Physical Properties
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Cp,liquid
[175.40; 194.60]
J/mol×K
[283.15; 333.15]
Cp,liquid
175.40
J/mol×K
283.15
Excess Molar Enthalpies and Heat Capacities of {2-Methylpiperidine Water} and {N-Methylpiperidine Water} Systems of Low to Moderate Amine Compositions
Cp,liquid
177.60
J/mol×K
288.15
Excess Molar Enthalpies and Heat Capacities of {2-Methylpiperidine Water} and {N-Methylpiperidine Water} Systems of Low to Moderate Amine Compositions
Cp,liquid
179.50
J/mol×K
293.15
Excess Molar Enthalpies and Heat Capacities of {2-Methylpiperidine Water} and {N-Methylpiperidine Water} Systems of Low to Moderate Amine Compositions
Cp,liquid
184.90
J/mol×K
298.00
NIST
Cp,liquid
181.50
J/mol×K
298.15
Excess Molar Enthalpies and Heat Capacities of {2-Methylpiperidine Water} and {N-Methylpiperidine Water} Systems of Low to Moderate Amine Compositions
Cp,liquid
183.50
J/mol×K
303.16
Excess Molar Enthalpies and Heat Capacities of {2-Methylpiperidine Water} and {N-Methylpiperidine Water} Systems of Low to Moderate Amine Compositions
Cp,liquid
185.50
J/mol×K
308.15
Excess Molar Enthalpies and Heat Capacities of {2-Methylpiperidine Water} and {N-Methylpiperidine Water} Systems of Low to Moderate Amine Compositions
Cp,liquid
187.50
J/mol×K
313.16
Excess Molar Enthalpies and Heat Capacities of {2-Methylpiperidine Water} and {N-Methylpiperidine Water} Systems of Low to Moderate Amine Compositions
Cp,liquid
189.10
J/mol×K
318.15
Excess Molar Enthalpies and Heat Capacities of {2-Methylpiperidine Water} and {N-Methylpiperidine Water} Systems of Low to Moderate Amine Compositions
Cp,liquid
191.20
J/mol×K
323.15
Excess Molar Enthalpies and Heat Capacities of {2-Methylpiperidine Water} and {N-Methylpiperidine Water} Systems of Low to Moderate Amine Compositions
Cp,liquid
192.70
J/mol×K
328.15
Excess Molar Enthalpies and Heat Capacities of {2-Methylpiperidine Water} and {N-Methylpiperidine Water} Systems of Low to Moderate Amine Compositions
Cp,liquid
194.60
J/mol×K
333.15
Excess Molar Enthalpies and Heat Capacities of {2-Methylpiperidine Water} and {N-Methylpiperidine Water} Systems of Low to Moderate Amine Compositions
Δvap H
[36.50; 37.30]
kJ/mol
[320.50; 326.50]
Δvap H
36.50
kJ/mol
320.50
NIST
Δvap H
37.30
kJ/mol
326.50
NIST
Pvap
[1.24; 9.86]
kPa
[273.18; 313.47]
Pvap
1.24
kPa
273.18
Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap
2.23
kPa
282.90
Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap
2.90
kPa
287.85
Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap
3.75
kPa
292.70
Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap
3.92
kPa
293.51
Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap
4.96
kPa
298.15
Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap
5.49
kPa
300.35
Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap
6.16
kPa
302.86
Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap
7.95
kPa
308.47
Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap
9.86
kPa
313.47
Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
ρl
[781.62; 822.24]
kg/m3
[288.15; 338.15]
ρl
822.24
kg/m3
288.15
Temperatures of liquid-liquid separation and excess molar volumes of {N-methylpiperidine-water} and {2-methylpiperidine-water} systems
ρl
821.53
kg/m3
288.15
Determination of Infinite Dilution Partial Molar Excess Enthalpies and Volumes for Some Ionic Liquid Precursors in Water and Methanol Using Tandem Flow Mixing Calorimetry and Vibrating-Tube Densimetry
ρl
817.22
kg/m3
293.15
Determination of Infinite Dilution Partial Molar Excess Enthalpies and Volumes for Some Ionic Liquid Precursors in Water and Methanol Using Tandem Flow Mixing Calorimetry and Vibrating-Tube Densimetry
ρl
810.89
kg/m3
298.15
Temperatures of liquid-liquid separation and excess molar volumes of {N-methylpiperidine-water} and {2-methylpiperidine-water} systems
ρl
812.62
kg/m3
298.15
Determination of Infinite Dilution Partial Molar Excess Enthalpies and Volumes for Some Ionic Liquid Precursors in Water and Methanol Using Tandem Flow Mixing Calorimetry and Vibrating-Tube Densimetry
ρl
808.16
kg/m3
303.15
Determination of Infinite Dilution Partial Molar Excess Enthalpies and Volumes for Some Ionic Liquid Precursors in Water and Methanol Using Tandem Flow Mixing Calorimetry and Vibrating-Tube Densimetry
ρl
803.85
kg/m3
308.15
Temperatures of liquid-liquid separation and excess molar volumes of {N-methylpiperidine-water} and {2-methylpiperidine-water} systems
ρl
803.61
kg/m3
308.15
Determination of Infinite Dilution Partial Molar Excess Enthalpies and Volumes for Some Ionic Liquid Precursors in Water and Methanol Using Tandem Flow Mixing Calorimetry and Vibrating-Tube Densimetry
ρl
796.93
kg/m3
318.15
Temperatures of liquid-liquid separation and excess molar volumes of {N-methylpiperidine-water} and {2-methylpiperidine-water} systems
ρl
785.64
kg/m3
328.15
Temperatures of liquid-liquid separation and excess molar volumes of {N-methylpiperidine-water} and {2-methylpiperidine-water} systems
ρl
781.62
kg/m3
338.15
Temperatures of liquid-liquid separation and excess molar volumes of {N-methylpiperidine-water} and {2-methylpiperidine-water} systems
Correlations
Property
Value
Unit
Temperature (K)
Source
Pvap
[1.33; 202.64]
kPa
[276.62; 406.12]
The Yaws Handbook of Vapor Pressure
Equation ln(Pvp) = A + B/(T + C) Coefficient A 1.42259e+01 Coefficient B -3.20286e+03 Coefficient C -4.68320e+01 Temperature range, min. 276.62
Temperature range, max. 406.12
Pvap
1.33
kPa
276.62
Calculated Property
Pvap
3.03
kPa
291.01
Calculated Property
Pvap
6.29
kPa
305.40
Calculated Property
Pvap
12.08
kPa
319.79
Calculated Property
Pvap
21.75
kPa
334.18
Calculated Property
Pvap
37.00
kPa
348.56
Calculated Property
Pvap
59.99
kPa
362.95
Calculated Property
Pvap
93.25
kPa
377.34
Calculated Property
Pvap
139.71
kPa
391.73
Calculated Property
Pvap
202.64
kPa
406.12
Calculated Property
Similar Compounds
Find more compounds similar to Piperidine, 1-methyl- .
Mixtures
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