- InChI
- InChI=1S/C10H20O5/c1-2-12-5-6-14-9-10-15-8-7-13-4-3-11-1/h1-10H2
- InChI Key
- VFTFKUDGYRBSAL-UHFFFAOYSA-N
- Formula
- C10H20O5
- SMILES
- C1COCCOCCOCCOCCO1
- Molecular Weight1
- 220.26
- CAS
- 33100-27-5
- Other Names
-
- 1,4,10,13-pentaoxacyclopentadecane
- 1,4,7,10,13-pentaoxacyclopentadecane
- 15-crown-5 ether
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas 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).
- ΔfH°liquid : Liquid phase 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).
- IE : Ionization energy (eV).
- 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).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (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.
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 |
|---|---|---|---|
| ω | 0.4079 | Relay (1.0) Calculated Property | |
| PAff | 943.80 | kJ/mol | NIST |
| BasG | 899.70 | kJ/mol | NIST |
| ΔcH°liquid | [-5914.30; -5903.00] | kJ/mol |
|
| ΔcH°liquid | -5914.30 ± 1.40 | kJ/mol | NIST |
| ΔcH°liquid | -5903.00 ± 7.30 | kJ/mol | NIST |
| ΔfG° | -474.02 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -799.50 ± 2.00 | kJ/mol | NIST |
| ΔfH°liquid | -879.10 ± 2.00 | kJ/mol | NIST |
| ΔfusH° | 33.41 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [75.70; 79.60] | kJ/mol |
|
| ΔvapH° | 79.57 | kJ/mol | NIST |
| ΔvapH° | 75.70 ± 1.70 | kJ/mol | NIST |
| ΔvapH° | 79.57 ± 0.29 | kJ/mol | NIST |
| ΔvapH° | 79.60 | kJ/mol | NIST |
| ΔvapH° | 79.60 ± 0.30 | kJ/mol | NIST |
| IE | [8.90; 9.60] | eV |
|
| IE | 8.90 | eV | NIST |
| IE | 9.60 | eV | NIST |
| IE | 9.58 | eV | NIST |
| log10WS | -0.12 | Relay (1.0) Calculated Property | |
| logPoct/wat | 0.083 | Crippen Calculated Property | |
| McVol | 170.250 | ml/mol | McGowan Calculated Property |
| Pc | 3228.31 | kPa | Joback Calculated Property |
| Inp | 1554.00 | NIST | |
| I | 2431.00 | NIST | |
| Tboil | 587.42 | K | Relay (1.0) Calculated Property |
| Tc | 771.65 | K | Relay (1.0) Calculated Property |
| Tfus | 253.00 | K | Static Dielectric Permittivity of Homologous Series of Liquid Cyclic Ethers, 3n-Crown-n, n = 4 to 6 |
| Vc | 0.588 | m3/kmol | Relay (1.0) Calculated Property |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | [351.00; 390.70] | K | [0.01; 0.03] |
|
| Tboilr | 351.00 | K | 0.01 | NIST |
| Tboilr | 390.70 | K | 0.03 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [220.01; 627.27] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | -3.72300e+01 | |||
| Coefficient B | 1.00100e+00 | |||
| Coefficient C | -1.69500e-04 | |||
| Coefficient D | -1.67000e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 220.01 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 288.29 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 352.05 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 410.75 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 463.87 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 510.88 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 551.26 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 584.46 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 609.98 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 627.27 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.9423653; 0.0000164] | Pa×s | [253.00; 620.85] |
Joback Predicted correlation
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.85522e+01 | |||
| Coefficient B | 4.67868e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 253.00 | |||
| Temperature range, max. | 620.85 | |||
| η | 0.9423653 | Pa×s | 253.00 | Calculated Property |
| η | 0.0719808 | Pa×s | 293.87 | Calculated Property |
| η | 0.0103035 | Pa×s | 334.74 | Calculated Property |
| η | 0.0022515 | Pa×s | 375.62 | Calculated Property |
| η | 0.0006631 | Pa×s | 416.49 | Calculated Property |
| η | 0.0002430 | Pa×s | 457.36 | Calculated Property |
| η | 0.0001050 | Pa×s | 498.23 | Calculated Property |
| η | 0.0000515 | Pa×s | 539.10 | Calculated Property |
| η | 0.0000279 | Pa×s | 579.98 | Calculated Property |
| η | 0.0000164 | Pa×s | 620.85 | Calculated Property |
Similar Compounds
Find more compounds similar to 15-Crown-5.
Mixtures
- 15-Crown-5 + Carbon dioxide
- lithium bromide + 15-Crown-5 + Water
- 1-Propanol + 15-Crown-5 + sodium iodide
Sources
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Measurements of binary diffusion coefficients and retention factors for dibenzo-24-crown-8 and 15-crown-5 in supercritical carbon dioxide by chromatographic impulse response technique
- The experimental study on the influence of crown ethers and glycols on the mutual solubility of lithium bromide in water
- Effect of temperature on the process of complex formation crown ether 15C5 with Na+ in the mixture of water with methanol
- Partial molar volumes of organic solutes in water. XXVI. 15-Crown-5 and 18-crown-6 ethers at temperatures (298 to 573) K and pressures up to 30 MPa
- Effect of temperature and solvent properties on the process of complex formation between crown ether 15C5 and Na+ in the (propan-1-ol + water) mixture at temperatures from T = 293.15 K to T = 308.15 K
- Effect of temperature on the solvation of 15-crown-5 ether in water-methanol mixtures
- Effect of temperature on the solvation of 15-crown-5 ether inwater ethanol and water propan-1-ol mixtures
- Effect of temperature on the process of complex formation crownether 15C5 with Na+in the (water + ethanol) mixture at temperaturesfrom (293.15 to 308.15) K
- Examination of hydrogen-bonding interactions between dissolved solutes and alkylbenzene solvents based on Abraham model correlations derived from measured enthalpies of solvation
- Effect of Temperature on the Process of Hydrophobic Hydration. Part II. Hydrophobic Hydration of 15-Crown-5 and 18-Crown-6 Ethers
- Static Dielectric Permittivity of Homologous Series of Liquid Cyclic Ethers, 3n-Crown-n, n = 4 to 6
- Partial Molar Volumes and Partial Molar Isentropic Compressions of 15-Crown-5 and 18-Crown-6 Ethers at Infinite Dilution in Water at Temperatures T = (278 to 343) K and Atmospheric Pressure
- Joback Method
- McGowan Method
- NIST Webbook
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.
These property values are available through the Cheméo API. A free account gives you an access key.