Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Monoethanolamine (1) - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 0.0000 | 0.0056 |
| 298.15 | 0.1619 | 0.0083 |
| 298.15 | 0.2973 | 0.0104 |
| 298.15 | 0.4258 | 0.0121 |
| 298.15 | 0.5307 | 0.0139 |
| 298.15 | 0.6308 | 0.0155 |
| 298.15 | 0.7174 | 0.0168 |
| 298.15 | 0.7980 | 0.0182 |
| 298.15 | 0.8790 | 0.0192 |
| 298.15 | 0.9336 | 0.0193 |
| 298.15 | 1.0000 | 0.0187 |
| 303.15 | 0.0000 | 0.0045 |
| 303.15 | 0.1619 | 0.0066 |
| 303.15 | 0.2973 | 0.0083 |
| 303.15 | 0.4258 | 0.0098 |
| 303.15 | 0.5307 | 0.0112 |
| 303.15 | 0.6308 | 0.0125 |
| 303.15 | 0.7174 | 0.0136 |
| 303.15 | 0.7980 | 0.0147 |
| 303.15 | 0.8790 | 0.0155 |
| 303.15 | 0.9336 | 0.0155 |
| 303.15 | 1.0000 | 0.0152 |
| 308.15 | 0.0000 | 0.0039 |
| 308.15 | 0.1619 | 0.0054 |
| 308.15 | 0.2973 | 0.0067 |
| 308.15 | 0.4258 | 0.0078 |
| 308.15 | 0.5307 | 0.0089 |
| 308.15 | 0.6308 | 0.0100 |
| 308.15 | 0.7174 | 0.0109 |
| 308.15 | 0.7980 | 0.0118 |
| 308.15 | 0.8790 | 0.0124 |
| 308.15 | 0.9336 | 0.0123 |
| 308.15 | 1.0000 | 0.0119 |
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Monoethanolamine (1) - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 0.0000 | 0.0056 |
| 298.15 | 0.1619 | 0.0083 |
| 298.15 | 0.2973 | 0.0104 |
| 298.15 | 0.4258 | 0.0121 |
| 298.15 | 0.5307 | 0.0139 |
| 298.15 | 0.6308 | 0.0155 |
| 298.15 | 0.7174 | 0.0168 |
| 298.15 | 0.7980 | 0.0182 |
| 298.15 | 0.8790 | 0.0192 |
| 298.15 | 0.9336 | 0.0193 |
| 298.15 | 1.0000 | 0.0187 |
| 303.15 | 0.0000 | 0.0045 |
| 303.15 | 0.1619 | 0.0066 |
| 303.15 | 0.2973 | 0.0083 |
| 303.15 | 0.4258 | 0.0098 |
| 303.15 | 0.5307 | 0.0112 |
| 303.15 | 0.6308 | 0.0125 |
| 303.15 | 0.7174 | 0.0136 |
| 303.15 | 0.7980 | 0.0147 |
| 303.15 | 0.8790 | 0.0155 |
| 303.15 | 0.9336 | 0.0155 |
| 303.15 | 1.0000 | 0.0152 |
| 308.15 | 0.0000 | 0.0039 |
| 308.15 | 0.1619 | 0.0054 |
| 308.15 | 0.2973 | 0.0067 |
| 308.15 | 0.4258 | 0.0078 |
| 308.15 | 0.5307 | 0.0089 |
| 308.15 | 0.6308 | 0.0100 |
| 308.15 | 0.7174 | 0.0109 |
| 308.15 | 0.7980 | 0.0118 |
| 308.15 | 0.8790 | 0.0124 |
| 308.15 | 0.9336 | 0.0123 |
| 308.15 | 1.0000 | 0.0119 |
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Monoethanolamine (1) - Liquid | Refractive index (Na D-line) - Liquid |
| 298.15 | 0.0000 | 1.4822 |
| 298.15 | 0.0989 | 1.4815 |
| 298.15 | 0.2021 | 1.4806 |
| 298.15 | 0.3013 | 1.4794 |
| 298.15 | 0.4007 | 1.4778 |
| 298.15 | 0.4984 | 1.4758 |
| 298.15 | 0.6007 | 1.4731 |
| 298.15 | 0.7027 | 1.4696 |
| 298.15 | 0.8002 | 1.4657 |
| 298.15 | 0.8987 | 1.4608 |
| 298.15 | 1.0000 | 1.4535 |
| 303.15 | 0.0000 | 1.4808 |
| 303.15 | 0.0989 | 1.4802 |
| 303.15 | 0.2021 | 1.4791 |
| 303.15 | 0.3013 | 1.4778 |
| 303.15 | 0.4007 | 1.4764 |
| 303.15 | 0.4984 | 1.4743 |
| 303.15 | 0.6007 | 1.4717 |
| 303.15 | 0.7027 | 1.4683 |
| 303.15 | 0.8002 | 1.4643 |
| 303.15 | 0.8987 | 1.4591 |
| 303.15 | 1.0000 | 1.4519 |
| 308.15 | 0.0000 | 1.4793 |
| 308.15 | 0.0989 | 1.4791 |
| 308.15 | 0.2021 | 1.4778 |
| 308.15 | 0.3013 | 1.4765 |
| 308.15 | 0.4007 | 1.4752 |
| 308.15 | 0.4984 | 1.4729 |
| 308.15 | 0.6007 | 1.4703 |
| 308.15 | 0.7027 | 1.467 |
| 308.15 | 0.8002 | 1.4631 |
| 308.15 | 0.8987 | 1.4577 |
| 308.15 | 1.0000 | 1.4505 |
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Monoethanolamine (1) - Liquid | Refractive index (Na D-line) - Liquid |
| 298.15 | 0.0000 | 1.4822 |
| 298.15 | 0.0989 | 1.4815 |
| 298.15 | 0.2021 | 1.4806 |
| 298.15 | 0.3013 | 1.4794 |
| 298.15 | 0.4007 | 1.4778 |
| 298.15 | 0.4984 | 1.4758 |
| 298.15 | 0.6007 | 1.4731 |
| 298.15 | 0.7027 | 1.4696 |
| 298.15 | 0.8002 | 1.4657 |
| 298.15 | 0.8987 | 1.4608 |
| 298.15 | 1.0000 | 1.4535 |
| 303.15 | 0.0000 | 1.4808 |
| 303.15 | 0.0989 | 1.4802 |
| 303.15 | 0.2021 | 1.4791 |
| 303.15 | 0.3013 | 1.4778 |
| 303.15 | 0.4007 | 1.4764 |
| 303.15 | 0.4984 | 1.4743 |
| 303.15 | 0.6007 | 1.4717 |
| 303.15 | 0.7027 | 1.4683 |
| 303.15 | 0.8002 | 1.4643 |
| 303.15 | 0.8987 | 1.4591 |
| 303.15 | 1.0000 | 1.4519 |
| 308.15 | 0.0000 | 1.4793 |
| 308.15 | 0.0989 | 1.4791 |
| 308.15 | 0.2021 | 1.4778 |
| 308.15 | 0.3013 | 1.4765 |
| 308.15 | 0.4007 | 1.4752 |
| 308.15 | 0.4984 | 1.4729 |
| 308.15 | 0.6007 | 1.4703 |
| 308.15 | 0.7027 | 1.467 |
| 308.15 | 0.8002 | 1.4631 |
| 308.15 | 0.8987 | 1.4577 |
| 308.15 | 1.0000 | 1.4505 |
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Monoethanolamine (1) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.0000 | 945.8 |
| 298.15 | 0.1619 | 956.5 |
| 298.15 | 0.2973 | 964.6 |
| 298.15 | 0.4258 | 972.6 |
| 298.15 | 0.5307 | 979.4 |
| 298.15 | 0.6308 | 986.3 |
| 298.15 | 0.7174 | 992.7 |
| 298.15 | 0.7980 | 998.7 |
| 298.15 | 0.8790 | 1005.1 |
| 298.15 | 0.9336 | 1008.9 |
| 298.15 | 1.0000 | 1012.4 |
| 303.15 | 0.0000 | 942.1 |
| 303.15 | 0.1619 | 953.1 |
| 303.15 | 0.2973 | 961.1 |
| 303.15 | 0.4258 | 969.0 |
| 303.15 | 0.5307 | 975.9 |
| 303.15 | 0.6308 | 982.8 |
| 303.15 | 0.7174 | 989.2 |
| 303.15 | 0.7980 | 995.5 |
| 303.15 | 0.8790 | 1001.7 |
| 303.15 | 0.9336 | 1005.6 |
| 303.15 | 1.0000 | 1008.4 |
| 308.15 | 0.0000 | 937.8 |
| 308.15 | 0.1619 | 949.1 |
| 308.15 | 0.2973 | 957.1 |
| 308.15 | 0.4258 | 965.3 |
| 308.15 | 0.5307 | 972.3 |
| 308.15 | 0.6308 | 979.2 |
| 308.15 | 0.7174 | 985.6 |
| 308.15 | 0.7980 | 992.0 |
| 308.15 | 0.8790 | 998.5 |
| 308.15 | 0.9336 | 1002.4 |
| 308.15 | 1.0000 | 1004.5 |
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Monoethanolamine (1) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.0000 | 945.8 |
| 298.15 | 0.1619 | 956.5 |
| 298.15 | 0.2973 | 964.6 |
| 298.15 | 0.4258 | 972.6 |
| 298.15 | 0.5307 | 979.4 |
| 298.15 | 0.6308 | 986.3 |
| 298.15 | 0.7174 | 992.7 |
| 298.15 | 0.7980 | 998.7 |
| 298.15 | 0.8790 | 1005.1 |
| 298.15 | 0.9336 | 1008.9 |
| 298.15 | 1.0000 | 1012.4 |
| 303.15 | 0.0000 | 942.1 |
| 303.15 | 0.1619 | 953.1 |
| 303.15 | 0.2973 | 961.1 |
| 303.15 | 0.4258 | 969.0 |
| 303.15 | 0.5307 | 975.9 |
| 303.15 | 0.6308 | 982.8 |
| 303.15 | 0.7174 | 989.2 |
| 303.15 | 0.7980 | 995.5 |
| 303.15 | 0.8790 | 1001.7 |
| 303.15 | 0.9336 | 1005.6 |
| 303.15 | 1.0000 | 1008.4 |
| 308.15 | 0.0000 | 937.8 |
| 308.15 | 0.1619 | 949.1 |
| 308.15 | 0.2973 | 957.1 |
| 308.15 | 0.4258 | 965.3 |
| 308.15 | 0.5307 | 972.3 |
| 308.15 | 0.6308 | 979.2 |
| 308.15 | 0.7174 | 985.6 |
| 308.15 | 0.7980 | 992.0 |
| 308.15 | 0.8790 | 998.5 |
| 308.15 | 0.9336 | 1002.4 |
| 308.15 | 1.0000 | 1004.5 |