please re-login

Mixture of Diisopropyl ether + Ethane, 1,2-dichloro-

Excel

Diisopropyl ether

Name
Diisopropyl ether
InChI
InChI=1S/C6H14O/c1-5(2)7-6(3)4/h5-6H,1-4H3
InChI Key
ZAFNJMIOTHYJRJ-UHFFFAOYSA-N
Formula
C6H14O
SMILES
CC(C)OC(C)C
Mol. Weight (g/mol)
102.17
CAS
108-20-3

Ethane, 1,2-dichloro-

Name
Ethane, 1,2-dichloro-
InChI
InChI=1S/C2H4Cl2/c3-1-2-4/h1-2H2
InChI Key
WSLDOOZREJYCGB-UHFFFAOYSA-N
Formula
C2H4Cl2
SMILES
ClCCCl
Mol. Weight (g/mol)
98.96
CAS
107-06-2
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry. Do not hesitate to contact us for your projects.

Datasets

  1. Pvap - Vapor or sublimation pressure, kPa (2)

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethane, 1,2-dichloro- (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
284.84 0.8630 6.98
284.85 0.8630 6.98
284.86 0.3580 9.39
284.86 0.5386 8.64
284.86 0.6874 8.64
284.86 0.3580 9.39
284.88 0.6874 7.91
284.89 0.6874 7.92
294.79 0.8630 11.43
294.80 0.1574 16.67
294.80 0.8630 11.44
294.81 0.5386 14.05
294.82 0.5386 14.05
294.83 0.3580 15.22
294.83 0.6874 12.89
294.83 0.6874 12.90
294.84 0.3580 15.21
304.76 0.8630 18.06
304.76 0.8630 18.05
304.78 0.1574 25.55
304.78 0.3580 23.71
304.78 0.1574 25.55
304.79 0.3580 23.71
304.80 0.5386 22.00
304.81 0.5386 22.00
304.82 0.6874 20.26
304.83 0.6874 20.27
314.74 0.8630 27.54
314.74 0.8630 27.54
314.75 0.1574 38.12
314.76 0.1574 38.12
314.76 0.3580 35.75
314.77 0.3580 35.75
314.77 0.5386 33.30
314.79 0.6874 30.77
314.79 0.6874 30.77
324.76 0.1574 55.43
324.76 0.1574 55.43
324.87 0.8630 40.96
324.88 0.3580 52.56
324.89 0.8630 40.97
324.90 0.3580 52.57
324.91 0.5386 49.13
324.91 0.6874 45.57
324.92 0.6874 45.59
334.76 0.1574 78.59
334.77 0.1574 78.60
334.85 0.8630 58.93
334.85 0.8630 58.90
334.87 0.3580 74.82
334.87 0.6874 65.24
334.88 0.3580 74.83
334.88 0.6874 65.24
334.90 0.5386 70.15
344.83 0.8630 82.70
344.84 0.1574 108.93
344.84 0.3580 103.93
344.86 0.6874 91.24
344.86 0.6874 91.23
344.87 0.1574 109.02
344.89 0.5386 97.77
354.78 0.8630 113.39
354.80 0.8630 113.39
354.81 0.6874 124.72
354.84 0.3580 141.15
354.85 0.5386 133.50

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethane, 1,2-dichloro- (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
284.84 0.8630 6.98
284.85 0.8630 6.98
284.86 0.3580 9.39
284.86 0.5386 8.64
284.86 0.6874 8.64
284.86 0.3580 9.39
284.88 0.6874 7.91
284.89 0.6874 7.92
294.79 0.8630 11.43
294.80 0.1574 16.67
294.80 0.8630 11.44
294.81 0.5386 14.05
294.82 0.5386 14.05
294.83 0.3580 15.22
294.83 0.6874 12.89
294.83 0.6874 12.90
294.84 0.3580 15.21
304.76 0.8630 18.06
304.76 0.8630 18.05
304.78 0.1574 25.55
304.78 0.3580 23.71
304.78 0.1574 25.55
304.79 0.3580 23.71
304.80 0.5386 22.00
304.81 0.5386 22.00
304.82 0.6874 20.26
304.83 0.6874 20.27
314.74 0.8630 27.54
314.74 0.8630 27.54
314.75 0.1574 38.12
314.76 0.1574 38.12
314.76 0.3580 35.75
314.77 0.3580 35.75
314.77 0.5386 33.30
314.79 0.6874 30.77
314.79 0.6874 30.77
324.76 0.1574 55.43
324.76 0.1574 55.43
324.87 0.8630 40.96
324.88 0.3580 52.56
324.89 0.8630 40.97
324.90 0.3580 52.57
324.91 0.5386 49.13
324.91 0.6874 45.57
324.92 0.6874 45.59
334.76 0.1574 78.59
334.77 0.1574 78.60
334.85 0.8630 58.93
334.85 0.8630 58.90
334.87 0.3580 74.82
334.87 0.6874 65.24
334.88 0.3580 74.83
334.88 0.6874 65.24
334.90 0.5386 70.15
344.83 0.8630 82.70
344.84 0.1574 108.93
344.84 0.3580 103.93
344.86 0.6874 91.24
344.86 0.6874 91.23
344.87 0.1574 109.02
344.89 0.5386 97.77
354.78 0.8630 113.39
354.80 0.8630 113.39
354.81 0.6874 124.72
354.84 0.3580 141.15
354.85 0.5386 133.50

Sources