02 5.700000e-04 3.576500e+02 5.340000e-04 3.671500e+02 4.840000e-04 3.731500e+02 4.300000e-04 3.760500e+02 4.450000e-04 3.857500e+02 4.060000e-04 COMM Values for Viscosity, Vapor - f(T) COMM Reference: Visc,v (T): Reichenberg Technique [MKS]: 15,16,17,18,19,20,21 COMM Reference: Visc,v (T): Dippr Equation 102 [MKS]: 1,2,3,4,5,6,7,8,9,10,11,12,13,14 EVV 1 6 21 3.910500e+02 9.704049e-06 4.011330e+02 1.011690e-05 4.112160e+02 1.053477e-05 4.212990e+02 1.095752e-05 4.313820e+02 1.138502e-05 4.414650e+02 1.181715e-05 4.515480e+02 1.225379e-05 4.616310e+02 1.269482e-05 4.717140e+02 1.314013e-05 4.817970e+02 1.358961e-05 4.918800e+02 1.404315e-05 5.019630e+02 1.450067e-05 5.120460e+02 1.496206e-05 5.221290e+02 1.542724e-05 5.322120e+02 1.497870e-05 5.422950e+02 1.524934e-05 5.523780e+02 1.551900e-05 5.624610e+02 1.578769e-05 5.725440e+02 1.605538e-05 5.826270e+02 1.632206e-05 5.927100e+02 1.658772e-05 COMM ----- End: Acetic acid ----- ENDC STRC COMM ----- Start: Cyclohexanol ----- COMM Descriptive Properties NAME Cyclohexanol FRM C6H12O CASNO 108-93-0 SYN ASPEN:C6H12O-1 SYN Cyclohexyl alcohol SYN Hexalin SYN MBDS:Cmp00286 COMM Structural Groups IDG1 3 NGI1 1 IDG2 2 NGI2 5 IDG3 15 NGI3 1 COMM Constant Properties WM 100.161 TC 1 650.1 PC 7 4.26e+06 VC 3 0.3235 LSGF 7 -1.35091e+06 HGIB 7 -1.18724e+06 LSHF 7 -3.48594e+06 HFOR 7 -2.8574e+06 HVP 7 406744 SOL 0 11.5728 TBOL 1 434 MP 1 296.6 DPM 1 6.2043e-30 WI 0.528 COMM Values for Thermal Conductivity, Liquid - f(T) COMM Reference: ThrmCnd,l (T): Missenard + Riedel Method [MKS]: 1,14,15,16,17,18,19,20 COMM Reference: ThrmCnd,l (T): Dippr Equation 100 [MKS]: 2,3,4,5,6,7 COMM Reference: ThrmCnd,l (T): Mallan + Michaelian + Lockhart Method [MKS]: 8,9,10,11,12,13 ELTC 1 1 20 2.966000e+02 1.719146e-01 3.034700e+02 1.334939e-01 3.103400e+02 1.325889e-01 3.172100e+02 1.316839e-01 3.240800e+02 1.307789e-01 3.309500e+02 1.298740e-01 3.378200e+02 1.289690e-01 3.446900e+02 1.272544e-01 3.515600e+02 1.262033e-01 3.584300e+02 1.251522e-01 3.653000e+02 1.241010e-01 3.721700e+02 1.230499e-01 3.790400e+02 1.219988e-01 3.859100e+02 1.471537e-01 3.927800e+02 1.451415e-01 3.996500e+02 1.431114e-01 4.065200e+02 1.410626e-01 4.133900e+02 1.389945e-01 4.202600e+02 1.369063e-01 4.271300e+02 1.347972e-01 COMM Values for Thermal Conductivity, Vapor - f(T) COMM Reference: ThrmCnd,v (T): Dippr Equation 102 [MKS]: 1,2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20,21 EVTC 1 1 21 4.340000e+02 2.433912e-02 4.448050e+02 2.553809e-02 4.556100e+02 2.675457e-02 4.664150e+02 2.798766e-02 4.772200e+02 2.923652e-02 4.880250e+02 3.050031e-02 4.988300e+02 3.177820e-02 5.096350e+02 3.306941e-02 5.204400e+02 3.437316e-02 5.312450e+02 3.568871e-02 5.420500e+02 3.701534e-02 5.528550e+02 3.835234e-02 5.636600e+02 3.969904e-02 5.744650e+02 4.105479e-02 5.852700e+02 4.241896e-02 5.960750e+02 4.379094e-02 6.068800e+02 4.517014e-02 6.176850e+02 4.655601e-02 6.284900e+02 4.794801e-02 6.392950e+02 4.934561e-02 6.501000e+02 5.074832e-02 COMM Values for Heat Capacity - Isobaric, Liquid - f(T) COMM Reference: Cp,l (T): Dippr Equation 100 [MKS]: 1,2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20 ECPL 1 7 20 2.966000e+02 2.072249e+03 3.034700e+02 2.100522e+03 3.103400e+02 2.128794e+03 3.172100e+02 2.157067e+03 3.240800e+02 2.185339e+03 3.309500e+02 2.213612e+03 3.378200e+02 2.241885e+03 3.446900e+02 2.270157e+03 3.515600e+02 2.298430e+03 3.584300e+02 2.326702e+03 3.653000e+02 2.354975e+03 3.721700e+02 2.383248e+03 3.790400e+02 2.411520e+03 3.859100e+02 2.439793e+03 3.927800e+02 2.468066e+03 3.996500e+02 2.496338e+03 4.065200e+02 2.524611e+03 4.133900e+02 2.552883e+03 4.202600e+02 2.581156e+03 4.271300e+02 2.609429e+03 COMM Values for Heat Capacity - Isobaric, Vapor - f(T) COMM Reference: Cp,v (T): Dippr Equation 107 [MKS]: 1,2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20,21 ECPV 1 7 21 4.340000e+02 1.863480e+03 4.448050e+02 1.908585e+03 4.556100e+02 1.952997e+03 4.664150e+02 1.996693e+03 4.772200e+02 2.039654e+03 4.880250e+02 2.081872e+03 4.988300e+02 2.123342e+03 5.096350e+02 2.164064e+03 5.204400e+02 2.204042e+03 5.312450e+02 2.243283e+03 5.420500e+02 2.281797e+03 5.528550e+02 2.319593e+03 5.636600e+02 2.356684e+03 5.744650e+02 2.393082e+03 5.852700e+02 2.428800e+03 5.960750e+02 2.463852e+03 6.068800e+02 2.498250e+03 6.176850e+02 2.532008e+03 6.284900e+02 2.565138e+03 6.392950e+02 2.597653e+03 6.501000e+02 2.629565e+03 COMM Values for Surface Tension, Liquid - f(T) COMM Reference: SurfTn,l (T): Dippr Equation 106 [MKS]: 1,2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20 ESUR 1 2 20 2.966000e+02 3.479059e-02 3.034700e+02 3.409036e-02 3.103400e+02 3.339064e-02 3.172100e+02 3.269143e-02 3.240800e+02 3.199273e-02 3.309500e+02 3.129457e-02 3.378200e+02 3.059694e-02 3.446900e+02 2.989987e-02 3.515600e+02 2.920337e-02 3.584300e+02 2.850744e-02 3.653000e+02 2.781210e-02 3.721700e+02 2.711736e-02 3.790400e+02 2.642324e-02 3.859100e+02 2.572976e-02 3.927800e+02 2.503692e-02 3.996500e+02 2.434475e-02 4.065200e+02 2.365326e-02 4.133900e+02 2.296248e-02 4.202600e+02 2.227241e-02 4.271300e+02 2.158309e-02 COMM Values for Enthalpy of Vaporization - f(T) COMM Reference: Mathews + Fehlandt (1931): 21 COMM Reference: Hv (T): Dippr Equation 106 [MKS]: 1,2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20 EDHV 1 7 21 2.966000e+02 6.207957e+05 3.034700e+02 6.144129e+05 3.103400e+02 6.079700e+05 3.172100e+02 6.014650e+05 3.240800e+02 5.948963e+05 3.309500e+02 5.882616e+05 3.378200e+02 5.815590e+05 3.446900e+02 5.747862e+05 3.515600e+02 5.679409e+05 3.584300e+02 5.610206e+05 3.653000e+02 5.540227e+05 3.721700e+02 5.469444e+05 3.790400e+02 5.397828e+05 3.859100e+02 5.325348e+05 3.927800e+02 5.251969e+05 3.996500e+02 5.177657e+05 4.065200e+02 5.102374e+05 4.133900e+02 5.026079e+05 4.202600e+02 4.948728e+05 4.271300e+02 4.870274e+05 4.318500e+02 4.542987e+05 COMM Values for Vapor Pressure, Liquid - f(T) COMM Reference: Burguet + Montón + Sanchotello + Vázquez (1993): 24,26,34,39,43,50,54,62,67,72,77,80,84,87,89 COMM Reference: Goodwin + Newsham (1974): 14,15,19,22,28,29,32,38,48,60,61,68,73,74,78,88 COMM Reference: Ambrose + Ghiassee (1987): 27,33,35,37,40,42,45,47,51,53,56,59,63,66,71,75,79,83,86 COMM Reference: Gardner + Brewer (1937): 8,10,17,18,20,21,25,30,44,57,69,82 COMM Reference: Steele + Chirico + Knipmeyer + Nguyen (1997): 23,31,36,41,46,49,52,55,58,64,65,70,76,81,85,90 COMM Reference: Lepori + Matteoli + Gianni (2017): 1,2,3,4,5,6,7,9,11,12,13,16 EVPL 1 7 90 2.988400e+02 1.020000e+02 2.991500e+02 1.040000e+02 3.001700e+02 1.139000e+02 3.015200e+02 1.265000e+02 3.021800e+02 1.349000e+02 3.034700e+02 1.496000e+02 3.065700e+02 1.900000e+02 3.071500e+02 4.666284e+02 3.094500e+02 2.360000e+02 3.106500e+02 5.599541e+02 3.128000e+02 3.040000e+02 3.166200e+02 4.000000e+02 3.167900e+02 4.060000e+02 3.186500e+02 4.399639e+02 3.191500e+02 4.466300e+02 3.195100e+02 4.920000e+02 3.195500e+02 5.866186e+02 3.209500e+02 6.932765e+02 3.219500e+02 5.666202e+02 3.267500e+02 9.065923e+02 3.325500e+02 1.133240e+03 3.369500e+02 1.533208e+03 3.412410e+02 1.988800e+03 3.434500e+02 2.270000e+03 3.461500e+02 2.773106e+03 3.498500e+02 3.240000e+03 3.508010e+02 3.420000e+03 3.517500e+02 3.599705e+03 3.526500e+02 3.799688e+03 3.536500e+02 4.146327e+03 3.536640e+02 4.006400e+03 3.541500e+02 4.026336e+03 3.542920e+02 4.130000e+03 3.546500e+02 4.200000e+03 3.571510e+02 4.803000e+03 3.590710e+02 5.321800e+03 3.618950e+02 6.125000e+03 3.642500e+02 6.906100e+03 3.647500e+02 7.080000e+03 3.660300e+02 7.522000e+03 3.672480e+02 7.998200e+03 3.679120e+02 8.251000e+03 3.698500e+02 9.090000e+03 3.709500e+02 9.825861e+03 3.716690e+02 9.872000e+03 3.733500e+02 1.066510e+04 3.752530e+02 1.160900e+04 3.781500e+02 1.334557e+04 3.782490e+02 1.331000e+04 3.792500e+02 1.396000e+04 3.810660e+02 1.504100e+04 3.834270e+02 1.667300e+04 3.857760e+02 1.841800e+04 3.863500e+02 1.892000e+04 3.876830e+02 1.993700e+04 3.899200e+02 2.181300e+04 3.922500e+02 2.377138e+04 3.933210e+02 2.505000e+04 3.934980e+02 2.522100e+04 3.941500e+02 2.581122e+04 3.945500e+02 2.666448e+04 3.965500e+02 2.850000e+04 3.982370e+02 3.030700e+04 3.989800e+02 3.120900e+04 4.046570e+02 3.856300e+04 4.048960e+02 3.885900e+04 4.053500e+02 3.972000e+04 4.098500e+02 4.646286e+04 4.100500e+02 4.703614e+04 4.103990e+02 4.736200e+04 4.114480e+02 4.905300e+04 4.115500e+02 4.980000e+04 4.128500e+02 5.151578e+04 4.133500e+02 5.266235e+04 4.152390e+02 5.588300e+04 4.162050e+02 5.780700e+04 4.169500e+02 5.939000e+04 4.183500e+02 6.238155e+04 4.186590e+02 6.269000e+04 4.215500e+02 6.938000e+04 4.220630e+02 7.011200e+04 4.221500e+02 7.199410e+04 4.247590e+02 7.632700e+04 4.254500e+02 7.830000e+04 4.279750e+02 8.452800e+04 4.287840e+02 8.654400e+04 4.302500e+02 9.100000e+04 4.332500e+02 9.999180e+04 4.335500e+02 1.006900e+05 4.339420e+02 1.013170e+05 COMM Values for Density, Liquid - f(T) COMM Reference: Den,l (T): Dippr Equation 105 [MKS]: 1,2,3,4,6,7,8,9,11,12,13,14,16,17,18,20,21,22,23,25 COMM Reference: Steele + Chirico + Knipmeyer + Nguyen (1997): 5,10,15,19,24 EDY 1 3 25 2.966000e+02 9.619008e+02 3.034700e+02 9.551171e+02 3.103400e+02 9.482780e+02 3.172100e+02 9.413816e+02 3.231370e+02 9.185000e+02 3.240800e+02 9.344258e+02 3.309500e+02 9.274084e+02 3.378200e+02 9.203269e+02 3.446900e+02 9.131789e+02 3.481310e+02 8.996000e+02 3.515600e+02 9.059617e+02 3.584300e+02 8.986725e+02 3.653000e+02 8.913082e+02 3.721700e+02 8.838655e+02 3.731240e+02 8.799000e+02 3.790400e+02 8.763411e+02 3.859100e+02 8.687310e+02 3.927800e+02 8.610314e+02 3.981190e+02 8.594000e+02 3.996500e+02 8.532379e+02 4.065200e+02 8.453457e+02 4.133900e+02 8.373499e+02 4.202600e+02 8.292448e+02 4.231160e+02 8.343000e+02 4.271300e+02 8.210246e+02 COMM Values for Viscosity, Liquid - f(T) COMM Reference: Visc,l (T): Przezdziecki + Sridhar Method [MKS]: 1 COMM Reference: Visc,l (T): Dippr Equation 101 [MKS]: 2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20 EVIS 1 6 20 2.966000e+02 1.665881e-03 3.034700e+02 2.268456e-02 3.103400e+02 1.663701e-02 3.172100e+02 1.242805e-02 3.240800e+02 9.444100e-03 3.309500e+02 7.291930e-03 3.378200e+02 5.714603e-03 3.446900e+02 4.541165e-03 3.515600e+02 3.655920e-03 3.584300e+02 2.979311e-03 3.653000e+02 2.455811e-03 3.721700e+02 2.046111e-03 3.790400e+02 1.722018e-03 3.859100e+02 1.463051e-03 3.927800e+02 1.254163e-03 3.996500e+02 1.084169e-03 4.065200e+02 9.446726e-04 4.133900e+02 8.293031e-04 4.202600e+02 7.331842e-04 4.271300e+02 6.525492e-04 COMM Values for Viscosity, Vapor - f(T) COMM Reference: Visc,v (T): Dippr Equation 102 [MKS]: 1,2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20,21 EVV 1 6 21 4.340000e+02 1.052104e-05 4.448050e+02 1.079948e-05 4.556100e+02 1.107685e-05 4.664150e+02 1.135315e-05 4.772200e+02 1.162840e-05 4.880250e+02 1.190257e-05 4.988300e+02 1.217568e-05 5.096350e+02 1.244772e-05 5.204400e+02 1.271871e-05 5.312450e+02 1.298863e-05 5.420500e+02 1.325750e-05 5.528550e+02 1.352533e-05 5.636600e+02 1.379211e-05 5.744650e+02 1.405786e-05 5.852700e+02 1.432258e-05 5.960750e+02 1.458628e-05 6.068800e+02 1.484897e-05 6.176850e+02 1.511066e-05 6.284900e+02 1.537135e-05 6.392950e+02 1.563105e-05 6.501000e+02 1.588978e-05 COMM ----- End: Cyclohexanol ----- ENDC STRC COMM ----- Start: Ethanol ----- COMM Descriptive Properties NAME Ethanol FRM C2H6O CASNO 64-17-5 SYN ASPEN:C2H6O-2 SYN Ethyl alcohol SYN MBDS:Cmp00338 COMM Structural Groups IDG1 2 NGI1 1 IDG2 1 NGI2 1 IDG3 15 NGI3 1 COMM Constant Properties WM 46.069 TC 1 513.92 PC 7 6.137e+06 VC 3 0.167 LSGF 7 -3.78493e+06 HGIB 7 -3.66103e+06 LSHF 7 -6.02574e+06 HFOR 7 -5.10756e+06 HVP 7 851840 SOL 0 12.7598 TBOL 1 351.44 MP 1 159.05 DPM 1 5.63723e-30 WI 0.644 COMM Values for Thermal Conductivity, Liquid - f(T) COMM Reference: Qun-Fang + Rui-Sen + Dan-Yan + Yu-Chun (1997): 11,13,15,17,19,22 COMM Reference: ThrmCnd,l (T): Missenard + Riedel Method [MKS]: 1,2,3,4,5,6,7,8,9,10,12,14 COMM Reference: Baroncini + Latini + Pierpaoli (1984): 21,27 COMM Reference: ThrmCnd,l (T): Dippr Equation 100 [MKS]: 16,18,20,24,25,26,28 COMM Reference: Cai + Zong + Yu + Lin (1993): 23 COMM Reference: ThrmCnd,l (T): Mallan + Michaelian + Lockhart Method [MKS]: 29 ELTC 1 1 29 1.590500e+02 2.273334e-01 1.686695e+02 2.238711e-01 1.782890e+02 2.203765e-01 1.879085e+02 2.168484e-01 1.975280e+02 2.132854e-01 2.071475e+02 2.096861e-01 2.167670e+02 2.060490e-01 2.263865e+02 2.023724e-01 2.360060e+02 1.986546e-01 2.456255e+02 1.948936e-01 2.531500e+02 1.755000e-01 2.552450e+02 1.910874e-01 2.631500e+02 1.723000e-01 2.648645e+02 1.872337e-01 2.731500e+02 1.695000e-01 2.744840e+02 1.758700e-01 2.831500e+02 1.665000e-01 2.841035e+02 1.731669e-01 2.931500e+02 1.635000e-01 2.937230e+02 1.704638e-01 2.981500e+02 1.603000e-01 3.031500e+02 1.615000e-01 3.031500e+02 1.626000e-01 3.033425e+02 1.677608e-01 3.129620e+02 1.650577e-01 3.225815e+02 1.623546e-01 3.231500e+02 1.513000e-01 3.322010e+02 1.596515e-01 3.418205e+02 1.534387e-01 COMM Values for Thermal Conductivity, Vapor - f(T) COMM Reference: Frurip + Curtiss + Blander (1981): 2,4,7,11,14 COMM Reference: ThrmCnd,v (T): Dippr Equation 102 [MKS]: 1,3,5,6,8,9,10,12,13,15,16,17,18,19,20,21,22,23,24,25 EVTC 1 1 25 3.514400e+02 2.044623e-02 3.571000e+02 1.979032e-02 3.595640e+02 2.126364e-02 3.667000e+02 2.092000e-02 3.676880e+02 2.209437e-02 3.758120e+02 2.293833e-02 3.774000e+02 2.213336e-02 3.839360e+02 2.379545e-02 3.920600e+02 2.466564e-02 4.001840e+02 2.554883e-02 4.053000e+02 2.472744e-02 4.083080e+02 2.644494e-02 4.164320e+02 2.735390e-02 4.187000e+02 2.673576e-02 4.245560e+02 2.827563e-02 4.326800e+02 2.921006e-02 4.408040e+02 3.015714e-02 4.489280e+02 3.111678e-02 4.570520e+02 3.208893e-02 4.651760e+02 3.307351e-02 4.733000e+02 3.407048e-02 4.814240e+02 3.507977e-02 4.895480e+02 3.610131e-02 4.976720e+02 3.713506e-02 5.057960e+02 3.818095e-02 COMM Values for Heat Capacity - Isobaric, Liquid - f(T) COMM Reference: Cp,l (T): Dippr Equation 100 [MKS]: 1,2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20 ECPL 1 7 20 1.590500e+02 1.887321e+03 1.686695e+02 1.893417e+03 1.782890e+02 1.903066e+03 1.879085e+02 1.916546e+03 1.975280e+02 1.934135e+03 2.071475e+02 1.956110e+03 2.167670e+02 1.982751e+03 2.263865e+02 2.014334e+03 2.360060e+02 2.051138e+03 2.456255e+02 2.093441e+03 2.552450e+02 2.141521e+03 2.648645e+02 2.195656e+03 2.744840e+02 2.256124e+03 2.841035e+02 2.323202e+03 2.937230e+02 2.397170e+03 3.033425e+02 2.478304e+03 3.129620e+02 2.566884e+03 3.225815e+02 2.663186e+03 3.322010e+02 2.767489e+03 3.418205e+02 2.880071e+03 COMM Values for Heat Capacity - Isobaric, Vapor - f(T) COMM Reference: Strömsöe + Rönne + Lydersen (1970): 2,4,6,9,10,17,19,24 COMM Reference: Cp,v (T): Dippr Equation 107 [MKS]: 1,3,5,7,8,11,12,13,14,15,16,18,20,21,22,23,25,26,27,28 ECPV 1 7 28 3.514400e+02 1.621347e+03 3.565500e+02 2.238720e+03 3.595640e+02 1.650141e+03 3.617500e+02 2.083417e+03 3.676880e+02 1.678369e+03 3.718500e+02 1.890878e+03 3.758120e+02 1.706036e+03 3.839360e+02 1.733157e+03 3.872500e+02 1.824580e+03 3.888500e+02 1.811865e+03 3.920600e+02 1.759746e+03 4.001840e+02 1.785822e+03 4.083080e+02 1.811408e+03 4.164320e+02 1.836526e+03 4.245560e+02 1.861199e+03 4.326800e+02 1.885451e+03 4.332500e+02 1.882705e+03 4.408040e+02 1.909306e+03 4.433500e+02 1.899960e+03 4.489280e+02 1.932788e+03 4.570520e+02 1.955918e+03 4.651760e+02 1.978718e+03 4.733000e+02 2.001210e+03 4.804500e+02 1.999863e+03 4.814240e+02 2.023412e+03 4.895480e+02 2.045342e+03 4.976720e+02 2.067018e+03 5.057960e+02 2.088454e+03 COMM Values for Surface Tension, Liquid - f(T) COMM Reference: Vogel (1948): 12,16,21,29,31 COMM Reference: Gonçalves + Trindade + Costa + Bernardo + Johnson + Fonseca + Ferreira (2010): 1,2,3,4,5,7,9,10,11,13,15,17,19,20,23,24,26,27,30 COMM Reference: Giner + Villares + Martín + Artigas + Lafuente (2007): 6,8,14,18,22,25,28 ESUR 1 2 31 2.747700e+02 2.359000e-02 2.748700e+02 2.354000e-02 2.805600e+02 2.315000e-02 2.810500e+02 2.295000e-02 2.811700e+02 2.309000e-02 2.831500e+02 2.312000e-02 2.842500e+02 2.278000e-02 2.881500e+02 2.275000e-02 2.882100e+02 2.270000e-02 2.882300e+02 2.261000e-02 2.886500e+02 2.263000e-02 2.899500e+02 2.256000e-02 2.931500e+02 2.236000e-02 2.931500e+02 2.228000e-02 2.941900e+02 2.240000e-02 2.954500e+02 2.219000e-02 2.981500e+02 2.225000e-02 2.981500e+02 2.186000e-02 2.984100e+02 2.207000e-02 2.985500e+02 2.206000e-02 2.989500e+02 2.198000e-02 3.031500e+02 2.149000e-02 3.031500e+02 2.163000e-02 3.032000e+02 2.166000e-02 3.081500e+02 2.115000e-02 3.082300e+02 2.133000e-02 3.117900e+02 2.109000e-02 3.131500e+02 2.066000e-02 3.134500e+02 2.076000e-02 3.189900e+02 2.020000e-02 3.324500e+02 1.906000e-02 COMM Values for Enthalpy of Vaporization - f(T) COMM Reference: Polák + Benson (1971): 16,18,20,23 COMM Reference: Hv (T): Dippr Equation 106 [MKS]: 1,2,3,4,5,6,7,8,9,10,11,12,13,14,15,17,19,21,22,24 EDHV 1 7 24 1.590500e+02 1.024466e+06 1.686695e+02 1.023790e+06 1.782890e+02 1.022442e+06 1.879085e+02 1.020397e+06 1.975280e+02 1.017632e+06 2.071475e+02 1.014119e+06 2.167670e+02 1.009834e+06 2.263865e+02 1.004749e+06 2.360060e+02 9.988370e+05 2.456255e+02 9.920705e+05 2.552450e+02 9.844206e+05 2.648645e+02 9.758577e+05 2.744840e+02 9.663513e+05 2.841035e+02 9.558697e+05 2.937230e+02 9.443800e+05 2.981500e+02 9.173197e+05 3.033425e+02 9.318475e+05 3.081500e+02 9.055981e+05 3.129620e+02 9.182361e+05 3.181500e+02 8.945278e+05 3.225815e+02 9.035070e+05 3.322010e+02 8.876191e+05 3.331500e+02 8.693482e+05 3.418205e+02 8.705278e+05 COMM Values for Vapor Pressure, Liquid - f(T) COMM Reference: Kamihama + Matsuda + Kurihara + Tochigi + Oba (2012): 18,19,20,21,22,23 COMM Reference: Garriga + Sánchez + Pérez + Gracia (1996): 2,5,8,9,12,13,17 COMM Reference: Garriga + Martínez + Pérez + Gracia (2003): 1,3,4,6,7,10,11,14,15,16 EVPL 1 7 23 2.781500e+02 2.237000e+03 2.781500e+02 2.246000e+03 2.831500e+02 3.142000e+03 2.881500e+02 4.310000e+03 2.881500e+02 4.314000e+03 2.931500e+02 5.856000e+03 2.981500e+02 7.871000e+03 2.981500e+02 7.867000e+03 3.031500e+02 1.053100e+04 3.031500e+02 1.047500e+04 3.081500e+02 1.377600e+04 3.081500e+02 1.382300e+04 3.131500e+02 1.798000e+04 3.131500e+02 1.795600e+04 3.181500e+02 2.306700e+04 3.231500e+02 2.937900e+04 3.231500e+02 2.941900e+04 3.296700e+02 4.000000e+04 3.360600e+02 5.333000e+04 3.412300e+02 6.666000e+04 3.455900e+02 7.999000e+04 3.493800e+02 9.332000e+04 3.510300e+02 9.974000e+04 COMM Values for Density, Liquid - f(T) COMM Reference: Rauf + Stewart + Farhataziz (1983): 11,16,24,28,33 COMM Reference: Yao + Zhang + Wang + Zhou + Dong + Zhang (2012): 13,19,20,23,25,29,31 COMM Reference: Vogel (1948): 15,27,34 COMM Reference: Hales + Ellender (1976): 14,18,21,30,36 COMM Reference: Sun + Schouten + Trappeniers + Biswas (1988): 1,2,3,4,5,6,7,8,9,10,12,17,22,26,32,35 EDY 1 3 36 1.911500e+02 8.780800e+02 2.023400e+02 8.677800e+02 2.129800e+02 8.582400e+02 2.221800e+02 8.501300e+02 2.299500e+02 8.433700e+02 2.393500e+02 8.352800e+02 2.508500e+02 8.252500e+02 2.604900e+02 8.173500e+02 2.685800e+02 8.104600e+02 2.807800e+02 8.001400e+02 2.881500e+02 7.934000e+02 2.923900e+02 7.902500e+02 2.931500e+02 7.898310e+02 2.931500e+02 7.892000e+02 2.931500e+02 7.910000e+02 2.981500e+02 7.845000e+02 2.981500e+02 7.853100e+02 2.981500e+02 7.849300e+02 2.981500e+02 7.855350e+02 3.031500e+02 7.812200e+02 3.031500e+02 7.806400e+02 3.031500e+02 7.809300e+02 3.081500e+02 7.768750e+02 3.081500e+02 7.767000e+02 3.131500e+02 7.724800e+02 3.131700e+02 7.721700e+02 3.144500e+02 7.735000e+02 3.181500e+02 7.681000e+02 3.181500e+02 7.680420e+02 3.200000e+02 7.658300e+02 3.231500e+02 7.625640e+02 3.232100e+02 7.632000e+02 3.281500e+02 7.599000e+02 3.303500e+02 7.597000e+02 3.331500e+02 7.541500e+02 3.400000e+02 7.474700e+02 COMM Values for Viscosity, Liquid - f(T) COMM Reference: Rauf + Stewart + Farhataziz (1983): 9,19,27,35,42 COMM Reference: Yao + Zhang + Wang + Zhou + Dong + Zhang (2012): 13,18,22,26,31,34,40 COMM Reference: Gonçalves + Trindade + Costa + Bernardo + Johnson + Fonseca + Ferreira (2010): 1,4,5,6,8,11,12,15,17,20,21,23,25,29,30,36,37,39,43,44,47,49,50 COMM Reference: Phillips + Murphy (1970): 2,3,7,10,14,16,24,28,32,33,38,41,45,46,48,51 EVIS 1 6 51 2.731500e+02 1.832000e-03 2.731500e+02 1.785000e-03 2.781500e+02 1.611000e-03 2.786000e+02 1.649000e-03 2.805600e+02 1.537000e-03 2.811700e+02 1.527000e-03 2.831500e+02 1.456000e-03 2.842500e+02 1.455000e-03 2.881500e+02 1.280000e-03 2.881500e+02 1.321000e-03 2.882100e+02 1.338000e-03 2.931500e+02 1.203000e-03 2.931500e+02 1.189000e-03 2.931500e+02 1.200000e-03 2.941900e+02 1.192000e-03 2.981500e+02 1.092000e-03 2.981500e+02 1.096000e-03 2.981500e+02 1.095000e-03 2.981500e+02 1.056000e-03 2.984100e+02 1.088000e-03 2.985500e+02 1.088000e-03 3.031500e+02 1.003000e-03 3.031500e+02 1.002000e-03 3.031500e+02 9.960000e-04 3.032000e+02 1.000000e-03 3.081500e+02 9.140000e-04 3.081500e+02 8.818000e-04 3.081500e+02 9.100000e-04 3.082300e+02 9.140000e-04 3.117900e+02 8.550000e-04 3.131500e+02 8.450000e-04 3.131500e+02 8.330000e-04 3.181500e+02 7.630000e-04 3.181500e+02 7.650000e-04 3.181500e+02 7.461000e-04 3.189900e+02 7.560000e-04 3.211500e+02 7.300000e-04 3.231500e+02 7.010000e-04 3.231500e+02 7.150000e-04 3.231500e+02 7.040000e-04 3.281500e+02 6.450000e-04 3.281500e+02 6.302000e-04 3.281500e+02 6.560000e-04 3.331500e+02 6.020000e-04 3.331500e+02 5.950000e-04 3.381500e+02 5.490000e-04 3.381600e+02 5.710000e-04 3.431500e+02 5.080000e-04 3.431500e+02 5.040000e-04 3.461500e+02 4.880000e-04 3.481500e+02 4.700000e-04 COMM Values for Viscosity, Vapor - f(T) COMM Reference: Titani (1933): 8,14,17,22 COMM Reference: Visc,v (T): Dippr Equation 102 [MKS]: 1,2,3,4,5,6,7,9,10,11,12,13,15,16,18,19,20,21,23,24 EVV 1 6 24 3.514400e+02 1.043857e-05 3.595640e+02 1.066419e-05 3.676880e+02 1.088888e-05 3.758120e+02 1.111264e-05 3.839360e+02 1.133550e-05 3.920600e+02 1.155748e-05 4.001840e+02 1.177860e-05 4.033500e+02 1.173000e-05 4.083080e+02 1.199887e-05 4.164320e+02 1.221832e-05 4.245560e+02 1.243696e-05 4.326800e+02 1.265480e-05 4.408040e+02 1.287186e-05 4.438500e+02 1.293000e-05 4.489280e+02 1.308817e-05 4.570520e+02 1.330372e-05 4.649500e+02 1.355000e-05 4.651760e+02 1.351854e-05 4.733000e+02 1.373264e-05 4.814240e+02 1.394603e-05 4.895480e+02 1.415873e-05 4.906500e+02 1.421000e-05 4.976720e+02 1.437075e-05 5.057960e+02 1.458210e-05 COMM ----- End: Ethanol ----- ENDC STRC COMM ----- Start: Ethyl acetate ----- COMM Descriptive Properties NAME Ethyl acetate FRM C4H8O2 CASNO 141-78-6 SYN Acetic acid, ethyl ester SYN Acetic ether SYN ASPEN:C4H8O2-3 SYN Ethyl ethanoate SYN FEMA Number: 2414 SYN Flavis Number: 9.001 SYN MBDS:Cmp00339 COMM Structural Groups IDG1 2 NGI1 1 IDG2 1 NGI2 1 IDG3 22 NGI3 1 COMM Constant Properties WM 88.1051 TC 1 523.2 PC 7 3.83e+06 VC 3 0.286 LSGF 7 -3.7835e+06 HGIB 7 -3.72729e+06 LSHF 7 -5.44648e+06 HFOR 7 -5.04057e+06 HVP 7 362091 SOL 0 8.89765 TBOL 1 350.3 MP 1 189.6 DPM 1 5.93744e-30 WI 0.362 COMM Values for Thermal Conductivity, Liquid - f(T) COMM Reference: Qun-Fang + Rui-Sen + Dan-Yan + Yu-Chun (1997): 9,12,14,16,18,21 COMM Reference: ThrmCnd,l (T): Dippr Equation 100 [MKS]: 1,2,3,4,5,6,7,8,10,11,13,15,17,19,20,22,23,24,25,26 ELTC 1 1 26 1.896000e+02 1.825455e-01 1.976350e+02 1.796826e-01 2.056700e+02 1.768198e-01 2.137050e+02 1.739569e-01 2.217400e+02 1.710940e-01 2.297750e+02 1.682312e-01 2.378100e+02 1.653683e-01 2.458450e+02 1.625054e-01 2.531500e+02 1.584000e-01 2.538800e+02 1.596426e-01 2.619150e+02 1.567797e-01 2.631500e+02 1.555000e-01 2.699500e+02 1.539168e-01 2.731500e+02 1.526000e-01 2.779850e+02 1.510539e-01 2.831500e+02 1.496000e-01 2.860200e+02 1.481911e-01 2.931500e+02 1.465000e-01 2.940550e+02 1.453282e-01 3.020900e+02 1.424653e-01 3.031500e+02 1.429000e-01 3.101250e+02 1.396025e-01 3.181600e+02 1.367396e-01 3.261950e+02 1.338767e-01 3.342300e+02 1.310139e-01 3.422650e+02 1.281510e-01 COMM Values for Thermal Conductivity, Vapor - f(T) COMM Reference: ThrmCnd,v (T): Dippr Equation 102 [MKS]: 1,2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20,21 EVTC 1 1 21 3.503000e+02 1.413225e-02 3.589450e+02 1.476750e-02 3.675900e+02 1.542066e-02 3.762350e+02 1.609165e-02 3.848800e+02 1.678040e-02 3.935250e+02 1.748685e-02 4.021700e+02 1.821095e-02 4.108150e+02 1.895265e-02 4.194600e+02 1.971191e-02 4.281050e+02 2.048869e-02 4.367500e+02 2.128296e-02 4.453950e+02 2.209468e-02 4.540400e+02 2.292382e-02 4.626850e+02 2.377034e-02 4.713300e+02 2.463423e-02 4.799750e+02 2.551544e-02 4.886200e+02 2.641396e-02 4.972650e+02 2.732976e-02 5.059100e+02 2.826280e-02 5.145550e+02 2.921307e-02 5.232000e+02 3.018052e-02 COMM Values for Heat Capacity - Isobaric, Liquid - f(T) COMM Reference: Cp,l (T): Dippr Equation 100 [MKS]: 1,2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20 ECPL 1 7 20 1.896000e+02 1.823772e+03 1.976350e+02 1.818775e+03 2.056700e+02 1.815936e+03 2.137050e+02 1.815254e+03 2.217400e+02 1.816729e+03 2.297750e+02 1.820361e+03 2.378100e+02 1.826151e+03 2.458450e+02 1.834098e+03 2.538800e+02 1.844202e+03 2.619150e+02 1.856464e+03 2.699500e+02 1.870883e+03 2.779850e+02 1.887459e+03 2.860200e+02 1.906192e+03 2.940550e+02 1.927083e+03 3.020900e+02 1.950131e+03 3.101250e+02 1.975336e+03 3.181600e+02 2.002699e+03 3.261950e+02 2.032219e+03 3.342300e+02 2.063896e+03 3.422650e+02 2.097730e+03 COMM Values for Heat Capacity - Isobaric, Vapor - f(T) COMM Reference: Cp,v (T): Dippr Equation 107 [MKS]: 1,2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20,21 ECPV 1 7 21 3.503000e+02 1.420248e+03 3.589450e+02 1.443950e+03 3.675900e+02 1.468005e+03 3.762350e+02 1.492335e+03 3.848800e+02 1.516866e+03 3.935250e+02 1.541530e+03 4.021700e+02 1.566262e+03 4.108150e+02 1.591004e+03 4.194600e+02 1.615704e+03 4.281050e+02 1.640313e+03 4.367500e+02 1.664789e+03 4.453950e+02 1.689094e+03 4.540400e+02 1.713194e+03 4.626850e+02 1.737060e+03 4.713300e+02 1.760667e+03 4.799750e+02 1.783992e+03 4.886200e+02 1.807018e+03 4.972650e+02 1.829730e+03 5.059100e+02 1.852115e+03 5.145550e+02 1.874164e+03 5.232000e+02 1.895868e+03 COMM Values for Surface Tension, Liquid - f(T) COMM Reference: Mumford + Phillips (1950): 14,17 COMM Reference: SurfTn,l (T): Somayajulu [MKS]: 1,2,3,4,5,6,7,8,9,10,11,12,13,16,18,20,22,23,24,26 COMM Reference: Vogel (1948c): 15,19,21,25 ESUR 1 2 26 1.896000e+02 3.812068e-02 1.976350e+02 3.701036e-02 2.056700e+02 3.590536e-02 2.137050e+02 3.480581e-02 2.217400e+02 3.371184e-02 2.297750e+02 3.262358e-02 2.378100e+02 3.154116e-02 2.458450e+02 3.046474e-02 2.538800e+02 2.939446e-02 2.619150e+02 2.833051e-02 2.699500e+02 2.727305e-02 2.779850e+02 2.622228e-02 2.860200e+02 2.517840e-02 2.931500e+02 2.395000e-02 2.934500e+02 2.375000e-02 2.940550e+02 2.414162e-02 2.981500e+02 2.330000e-02 3.020900e+02 2.311218e-02 3.022500e+02 2.287000e-02 3.101250e+02 2.209033e-02 3.157500e+02 2.107000e-02 3.181600e+02 2.107633e-02 3.261950e+02 2.007046e-02 3.342300e+02 1.907305e-02 3.345500e+02 1.880000e-02 3.422650e+02 1.808442e-02 COMM Values for Enthalpy of Vaporization - f(T) COMM Reference: Hv (T): Dippr Equation 106 [MKS]: 1,2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20 EDHV 1 7 20 1.896000e+02 4.708945e+05 1.976350e+02 4.664986e+05 2.056700e+02 4.620353e+05 2.137050e+02 4.575020e+05 2.217400e+02 4.528958e+05 2.297750e+02 4.482133e+05 2.378100e+02 4.434512e+05 2.458450e+02 4.386060e+05 2.538800e+02 4.336735e+05 2.619150e+02 4.286497e+05 2.699500e+02 4.235299e+05 2.779850e+02 4.183091e+05 2.860200e+02 4.129820e+05 2.940550e+02 4.075426e+05 3.020900e+02 4.019846e+05 3.101250e+02 3.963009e+05 3.181600e+02 3.904837e+05 3.261950e+02 3.845245e+05 3.342300e+02 3.784138e+05 3.422650e+02 3.721410e+05 COMM Values for Vapor Pressure, Liquid - f(T) COMM Reference: Polák + Mertl (1965): 8,9,11,13,15,18,21,22,25,28,32,34,37,39,41,44 COMM Reference: Novotná + Dohnal + Holub (1986): 29,36,43 COMM Reference: Ambrose + Ellender + Gundry + Lee + Townsend (1981): 1,2,3,4,5,6,7,10,12,14,16,17,19,20,23,24,26,27,30,31,33,35,38,40,42,45 EVPL 1 7 45 2.710730e+02 2.868000e+03 2.730540e+02 3.236000e+03 2.755480e+02 3.754000e+03 2.788870e+02 4.560000e+03 2.818420e+02 5.385000e+03 2.852480e+02 6.494000e+03 2.883920e+02 7.683000e+03 2.887300e+02 7.838024e+03 2.918300e+02 9.201912e+03 2.918310e+02 9.187000e+03 2.942700e+02 1.041515e+04 2.951720e+02 1.087800e+04 2.969100e+02 1.186969e+04 2.986820e+02 1.292500e+04 2.990100e+02 1.315492e+04 3.022620e+02 1.533900e+04 3.022690e+02 1.533600e+04 3.022900e+02 1.536941e+04 3.057030e+02 1.799000e+04 3.057090e+02 1.799000e+04 3.059800e+02 1.824384e+04 3.100300e+02 2.186887e+04 3.102100e+02 2.203100e+04 3.102180e+02 2.203300e+04 3.133300e+02 2.524193e+04 3.140700e+02 2.605600e+04 3.140790e+02 2.605600e+04 3.180500e+02 3.084414e+04 3.181500e+02 3.095000e+04 3.184830e+02 3.137400e+04 3.228070e+02 3.740600e+04 3.228700e+02 3.751692e+04 3.273640e+02 4.476000e+04 3.276500e+02 4.534561e+04 3.323810e+02 5.416800e+04 3.331500e+02 5.572000e+04 3.334700e+02 5.643537e+04 3.367380e+02 6.356500e+04 3.391900e+02 6.946097e+04 3.413680e+02 7.493800e+04 3.453400e+02 8.606628e+04 3.463740e+02 8.901600e+04 3.481500e+02 9.444000e+04 3.489800e+02 9.727202e+04 3.502060e+02 1.011440e+05 COMM Values for Density, Liquid - f(T) COMM Reference: Kumar + Reddy + Rao + Sandhyasri + Begum + Rambabu (2013): 10,14,17,21 COMM Reference: Acosta + Arce + Ageitos + Rodil + Soto (2002): 7 COMM Reference: Mumford + Phillips (1950): 4,6 COMM Reference: Abraham + Bery + Kudchadker (1971): 5,12,16,22,24,25 COMM Reference: Sakurai + Nakamura + Nitta (1996): 1,2,8,13,20 COMM Reference: Sastry + Patel (2003): 9,11,15,18 COMM Reference: Vogel (1948c): 3,19,23 EDY 1 3 25 2.781500e+02 9.184400e+02 2.881500e+02 9.065100e+02 2.931500e+02 9.009000e+02 2.931500e+02 9.007000e+02 2.981500e+02 8.939000e+02 2.981500e+02 8.946000e+02 2.981500e+02 8.943100e+02 2.981500e+02 8.943700e+02 2.981500e+02 8.945560e+02 3.031500e+02 8.884000e+02 3.031500e+02 8.884810e+02 3.031500e+02 8.876000e+02 3.081500e+02 8.821000e+02 3.081500e+02 8.826000e+02 3.081500e+02 8.825010e+02 3.131500e+02 8.755000e+02 3.131500e+02 8.756000e+02 3.131500e+02 8.759750e+02 3.151500e+02 8.747000e+02 3.181500e+02 8.696500e+02 3.181500e+02 8.695000e+02 3.231500e+02 8.630000e+02 3.321500e+02 8.533000e+02 3.331500e+02 8.499000e+02 3.431500e+02 8.364000e+02 COMM Values for Viscosity, Liquid - f(T) COMM Reference: Kumar + Reddy + Rao + Sandhyasri + Begum + Rambabu (2013): 19,20,23,24 COMM Reference: Visc,l (T): Przezdziecki + Sridhar Method [MKS]: 1,2,3,4 COMM Reference: Mumford + Phillips (1950): 14,16 COMM Reference: Visc,l (T): Dippr Equation 101 [MKS]: 5,6,7,8,9,10,11,12,13,15,18,22,25,26,27,28 COMM Reference: Sastry + Patel (2003): 17,21 EVIS 1 6 28 1.896000e+02 2.701817e-03 1.976350e+02 1.927414e-03 2.056700e+02 1.487930e-03 2.137050e+02 1.205491e-03 2.217400e+02 1.105014e-03 2.297750e+02 9.894364e-04 2.378100e+02 8.885986e-04 2.458450e+02 8.003086e-04 2.538800e+02 7.227428e-04 2.619150e+02 6.543781e-04 2.699500e+02 5.939364e-04 2.779850e+02 5.403417e-04 2.860200e+02 4.926839e-04 2.931500e+02 4.520000e-04 2.940550e+02 4.501907e-04 2.981500e+02 4.250000e-04 2.981500e+02 4.280000e-04 3.020900e+02 4.122042e-04 3.031500e+02 3.800000e-04 3.081500e+02 3.680000e-04 3.081500e+02 3.870000e-04 3.101250e+02 3.781621e-04 3.131500e+02 3.500000e-04 3.181500e+02 3.340000e-04 3.181600e+02 3.475824e-04 3.261950e+02 3.200500e-04 3.342300e+02 2.952070e-04 3.422650e+02 2.727435e-04 COMM Values for Viscosity, Vapor - f(T) COMM Reference: Titani (1933): 7,12,17,21,25 COMM Reference: Visc,v (T): Dippr Equation 102 [MKS]: 1,2,3,4,5,6,8,9,10,11,13,14,15,16,18,19,20,22,23,24,26 EVV 1 6 26 3.503000e+02 8.972449e-06 3.589450e+02 9.196142e-06 3.675900e+02 9.418662e-06 3.762350e+02 9.639998e-06 3.848800e+02 9.860143e-06 3.935250e+02 1.007909e-05 4.012500e+02 1.018000e-05 4.021700e+02 1.029684e-05 4.108150e+02 1.051338e-05 4.194600e+02 1.072872e-05 4.281050e+02 1.094284e-05 4.317500e+02 1.098000e-05 4.367500e+02 1.115576e-05 4.453950e+02 1.136748e-05 4.540400e+02 1.157798e-05 4.626850e+02 1.178729e-05 4.660500e+02 1.195000e-05 4.713300e+02 1.199539e-05 4.799750e+02 1.220230e-05 4.886200e+02 1.240802e-05 4.914500e+02 1.250000e-05 4.972650e+02 1.261256e-05 5.059100e+02 1.281591e-05 5.145550e+02 1.301809e-05 5.217500e+02 1.332000e-05 5.232000e+02 1.321910e-05 COMM ----- End: Ethyl acetate ----- ENDC STRC COMM ----- Start: n-Hexane ----- COMM Descriptive Properties NAME n-Hexane FRM C6H14 CASNO 110-54-3 SYN ASPEN:C6H14-1 SYN Hexane SYN MBDS:Cmp00381 COMM Structural Groups IDG1 2 NGI1 4 IDG2 1 NGI2 2 COMM Constant Properties WM 86.177 TC 1 507.5 PC 7 3.012e+06 VC 3 0.37 LSGF 7 -45498.5 HGIB 7 -836.582 LSHF 7 -2.30526e+06 HFOR 7 -1.94112e+06 HVP 7 335013 SOL 0 7.28434 TBOL 1 341.85 MP 1 177.83 DPM 1 0 WI 0.299 COMM Values for Thermal Conductivity, Liquid - f(T) COMM Reference: ThrmCnd,l (T): Missenard + Riedel Method [MKS]: 1 COMM Reference: ThrmCnd,l (T): Dippr Equation 100 [MKS]: 2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20 ELTC 1 1 20 1.778300e+02 1.584114e-01 1.860310e+02 1.591952e-01 1.942320e+02 1.562978e-01 2.024330e+02 1.534004e-01 2.106340e+02 1.505030e-01 2.188350e+02 1.476056e-01 2.270360e+02 1.447082e-01 2.352370e+02 1.418108e-01 2.434380e+02 1.389134e-01 2.516390e+02 1.360159e-01 2.598400e+02 1.331185e-01 2.680410e+02 1.302211e-01 2.762420e+02 1.273237e-01 2.844430e+02 1.244263e-01 2.926440e+02 1.215289e-01 3.008450e+02 1.186315e-01 3.090460e+02 1.157340e-01 3.172470e+02 1.128366e-01 3.254480e+02 1.099392e-01 3.336490e+02 1.070418e-01 COMM Values for Thermal Conductivity, Vapor - f(T) COMM Reference: ThrmCnd,v (T): Stiel + Thodos Method [MKS]: 18,19,20 COMM Reference: ThrmCnd,v (T): Dippr Equation 102 [MKS]: 1,2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17 EVTC 1 1 20 3.418500e+02 1.680727e-02 3.501325e+02 1.766436e-02 3.584150e+02 1.854102e-02 3.666975e+02 1.943710e-02 3.749800e+02 2.035246e-02 3.832625e+02 2.128693e-02 3.915450e+02 2.224038e-02 3.998275e+02 2.321267e-02 4.081100e+02 2.420366e-02 4.163925e+02 2.521320e-02 4.246750e+02 2.624116e-02 4.329575e+02 2.728741e-02 4.412400e+02 2.835181e-02 4.495225e+02 2.943423e-02 4.578050e+02 3.053454e-02 4.660875e+02 3.165261e-02 4.743700e+02 3.278832e-02 4.826525e+02 3.068434e-02 4.909350e+02 3.157560e-02 4.992175e+02 3.247086e-02 COMM Values for Heat Capacity - Isobaric, Liquid - f(T) COMM Reference: Cp,l (T): IUPAC Cubic Splines [MKS]: 2,4,5,6,8,9,10,11,12,13,14,17,18,19,21,22,23,24,25 COMM Reference: Huffman + Parks + Barmore (1931): 3,7,15,16,20 COMM Reference: Cp,l (T): Poling + Prausnitz + O'Connell CSP Method [MKS]: 1 ECPL 1 7 25 1.778300e+02 1.864982e+03 1.860310e+02 1.979382e+03 1.888000e+02 1.974848e+03 1.942320e+02 1.982320e+03 2.024330e+02 1.990091e+03 2.106340e+02 2.002127e+03 2.178000e+02 2.016688e+03 2.188350e+02 2.017863e+03 2.270360e+02 2.036732e+03 2.352370e+02 2.058168e+03 2.434380e+02 2.081604e+03 2.516390e+02 2.106483e+03 2.598400e+02 2.132417e+03 2.680410e+02 2.159480e+03 2.754000e+02 2.179864e+03 2.762000e+02 2.188232e+03 2.762420e+02 2.187792e+03 2.844430e+02 2.217477e+03 2.926440e+02 2.248656e+03 2.935000e+02 2.242624e+03 3.008450e+02 2.281452e+03 3.090460e+02 2.315988e+03 3.172470e+02 2.352386e+03 3.254480e+02 2.390768e+03 3.336490e+02 2.431235e+03 COMM Values for Heat Capacity - Isobaric, Vapor - f(T) COMM Reference: Cp,v (T): Dippr Equation 107 [MKS]: 1,2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20 ECPV 1 7 20 3.418500e+02 1.850606e+03 3.501325e+02 1.889682e+03 3.584150e+02 1.928607e+03 3.666975e+02 1.967306e+03 3.749800e+02 2.005716e+03 3.832625e+02 2.043784e+03 3.915450e+02 2.081466e+03 3.998275e+02 2.118725e+03 4.081100e+02 2.155533e+03 4.163925e+02 2.191869e+03 4.246750e+02 2.227718e+03 4.329575e+02 2.263068e+03 4.412400e+02 2.297913e+03 4.495225e+02 2.332252e+03 4.578050e+02 2.366084e+03 4.660875e+02 2.399412e+03 4.743700e+02 2.432243e+03 4.826525e+02 2.464583e+03 4.909350e+02 2.496440e+03 4.992175e+02 2.527825e+03 COMM Values for Surface Tension, Liquid - f(T) COMM Reference: SurfTn,l (T): Sastri + Rao Method [MKS]: 1 COMM Reference: Giner + Villares + Martín + Artigas + Lafuente (2007): 16,18,20,22,25,26,28 COMM Reference: Jasper + Kerr + Gregorich (1953): 13,15,21,24,29,31,33 COMM Reference: SurfTn,l (T): Dippr Equation 106 [MKS]: 2,3,4,5,6,7,8,9,10,11,12,14,17,19,23,27,30,32,34 ESUR 1 2 34 1.778300e+02 3.218811e-02 1.860310e+02 3.119917e-02 1.942320e+02 3.018069e-02 2.024330e+02 2.916977e-02 2.106340e+02 2.816655e-02 2.188350e+02 2.717117e-02 2.270360e+02 2.618381e-02 2.352370e+02 2.520462e-02 2.434380e+02 2.423378e-02 2.516390e+02 2.327147e-02 2.598400e+02 2.231790e-02 2.680410e+02 2.137326e-02 2.731500e+02 2.050000e-02 2.762420e+02 2.043778e-02 2.831500e+02 1.946000e-02 2.831500e+02 1.963000e-02 2.844430e+02 1.951168e-02 2.881500e+02 1.904000e-02 2.926440e+02 1.859522e-02 2.931500e+02 1.852000e-02 2.931500e+02 1.841000e-02 2.981500e+02 1.806000e-02 3.008450e+02 1.768865e-02 3.031500e+02 1.737000e-02 3.031500e+02 1.753000e-02 3.081500e+02 1.674000e-02 3.090460e+02 1.679225e-02 3.131500e+02 1.647000e-02 3.131500e+02 1.632000e-02 3.172470e+02 1.590632e-02 3.231500e+02 1.528000e-02 3.254480e+02 1.503119e-02 3.331500e+02 1.424000e-02 3.336490e+02 1.416719e-02 COMM Values for Enthalpy of Vaporization - f(T) COMM Reference: Lemons + Felsing (1943): 16,19,22 COMM Reference: Hv (T): Dippr Equation 106 [MKS]: 2,3,4,5,6,7,8,9,10,11,12,13,14,15,17,18,20,21,23 COMM Reference: Hv (T): Watson Relation [MKS]: 1 EDHV 1 7 23 1.778300e+02 4.351506e+05 1.860310e+02 4.407087e+05 1.942320e+02 4.361654e+05 2.024330e+02 4.315502e+05 2.106340e+02 4.268601e+05 2.188350e+02 4.220918e+05 2.270360e+02 4.172416e+05 2.352370e+02 4.123056e+05 2.434380e+02 4.072798e+05 2.516390e+02 4.021596e+05 2.598400e+02 3.969402e+05 2.680410e+02 3.916161e+05 2.762420e+02 3.861817e+05 2.844430e+02 3.806305e+05 2.926440e+02 3.749557e+05 2.981500e+02 3.594056e+05 3.008450e+02 3.691496e+05 3.090460e+02 3.632039e+05 3.131500e+02 3.535480e+05 3.172470e+02 3.571090e+05 3.254480e+02 3.508546e+05 3.331500e+02 3.363936e+05 3.336490e+02 3.444292e+05 COMM Values for Vapor Pressure, Liquid - f(T) COMM Reference: Carruth + Kobayashi (1973): 1,2,3,4,5,6,7,8,9,10,11 COMM Reference: Willingham + Taylor + Pignocco + Rossini (1945): 12,13,14,15,16,17,18,19,20,21,22,23,24,25 EVPL 1 7 25 1.780200e+02 1.373221e+00 1.814500e+02 2.266481e+00 1.842200e+02 3.213070e+00 1.891600e+02 5.972844e+00 1.972100e+02 1.359888e+01 2.119000e+02 6.412807e+01 2.198600e+02 1.282561e+02 2.383100e+02 6.559462e+02 2.482400e+02 1.263896e+03 2.587600e+02 2.559790e+03 2.649400e+02 3.119744e+03 2.861830e+02 1.169771e+04 2.897260e+02 1.381887e+04 2.937680e+02 1.661997e+04 2.978670e+02 1.991970e+04 3.016780e+02 2.345141e+04 3.067810e+02 2.895629e+04 3.114610e+02 3.489580e+04 3.171170e+02 4.332178e+04 3.229530e+02 5.365560e+04 3.291800e+02 6.675719e+04 3.359350e+02 8.371980e+04 3.407040e+02 9.760533e+04 3.412170e+02 9.920386e+04 3.416900e+02 1.006944e+05 COMM Values for Density, Liquid - f(T) COMM Reference: Beg + Tukur + Al-Harbi + Hamad (1993): 19,23,26,30 COMM Reference: Acosta + Arce + Ageitos + Rodil + Soto (2002): 20 COMM Reference: Rivas + Buep + Iglesias (2015): 16,21,24 COMM Reference: Geist + Cannon (1946): 13,18,27 COMM Reference: Den,l (T): Dippr Equation 105 [MKS]: 2,3,4,5,6,7,8,9,10,11,12,14,15,17,22,25,28,29,31 COMM Reference: Den,l (T): Hankinson + Thomson [MKS]: 1 EDY 1 3 31 1.778300e+02 7.590666e+02 1.860310e+02 7.485750e+02 1.942320e+02 7.423300e+02 2.024330e+02 7.360194e+02 2.106340e+02 7.296404e+02 2.188350e+02 7.231897e+02 2.270360e+02 7.166642e+02 2.352370e+02 7.100601e+02 2.434380e+02 7.033737e+02 2.516390e+02 6.966007e+02 2.598400e+02 6.897366e+02 2.680410e+02 6.827765e+02 2.731500e+02 6.770000e+02 2.762420e+02 6.757150e+02 2.844430e+02 6.685461e+02 2.881500e+02 6.641300e+02 2.926440e+02 6.612634e+02 2.931500e+02 6.590000e+02 2.981500e+02 6.548000e+02 2.981500e+02 6.550700e+02 2.981500e+02 6.551400e+02 3.008450e+02 6.538598e+02 3.031500e+02 6.504000e+02 3.081500e+02 6.461000e+02 3.090460e+02 6.463274e+02 3.131500e+02 6.409000e+02 3.131500e+02 6.410000e+02 3.172470e+02 6.386575e+02 3.254480e+02 6.308403e+02 3.331500e+02 6.221000e+02 3.336490e+02 6.228650e+02 COMM Values for Viscosity, Liquid - f(T) COMM Reference: Visc,l (T): Przezdziecki + Sridhar Method [MKS]: 1 COMM Reference: Geist + Cannon (1946): 13,17,20 COMM Reference: Visc,l (T): Dippr Equation 101 [MKS]: 2,3,4,5,6,7,8,9,10,11,12,14,15,16,18,19,21,22,23 EVIS 1 6 23 1.778300e+02 2.489956e-03 1.860310e+02 1.681389e-03 1.942320e+02 1.365445e-03 2.024330e+02 1.130140e-03 2.106340e+02 9.511338e-04 2.188350e+02 8.123729e-04 2.270360e+02 7.029929e-04 2.352370e+02 6.154721e-04 2.434380e+02 5.444939e-04 2.516390e+02 4.862298e-04 2.598400e+02 4.378753e-04 2.680410e+02 3.973439e-04 2.731500e+02 3.820000e-04 2.762420e+02 3.630612e-04 2.844430e+02 3.338234e-04 2.926440e+02 3.086992e-04 2.931500e+02 3.080000e-04 3.008450e+02 2.869598e-04 3.090460e+02 2.680291e-04 3.131500e+02 2.540000e-04 3.172470e+02 2.514474e-04 3.254480e+02 2.368445e-04 3.336490e+02 2.239198e-04 COMM Values for Viscosity, Vapor - f(T) COMM Reference: Titani (1933): 10,16,20,25 COMM Reference: Craven + Lambert (1951): 3 COMM Reference: Visc,v (T): Dippr Equation 102 [MKS]: 1,2,5,6,7,8,9,11,12,13,14,15,17,18,19,21,22,23,24,26 COMM Reference: Lambert + Cotton + Pailthorpe + Robinson + Scrivins + Vale + Young (1955): 4 EVV 1 6 26 3.418500e+02 7.465059e-06 3.501325e+02 7.651167e-06 3.509500e+02 7.950000e-06 3.511500e+02 7.750000e-06 3.584150e+02 7.836446e-06 3.666975e+02 8.020885e-06 3.749800e+02 8.204473e-06 3.832625e+02 8.387203e-06 3.915450e+02 8.569068e-06 3.938500e+02 8.660000e-06 3.998275e+02 8.750060e-06 4.081100e+02 8.930175e-06 4.163925e+02 9.109409e-06 4.246750e+02 9.287759e-06 4.329575e+02 9.465222e-06 4.339500e+02 9.580000e-06 4.412400e+02 9.641797e-06 4.495225e+02 9.817482e-06 4.578050e+02 9.992277e-06 4.620500e+02 1.021000e-05 4.660875e+02 1.016618e-05 4.743700e+02 1.033920e-05 4.826525e+02 1.051133e-05 4.909350e+02 1.068257e-05 4.932500e+02 1.088000e-05 4.992175e+02 1.085293e-05 COMM ----- End: n-Hexane ----- ENDC STRC COMM ----- Start: Toluene ----- COMM Descriptive Properties NAME Toluene FRM C7H8 CASNO 108-88-3 SYN ASPEN:C7H8 SYN Benzene, methyl SYN MBDS:Cmp00605 SYN Methylbenzene SYN Toluol COMM Structural Groups IDG1 12 NGI1 1 IDG2 10 NGI2 5 COMM Constant Properties WM 92.141 TC 1 591.75 PC 7 4.108e+06 VC 3 0.316 LSGF 7 1.23684e+06 HGIB 7 1.32654e+06 LSHF 7 130344 HFOR 7 542647 HVP 7 361609 SOL 0 8.94654 TBOL 1 383.78 MP 1 178.159 DPM 1 1.20083e-30 WI 0.263 COMM Values for Thermal Conductivity, Liquid - f(T) COMM Reference: Qun-Fang + Rui-Sen + Dan-Yan + Yu-Chun (1997): 2,4,5,8,9,14 COMM Reference: Nagasaka + Nagashima (1981): 7,11,17,21,24 COMM Reference: Wu + Liu + Jin + Pan (2005): 1,3,6,10,15,19,25,26 COMM Reference: DiGullio + McGregor + Teja (1992): 12,13,16,18,20,22,23 ELTC 1 1 26 2.346000e+02 1.477000e-01 2.531500e+02 1.434000e-01 2.545800e+02 1.434000e-01 2.631500e+02 1.407000e-01 2.731500e+02 1.385000e-01 2.731700e+02 1.374000e-01 2.745800e+02 1.374000e-01 2.831500e+02 1.343000e-01 2.931500e+02 1.318000e-01 2.932300e+02 1.334000e-01 2.968900e+02 1.308000e-01 2.985000e+02 1.306000e-01 2.989000e+02 1.306000e-01 3.031500e+02 1.302000e-01 3.146800e+02 1.264000e-01 3.152000e+02 1.259000e-01 3.170500e+02 1.251000e-01 3.253000e+02 1.232000e-01 3.349900e+02 1.211000e-01 3.366000e+02 1.192000e-01 3.410000e+02 1.180000e-01 3.536000e+02 1.137000e-01 3.547000e+02 1.131000e-01 3.548800e+02 1.140000e-01 3.548900e+02 1.136000e-01 3.739200e+02 1.105000e-01 COMM Values for Thermal Conductivity, Vapor - f(T) COMM Reference: ThrmCnd,v (T): Dippr Equation 102 [MKS]: 1,2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20 EVTC 1 1 20 3.837800e+02 1.900736e-02 3.941785e+02 1.997072e-02 4.045770e+02 2.095240e-02 4.149755e+02 2.195207e-02 4.253740e+02 2.296942e-02 4.357725e+02 2.400414e-02 4.461710e+02 2.505593e-02 4.565695e+02 2.612449e-02 4.669680e+02 2.720956e-02 4.773665e+02 2.831085e-02 4.877650e+02 2.942809e-02 4.981635e+02 3.056103e-02 5.085620e+02 3.170942e-02 5.189605e+02 3.287300e-02 5.293590e+02 3.405153e-02 5.397575e+02 3.524479e-02 5.501560e+02 3.645255e-02 5.605545e+02 3.767458e-02 5.709530e+02 3.891067e-02 5.813515e+02 4.016061e-02 COMM Values for Heat Capacity - Isobaric, Liquid - f(T) COMM Reference: Cp,l (T): Poling + Prausnitz + O'Connell CSP Method [MKS]: 1 COMM Reference: Cp,l (T): Dippr Equation 100 [MKS]: 2,3,4,5,6,7,8,9,10,11,12,13,16,20,23,25,26,27,28,29 COMM Reference: Becker + Aufderhaar + Gmehling (2000): 14,15,17,18,19,21,22,24 ECPL 1 7 29 1.781590e+02 1.370608e+03 1.884400e+02 1.475593e+03 1.987211e+02 1.485415e+03 2.090021e+02 1.498259e+03 2.192832e+02 1.513931e+03 2.295642e+02 1.532232e+03 2.398453e+02 1.552968e+03 2.501263e+02 1.575941e+03 2.604074e+02 1.600955e+03 2.706884e+02 1.627814e+03 2.809695e+02 1.656321e+03 2.912505e+02 1.686279e+03 3.015316e+02 1.717494e+03 3.020500e+02 1.713135e+03 3.070500e+02 1.729740e+03 3.118126e+02 1.749767e+03 3.125000e+02 1.747431e+03 3.170000e+02 1.762950e+03 3.219500e+02 1.780423e+03 3.220937e+02 1.782903e+03 3.269500e+02 1.804734e+03 3.319500e+02 1.813742e+03 3.323747e+02 1.816705e+03 3.369500e+02 1.834145e+03 3.426558e+02 1.850977e+03 3.529368e+02 1.885523e+03 3.632179e+02 1.920145e+03 3.734989e+02 1.954649e+03 3.837800e+02 1.988836e+03 COMM Values for Heat Capacity - Isobaric, Vapor - f(T) COMM Reference: Cp,v (T): Dippr Equation 107 [MKS]: 1,2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20 ECPV 1 7 20 3.837800e+02 1.474113e+03 3.941785e+02 1.511747e+03 4.045770e+02 1.548594e+03 4.149755e+02 1.584668e+03 4.253740e+02 1.619988e+03 4.357725e+02 1.654575e+03 4.461710e+02 1.688452e+03 4.565695e+02 1.721645e+03 4.669680e+02 1.754177e+03 4.773665e+02 1.786073e+03 4.877650e+02 1.817357e+03 4.981635e+02 1.848050e+03 5.085620e+02 1.878174e+03 5.189605e+02 1.907748e+03 5.293590e+02 1.936791e+03 5.397575e+02 1.965320e+03 5.501560e+02 1.993349e+03 5.605545e+02 2.020893e+03 5.709530e+02 2.047966e+03 5.813515e+02 2.074578e+03 COMM Values for Surface Tension, Liquid - f(T) COMM Reference: Donaldson + Quayle (1950): 15,19,23 COMM Reference: SurfTn,l (T): Sastri + Rao Method [MKS]: 1 COMM Reference: Kahl + Wadewitz + Winkelmann (2003): 11,13,16,18,20,22,24,26,28 COMM Reference: SurfTn,l (T): Dippr Equation 106 [MKS]: 2,3,4,5,6,7,8,9,10,12,14,17,21,25,27,29,30,31,32,33 ESUR 1 2 33 1.781590e+02 4.194923e-02 1.884400e+02 4.146769e-02 1.987211e+02 4.015514e-02 2.090021e+02 3.885099e-02 2.192832e+02 3.755542e-02 2.295642e+02 3.626861e-02 2.398453e+02 3.499073e-02 2.501263e+02 3.372200e-02 2.604074e+02 3.246260e-02 2.706884e+02 3.121277e-02 2.778500e+02 3.011000e-02 2.809695e+02 2.997274e-02 2.878100e+02 2.893000e-02 2.912505e+02 2.874273e-02 2.931500e+02 2.853000e-02 2.978200e+02 2.776000e-02 3.015316e+02 2.752303e-02 3.028300e+02 2.717000e-02 3.031500e+02 2.732000e-02 3.078600e+02 2.660000e-02 3.118126e+02 2.631389e-02 3.128700e+02 2.603000e-02 3.131500e+02 2.615000e-02 3.178600e+02 2.546000e-02 3.220937e+02 2.511560e-02 3.278800e+02 2.429000e-02 3.323747e+02 2.392849e-02 3.378800e+02 2.322000e-02 3.426558e+02 2.275289e-02 3.529368e+02 2.158914e-02 3.632179e+02 2.043763e-02 3.734989e+02 1.929879e-02 3.837800e+02 1.817304e-02 COMM Values for Enthalpy of Vaporization - f(T) COMM Reference: Majer + Svoboda (1985): 13,14,19,22 COMM Reference: Hv (T): Dippr Equation 106 [MKS]: 2,3,4,5,6,7,8,9,10,11,12,15,16,17,18,20,21,23,24,25 COMM Reference: Hv (T): Watson Relation [MKS]: 1 EDHV 1 7 25 1.781590e+02 4.695656e+05 1.884400e+02 4.699685e+05 1.987211e+02 4.653387e+05 2.090021e+02 4.606335e+05 2.192832e+02 4.558498e+05 2.295642e+02 4.509839e+05 2.398453e+02 4.460322e+05 2.501263e+02 4.409903e+05 2.604074e+02 4.358541e+05 2.706884e+02 4.306186e+05 2.809695e+02 4.252786e+05 2.912505e+02 4.198286e+05 2.982000e+02 4.123029e+05 2.982000e+02 4.083958e+05 3.015316e+02 4.142624e+05 3.118126e+02 4.085732e+05 3.220937e+02 4.027537e+05 3.323747e+02 3.967957e+05 3.413000e+02 3.869070e+05 3.426558e+02 3.906903e+05 3.529368e+02 3.844274e+05 3.611000e+02 3.747517e+05 3.632179e+02 3.779960e+05 3.734989e+02 3.713835e+05 3.837800e+02 3.645762e+05 COMM Values for Vapor Pressure, Liquid - f(T) COMM Reference: Pvp,l (T): Antoine Equation - PGL 2001 [MKS]: 15,17,19,21,23,24,25,26,27,28 COMM Reference: Munday + Mullins + Edie (1980): 11,12,14,16,18,20,22 COMM Reference: Pvp,l (T): Gómez-Nieto + Thodos Equation [MKS]: 1 COMM Reference: Pvp,l (T): Dippr Equation 101 [MKS]: 2,3,4,5,6,7,8,9,10,13 EVPL 1 7 28 1.781590e+02 3.238010e-02 1.884400e+02 2.130835e-01 1.987211e+02 9.161197e-01 2.090021e+02 3.346083e+00 2.192832e+02 1.063702e+01 2.295642e+02 3.001872e+01 2.398453e+02 7.644254e+01 2.501263e+02 1.780479e+02 2.604074e+02 3.836461e+02 2.706884e+02 7.721109e+02 2.731500e+02 9.012594e+02 2.792100e+02 1.309226e+03 2.809695e+02 1.463252e+03 2.841700e+02 1.762522e+03 2.912505e+02 2.620426e+03 2.931400e+02 2.903762e+03 3.015316e+02 4.505526e+03 3.030400e+02 4.863601e+03 3.118126e+02 7.417115e+03 3.127500e+02 7.743365e+03 3.220937e+02 1.174966e+04 3.224100e+02 1.186969e+04 3.323747e+02 1.798775e+04 3.426558e+02 2.671060e+04 3.529368e+02 3.859394e+04 3.632179e+02 5.440932e+04 3.734989e+02 7.502091e+04 3.837800e+02 1.013800e+05 COMM Values for Density, Liquid - f(T) COMM Reference: Donaldson + Quayle (1950): 3,12,17 COMM Reference: Song + Shen + Zhao + Wang + Wang (2008): 11,16,22,23,25,27,28 COMM Reference: Yang + Liu + Lai + Ma (2007): 8,10,19,26,30,31,33 COMM Reference: Prak + Ye + McLaughlin + Cowart + Trulove (2017): 5,13,21,24,29,32 COMM Reference: Geist + Cannon (1946): 1,4,18 COMM Reference: Nikam + Kharat (2005): 7,9,15,20 COMM Reference: Ritzoulis + Papadopoulos + Jannakoudakis (1986): 2,6,14 EDY 1 3 33 2.731500e+02 8.830000e+02 2.881500e+02 8.716000e+02 2.931500e+02 8.669600e+02 2.931500e+02 8.650000e+02 2.931500e+02 8.668400e+02 2.981500e+02 8.623000e+02 2.981500e+02 8.622000e+02 2.981500e+02 8.630100e+02 3.031500e+02 8.576000e+02 3.031500e+02 8.583200e+02 3.031500e+02 8.575000e+02 3.031500e+02 8.576600e+02 3.031500e+02 8.575200e+02 3.081500e+02 8.527000e+02 3.081500e+02 8.530000e+02 3.081500e+02 8.529000e+02 3.131500e+02 8.483600e+02 3.131500e+02 8.480000e+02 3.131500e+02 8.489200e+02 3.131500e+02 8.482000e+02 3.131500e+02 8.481400e+02 3.131500e+02 8.479000e+02 3.181500e+02 8.435000e+02 3.231500e+02 8.386800e+02 3.231500e+02 8.387000e+02 3.231500e+02 8.394500e+02 3.281500e+02 8.340000e+02 3.331500e+02 8.291000e+02 3.331500e+02 8.291500e+02 3.331500e+02 8.299300e+02 3.431500e+02 8.203000e+02 3.431500e+02 8.196000e+02 3.531500e+02 8.105400e+02 COMM Values for Viscosity, Liquid - f(T) COMM Reference: Song + Shen + Zhao + Wang + Wang (2008): 10,14,17,19,21,23,26 COMM Reference: Yang + Liu + Lai + Ma (2007): 6,9,15,22,24,28,29 COMM Reference: Prak + Ye + McLaughlin + Cowart + Trulove (2017): 4,11,16,20,25,27 COMM Reference: Geist + Cannon (1946): 1,3,18 COMM Reference: Nikam + Kharat (2005): 5,8,12 COMM Reference: Ritzoulis + Papadopoulos + Jannakoudakis (1986): 2,7,13 EVIS 1 6 29 2.731500e+02 7.740000e-04 2.881500e+02 6.230000e-04 2.931500e+02 5.850000e-04 2.931500e+02 6.070000e-04 2.981500e+02 5.580000e-04 2.981500e+02 5.540000e-04 2.981500e+02 5.560000e-04 3.031500e+02 5.260000e-04 3.031500e+02 5.250000e-04 3.031500e+02 5.253000e-04 3.031500e+02 5.400000e-04 3.081500e+02 4.960000e-04 3.081500e+02 4.920000e-04 3.081500e+02 4.933000e-04 3.131500e+02 4.700000e-04 3.131500e+02 4.830000e-04 3.131500e+02 4.717000e-04 3.131500e+02 4.650000e-04 3.181500e+02 4.491000e-04 3.231500e+02 4.340000e-04 3.231500e+02 4.244000e-04 3.231500e+02 4.230000e-04 3.281500e+02 4.082000e-04 3.331500e+02 3.850000e-04 3.331500e+02 3.910000e-04 3.331500e+02 3.835000e-04 3.431500e+02 3.490000e-04 3.431500e+02 3.500000e-04 3.531500e+02 3.230000e-04 COMM Values for Viscosity, Vapor - f(T) COMM Reference: Visc,v (T): Dippr Equation 102 [MKS]: 1,2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20 EVV 1 6 20 3.837800e+02 9.085665e-06 3.941785e+02 9.323063e-06 4.045770e+02 9.560241e-06 4.149755e+02 9.797204e-06 4.253740e+02 1.003396e-05 4.357725e+02 1.027051e-05 4.461710e+02 1.050686e-05 4.565695e+02 1.074302e-05 4.669680e+02 1.097899e-05 4.773665e+02 1.121477e-05 4.877650e+02 1.145038e-05 4.981635e+02 1.168580e-05 5.085620e+02 1.192106e-05 5.189605e+02 1.215614e-05 5.293590e+02 1.239106e-05 5.397575e+02 1.262581e-05 5.501560e+02 1.286041e-05 5.605545e+02 1.309485e-05 5.709530e+02 1.332914e-05 5.813515e+02 1.356328e-05 COMM ----- End: Toluene ----- ENDC STRC COMM ----- Start: Vinyl chloride ----- COMM Descriptive Properties NAME Vinyl chloride FRM C2H3Cl CASNO 75-01-4 SYN ASPEN:C2H3CL SYN Chloroethene SYN Chloroethylene SYN MBDS:Cmp00634 COMM Structural Groups IDG1 70 NGI1 1 IDG2 5 NGI2 1 COMM Constant Properties WM 62.499 TC 1 429 PC 7 5.3e+06 VC 3 0.181 HGIB 7 900494 LSHF 7 80368.9 HFOR 7 401286 HVP 7 342298 SOL 0 7.79045 TBOL 1 259.78 MP 1 119.31 DPM 1 4.83668e-30 WI 0.0975745 COMM Values for Thermal Conductivity, Liquid - f(T) COMM Reference: ThrmCnd,l (T): Missenard + Riedel Method [MKS]: 1 COMM Reference: ThrmCnd,l (T): Dippr Equation 100 [MKS]: 2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20 ELTC 1 1 20 1.193100e+02 1.516998e-01 1.263335e+02 1.494095e-01 1.333570e+02 1.473263e-01 1.403805e+02 1.452431e-01 1.474040e+02 1.431600e-01 1.544275e+02 1.410768e-01 1.614510e+02 1.389936e-01 1.684745e+02 1.369105e-01 1.754980e+02 1.348273e-01 1.825215e+02 1.327441e-01 1.895450e+02 1.306610e-01 1.965685e+02 1.285778e-01 2.035920e+02 1.264946e-01 2.106155e+02 1.244114e-01 2.176390e+02 1.223283e-01 2.246625e+02 1.202451e-01 2.316860e+02 1.181619e-01 2.387095e+02 1.160788e-01 2.457330e+02 1.139956e-01 2.527565e+02 1.119124e-01 COMM Values for Thermal Conductivity, Vapor - f(T) COMM Reference: ThrmCnd,v (T): Dippr Equation 102 [MKS]: 1,2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20 EVTC 1 1 20 2.597800e+02 9.655895e-03 2.682410e+02 1.018098e-02 2.767020e+02 1.071518e-02 2.851630e+02 1.125825e-02 2.936240e+02 1.180993e-02 3.020850e+02 1.237000e-02 3.105460e+02 1.293822e-02 3.190070e+02 1.351438e-02 3.274680e+02 1.409827e-02 3.359290e+02 1.468969e-02 3.443900e+02 1.528842e-02 3.528510e+02 1.589430e-02 3.613120e+02 1.650712e-02 3.697730e+02 1.712671e-02 3.782340e+02 1.775290e-02 3.866950e+02 1.838552e-02 3.951560e+02 1.902441e-02 4.036170e+02 1.966941e-02 4.120780e+02 2.032037e-02 4.205390e+02 2.097713e-02 COMM Values for Heat Capacity - Isobaric, Liquid - f(T) COMM Reference: Cp,l (T): Poling + Prausnitz + O'Connell CSP Method [MKS]: 1,2,3,4,5,6,7,8,9,10,11,12 COMM Reference: Cp,l (T): Dippr Equation 100 [MKS]: 13,14,15,16,17,18,19,20 ECPL 1 7 20 1.193100e+02 1.120552e+03 1.263335e+02 1.123219e+03 1.333570e+02 1.127531e+03 1.403805e+02 1.133240e+03 1.474040e+02 1.140145e+03 1.544275e+02 1.148086e+03 1.614510e+02 1.156933e+03 1.684745e+02 1.166581e+03 1.754980e+02 1.176945e+03 1.825215e+02 1.187958e+03 1.895450e+02 1.199563e+03 1.965685e+02 1.211721e+03 2.035920e+02 8.864061e+02 2.106155e+02 9.226817e+02 2.176390e+02 9.589573e+02 2.246625e+02 9.952328e+02 2.316860e+02 1.031508e+03 2.387095e+02 1.067784e+03 2.457330e+02 1.104059e+03 2.527565e+02 1.140335e+03 COMM Values for Heat Capacity - Isobaric, Vapor - f(T) COMM Reference: Cp,v (T): Dippr Equation 107 [MKS]: 1,2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20 ECPV 1 7 20 2.597800e+02 7.925319e+02 2.682410e+02 8.065807e+02 2.767020e+02 8.210708e+02 2.851630e+02 8.359184e+02 2.936240e+02 8.510442e+02 3.020850e+02 8.663742e+02 3.105460e+02 8.818402e+02 3.190070e+02 8.973805e+02 3.274680e+02 9.129395e+02 3.359290e+02 9.284680e+02 3.443900e+02 9.439231e+02 3.528510e+02 9.592676e+02 3.613120e+02 9.744698e+02 3.697730e+02 9.895032e+02 3.782340e+02 1.004346e+03 3.866950e+02 1.018980e+03 3.951560e+02 1.033392e+03 4.036170e+02 1.047571e+03 4.120780e+02 1.061510e+03 4.205390e+02 1.075203e+03 COMM Values for Surface Tension, Liquid - f(T) COMM Reference: SurfTn,l (T): Sastri + Rao Method [MKS]: 1 COMM Reference: SurfTn,l (T): Dippr Equation 106 [MKS]: 2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20 ESUR 1 2 20 1.193100e+02 4.263201e-02 1.263335e+02 4.507909e-02 1.333570e+02 4.375373e-02 1.403805e+02 4.243687e-02 1.474040e+02 4.112867e-02 1.544275e+02 3.982929e-02 1.614510e+02 3.853888e-02 1.684745e+02 3.725762e-02 1.754980e+02 3.598569e-02 1.825215e+02 3.472327e-02 1.895450e+02 3.347056e-02 1.965685e+02 3.222778e-02 2.035920e+02 3.099513e-02 2.106155e+02 2.977285e-02 2.176390e+02 2.856117e-02 2.246625e+02 2.736036e-02 2.316860e+02 2.617069e-02 2.387095e+02 2.499244e-02 2.457330e+02 2.382591e-02 2.527565e+02 2.267145e-02 COMM Values for Enthalpy of Vaporization - f(T) COMM Reference: Hv (T): Dippr Equation 106 [MKS]: 2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20 COMM Reference: Hv (T): Watson Relation [MKS]: 1 EDHV 1 7 20 1.193100e+02 4.306699e+05 1.263335e+02 4.809672e+05 1.333570e+02 4.755493e+05 1.403805e+02 4.700643e+05 1.474040e+02 4.645099e+05 1.544275e+02 4.588832e+05 1.614510e+02 4.531816e+05 1.684745e+02 4.474020e+05 1.754980e+02 4.415411e+05 1.825215e+02 4.355957e+05 1.895450e+02 4.295618e+05 1.965685e+02 4.234357e+05 2.035920e+02 4.172130e+05 2.106155e+02 4.108892e+05 2.176390e+02 4.044591e+05 2.246625e+02 3.979176e+05 2.316860e+02 3.912585e+05 2.387095e+02 3.844757e+05 2.457330e+02 3.775620e+05 2.527565e+02 3.705098e+05 COMM Values for Vapor Pressure, Liquid - f(T) COMM Reference: Pvp,l (T): Gómez-Nieto + Thodos Equation [MKS]: 1 COMM Reference: Dana + Burdick + Jenkins (1927): 19,21,23,24 COMM Reference: Pvp,l (T): Dippr Equation 101 [MKS]: 2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,20,22 EVPL 1 7 24 1.193100e+02 1.285814e-01 1.263335e+02 1.021765e-01 1.333570e+02 5.096854e-01 1.403805e+02 2.101402e+00 1.474040e+02 7.375267e+00 1.544275e+02 2.256810e+01 1.614510e+02 6.139982e+01 1.684745e+02 1.509456e+02 1.754980e+02 3.398639e+02 1.825215e+02 7.088057e+02 1.895450e+02 1.382384e+03 1.965685e+02 2.541719e+03 2.035920e+02 4.436385e+03 2.106155e+02 7.394594e+03 2.176390e+02 1.183068e+04 2.246625e+02 1.824929e+04 2.316860e+02 2.724602e+04 2.387095e+02 3.950479e+04 2.444200e+02 5.274234e+04 2.457330e+02 5.579233e+04 2.501300e+02 6.839439e+04 2.527565e+02 7.695045e+04 2.565400e+02 9.033926e+04 2.595400e+02 1.023249e+05 COMM Values for Density, Liquid - f(T) COMM Reference: Den,l (T): Dippr Equation 105 [MKS]: 2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20 COMM Reference: Den,l (T): Hankinson + Thomson [MKS]: 1 EDY 1 3 20 1.193100e+02 1.165180e+03 1.263335e+02 1.146601e+03 1.333570e+02 1.138049e+03 1.403805e+02 1.129415e+03 1.474040e+02 1.120695e+03 1.544275e+02 1.111885e+03 1.614510e+02 1.102984e+03 1.684745e+02 1.093985e+03 1.754980e+02 1.084886e+03 1.825215e+02 1.075681e+03 1.895450e+02 1.066366e+03 1.965685e+02 1.056936e+03 2.035920e+02 1.047385e+03 2.106155e+02 1.037706e+03 2.176390e+02 1.027894e+03 2.246625e+02 1.017941e+03 2.316860e+02 1.007839e+03 2.387095e+02 9.975801e+02 2.457330e+02 9.871545e+02 2.527565e+02 9.765520e+02 COMM Values for Viscosity, Liquid - f(T) COMM Reference: Visc,l (T): Przezdziecki + Sridhar Method [MKS]: 1,2 COMM Reference: Visc,l (T): Dippr Equation 101 [MKS]: 3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20 EVIS 1 6 20 1.193100e+02 2.704236e-03 1.263335e+02 1.943767e-03 1.333570e+02 2.258717e-03 1.403805e+02 1.869472e-03 1.474040e+02 1.567570e-03 1.544275e+02 1.329578e-03 1.614510e+02 1.139243e-03 1.684745e+02 9.850472e-04 1.754980e+02 8.586770e-04 1.825215e+02 7.540246e-04 1.895450e+02 6.665340e-04 1.965685e+02 5.927588e-04 2.035920e+02 5.300579e-04 2.106155e+02 4.763834e-04 2.176390e+02 4.301303e-04 2.246625e+02 3.900280e-04 2.316860e+02 3.550613e-04 2.387095e+02 3.244121e-04 2.457330e+02 2.974160e-04 2.527565e+02 2.735290e-04 COMM Values for Viscosity, Vapor - f(T) COMM Reference: Visc,v (T): Dippr Equation 102 [MKS]: 1,2,3,4,5,6,7,8,9,10,11,12,13,14,15,16,17,18,19,20 EVV 1 6 20 2.597800e+02 8.874175e-06 2.682410e+02 9.178717e-06 2.767020e+02 9.481466e-06 2.851630e+02 9.782408e-06 2.936240e+02 1.008153e-05 3.020850e+02 1.037883e-05 3.105460e+02 1.067431e-05 3.190070e+02 1.096797e-05 3.274680e+02 1.125982e-05 3.359290e+02 1.154986e-05 3.443900e+02 1.183810e-05 3.528510e+02 1.212456e-05 3.613120e+02 1.240925e-05 3.697730e+02 1.269218e-05 3.782340e+02 1.297337e-05 3.866950e+02 1.325284e-05 3.951560e+02 1.353060e-05 4.036170e+02 1.380667e-05 4.120780e+02 1.408108e-05 4.205390e+02 1.435383e-05 COMM ----- End: Vinyl chloride ----- ENDC COMM End of neutral file ENDF