- InChI
- InChI=1S/C3H9NO/c1-3(5)2-4/h3,5H,2,4H2,1H3
- InChI Key
- HXKKHQJGJAFBHI-UHFFFAOYSA-N
- Formula
- C3H9NO
- SMILES
- CC(O)CN
- Molecular Weight1
- 75.11
- CAS
- 78-96-6
- Other Names
-
- (.+/-.)-1-Amino-2-propanol
- (RS)-1-Amino-2-hydroxypropane
- .alpha.-aminoisopropyl alcohol
- 1-Amino-2-hydroxypropane
- 1-Amino-2-propanol
- 1-Aminoisopropylalcohol
- 1-Aminopropanol-(2)
- 1-Methyl-2-aminoethanol
- 1-aminopropan-2-ol
- 2-Amino-1-methylethanol
- 2-Hydroxy-1-propylamine
- 2-Hydroxypropanamine
- 2-Hydroxypropylamine
- 2-Propanol, 1-amino-, (.+/-.)-
- Isopropanolamine
- MIPA
- Monoisopropanolamine
- NSC 3188
- Threamine
- dl-1-Amino-2-propanol
- «alpha»-Aminoisopropyl alcohol
- «alpha»-Aminoisopropyl alcohol
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| η | 0.0232590 | Pa×s | Densiti... |
| ΔfG° | -98.43 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -228.97 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 9.29 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 49.20 | kJ/mol | Joback Calculated Property |
| log10WS | 0.11 | Crippen Calculated Property | |
| logPoct/wat | -0.674 | Crippen Calculated Property | |
| McVol | 68.980 | ml/mol | McGowan Calculated Property |
| Pc | 5495.11 | kPa | Joback Calculated Property |
| Inp | [660.00; 672.00] |
|
|
| Inp | 672.00 | NIST | |
| Inp | 660.00 | NIST | |
| I | [1342.00; 1380.00] |
|
|
| I | 1350.00 | NIST | |
| I | 1342.00 | NIST | |
| I | 1368.00 | NIST | |
| I | 1352.00 | NIST | |
| I | 1356.00 | NIST | |
| I | 1380.00 | NIST | |
| Tboil | [433.00; 433.20] | K |
|
| Tboil | 433.20 | K | NIST |
| Tboil | 433.00 | K | NIST |
| Tc | 613.40 | K | Joback Calculated Property |
| Tfus | 275.00 ± 0.02 | K | NIST |
| Vc | 0.245 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [142.31; 178.78] | J/mol×K | [432.31; 613.40] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 140 150 160 170 180 450 500 550 600 | ||||
| Cp,gas | 142.31 | J/mol×K | 432.31 | Joback Calculated Property |
| Cp,gas | 149.06 | J/mol×K | 462.49 | Joback Calculated Property |
| Cp,gas | 155.54 | J/mol×K | 492.67 | Joback Calculated Property |
| Cp,gas | 161.74 | J/mol×K | 522.85 | Joback Calculated Property |
| Cp,gas | 167.68 | J/mol×K | 553.03 | Joback Calculated Property |
| Cp,gas | 173.36 | J/mol×K | 583.21 | Joback Calculated Property |
| Cp,gas | 178.78 | J/mol×K | 613.40 | Joback Calculated Property |
| Cp,liquid | [209.00; 230.00] | J/mol×K | [303.15; 353.15] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 210 215 220 225 230 320 340 | ||||
| Cp,liquid | 209.00 | J/mol×K | 303.15 | Molar H... |
| Cp,liquid | 213.00 | J/mol×K | 308.15 | Molar H... |
| Cp,liquid | 214.00 | J/mol×K | 313.15 | Molar H... |
| Cp,liquid | 215.00 | J/mol×K | 318.15 | Molar H... |
| Cp,liquid | 217.00 | J/mol×K | 323.15 | Molar H... |
| Cp,liquid | 218.00 | J/mol×K | 328.15 | Molar H... |
| Cp,liquid | 221.00 | J/mol×K | 333.15 | Molar H... |
| Cp,liquid | 223.00 | J/mol×K | 338.15 | Molar H... |
| Cp,liquid | 225.00 | J/mol×K | 343.15 | Molar H... |
| Cp,liquid | 228.00 | J/mol×K | 348.15 | Molar H... |
| Cp,liquid | 230.00 | J/mol×K | 353.15 | Molar H... |
| ΔvapH | 51.60 | kJ/mol | 368.50 | NIST |
| n0 | [1.43208; 1.44800] | [293.15; 333.15] |
|
|
|
T(K) Refractive Index 1.43 1.44 1.44 300 310 320 330 | ||||
| n0 | 1.44800 | 293.15 | Volumet... | |
| n0 | 1.44609 | 298.15 | Volumet... | |
| n0 | 1.44610 | 298.15 | Density... | |
| n0 | 1.44409 | 303.15 | Volumet... | |
| n0 | 1.44211 | 308.15 | Volumet... | |
| n0 | 1.44009 | 313.15 | Volumet... | |
| n0 | 1.43817 | 318.15 | Volumet... | |
| n0 | 1.43631 | 323.15 | Volumet... | |
| n0 | 1.43405 | 328.15 | Volumet... | |
| n0 | 1.43208 | 333.15 | Volumet... | |
| ρl | [901.68; 972.17] | kg/m3 | [278.16; 363.16] |
|
|
T(K) Liquid Density (kg/m3) 900 910 920 930 940 950 960 970 300 350 | ||||
| ρl | 972.17 | kg/m3 | 278.16 | Volumet... |
| ρl | 971.79 | kg/m3 | 278.65 | Volumet... |
| ρl | 971.40 | kg/m3 | 279.14 | Volumet... |
| ρl | 971.01 | kg/m3 | 279.65 | Volumet... |
| ρl | 970.62 | kg/m3 | 280.15 | Volumet... |
| ρl | 970.23 | kg/m3 | 280.65 | Volumet... |
| ρl | 969.84 | kg/m3 | 281.15 | Volumet... |
| ρl | 969.45 | kg/m3 | 281.65 | Volumet... |
| ρl | 969.05 | kg/m3 | 282.15 | Volumet... |
| ρl | 968.66 | kg/m3 | 282.65 | Volumet... |
| ρl | 968.27 | kg/m3 | 283.15 | Volumet... |
| ρl | 967.88 | kg/m3 | 283.65 | Volumet... |
| ρl | 967.49 | kg/m3 | 284.15 | Volumet... |
| ρl | 967.10 | kg/m3 | 284.65 | Volumet... |
| ρl | 966.70 | kg/m3 | 285.15 | Volumet... |
| ρl | 966.31 | kg/m3 | 285.65 | Volumet... |
| ρl | 965.92 | kg/m3 | 286.15 | Volumet... |
| ρl | 965.52 | kg/m3 | 286.64 | Volumet... |
| ρl | 965.13 | kg/m3 | 287.15 | Volumet... |
| ρl | 964.73 | kg/m3 | 287.65 | Volumet... |
| ρl | 964.34 | kg/m3 | 288.15 | Volumet... |
| ρl | 964.54 | kg/m3 | 288.15 | Densiti... |
| ρl | 963.95 | kg/m3 | 288.65 | Volumet... |
| ρl | 963.55 | kg/m3 | 289.15 | Volumet... |
| ρl | 963.15 | kg/m3 | 289.65 | Volumet... |
| ρl | 962.76 | kg/m3 | 290.15 | Volumet... |
| ρl | 962.36 | kg/m3 | 290.65 | Volumet... |
| ρl | 961.97 | kg/m3 | 291.15 | Volumet... |
| ρl | 961.57 | kg/m3 | 291.64 | Volumet... |
| ρl | 961.18 | kg/m3 | 292.15 | Volumet... |
| ρl | 960.78 | kg/m3 | 292.65 | Volumet... |
| ρl | 960.38 | kg/m3 | 293.15 | Volumet... |
| ρl | 960.60 | kg/m3 | 293.15 | Densiti... |
| ρl | 960.81 | kg/m3 | 293.15 | Volumet... |
| ρl | 959.99 | kg/m3 | 293.64 | Volumet... |
| ρl | 959.59 | kg/m3 | 294.14 | Volumet... |
| ρl | 959.19 | kg/m3 | 294.64 | Volumet... |
| ρl | 958.79 | kg/m3 | 295.15 | Volumet... |
| ρl | 958.39 | kg/m3 | 295.65 | Volumet... |
| ρl | 957.99 | kg/m3 | 296.15 | Volumet... |
| ρl | 957.60 | kg/m3 | 296.65 | Volumet... |
| ρl | 957.20 | kg/m3 | 297.15 | Volumet... |
| ρl | 956.80 | kg/m3 | 297.64 | Volumet... |
| ρl | 956.62 | kg/m3 | 298.15 | Densiti... |
| ρl | 956.40 | kg/m3 | 298.15 | Volumet... |
| ρl | 956.00 | kg/m3 | 298.65 | Volumet... |
| ρl | 955.60 | kg/m3 | 299.15 | Volumet... |
| ρl | 955.20 | kg/m3 | 299.64 | Volumet... |
| ρl | 954.80 | kg/m3 | 300.14 | Volumet... |
| ρl | 954.40 | kg/m3 | 300.64 | Volumet... |
| ρl | 954.00 | kg/m3 | 301.15 | Volumet... |
| ρl | 953.59 | kg/m3 | 301.65 | Volumet... |
| ρl | 953.20 | kg/m3 | 302.14 | Volumet... |
| ρl | 952.79 | kg/m3 | 302.65 | Volumet... |
| ρl | 952.25 | kg/m3 | 303.15 | Volumet... |
| ρl | 952.39 | kg/m3 | 303.15 | Volumet... |
| ρl | 952.61 | kg/m3 | 303.15 | Densiti... |
| ρl | 951.99 | kg/m3 | 303.64 | Volumet... |
| ρl | 951.59 | kg/m3 | 304.15 | Volumet... |
| ρl | 951.18 | kg/m3 | 304.65 | Volumet... |
| ρl | 950.78 | kg/m3 | 305.15 | Volumet... |
| ρl | 950.38 | kg/m3 | 305.64 | Volumet... |
| ρl | 949.98 | kg/m3 | 306.15 | Volumet... |
| ρl | 949.57 | kg/m3 | 306.65 | Volumet... |
| ρl | 949.17 | kg/m3 | 307.15 | Volumet... |
| ρl | 948.77 | kg/m3 | 307.64 | Volumet... |
| ρl | 948.36 | kg/m3 | 308.15 | Volumet... |
| ρl | 948.58 | kg/m3 | 308.15 | Densiti... |
| ρl | 947.95 | kg/m3 | 308.65 | Volumet... |
| ρl | 947.55 | kg/m3 | 309.15 | Volumet... |
| ρl | 947.14 | kg/m3 | 309.65 | Volumet... |
| ρl | 946.74 | kg/m3 | 310.15 | Volumet... |
| ρl | 946.33 | kg/m3 | 310.65 | Volumet... |
| ρl | 945.92 | kg/m3 | 311.15 | Volumet... |
| ρl | 945.52 | kg/m3 | 311.64 | Volumet... |
| ρl | 945.11 | kg/m3 | 312.15 | Volumet... |
| ρl | 944.70 | kg/m3 | 312.64 | Volumet... |
| ρl | 944.43 | kg/m3 | 313.15 | Volumet... |
| ρl | 944.30 | kg/m3 | 313.15 | Volumet... |
| ρl | 944.51 | kg/m3 | 313.15 | Densiti... |
| ρl | 943.89 | kg/m3 | 313.65 | Volumet... |
| ρl | 943.48 | kg/m3 | 314.15 | Volumet... |
| ρl | 943.07 | kg/m3 | 314.65 | Volumet... |
| ρl | 942.66 | kg/m3 | 315.15 | Volumet... |
| ρl | 942.25 | kg/m3 | 315.65 | Volumet... |
| ρl | 941.84 | kg/m3 | 316.15 | Volumet... |
| ρl | 941.43 | kg/m3 | 316.65 | Volumet... |
| ρl | 941.03 | kg/m3 | 317.15 | Volumet... |
| ρl | 940.61 | kg/m3 | 317.65 | Volumet... |
| ρl | 940.42 | kg/m3 | 318.15 | Densiti... |
| ρl | 940.20 | kg/m3 | 318.15 | Volumet... |
| ρl | 939.79 | kg/m3 | 318.65 | Volumet... |
| ρl | 939.38 | kg/m3 | 319.14 | Volumet... |
| ρl | 938.96 | kg/m3 | 319.65 | Volumet... |
| ρl | 938.55 | kg/m3 | 320.15 | Volumet... |
| ρl | 938.14 | kg/m3 | 320.64 | Volumet... |
| ρl | 937.72 | kg/m3 | 321.15 | Volumet... |
| ρl | 937.31 | kg/m3 | 321.65 | Volumet... |
| ρl | 936.90 | kg/m3 | 322.15 | Volumet... |
| ρl | 936.49 | kg/m3 | 322.65 | Volumet... |
| ρl | 936.29 | kg/m3 | 323.15 | Densiti... |
| ρl | 936.08 | kg/m3 | 323.15 | Volumet... |
| ρl | 936.21 | kg/m3 | 323.15 | Volumet... |
| ρl | 935.66 | kg/m3 | 323.65 | Volumet... |
| ρl | 935.25 | kg/m3 | 324.15 | Volumet... |
| ρl | 934.83 | kg/m3 | 324.65 | Volumet... |
| ρl | 934.42 | kg/m3 | 325.15 | Volumet... |
| ρl | 934.01 | kg/m3 | 325.65 | Volumet... |
| ρl | 933.59 | kg/m3 | 326.15 | Volumet... |
| ρl | 933.18 | kg/m3 | 326.65 | Volumet... |
| ρl | 932.76 | kg/m3 | 327.15 | Volumet... |
| ρl | 932.35 | kg/m3 | 327.65 | Volumet... |
| ρl | 931.93 | kg/m3 | 328.15 | Volumet... |
| ρl | 932.13 | kg/m3 | 328.15 | Densiti... |
| ρl | 931.51 | kg/m3 | 328.66 | Volumet... |
| ρl | 931.09 | kg/m3 | 329.15 | Volumet... |
| ρl | 930.68 | kg/m3 | 329.66 | Volumet... |
| ρl | 930.26 | kg/m3 | 330.16 | Volumet... |
| ρl | 929.84 | kg/m3 | 330.66 | Volumet... |
| ρl | 929.42 | kg/m3 | 331.15 | Volumet... |
| ρl | 929.00 | kg/m3 | 331.66 | Volumet... |
| ρl | 928.58 | kg/m3 | 332.16 | Volumet... |
| ρl | 928.16 | kg/m3 | 332.66 | Volumet... |
| ρl | 927.93 | kg/m3 | 333.15 | Densiti... |
| ρl | 927.74 | kg/m3 | 333.16 | Volumet... |
| ρl | 927.31 | kg/m3 | 333.66 | Volumet... |
| ρl | 926.89 | kg/m3 | 334.16 | Volumet... |
| ρl | 926.47 | kg/m3 | 334.66 | Volumet... |
| ρl | 926.05 | kg/m3 | 335.16 | Volumet... |
| ρl | 925.63 | kg/m3 | 335.66 | Volumet... |
| ρl | 925.20 | kg/m3 | 336.16 | Volumet... |
| ρl | 924.78 | kg/m3 | 336.66 | Volumet... |
| ρl | 924.36 | kg/m3 | 337.16 | Volumet... |
| ρl | 923.93 | kg/m3 | 337.66 | Volumet... |
| ρl | 923.50 | kg/m3 | 338.16 | Volumet... |
| ρl | 923.08 | kg/m3 | 338.66 | Volumet... |
| ρl | 922.65 | kg/m3 | 339.16 | Volumet... |
| ρl | 922.23 | kg/m3 | 339.66 | Volumet... |
| ρl | 921.80 | kg/m3 | 340.16 | Volumet... |
| ρl | 921.38 | kg/m3 | 340.66 | Volumet... |
| ρl | 920.95 | kg/m3 | 341.16 | Volumet... |
| ρl | 920.52 | kg/m3 | 341.66 | Volumet... |
| ρl | 920.09 | kg/m3 | 342.16 | Volumet... |
| ρl | 919.66 | kg/m3 | 342.66 | Volumet... |
| ρl | 919.23 | kg/m3 | 343.16 | Volumet... |
| ρl | 918.80 | kg/m3 | 343.66 | Volumet... |
| ρl | 918.37 | kg/m3 | 344.16 | Volumet... |
| ρl | 917.94 | kg/m3 | 344.66 | Volumet... |
| ρl | 917.51 | kg/m3 | 345.16 | Volumet... |
| ρl | 917.08 | kg/m3 | 345.66 | Volumet... |
| ρl | 916.65 | kg/m3 | 346.16 | Volumet... |
| ρl | 916.21 | kg/m3 | 346.66 | Volumet... |
| ρl | 915.78 | kg/m3 | 347.16 | Volumet... |
| ρl | 915.35 | kg/m3 | 347.66 | Volumet... |
| ρl | 914.92 | kg/m3 | 348.16 | Volumet... |
| ρl | 914.48 | kg/m3 | 348.66 | Volumet... |
| ρl | 914.05 | kg/m3 | 349.16 | Volumet... |
| ρl | 913.61 | kg/m3 | 349.66 | Volumet... |
| ρl | 913.18 | kg/m3 | 350.16 | Volumet... |
| ρl | 912.74 | kg/m3 | 350.66 | Volumet... |
| ρl | 912.30 | kg/m3 | 351.16 | Volumet... |
| ρl | 911.87 | kg/m3 | 351.66 | Volumet... |
| ρl | 911.43 | kg/m3 | 352.16 | Volumet... |
| ρl | 910.99 | kg/m3 | 352.66 | Volumet... |
| ρl | 910.55 | kg/m3 | 353.16 | Volumet... |
| ρl | 910.12 | kg/m3 | 353.66 | Volumet... |
| ρl | 909.68 | kg/m3 | 354.16 | Volumet... |
| ρl | 909.23 | kg/m3 | 354.66 | Volumet... |
| ρl | 908.80 | kg/m3 | 355.16 | Volumet... |
| ρl | 908.35 | kg/m3 | 355.66 | Volumet... |
| ρl | 907.91 | kg/m3 | 356.16 | Volumet... |
| ρl | 907.47 | kg/m3 | 356.66 | Volumet... |
| ρl | 907.03 | kg/m3 | 357.16 | Volumet... |
| ρl | 906.59 | kg/m3 | 357.66 | Volumet... |
| ρl | 906.14 | kg/m3 | 358.16 | Volumet... |
| ρl | 905.70 | kg/m3 | 358.66 | Volumet... |
| ρl | 905.26 | kg/m3 | 359.16 | Volumet... |
| ρl | 904.81 | kg/m3 | 359.66 | Volumet... |
| ρl | 904.36 | kg/m3 | 360.16 | Volumet... |
| ρl | 903.92 | kg/m3 | 360.65 | Volumet... |
| ρl | 903.47 | kg/m3 | 361.16 | Volumet... |
| ρl | 903.03 | kg/m3 | 361.66 | Volumet... |
| ρl | 902.58 | kg/m3 | 362.16 | Volumet... |
| ρl | 902.13 | kg/m3 | 362.66 | Volumet... |
| ρl | 901.68 | kg/m3 | 363.15 | Volumet... |
| ρl | 901.69 | kg/m3 | 363.16 | Volumet... |
| γ | [0.03; 0.04] | N/m | [298.15; 323.15] |
|
|
T(K) Surface Tension (N/m) 0.03 0.03 0.03 0.03 0.03 0.04 0.04 300 310 320 | ||||
| γ | 0.04 | N/m | 298.15 | Surface... |
| γ | 0.04 | N/m | 303.15 | Surface... |
| γ | 0.03 | N/m | 308.15 | Surface... |
| γ | 0.03 | N/m | 313.15 | Surface... |
| γ | 0.03 | N/m | 318.15 | Surface... |
| γ | 0.03 | N/m | 323.15 | Surface... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.62] | kPa | [331.00; 456.17] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.77283e+01 | |||
| Coefficient B | -5.39563e+03 | |||
| Coefficient C | -2.16350e+01 | |||
| Temperature range, min. | 331.00 | |||
| Temperature range, max. | 456.17 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
| Pvap | 1.33 | kPa | 331.00 | Calculated Property |
| Pvap | 2.82 | kPa | 344.91 | Calculated Property |
| Pvap | 5.62 | kPa | 358.82 | Calculated Property |
| Pvap | 10.59 | kPa | 372.72 | Calculated Property |
| Pvap | 19.02 | kPa | 386.63 | Calculated Property |
| Pvap | 32.73 | kPa | 400.54 | Calculated Property |
| Pvap | 54.19 | kPa | 414.45 | Calculated Property |
| Pvap | 86.67 | kPa | 428.35 | Calculated Property |
| Pvap | 134.39 | kPa | 442.26 | Calculated Property |
| Pvap | 202.62 | kPa | 456.17 | Calculated Property |
Similar Compounds
Find more compounds similar to 2-Propanol, 1-amino-.
Mixtures
- 2-Propanol, 1-amino- + Water
- 2-Propanol, 1-amino- + Ethanol
- 2-Propanol, 1-amino- + Diethanolamine + Water
- 2-Propanol, 1-amino- + Triethanolamine + Water
- 2-Propanol, 1-amino- + Water + 1-Propanol, 2-amino-2-methyl-
- 2-Propanol, 1-amino- + 1-Butanol
- 2-Propanol, 1-amino- + Carbon dioxide + Water
- 2-Propanol, 1-amino- + Hydrogen sulfide + Water
Sources
- Crippen Method
- Crippen Method
- Molar excess enthalpy (HEm) for various {alkanolamine (1) + water (2)} systems at T = (298.15, 313.15, and 323.15) K
- Equilibrium solubility of CO2 in aqueous solutions of 1-amino-2-propanol as function of concentration, temperature, and pressure
- Equilibrium solubility of H2S in aqueous solutions of 1-amino-2-propanol as function of concentration, temperature, and pressure
- Volumetric properties of the isopropanolamine water mixture at atmospheric pressure from 283.15 to 353.15K
- Low-temperature thermal properties of the aqueous solutions of simple aminoalcohols: Finding of peculiarities in 1-amino-2-propanol solutions
- Volumetric and Viscometric Properties of Alcohol Amines + Ethanol Binary Mixtures
- Surface Tension of aqueous vinary mixtures of 1-amino-2-propanol and 3-amino-1-propanol, and aqueous ternary mixtures of these amines with diethanolamine, triethanolamine, and 2-amino-2-methyl-1-propanol from (298.15 to 323.15) K
- Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
- Volumetric Properties, Viscosities, and Refractive Indices for Aqueous 1-Amino-2-Propanol (Monoisopropanolamine (MIPA)) Solutions from (298.15 to 343.15) K
- Density, Speed of Sound, Refractive Index, and Viscosity of 1-Amino-2-Propanol {or Bis(2-hydroxypropyl)amine} + Triethanolamine + Water from T = (288.15 to 333.15) K
- Densities, Viscosities, and Refractive Indices of Aqueous Alkanolamine Solutions as Potential Carbon Dioxide Removal Reagents
- Densities, Refractive Indices, Viscosities, and Spectroscopic Study of 1-Amino-2-propanol + 1-Butanol and + 2-Butanol Solutions at (288.15 to 333.15) K
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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