Mixture of Propane, 1-chloro-2-methyl- + Propane, 2-methoxy-2-methyl-

Excel

Propane, 1-chloro-2-methyl-

Name
Propane, 1-chloro-2-methyl-
InChI
InChI=1S/C4H9Cl/c1-4(2)3-5/h4H,3H2,1-2H3
InChI Key
QTBFPMKWQKYFLR-UHFFFAOYSA-N
Formula
C4H9Cl
SMILES
CC(C)CCl
Mol. Weight (g/mol)
92.57
CAS
513-36-0

Propane, 2-methoxy-2-methyl-

Name
Propane, 2-methoxy-2-methyl-
InChI
InChI=1S/C5H12O/c1-5(2,3)6-4/h1-4H3
InChI Key
BZLVMXJERCGZMT-UHFFFAOYSA-N
Formula
C5H12O
SMILES
COC(C)(C)C
Mol. Weight (g/mol)
88.15
CAS
1634-04-4
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. η - Viscosity, Pa*s (2)

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Propane, 1-chloro-2-methyl- (1) - Liquid Viscosity, Pa*s - Liquid
283.15 0.0000 0.0004
283.15 0.0492 0.0004
283.15 0.0996 0.0004
283.15 0.1979 0.0004
283.15 0.3023 0.0004
283.15 0.4027 0.0004
283.15 0.5040 0.0004
283.15 0.5971 0.0005
283.15 0.7036 0.0005
283.15 0.8003 0.0005
283.15 0.9031 0.0005
283.15 0.9522 0.0005
283.15 1.0000 0.0005
288.15 0.0000 0.0004
288.15 0.0492 0.0004
288.15 0.0996 0.0004
288.15 0.1979 0.0004
288.15 0.3023 0.0004
288.15 0.4027 0.0004
288.15 0.5040 0.0004
288.15 0.5971 0.0004
288.15 0.7036 0.0004
288.15 0.8003 0.0005
288.15 0.9031 0.0005
288.15 0.9522 0.0005
288.15 1.0000 0.0005
293.15 0.0000 0.0003
293.15 0.0492 0.0004
293.15 0.0996 0.0004
293.15 0.1979 0.0004
293.15 0.3023 0.0004
293.15 0.4027 0.0004
293.15 0.5040 0.0004
293.15 0.5971 0.0004
293.15 0.7036 0.0004
293.15 0.8003 0.0004
293.15 0.9031 0.0004
293.15 0.9522 0.0004
293.15 1.0000 0.0005
298.15 0.0000 0.0003
298.15 0.0492 0.0003
298.15 0.0996 0.0003
298.15 0.1979 0.0003
298.15 0.3023 0.0004
298.15 0.4027 0.0004
298.15 0.5040 0.0004
298.15 0.5971 0.0004
298.15 0.7036 0.0004
298.15 0.8003 0.0004
298.15 0.9031 0.0004
298.15 0.9522 0.0004
298.15 1.0000 0.0004
303.15 0.0000 0.0003
303.15 0.0492 0.0003
303.15 0.0996 0.0003
303.15 0.1979 0.0003
303.15 0.3023 0.0003
303.15 0.4027 0.0004
303.15 0.5040 0.0004
303.15 0.5971 0.0004
303.15 0.7036 0.0004
303.15 0.8003 0.0004
303.15 0.9031 0.0004
303.15 0.9522 0.0004
303.15 1.0000 0.0004
308.15 0.0000 0.0003
308.15 0.0492 0.0003
308.15 0.0996 0.0003
308.15 0.1979 0.0003
308.15 0.3023 0.0003
308.15 0.4027 0.0003
308.15 0.5040 0.0003
308.15 0.5971 0.0004
308.15 0.7036 0.0004
308.15 0.8003 0.0004
308.15 0.9031 0.0004
308.15 0.9522 0.0004
308.15 1.0000 0.0004
313.15 0.0000 0.0003
313.15 0.0492 0.0003
313.15 0.0996 0.0003
313.15 0.1979 0.0003
313.15 0.3023 0.0003
313.15 0.4027 0.0003
313.15 0.5040 0.0003
313.15 0.5971 0.0003
313.15 0.7036 0.0003
313.15 0.8003 0.0004
313.15 0.9031 0.0004
313.15 0.9522 0.0004
313.15 1.0000 0.0004

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Propane, 1-chloro-2-methyl- (1) - Liquid Viscosity, Pa*s - Liquid
283.15 0.0000 0.0004
283.15 0.0492 0.0004
283.15 0.0996 0.0004
283.15 0.1979 0.0004
283.15 0.3023 0.0004
283.15 0.4027 0.0004
283.15 0.5040 0.0004
283.15 0.5971 0.0005
283.15 0.7036 0.0005
283.15 0.8003 0.0005
283.15 0.9031 0.0005
283.15 0.9522 0.0005
283.15 1.0000 0.0005
288.15 0.0000 0.0004
288.15 0.0492 0.0004
288.15 0.0996 0.0004
288.15 0.1979 0.0004
288.15 0.3023 0.0004
288.15 0.4027 0.0004
288.15 0.5040 0.0004
288.15 0.5971 0.0004
288.15 0.7036 0.0004
288.15 0.8003 0.0005
288.15 0.9031 0.0005
288.15 0.9522 0.0005
288.15 1.0000 0.0005
293.15 0.0000 0.0003
293.15 0.0492 0.0004
293.15 0.0996 0.0004
293.15 0.1979 0.0004
293.15 0.3023 0.0004
293.15 0.4027 0.0004
293.15 0.5040 0.0004
293.15 0.5971 0.0004
293.15 0.7036 0.0004
293.15 0.8003 0.0004
293.15 0.9031 0.0004
293.15 0.9522 0.0004
293.15 1.0000 0.0005
298.15 0.0000 0.0003
298.15 0.0492 0.0003
298.15 0.0996 0.0003
298.15 0.1979 0.0003
298.15 0.3023 0.0004
298.15 0.4027 0.0004
298.15 0.5040 0.0004
298.15 0.5971 0.0004
298.15 0.7036 0.0004
298.15 0.8003 0.0004
298.15 0.9031 0.0004
298.15 0.9522 0.0004
298.15 1.0000 0.0004
303.15 0.0000 0.0003
303.15 0.0492 0.0003
303.15 0.0996 0.0003
303.15 0.1979 0.0003
303.15 0.3023 0.0003
303.15 0.4027 0.0004
303.15 0.5040 0.0004
303.15 0.5971 0.0004
303.15 0.7036 0.0004
303.15 0.8003 0.0004
303.15 0.9031 0.0004
303.15 0.9522 0.0004
303.15 1.0000 0.0004
308.15 0.0000 0.0003
308.15 0.0492 0.0003
308.15 0.0996 0.0003
308.15 0.1979 0.0003
308.15 0.3023 0.0003
308.15 0.4027 0.0003
308.15 0.5040 0.0003
308.15 0.5971 0.0004
308.15 0.7036 0.0004
308.15 0.8003 0.0004
308.15 0.9031 0.0004
308.15 0.9522 0.0004
308.15 1.0000 0.0004
313.15 0.0000 0.0003
313.15 0.0492 0.0003
313.15 0.0996 0.0003
313.15 0.1979 0.0003
313.15 0.3023 0.0003
313.15 0.4027 0.0003
313.15 0.5040 0.0003
313.15 0.5971 0.0003
313.15 0.7036 0.0003
313.15 0.8003 0.0004
313.15 0.9031 0.0004
313.15 0.9522 0.0004
313.15 1.0000 0.0004

Sources