Mixture of Isopropyl Alcohol + Heptane

Excel

Isopropyl Alcohol

Name
Isopropyl Alcohol
InChI
InChI=1S/C3H8O/c1-3(2)4/h3-4H,1-2H3
InChI Key
KFZMGEQAYNKOFK-UHFFFAOYSA-N
Formula
C3H8O
SMILES
CC(C)O
Mol. Weight (g/mol)
60.09
CAS
67-63-0

Heptane

Name
Heptane
InChI
InChI=1S/C7H16/c1-3-5-7-6-4-2/h3-7H2,1-2H3
InChI Key
IMNFDUFMRHMDMM-UHFFFAOYSA-N
Formula
C7H16
SMILES
CCCCCCC
Mol. Weight (g/mol)
100.20
CAS
142-82-5
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Datasets

  1. Mole fraction (2)
  2. Pc - Critical pressure, kPa (2)
  3. Pvap - Vapor or sublimation pressure, kPa (2)
  4. Tc - Critical temperature, K (2)
  5. Binary diffusion coefficient, m2/s (2)

Mole fraction of Heptane (2) [ref]

Fixed Measured
Mole fraction of Heptane (2) - Liquid Temperature, K - Gas Mole fraction of Heptane (2) - Gas
0.0000 483.15 0.0000
0.0000 498.15 0.0000
0.0000 508.15 0.0000
0.0390 483.15 0.0390
0.0390 498.15 0.0390
0.0510 498.15 0.0460
0.0590 483.15 0.0540
0.1010 498.15 0.0940
0.1140 483.15 0.1090
0.1580 498.15 0.1480
0.1620 483.15 0.1510
0.2290 483.15 0.2080
0.2370 498.15 0.2190
0.3100 483.15 0.2660
0.3270 498.15 0.2950
0.4100 508.15 0.4100
0.4210 498.15 0.3650
0.4210 508.15 0.4060
0.4270 483.15 0.3500
0.5170 498.15 0.4330
0.5200 508.15 0.4750
0.5700 483.15 0.4870
0.6100 508.15 0.5300
0.6360 498.15 0.5370
0.6920 483.15 0.5880
0.7130 508.15 0.6320
0.7250 523.15 0.7250
0.7310 523.15 0.7240
0.7430 523.15 0.7140
0.7650 498.15 0.6650
0.7720 523.15 0.7230
0.8140 508.15 0.7320
0.8240 483.15 0.7300
0.8240 523.15 0.7630
0.8820 498.15 0.8060
0.8920 508.15 0.8370
0.8980 523.15 0.8480
0.9080 483.15 0.8530
1.0000 483.15 1.0000
1.0000 498.15 1.0000
1.0000 508.15 1.0000
1.0000 523.15 1.0000

Mole fraction of Heptane (2) [ref]

Fixed Measured
Mole fraction of Heptane (2) - Liquid Temperature, K - Gas Mole fraction of Heptane (2) - Gas
0.0000 483.15 0.0000
0.0000 498.15 0.0000
0.0000 508.15 0.0000
0.0390 483.15 0.0390
0.0390 498.15 0.0390
0.0510 498.15 0.0460
0.0590 483.15 0.0540
0.1010 498.15 0.0940
0.1140 483.15 0.1090
0.1580 498.15 0.1480
0.1620 483.15 0.1510
0.2290 483.15 0.2080
0.2370 498.15 0.2190
0.3100 483.15 0.2660
0.3270 498.15 0.2950
0.4100 508.15 0.4100
0.4210 498.15 0.3650
0.4210 508.15 0.4060
0.4270 483.15 0.3500
0.5170 498.15 0.4330
0.5200 508.15 0.4750
0.5700 483.15 0.4870
0.6100 508.15 0.5300
0.6360 498.15 0.5370
0.6920 483.15 0.5880
0.7130 508.15 0.6320
0.7250 523.15 0.7250
0.7310 523.15 0.7240
0.7430 523.15 0.7140
0.7650 498.15 0.6650
0.7720 523.15 0.7230
0.8140 508.15 0.7320
0.8240 483.15 0.7300
0.8240 523.15 0.7630
0.8820 498.15 0.8060
0.8920 508.15 0.8370
0.8980 523.15 0.8480
0.9080 483.15 0.8530
1.0000 483.15 1.0000
1.0000 498.15 1.0000
1.0000 508.15 1.0000
1.0000 523.15 1.0000

Critical pressure, kPa [ref]

Mole fraction of Heptane (2) - Liquid Critical pressure, kPa - Liquid
0.4100 3967.00
0.7250 3417.00

Critical pressure, kPa [ref]

Mole fraction of Heptane (2) - Liquid Critical pressure, kPa - Liquid
0.4100 3967.00
0.7250 3417.00

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Mole fraction of Heptane (2) - Liquid Temperature, K - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 483.15 3101.00
0.0000 498.15 4009.00
0.0000 508.15 4755.00
0.0390 483.15 3121.00
0.0390 498.15 4021.00
0.0510 498.15 4018.00
0.0590 483.15 3116.00
0.1010 498.15 3980.00
0.1140 483.15 3089.00
0.1580 498.15 3941.00
0.1620 483.15 3041.00
0.2290 483.15 2979.00
0.2370 498.15 3811.00
0.3100 483.15 2889.00
0.3270 498.15 3661.00
0.4100 508.15 3967.00
0.4210 498.15 3437.00
0.4210 508.15 3938.00
0.4270 483.15 2726.00
0.5170 498.15 3192.00
0.5200 508.15 3630.00
0.5700 483.15 2459.00
0.6100 508.15 3329.00
0.6360 498.15 2844.00
0.6920 483.15 2168.00
0.7130 508.15 2963.00
0.7250 523.15 3417.00
0.7310 523.15 3413.00
0.7430 523.15 3381.00
0.7650 498.15 2427.00
0.7720 523.15 3268.00
0.8140 508.15 2520.00
0.8240 483.15 1790.00
0.8240 523.15 3005.00
0.8820 498.15 1970.00
0.8920 508.15 2245.00
0.8980 523.15 2679.00
0.9080 483.15 1514.00
1.0000 483.15 1160.00
1.0000 498.15 1479.00
1.0000 508.15 1725.00
1.0000 523.15 2151.00

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Mole fraction of Heptane (2) - Liquid Temperature, K - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 483.15 3101.00
0.0000 498.15 4009.00
0.0000 508.15 4755.00
0.0390 483.15 3121.00
0.0390 498.15 4021.00
0.0510 498.15 4018.00
0.0590 483.15 3116.00
0.1010 498.15 3980.00
0.1140 483.15 3089.00
0.1580 498.15 3941.00
0.1620 483.15 3041.00
0.2290 483.15 2979.00
0.2370 498.15 3811.00
0.3100 483.15 2889.00
0.3270 498.15 3661.00
0.4100 508.15 3967.00
0.4210 498.15 3437.00
0.4210 508.15 3938.00
0.4270 483.15 2726.00
0.5170 498.15 3192.00
0.5200 508.15 3630.00
0.5700 483.15 2459.00
0.6100 508.15 3329.00
0.6360 498.15 2844.00
0.6920 483.15 2168.00
0.7130 508.15 2963.00
0.7250 523.15 3417.00
0.7310 523.15 3413.00
0.7430 523.15 3381.00
0.7650 498.15 2427.00
0.7720 523.15 3268.00
0.8140 508.15 2520.00
0.8240 483.15 1790.00
0.8240 523.15 3005.00
0.8820 498.15 1970.00
0.8920 508.15 2245.00
0.8980 523.15 2679.00
0.9080 483.15 1514.00
1.0000 483.15 1160.00
1.0000 498.15 1479.00
1.0000 508.15 1725.00
1.0000 523.15 2151.00

Critical temperature, K [ref]

Mole fraction of Heptane (2) - Liquid Critical temperature, K - Liquid
0.4100 508.15
0.7250 523.15

Critical temperature, K [ref]

Mole fraction of Heptane (2) - Liquid Critical temperature, K - Liquid
0.4100 508.15
0.7250 523.15

Binary diffusion coefficient, m2/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mass fraction of Isopropyl Alcohol (1) - Liquid Binary diffusion coefficient, m2/s - Liquid
283.15 0.0500 0.0000
283.15 0.1500 0.0000
283.15 0.2500 0.0000
283.15 0.3500 0.0000
283.15 0.4500 0.0000
283.15 0.5500 0.0000
283.15 0.6500 0.0000
283.15 0.7500 0.0000
283.15 0.8500 0.0000
283.15 0.9500 0.0000
293.15 0.0500 0.0000
293.15 0.1500 0.0000
293.15 0.2500 0.0000
293.15 0.3500 0.0000
293.15 0.4500 0.0000
293.15 0.5500 0.0000
293.15 0.6500 0.0000
293.15 0.7500 0.0000
293.15 0.8500 0.0000
293.15 0.9500 0.0000
303.15 0.0500 0.0000
303.15 0.1500 0.0000
303.15 0.2500 0.0000
303.15 0.3500 0.0000
303.15 0.4500 0.0000
303.15 0.5500 0.0000
303.15 0.6500 0.0000
303.15 0.7500 0.0000
303.15 0.8500 0.0000
303.15 0.9500 0.0000
313.15 0.0500 0.0000
313.15 0.1500 0.0000
313.15 0.2500 0.0000
313.15 0.3500 0.0000
313.15 0.4500 0.0000
313.15 0.5500 0.0000
313.15 0.6500 0.0000
313.15 0.7500 0.0000
313.15 0.8500 0.0000
313.15 0.9500 0.0000
323.15 0.0500 0.0000
323.15 0.1500 0.0000
323.15 0.2500 0.0000
323.15 0.3500 0.0000
323.15 0.4500 0.0000
323.15 0.5500 0.0000
323.15 0.6500 0.0000
323.15 0.7500 0.0000
323.15 0.8500 0.0000
323.15 0.9500 0.0000

Binary diffusion coefficient, m2/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mass fraction of Isopropyl Alcohol (1) - Liquid Binary diffusion coefficient, m2/s - Liquid
283.15 0.0500 0.0000
283.15 0.1500 0.0000
283.15 0.2500 0.0000
283.15 0.3500 0.0000
283.15 0.4500 0.0000
283.15 0.5500 0.0000
283.15 0.6500 0.0000
283.15 0.7500 0.0000
283.15 0.8500 0.0000
283.15 0.9500 0.0000
293.15 0.0500 0.0000
293.15 0.1500 0.0000
293.15 0.2500 0.0000
293.15 0.3500 0.0000
293.15 0.4500 0.0000
293.15 0.5500 0.0000
293.15 0.6500 0.0000
293.15 0.7500 0.0000
293.15 0.8500 0.0000
293.15 0.9500 0.0000
303.15 0.0500 0.0000
303.15 0.1500 0.0000
303.15 0.2500 0.0000
303.15 0.3500 0.0000
303.15 0.4500 0.0000
303.15 0.5500 0.0000
303.15 0.6500 0.0000
303.15 0.7500 0.0000
303.15 0.8500 0.0000
303.15 0.9500 0.0000
313.15 0.0500 0.0000
313.15 0.1500 0.0000
313.15 0.2500 0.0000
313.15 0.3500 0.0000
313.15 0.4500 0.0000
313.15 0.5500 0.0000
313.15 0.6500 0.0000
313.15 0.7500 0.0000
313.15 0.8500 0.0000
313.15 0.9500 0.0000
323.15 0.0500 0.0000
323.15 0.1500 0.0000
323.15 0.2500 0.0000
323.15 0.3500 0.0000
323.15 0.4500 0.0000
323.15 0.5500 0.0000
323.15 0.6500 0.0000
323.15 0.7500 0.0000
323.15 0.8500 0.0000
323.15 0.9500 0.0000

Sources