Mixture of Triethylene glycol + Dimethyl Sulfoxide + Sulfur dioxide

Excel

Triethylene glycol

Name
Triethylene glycol
InChI
InChI=1S/C6H14O4/c7-1-3-9-5-6-10-4-2-8/h7-8H,1-6H2
InChI Key
ZIBGPFATKBEMQZ-UHFFFAOYSA-N
Formula
C6H14O4
SMILES
OCCOCCOCCO
Mol. Weight (g/mol)
150.17
CAS
112-27-6

Dimethyl Sulfoxide

Name
Dimethyl Sulfoxide
InChI
InChI=1S/C2H6OS/c1-4(2)3/h1-2H3
InChI Key
IAZDPXIOMUYVGZ-UHFFFAOYSA-N
Formula
C2H6OS
SMILES
CS(C)=O
Mol. Weight (g/mol)
78.13
CAS
67-68-5

Sulfur dioxide

Name
Sulfur dioxide
InChI
InChI=1S/O2S/c1-3-2
InChI Key
RAHZWNYVWXNFOC-UHFFFAOYSA-N
Formula
O2S
SMILES
O=S=O
Mol. Weight (g/mol)
64.06
CAS
7446-09-5
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. Partial pressure, kPa (2)

Partial pressure, kPa of Sulfur dioxide (3) [ref]

Fixed Measured
Temperature, K - Liquid Molality, mol/kg of Sulfur dioxide (3) - Liquid Solvent: Mass fraction of Triethylene glycol (1) - Liquid Partial pressure, kPa of Sulfur dioxide (3) - Gas
298.15 0.0008 1.0000 0.01
298.15 0.0012 1.0000 0.01
298.15 0.0016 1.0000 0.01
298.15 0.0022 1.0000 0.02
298.15 0.0040 1.0000 0.04
298.15 0.0046 1.0000 0.05
298.15 0.0052 1.0000 0.06
298.15 0.0057 1.0000 0.07
298.15 0.0066 1.0000 0.07
298.15 0.0073 1.0000 0.08
298.15 0.0083 1.0000 0.09
298.15 0.0094 1.0000 0.11
298.15 0.0113 1.0000 0.13
298.15 0.0015 0.8000 0.01
298.15 0.0026 0.8000 0.02
298.15 0.0035 0.8000 0.03
298.15 0.0046 0.8000 0.03
298.15 0.0073 0.8000 0.05
298.15 0.0082 0.8000 0.06
298.15 0.0097 0.8000 0.07
298.15 0.0112 0.8000 0.08
298.15 0.0127 0.8000 0.09
298.15 0.0144 0.8000 0.10
298.15 0.0162 0.8000 0.11
298.15 0.0188 0.8000 0.13
298.15 0.0013 0.7000 0.01
298.15 0.0034 0.7000 0.02
298.15 0.0086 0.7000 0.05
298.15 0.0105 0.7000 0.06
298.15 0.0117 0.7000 0.06
298.15 0.0132 0.7000 0.07
298.15 0.0148 0.7000 0.08
298.15 0.0166 0.7000 0.09
298.15 0.0166 0.7000 0.09
298.15 0.0183 0.7000 0.10
298.15 0.0214 0.7000 0.11
298.15 0.0236 0.7000 0.12
298.15 0.0261 0.7000 0.14
298.15 0.0025 0.6000 0.01
298.15 0.0039 0.6000 0.02
298.15 0.0061 0.6000 0.03
298.15 0.0079 0.6000 0.03
298.15 0.0100 0.6000 0.04
303.15 0.0009 1.0000 0.01
303.15 0.0014 1.0000 0.01
303.15 0.0022 1.0000 0.02
303.15 0.0028 1.0000 0.03
303.15 0.0040 1.0000 0.05
303.15 0.0051 1.0000 0.07
303.15 0.0065 1.0000 0.09
303.15 0.0079 1.0000 0.11
303.15 0.0091 1.0000 0.12
303.15 0.0098 1.0000 0.13
303.15 0.0025 0.8000 0.01
303.15 0.0037 0.8000 0.03
303.15 0.0047 0.8000 0.04
303.15 0.0057 0.8000 0.05
303.15 0.0073 0.8000 0.06
303.15 0.0089 0.8000 0.07
303.15 0.0105 0.8000 0.09
303.15 0.0115 0.8000 0.10
303.15 0.0128 0.8000 0.11
303.15 0.0141 0.8000 0.12
303.15 0.0014 0.7000 0.01
303.15 0.0023 0.7000 0.01
303.15 0.0034 0.7000 0.02
303.15 0.0052 0.7000 0.04
303.15 0.0065 0.7000 0.05
303.15 0.0078 0.7000 0.06
303.15 0.0096 0.7000 0.07
303.15 0.0116 0.7000 0.08
303.15 0.0131 0.7000 0.09
303.15 0.0152 0.7000 0.10
303.15 0.0171 0.7000 0.12
303.15 0.0188 0.7000 0.13
303.15 0.0019 0.6000 0.01
303.15 0.0047 0.6000 0.02
303.15 0.0061 0.6000 0.03
303.15 0.0086 0.6000 0.04
303.15 0.0112 0.6000 0.06
303.15 0.0141 0.6000 0.07
303.15 0.0172 0.6000 0.09
303.15 0.0195 0.6000 0.10
308.15 0.0004 1.0000 0.01
308.15 0.0012 1.0000 0.02
308.15 0.0018 1.0000 0.03
308.15 0.0027 1.0000 0.04
308.15 0.0034 1.0000 0.05
308.15 0.0045 1.0000 0.07
308.15 0.0053 1.0000 0.09
308.15 0.0059 1.0000 0.10
308.15 0.0069 1.0000 0.11
308.15 0.0080 1.0000 0.13
308.15 0.0014 0.8000 0.02
308.15 0.0024 0.8000 0.03
308.15 0.0037 0.8000 0.04
308.15 0.0053 0.8000 0.05
308.15 0.0072 0.8000 0.07
308.15 0.0081 0.8000 0.09
308.15 0.0098 0.8000 0.10
308.15 0.0117 0.8000 0.12
308.15 0.0126 0.8000 0.13
308.15 0.0020 0.7000 0.02
308.15 0.0034 0.7000 0.03
308.15 0.0046 0.7000 0.04
308.15 0.0045 0.7000 0.04
308.15 0.0061 0.7000 0.05
308.15 0.0094 0.7000 0.08
308.15 0.0111 0.7000 0.09
308.15 0.0126 0.7000 0.11
308.15 0.0156 0.7000 0.13
308.15 0.0032 0.6000 0.03
308.15 0.0044 0.6000 0.04
308.15 0.0056 0.6000 0.04
308.15 0.0067 0.6000 0.05
308.15 0.0081 0.6000 0.06
308.15 0.0100 0.6000 0.07
308.15 0.0118 0.6000 0.08

Partial pressure, kPa of Sulfur dioxide (3) [ref]

Fixed Measured
Temperature, K - Liquid Molality, mol/kg of Sulfur dioxide (3) - Liquid Solvent: Mass fraction of Triethylene glycol (1) - Liquid Partial pressure, kPa of Sulfur dioxide (3) - Gas
298.15 0.0008 1.0000 0.01
298.15 0.0012 1.0000 0.01
298.15 0.0016 1.0000 0.01
298.15 0.0022 1.0000 0.02
298.15 0.0040 1.0000 0.04
298.15 0.0046 1.0000 0.05
298.15 0.0052 1.0000 0.06
298.15 0.0057 1.0000 0.07
298.15 0.0066 1.0000 0.07
298.15 0.0073 1.0000 0.08
298.15 0.0083 1.0000 0.09
298.15 0.0094 1.0000 0.11
298.15 0.0113 1.0000 0.13
298.15 0.0015 0.8000 0.01
298.15 0.0026 0.8000 0.02
298.15 0.0035 0.8000 0.03
298.15 0.0046 0.8000 0.03
298.15 0.0073 0.8000 0.05
298.15 0.0082 0.8000 0.06
298.15 0.0097 0.8000 0.07
298.15 0.0112 0.8000 0.08
298.15 0.0127 0.8000 0.09
298.15 0.0144 0.8000 0.10
298.15 0.0162 0.8000 0.11
298.15 0.0188 0.8000 0.13
298.15 0.0013 0.7000 0.01
298.15 0.0034 0.7000 0.02
298.15 0.0086 0.7000 0.05
298.15 0.0105 0.7000 0.06
298.15 0.0117 0.7000 0.06
298.15 0.0132 0.7000 0.07
298.15 0.0148 0.7000 0.08
298.15 0.0166 0.7000 0.09
298.15 0.0166 0.7000 0.09
298.15 0.0183 0.7000 0.10
298.15 0.0214 0.7000 0.11
298.15 0.0236 0.7000 0.12
298.15 0.0261 0.7000 0.14
298.15 0.0025 0.6000 0.01
298.15 0.0039 0.6000 0.02
298.15 0.0061 0.6000 0.03
298.15 0.0079 0.6000 0.03
298.15 0.0100 0.6000 0.04
303.15 0.0009 1.0000 0.01
303.15 0.0014 1.0000 0.01
303.15 0.0022 1.0000 0.02
303.15 0.0028 1.0000 0.03
303.15 0.0040 1.0000 0.05
303.15 0.0051 1.0000 0.07
303.15 0.0065 1.0000 0.09
303.15 0.0079 1.0000 0.11
303.15 0.0091 1.0000 0.12
303.15 0.0098 1.0000 0.13
303.15 0.0025 0.8000 0.01
303.15 0.0037 0.8000 0.03
303.15 0.0047 0.8000 0.04
303.15 0.0057 0.8000 0.05
303.15 0.0073 0.8000 0.06
303.15 0.0089 0.8000 0.07
303.15 0.0105 0.8000 0.09
303.15 0.0115 0.8000 0.10
303.15 0.0128 0.8000 0.11
303.15 0.0141 0.8000 0.12
303.15 0.0014 0.7000 0.01
303.15 0.0023 0.7000 0.01
303.15 0.0034 0.7000 0.02
303.15 0.0052 0.7000 0.04
303.15 0.0065 0.7000 0.05
303.15 0.0078 0.7000 0.06
303.15 0.0096 0.7000 0.07
303.15 0.0116 0.7000 0.08
303.15 0.0131 0.7000 0.09
303.15 0.0152 0.7000 0.10
303.15 0.0171 0.7000 0.12
303.15 0.0188 0.7000 0.13
303.15 0.0019 0.6000 0.01
303.15 0.0047 0.6000 0.02
303.15 0.0061 0.6000 0.03
303.15 0.0086 0.6000 0.04
303.15 0.0112 0.6000 0.06
303.15 0.0141 0.6000 0.07
303.15 0.0172 0.6000 0.09
303.15 0.0195 0.6000 0.10
308.15 0.0004 1.0000 0.01
308.15 0.0012 1.0000 0.02
308.15 0.0018 1.0000 0.03
308.15 0.0027 1.0000 0.04
308.15 0.0034 1.0000 0.05
308.15 0.0045 1.0000 0.07
308.15 0.0053 1.0000 0.09
308.15 0.0059 1.0000 0.10
308.15 0.0069 1.0000 0.11
308.15 0.0080 1.0000 0.13
308.15 0.0014 0.8000 0.02
308.15 0.0024 0.8000 0.03
308.15 0.0037 0.8000 0.04
308.15 0.0053 0.8000 0.05
308.15 0.0072 0.8000 0.07
308.15 0.0081 0.8000 0.09
308.15 0.0098 0.8000 0.10
308.15 0.0117 0.8000 0.12
308.15 0.0126 0.8000 0.13
308.15 0.0020 0.7000 0.02
308.15 0.0034 0.7000 0.03
308.15 0.0046 0.7000 0.04
308.15 0.0045 0.7000 0.04
308.15 0.0061 0.7000 0.05
308.15 0.0094 0.7000 0.08
308.15 0.0111 0.7000 0.09
308.15 0.0126 0.7000 0.11
308.15 0.0156 0.7000 0.13
308.15 0.0032 0.6000 0.03
308.15 0.0044 0.6000 0.04
308.15 0.0056 0.6000 0.04
308.15 0.0067 0.6000 0.05
308.15 0.0081 0.6000 0.06
308.15 0.0100 0.6000 0.07
308.15 0.0118 0.6000 0.08

Sources