Mixture of n-Propyl acetate + Thiophene, tetrahydro-, 1,1-dioxide

Excel

n-Propyl acetate

Name
n-Propyl acetate
InChI
InChI=1S/C5H10O2/c1-3-4-7-5(2)6/h3-4H2,1-2H3
InChI Key
YKYONYBAUNKHLG-UHFFFAOYSA-N
Formula
C5H10O2
SMILES
CCCOC(C)=O
Mol. Weight (g/mol)
102.13
CAS
109-60-4

Thiophene, tetrahydro-, 1,1-dioxide

Name
Thiophene, tetrahydro-, 1,1-dioxide
InChI
InChI=1S/C4H8O2S/c5-7(6)3-1-2-4-7/h1-4H2
InChI Key
HXJUTPCZVOIRIF-UHFFFAOYSA-N
Formula
C4H8O2S
SMILES
O=S1(=O)CCCC1
Mol. Weight (g/mol)
120.17
CAS
126-33-0
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)
  2. ρl - Mass density, kg/m3 (2)
  3. csound,fluid - Speed of Sound, m/s (2)

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Thiophene, tetrahydro-, 1,1-dioxide (2) - Liquid Viscosity, Pa*s - Liquid
303.15 0.0000 0.0005
303.15 0.0247 0.0005
303.15 0.1746 0.0007
303.15 0.3110 0.0010
303.15 0.4416 0.0014
303.15 0.5468 0.0019
303.15 0.6489 0.0026
303.15 0.7639 0.0039
303.15 0.8733 0.0059
303.15 0.9823 0.0093
303.15 1.0000 0.0100
308.15 0.0000 0.0005
308.15 0.0247 0.0005
308.15 0.1746 0.0007
308.15 0.3110 0.0009
308.15 0.4416 0.0013
308.15 0.5468 0.0018
308.15 0.6489 0.0024
308.15 0.7639 0.0035
308.15 0.8733 0.0052
308.15 0.9823 0.0081
308.15 1.0000 0.0088
313.15 0.0000 0.0004
313.15 0.0247 0.0005
313.15 0.1746 0.0006
313.15 0.3110 0.0009
313.15 0.4416 0.0012
313.15 0.5468 0.0016
313.15 0.6489 0.0022
313.15 0.7639 0.0032
313.15 0.8733 0.0047
313.15 0.9823 0.0072
313.15 1.0000 0.0078

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Thiophene, tetrahydro-, 1,1-dioxide (2) - Liquid Viscosity, Pa*s - Liquid
303.15 0.0000 0.0005
303.15 0.0247 0.0005
303.15 0.1746 0.0007
303.15 0.3110 0.0010
303.15 0.4416 0.0014
303.15 0.5468 0.0019
303.15 0.6489 0.0026
303.15 0.7639 0.0039
303.15 0.8733 0.0059
303.15 0.9823 0.0093
303.15 1.0000 0.0100
308.15 0.0000 0.0005
308.15 0.0247 0.0005
308.15 0.1746 0.0007
308.15 0.3110 0.0009
308.15 0.4416 0.0013
308.15 0.5468 0.0018
308.15 0.6489 0.0024
308.15 0.7639 0.0035
308.15 0.8733 0.0052
308.15 0.9823 0.0081
308.15 1.0000 0.0088
313.15 0.0000 0.0004
313.15 0.0247 0.0005
313.15 0.1746 0.0006
313.15 0.3110 0.0009
313.15 0.4416 0.0012
313.15 0.5468 0.0016
313.15 0.6489 0.0022
313.15 0.7639 0.0032
313.15 0.8733 0.0047
313.15 0.9823 0.0072
313.15 1.0000 0.0078

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Thiophene, tetrahydro-, 1,1-dioxide (2) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0000 883.7
303.15 0.0000 877.7
303.15 0.0247 886.9
303.15 0.1746 941.4
303.15 0.3110 992.9
303.15 0.4416 1043.1
303.15 0.5468 1084.6
303.15 0.6489 1124.9
303.15 0.7639 1169.5
303.15 0.8733 1212.3
303.15 0.9823 1255.4
303.15 1.0000 1261.8
308.15 0.0000 873.1
308.15 0.0247 881.9
308.15 0.1746 935.8
308.15 0.3110 986.9
308.15 0.4416 1037.9
308.15 0.5468 1079.6
308.15 0.6489 1120.1
308.15 0.7639 1164.7
308.15 0.8733 1207.6
308.15 0.9823 1251.0
308.15 1.0000 1257.0
313.15 0.0000 866.7
313.15 0.0247 875.7
313.15 0.1746 929.8
313.15 0.3110 981.3
313.15 0.4416 1032.4
313.15 0.5468 1074.0
313.15 0.6489 1114.1
313.15 0.7639 1159.4
313.15 0.8733 1202.2
313.15 0.9823 1245.4
313.15 1.0000 1251.6

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Thiophene, tetrahydro-, 1,1-dioxide (2) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0000 883.7
303.15 0.0000 877.7
303.15 0.0247 886.9
303.15 0.1746 941.4
303.15 0.3110 992.9
303.15 0.4416 1043.1
303.15 0.5468 1084.6
303.15 0.6489 1124.9
303.15 0.7639 1169.5
303.15 0.8733 1212.3
303.15 0.9823 1255.4
303.15 1.0000 1261.8
308.15 0.0000 873.1
308.15 0.0247 881.9
308.15 0.1746 935.8
308.15 0.3110 986.9
308.15 0.4416 1037.9
308.15 0.5468 1079.6
308.15 0.6489 1120.1
308.15 0.7639 1164.7
308.15 0.8733 1207.6
308.15 0.9823 1251.0
308.15 1.0000 1257.0
313.15 0.0000 866.7
313.15 0.0247 875.7
313.15 0.1746 929.8
313.15 0.3110 981.3
313.15 0.4416 1032.4
313.15 0.5468 1074.0
313.15 0.6489 1114.1
313.15 0.7639 1159.4
313.15 0.8733 1202.2
313.15 0.9823 1245.4
313.15 1.0000 1251.6

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Thiophene, tetrahydro-, 1,1-dioxide (2) - Liquid Speed of sound, m/s - Liquid
298.15 0.0000 1156.0
303.15 0.0000 1149.0
303.15 0.0247 1154.0
303.15 0.1746 1214.0
303.15 0.3110 1266.0
303.15 0.4416 1322.0
303.15 0.5468 1368.0
303.15 0.6489 1419.0
303.15 0.7639 1474.0
303.15 0.8733 1530.0
303.15 0.9823 1579.0
303.15 1.0000 1588.0
308.15 0.0000 1139.0
308.15 0.0247 1147.0
308.15 0.1746 1203.0
308.15 0.3110 1257.0
308.15 0.4416 1312.0
308.15 0.5468 1359.0
308.15 0.6489 1410.0
308.15 0.7639 1469.0
308.15 0.8733 1521.0
308.15 0.9823 1573.0
308.15 1.0000 1576.0
313.15 0.0000 1126.0
313.15 0.0247 1134.0
313.15 0.1746 1189.0
313.15 0.3110 1243.0
313.15 0.4416 1301.0
313.15 0.5468 1352.0
313.15 0.6489 1401.0
313.15 0.7639 1458.0
313.15 0.8733 1510.0
313.15 0.9823 1555.0
313.15 1.0000 1558.0

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Thiophene, tetrahydro-, 1,1-dioxide (2) - Liquid Speed of sound, m/s - Liquid
298.15 0.0000 1156.0
303.15 0.0000 1149.0
303.15 0.0247 1154.0
303.15 0.1746 1214.0
303.15 0.3110 1266.0
303.15 0.4416 1322.0
303.15 0.5468 1368.0
303.15 0.6489 1419.0
303.15 0.7639 1474.0
303.15 0.8733 1530.0
303.15 0.9823 1579.0
303.15 1.0000 1588.0
308.15 0.0000 1139.0
308.15 0.0247 1147.0
308.15 0.1746 1203.0
308.15 0.3110 1257.0
308.15 0.4416 1312.0
308.15 0.5468 1359.0
308.15 0.6489 1410.0
308.15 0.7639 1469.0
308.15 0.8733 1521.0
308.15 0.9823 1573.0
308.15 1.0000 1576.0
313.15 0.0000 1126.0
313.15 0.0247 1134.0
313.15 0.1746 1189.0
313.15 0.3110 1243.0
313.15 0.4416 1301.0
313.15 0.5468 1352.0
313.15 0.6489 1401.0
313.15 0.7639 1458.0
313.15 0.8733 1510.0
313.15 0.9823 1555.0
313.15 1.0000 1558.0

Sources