- InChI
- InChI=1S/C4H11NO/c1-4(2,5)3-6/h6H,3,5H2,1-2H3
- InChI Key
- CBTVGIZVANVGBH-UHFFFAOYSA-N
- Formula
- C4H11NO
- SMILES
- CC(C)(N)CO
- Molecular Weight1
- 89.14
- CAS
- 124-68-5
- Other Names
-
- 1,1-Dimethyl-2-hydroxyethylamine
- 2,2-Dimethyl-ethanolamine
- 2-Amino-1-hydroxy-2-methylpropane
- 2-Amino-2,2-dimethylethanol
- 2-Amino-2-methyl-1-propanol
- 2-Amino-2-methylpropan-1-ol
- 2-Amino-2-methylpropanol
- 2-Aminodimethylethanol
- 2-Aminoisobutanol
- 2-Hydroxymethyl-2-propylamine
- 2-Methyl-2-aminopropanol
- 2-Methyl-2-aminopropanol-1
- AMP
- AMP (thinner)
- AMP 75
- AMP Regular
- AMP-95
- Amino-2,2-dimethylethanol
- Amino-2-methyl-1-propanol
- Aminoisobutanol
- Aminomethylpropanol
- Corrguard 75
- Hydroxy-tert-butylamine
- Hydroxymethyl-2-propylamine
- Isobutanol-2-amine
- KV 5088
- NSC 441
- «beta»-Aminoisobutanol
- «beta»-Aminoisobutanol
- 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).
- 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).
- ρl : Liquid Density (kg/m3).
- I : Polar retention indices.
- csound,fluid : Speed of sound in fluid (m/s).
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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.
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔfG° | -84.73 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -253.08 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 7.99 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 50.52 | kJ/mol | Joback Calculated Property |
| log10WS | -0.31 | Crippen Calculated Property | |
| logPoct/wat | -0.284 | Crippen Calculated Property | |
| McVol | 83.070 | ml/mol | McGowan Calculated Property |
| Pc | 4862.97 | kPa | Joback Calculated Property |
| I | [1380.00; 1468.00] |
|
|
| I | 1468.00 | NIST | |
| I | 1460.00 | NIST | |
| I | 1380.00 | NIST | |
| I | 1384.00 | NIST | |
| I | 1452.00 | NIST | |
| I | 1468.00 | NIST | |
| Tboil | [436.85; 438.70] | K |
|
| Tboil | 436.85 | K | Measure... |
| Tboil | 438.70 | K | NIST |
| Tboil | 438.00 | K | NIST |
| Tc | 639.25 | K | Joback Calculated Property |
| Tfus | 303.50 ± 0.50 | K | NIST |
| Ttriple | 295.75 | K | Solid S... |
| Vc | 0.296 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [182.53; 227.82] | J/mol×K | [452.40; 639.25] |
|
| Cp,gas | 182.53 | J/mol×K | 452.40 | Joback Calculated Property |
| Cp,gas | 191.22 | J/mol×K | 483.54 | Joback Calculated Property |
| Cp,gas | 199.43 | J/mol×K | 514.68 | Joback Calculated Property |
| Cp,gas | 207.16 | J/mol×K | 545.82 | Joback Calculated Property |
| Cp,gas | 214.46 | J/mol×K | 576.96 | Joback Calculated Property |
| Cp,gas | 221.34 | J/mol×K | 608.11 | Joback Calculated Property |
| Cp,gas | 227.82 | J/mol×K | 639.25 | Joback Calculated Property |
| Cp,liquid | 229.50 | J/mol×K | 298.15 | NIST |
| η | [0.0089100; 0.0478000] | Pa×s | [313.15; 343.15] |
|
| η | 0.0478000 | Pa×s | 313.15 | Volumet... |
| η | 0.0251000 | Pa×s | 323.15 | Volumet... |
| η | 0.0144000 | Pa×s | 333.15 | Volumet... |
| η | 0.0089100 | Pa×s | 343.15 | Volumet... |
| Pvap | [0.04; 160.00] | kPa | [293.29; 452.00] |
|
| Pvap | 0.04 | kPa | 293.29 | Investi... |
| Pvap | 0.10 | kPa | 303.35 | Investi... |
| Pvap | 0.22 | kPa | 313.24 | Investi... |
| Pvap | 0.46 | kPa | 323.25 | Investi... |
| Pvap | 0.87 | kPa | 332.57 | Investi... |
| Pvap | 1.66 | kPa | 343.18 | Investi... |
| Pvap | 1.94 | kPa | 347.50 | Vapor P... |
| Pvap | 2.93 | kPa | 353.17 | Investi... |
| Pvap | 2.94 | kPa | 354.30 | Vapor P... |
| Pvap | 4.99 | kPa | 363.10 | Investi... |
| Pvap | 4.94 | kPa | 363.60 | Vapor P... |
| Pvap | 5.00 | kPa | 364.11 | Ternary... |
| Pvap | 7.44 | kPa | 371.40 | Vapor P... |
| Pvap | 8.14 | kPa | 373.00 | Investi... |
| Pvap | 8.00 | kPa | 373.25 | Measure... |
| Pvap | 9.94 | kPa | 377.20 | Vapor P... |
| Pvap | 10.00 | kPa | 377.39 | Ternary... |
| Pvap | 12.00 | kPa | 381.35 | Measure... |
| Pvap | 16.00 | kPa | 388.05 | Measure... |
| Pvap | 19.90 | kPa | 392.30 | Vapor P... |
| Pvap | 20.00 | kPa | 392.71 | Ternary... |
| Pvap | 20.00 | kPa | 393.05 | Measure... |
| Pvap | 24.00 | kPa | 397.25 | Measure... |
| Pvap | 28.00 | kPa | 401.05 | Measure... |
| Pvap | 29.90 | kPa | 402.10 | Vapor P... |
| Pvap | 30.00 | kPa | 402.56 | Ternary... |
| Pvap | 32.00 | kPa | 404.45 | Measure... |
| Pvap | 36.00 | kPa | 407.75 | Measure... |
| Pvap | 39.90 | kPa | 409.50 | Vapor P... |
| Pvap | 40.00 | kPa | 410.35 | Measure... |
| Pvap | 44.00 | kPa | 412.95 | Measure... |
| Pvap | 48.00 | kPa | 415.15 | Measure... |
| Pvap | 49.90 | kPa | 415.60 | Vapor P... |
| Pvap | 50.00 | kPa | 415.99 | Ternary... |
| Pvap | 50.70 | kPa | 416.65 | Measure... |
| Pvap | 53.30 | kPa | 418.15 | Measure... |
| Pvap | 57.30 | kPa | 419.95 | Measure... |
| Pvap | 61.30 | kPa | 421.85 | Measure... |
| Pvap | 65.00 | kPa | 423.00 | Vapor P... |
| Pvap | 65.30 | kPa | 423.65 | Measure... |
| Pvap | 66.70 | kPa | 424.45 | Measure... |
| Pvap | 70.00 | kPa | 425.48 | Ternary... |
| Pvap | 69.30 | kPa | 425.55 | Measure... |
| Pvap | 73.30 | kPa | 427.15 | Measure... |
| Pvap | 80.00 | kPa | 429.20 | Vapor P... |
| Pvap | 80.00 | kPa | 429.65 | Measure... |
| Pvap | 80.00 | kPa | 429.75 | Measure... |
| Pvap | 85.30 | kPa | 431.85 | Measure... |
| Pvap | 90.70 | kPa | 433.65 | Measure... |
| Pvap | 96.00 | kPa | 435.35 | Measure... |
| Pvap | 100.00 | kPa | 436.20 | Vapor P... |
| Pvap | 101.30 | kPa | 436.85 | Measure... |
| Pvap | 120.00 | kPa | 442.10 | Vapor P... |
| Pvap | 140.00 | kPa | 447.30 | Vapor P... |
| Pvap | 160.00 | kPa | 452.00 | Vapor P... |
| ρl | [900.70; 930.52] | kg/m3 | [298.15; 333.15] |
|
| ρl | 930.52 | kg/m3 | 298.15 | Densiti... |
| ρl | 926.40 | kg/m3 | 303.15 | Densiti... |
| ρl | 922.26 | kg/m3 | 308.15 | Densiti... |
| ρl | 917.20 | kg/m3 | 313.15 | Density... |
| ρl | 918.08 | kg/m3 | 313.15 | Densiti... |
| ρl | 913.87 | kg/m3 | 318.15 | Densiti... |
| ρl | 909.62 | kg/m3 | 323.15 | Densiti... |
| ρl | 909.20 | kg/m3 | 323.15 | Density... |
| ρl | 900.70 | kg/m3 | 333.15 | Density... |
| csound,fluid | [1386.93; 1501.44] | m/s | [293.15; 323.15] |
|
| csound,fluid | 1501.44 | m/s | 293.15 | Density... |
| csound,fluid | 1501.44 | m/s | 293.15 | Density... |
| csound,fluid | 1483.44 | m/s | 298.15 | Density... |
| csound,fluid | 1483.44 | m/s | 298.15 | Density... |
| csound,fluid | 1461.22 | m/s | 303.15 | Density... |
| csound,fluid | 1461.22 | m/s | 303.15 | Density... |
| csound,fluid | 1442.40 | m/s | 308.15 | Density... |
| csound,fluid | 1442.40 | m/s | 308.15 | Density... |
| csound,fluid | 1423.80 | m/s | 313.15 | Density... |
| csound,fluid | 1423.80 | m/s | 313.15 | Density... |
| csound,fluid | 1405.28 | m/s | 318.15 | Density... |
| csound,fluid | 1405.28 | m/s | 318.15 | Density... |
| csound,fluid | 1386.93 | m/s | 323.15 | Density... |
| csound,fluid | 1386.93 | m/s | 323.15 | Density... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 340.50 | K | 1.30 | NIST |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 313.06 | 1000.00 | 931.4 |
| 313.06 | 2000.00 | 931.9 |
| 313.06 | 3000.00 | 932.4 |
| 313.06 | 4000.00 | 932.9 |
| 313.06 | 5000.00 | 933.5 |
| 313.06 | 6000.00 | 933.9 |
| 313.06 | 7000.00 | 934.5 |
| 313.06 | 8000.00 | 935.0 |
| 313.06 | 9007.00 | 935.5 |
| 313.06 | 10003.00 | 936.0 |
| 313.06 | 11000.00 | 936.6 |
| 313.06 | 12000.00 | 937.0 |
| 313.06 | 13000.00 | 937.6 |
| 313.06 | 14000.00 | 938.1 |
| 313.06 | 15002.00 | 938.6 |
| 313.06 | 16000.00 | 939.1 |
| 313.06 | 17001.00 | 939.7 |
| 313.06 | 18002.00 | 940.2 |
| 313.06 | 19000.00 | 940.6 |
| 313.06 | 20029.00 | 941.1 |
| 313.06 | 21004.00 | 941.7 |
| 313.06 | 22004.00 | 942.1 |
| 313.06 | 24004.00 | 943.1 |
| 322.98 | 500.00 | 922.7 |
| 322.98 | 1000.00 | 922.8 |
| 322.98 | 2000.00 | 923.4 |
| 322.98 | 3000.00 | 924.0 |
| 322.98 | 4000.00 | 924.5 |
| 322.98 | 5000.00 | 925.1 |
| 322.98 | 6000.00 | 925.7 |
| 322.98 | 7000.00 | 926.2 |
| 322.98 | 8000.00 | 926.8 |
| 322.98 | 9007.00 | 927.4 |
| 322.98 | 10002.00 | 927.8 |
| 322.98 | 11000.00 | 928.4 |
| 322.98 | 12000.00 | 928.9 |
| 322.98 | 13000.00 | 929.5 |
| 322.98 | 14000.00 | 930.1 |
| 322.98 | 15003.00 | 930.6 |
| 322.98 | 16006.00 | 931.1 |
| 322.98 | 17001.00 | 931.6 |
| 322.98 | 18002.00 | 932.1 |
| 322.98 | 19000.00 | 932.6 |
| 322.98 | 20030.00 | 933.2 |
| 322.98 | 21005.00 | 933.7 |
| 322.98 | 22004.00 | 934.1 |
| 322.98 | 24004.00 | 935.2 |
| 332.91 | 500.00 | 914.0 |
| 332.91 | 1000.00 | 914.4 |
| 332.91 | 2000.00 | 915.0 |
| 332.91 | 3000.00 | 915.6 |
| 332.91 | 4000.00 | 916.1 |
| 332.91 | 5000.00 | 916.7 |
| 332.91 | 6000.00 | 917.3 |
| 332.91 | 7000.00 | 918.0 |
| 332.91 | 8000.00 | 918.5 |
| 332.91 | 9009.00 | 919.1 |
| 332.91 | 10003.00 | 919.7 |
| 332.91 | 11002.00 | 920.2 |
| 332.91 | 12001.00 | 920.8 |
| 332.91 | 13000.00 | 921.3 |
| 332.91 | 14000.00 | 921.9 |
| 332.91 | 15002.00 | 922.4 |
| 332.91 | 16001.00 | 923.0 |
| 332.91 | 17001.00 | 923.5 |
| 332.91 | 18002.00 | 924.1 |
| 332.91 | 19000.00 | 924.6 |
| 332.91 | 20030.00 | 925.2 |
| 332.91 | 21002.00 | 925.6 |
| 332.91 | 22004.00 | 926.2 |
| 332.91 | 23000.00 | 926.7 |
| 332.91 | 24004.00 | 927.3 |
| 342.84 | 500.00 | 905.4 |
| 342.84 | 1000.00 | 905.7 |
| 342.84 | 2000.00 | 906.4 |
| 342.84 | 3000.00 | 907.0 |
| 342.84 | 4000.00 | 907.6 |
| 342.84 | 5000.00 | 908.3 |
| 342.84 | 6000.00 | 908.9 |
| 342.84 | 7000.00 | 909.5 |
| 342.84 | 8001.00 | 910.1 |
| 342.84 | 9009.00 | 910.7 |
| 342.84 | 10003.00 | 911.3 |
| 342.84 | 11001.00 | 911.9 |
| 342.84 | 12000.00 | 912.5 |
| 342.84 | 13000.00 | 913.1 |
| 342.84 | 14000.00 | 913.6 |
| 342.84 | 15003.00 | 914.3 |
| 342.84 | 16001.00 | 914.8 |
| 342.84 | 17001.00 | 915.3 |
| 342.84 | 18002.00 | 915.9 |
| 342.84 | 19000.00 | 916.5 |
| 342.84 | 20030.00 | 917.1 |
| 342.84 | 21005.00 | 917.6 |
| 342.84 | 22004.00 | 918.1 |
| 342.84 | 23000.00 | 918.7 |
| 342.84 | 24004.00 | 919.2 |
| 352.79 | 500.00 | 896.8 |
| 352.79 | 1000.00 | 897.2 |
| 352.79 | 2000.00 | 897.9 |
| 352.79 | 3000.00 | 898.5 |
| 352.79 | 4001.00 | 899.2 |
| 352.79 | 5000.00 | 899.9 |
| 352.79 | 6000.00 | 900.5 |
| 352.79 | 7001.00 | 901.2 |
| 352.79 | 8000.00 | 901.8 |
| 352.79 | 9009.00 | 902.4 |
| 352.79 | 10003.00 | 903.1 |
| 352.79 | 11001.00 | 903.7 |
| 352.79 | 12000.00 | 904.3 |
| 352.79 | 13001.00 | 904.9 |
| 352.79 | 14000.00 | 905.5 |
| 352.79 | 15002.00 | 906.1 |
| 352.79 | 16001.00 | 906.7 |
| 352.79 | 17001.00 | 907.4 |
| 352.79 | 18002.00 | 907.9 |
| 352.79 | 18997.00 | 908.5 |
| 352.79 | 20030.00 | 909.1 |
| 352.79 | 21001.00 | 909.7 |
| 352.79 | 22004.00 | 910.3 |
| 352.79 | 23000.00 | 910.9 |
| 352.79 | 24004.00 | 911.4 |
| 362.65 | 504.00 | 888.0 |
| 362.65 | 1002.00 | 888.4 |
| 362.65 | 2000.00 | 889.0 |
| 362.65 | 3000.00 | 889.7 |
| 362.65 | 4000.00 | 890.5 |
| 362.65 | 5000.00 | 891.2 |
| 362.65 | 6000.00 | 891.8 |
| 362.65 | 7000.00 | 892.5 |
| 362.65 | 8001.00 | 893.2 |
| 362.65 | 9010.00 | 893.9 |
| 362.65 | 10003.00 | 894.6 |
| 362.65 | 11001.00 | 895.2 |
| 362.65 | 12000.00 | 895.8 |
| 362.65 | 13001.00 | 896.5 |
| 362.65 | 14000.00 | 897.1 |
| 362.65 | 15003.00 | 897.8 |
| 362.65 | 16001.00 | 898.4 |
| 362.65 | 17000.00 | 899.1 |
| 362.65 | 18002.00 | 899.7 |
| 362.65 | 19000.00 | 900.3 |
| 362.65 | 20030.00 | 901.0 |
| 362.65 | 21004.00 | 901.6 |
| 362.65 | 22004.00 | 902.2 |
| 362.65 | 23000.00 | 902.8 |
| 362.65 | 24003.00 | 903.3 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [335.92; 462.54] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.61365e+01 | |||
| Coefficient B | -4.32398e+03 | |||
| Coefficient C | -6.30950e+01 | |||
| Temperature range, min. | 335.92 | |||
| Temperature range, max. | 462.54 | |||
| Pvap | 1.33 | kPa | 335.92 | Calculated Property |
| Pvap | 2.90 | kPa | 349.99 | Calculated Property |
| Pvap | 5.87 | kPa | 364.06 | Calculated Property |
| Pvap | 11.14 | kPa | 378.13 | Calculated Property |
| Pvap | 20.04 | kPa | 392.20 | Calculated Property |
| Pvap | 34.34 | kPa | 406.26 | Calculated Property |
| Pvap | 56.41 | kPa | 420.33 | Calculated Property |
| Pvap | 89.23 | kPa | 434.40 | Calculated Property |
| Pvap | 136.50 | kPa | 448.47 | Calculated Property |
| Pvap | 202.66 | kPa | 462.54 | Calculated Property |
Similar Compounds
![2-Amino-3-[(trimethylsilyl)oxy]-2-([(trimethylsilyl)oxy]methyl)propan-1-ol.](data:image/png;base64,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)
Find more compounds similar to 1-Propanol, 2-amino-2-methyl-.
Mixtures
- Water + 1-Propanol, 2-amino-2-methyl-
- 1,6-Hexanediamine + Water + 1-Propanol, 2-amino-2-methyl-
- Piperazine + Water + 1-Propanol, 2-amino-2-methyl-
- 2-Propanol, 1-amino- + Water + 1-Propanol, 2-amino-2-methyl-
- 1-Propanol, 3-amino- + Water + 1-Propanol, 2-amino-2-methyl-
- Ethanol, 2-(methylamino)- + Water + 1-Propanol, 2-amino-2-methyl-
- Ethanol, 2-(ethylamino)- + Water + 1-Propanol, 2-amino-2-methyl-
- Methyl Alcohol + 1-Propanol, 2-amino-2-methyl-
- Methyl Alcohol + Water + 1-Propanol, 2-amino-2-methyl-
- Monoethanolamine + 1-Propanol, 2-amino-2-methyl-
- 2-Propanol, 1-amino-, (R)- + 1-Propanol, 2-amino-2-methyl-
- 1-Propanol, 3-amino- + 1-Propanol, 2-amino-2-methyl-
- Methyldiethanolamine + Water + 1-Propanol, 2-amino-2-methyl-
- Piperazine + 1-Propanol, 2-amino-2-methyl-
- Carbon dioxide + Water + 1-Propanol, 2-amino-2-methyl-
- Monoethanolamine + Water + 1-Propanol, 2-amino-2-methyl-
- Diethanolamine + Water + 1-Propanol, 2-amino-2-methyl-
- Nitrous oxide + Water + 1-Propanol, 2-amino-2-methyl-
- Nitrous oxide + Diethanolamine + 1-Propanol, 2-amino-2-methyl-
Sources
- Crippen Method
- Crippen Method
- Measurement and thermodynamic modeling of the phase equilibrium of aqueous 2-amino-2-methyl-1-propanol solutions
- The solubility measurement and modeling of CO2 in aqueous solution of N-methyldiethanolaminen + 2-amino-2-methyl-1- propanol + piperazine at high pressures
- Experimental investigation of the density and viscosity of CO2-loaded aqueous alkanolamine solutions
- Experimental measurement and Kent-Eisenberg modelling of CO2 solubility in aqueous mixture of 2-amino-2-methyl-1-propanol and hexamethylenediamine
- Liquid heat capacity of the solvent system (piperazine + 2-amino-2-methyl-lpropanol + water)
- Investigation of the isothermal (vapour + liquid) equilibria of aqueous 2-amino-2-methyl-1-propanol (AMP), N-benzylethanolamine, or 3-dimethylamino-1-propanol solutions at several temperatures
- (Vapour + liquid) equilibria (VLE) of CO2 in aqueous solutions of 2-amino-2-methyl-1-propanol: New data and modelling using eNRTL-equation
- Experimental analysis and modeling of CO2 solubility in AMP (2-amino-2-methyl-1-propanol) at low CO2 partial pressure using the models of Deshmukh-Mather and the artificial neural network
- Experimental and theoretical investigation of solubility of carbon dioxide in concentrated aqueous solution of 2-amino-2-methyl-1-propanol and piperazine
- Experiments and model for the viscosity of carbonated 2-amino-2-methyl-1-propanol and piperazine aqueous solution
- Solubility and thermodynamic modeling of hydrogen sulfide in aqueous (diisopropanolamine + 2-amino-2-methyl-1-propanol + piperazine) solution at high pressure
- Solid Solubility in the Aqueous 2-Amino-2-methyl-propanol (AMP) Plus Piperazine (PZ) System
- 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
- Volumetric Properties and Viscosities for Aqueous AMP Solutions from 25 0C to 70 0C
- Vapor-Liquid Equilibrium of CO2 in Aqueous Solutions of 2-Amino-2-methyl-1-propanol
- Density and Viscosity of Aqueous Solutions of (N-Methyldiethanolamine + Monoethanolamine), (N-Methyldiethanolamine + Diethanolamine), (2-Amino-2-methyl-1-propanol + Monoethanolamine) and (2-Amino-2-methyl-1-propanol + Diethanolamine
- Physical Solubility and Diffusivity of N2O and CO2 into Aqueous Solutions of (2-Amino-2-methyl-1-propanol + Diethanolamine) and (N-Methyldiethanolamine + Diethanolamine)
- Mutual Diffusion Coefficients of Some Aqueous Alkanolamines Solutions
- Density and Viscosity of Aqueous Solutions of Piperazine and (2-Amino-2-methyl-1-propanol + Piperazine) from 298 to 333 K
- Density and Viscosity of Aqueous Blends of Three Alkanolamines: N-Methyldiethanolamine, Diethanolamine, and 2-Amino-2-methyl-1-propanol in the Range of (303 to 343) K
- Densities and Viscosities of Aqueous Ternary Mixtures of 2-(Methylamino)ethanol and 2-(Ethylamino)ethanol with Diethanolamine, Triethanolamine, N-Methyldiethanolamine, or 2-Amino-1-methyl-1-propanol from 298.15 to 323.15 K
- Density and Viscosity of Aqueous Solutions of (N-Methyldiethanolamine + Piperazine) and (2-Amino-2-methyl-1-propanol + Piperazine) from (288 to 333) K
- Density and Viscosity of Aqueous Solutions of (2-Piperidineethanol + Piperazine) from (288 to 333) K and Surface Tension of Aqueous Solutions of (N-Methyldiethanolamine + Piperazine), (2-Amino-2-methyl-1-propanol + Piperazine), and (2-Piperidineethanol + Piperazine) from (293 to 323) K
- Ternary Isobaric Vapor-Liquid Equilibria of Methanol + N-Methyldiethanolamine + Water and Methanol + 2-Amino-2-methyl-1-propanol + Water Systems
- Density and Surface Tension of Aqueous Solutions of (2-(Methylamino)-ethanol +2-Amino-2-methyl-1-propanol) and (2-(Methylamino)-ethanol + N-Methyl-diethanolamine) from (298.15 to 323.15) K
- Physical Properties of Aqueous Solutions of Piperazine and (2-Amino-2-methyl-1-propanol + Piperazine) from (298.15 to 333.15) K
- Vapor Pressures of Several Commercially Used Alkanolamines
- Aqueous Solubility of Piperazine and 2-Amino-2-methyl-1-propanol plus Their Mixtures Using an Improved Freezing-Point Depression Method
- Densities and Derived Thermodynamic Properties of 2-Amino-2-methyl-1-propanol + Water Mixtures at Temperatures from (313 to 363) K and Pressures up to 24 MPa
- Density, Speed of Sound, Isentropic Compressibility, and Excess Volume of (Monoethanolamine + 2-Amino-2-methyl-1-propanol), (Monoethanolamine + Triethanolamine), and (Monoethanolamine + N-Methyldiethanolamine) at Temperatures from (293.15 to 323.15) K
- Density, Speed of Sound, Isentropic Compressibility, and Excess Volume of Binary Mixtures of 1-Amino-2-propanol or 3-Amino-1-propanol with 2-Amino-2-methyl-1-propanol, Diethanolamine, or Triethanolamine from (293.15 to 323.15) K
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.