- InChI
- InChI=1S/C28H40O10/c1-2-6-26-25(5-1)35-21-17-31-13-9-29-11-15-33-19-23-37-27-7-3-4-8-28(27)38-24-20-34-16-12-30-10-14-32-18-22-36-26/h1-8H,9-24H2
- InChI Key
- MXCSCGGRLMRZMF-UHFFFAOYSA-N
- Formula
- C28H40O10
- SMILES
-
c1ccc2c(c1)OCCOCCOCCOCCOc1cccc
c1OCCOCCOCCOCCO2 - Molecular Weight1
- 536.62
- Other Names
-
- 6,7,9,10,12,13,15,16,23,24,26,27,29,30,32,33-hexadecahydrodibenzo[b,q][1,4,7,10,13,16,19,22,25,28]decaoxacyclotriacontine
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- Cp,solid : Solid 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).
- 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.
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° | -680.60 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -1539.67 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 86.53 | kJ/mol | Enthalp... |
| ΔvapH° | 133.08 | kJ/mol | Joback Calculated Property |
| log10WS | -3.04 | Crippen Calculated Property | |
| logPoct/wat | 3.015 | Crippen Calculated Property | |
| McVol | 405.700 | ml/mol | McGowan Calculated Property |
| Pc | 1450.14 | kPa | Joback Calculated Property |
| Tboil | 1282.48 | K | Joback Calculated Property |
| Tc | 1590.25 | K | Joback Calculated Property |
| Tfus | 377.60 | K | Enthalp... |
| Vc | 1.371 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [1056.51; 1403.54] | J/mol×K | [1282.48; 1590.25] | 
|
|
T(K) Ideal gas heat capacity (J/mol×K) 1050 1100 1150 1200 1250 1300 1350 1400 1300 1400 1500 | ||||
| Cp,gas | 1403.54 | J/mol×K | 1282.48 | Joback Calculated Property |
| Cp,gas | 1370.17 | J/mol×K | 1333.78 | Joback Calculated Property |
| Cp,gas | 1327.37 | J/mol×K | 1385.07 | Joback Calculated Property |
| Cp,gas | 1274.86 | J/mol×K | 1436.37 | Joback Calculated Property |
| Cp,gas | 1212.39 | J/mol×K | 1487.66 | Joback Calculated Property |
| Cp,gas | 1139.70 | J/mol×K | 1538.96 | Joback Calculated Property |
| Cp,gas | 1056.51 | J/mol×K | 1590.25 | Joback Calculated Property |
| Cp,liquid | [1144.60; 1202.00] | J/mol×K | [390.00; 470.00] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 1140 1150 1160 1170 1180 1190 1200 400 420 440 460 | ||||
| Cp,liquid | 1144.60 | J/mol×K | 390.00 | Enthalp... |
| Cp,liquid | 1148.90 | J/mol×K | 395.00 | Enthalp... |
| Cp,liquid | 1153.00 | J/mol×K | 400.00 | Enthalp... |
| Cp,liquid | 1159.50 | J/mol×K | 405.00 | Enthalp... |
| Cp,liquid | 1164.60 | J/mol×K | 410.00 | Enthalp... |
| Cp,liquid | 1169.30 | J/mol×K | 415.00 | Enthalp... |
| Cp,liquid | 1179.20 | J/mol×K | 420.00 | Enthalp... |
| Cp,liquid | 1186.20 | J/mol×K | 425.00 | Enthalp... |
| Cp,liquid | 1187.90 | J/mol×K | 430.00 | Enthalp... |
| Cp,liquid | 1195.00 | J/mol×K | 435.00 | Enthalp... |
| Cp,liquid | 1196.60 | J/mol×K | 440.00 | Enthalp... |
| Cp,liquid | 1199.20 | J/mol×K | 445.00 | Enthalp... |
| Cp,liquid | 1201.20 | J/mol×K | 450.00 | Enthalp... |
| Cp,liquid | 1200.90 | J/mol×K | 455.00 | Enthalp... |
| Cp,liquid | 1201.60 | J/mol×K | 460.00 | Enthalp... |
| Cp,liquid | 1202.00 | J/mol×K | 465.00 | Enthalp... |
| Cp,liquid | 1201.90 | J/mol×K | 470.00 | Enthalp... |
| Cp,solid | [668.80; 868.20] | J/mol×K | [295.00; 360.00] |
|
|
T(K) Solid phase heat capacity (J/mol×K) 650 700 750 800 850 300 320 340 360 | ||||
| Cp,solid | 668.80 | J/mol×K | 295.00 | Enthalp... |
| Cp,solid | 680.40 | J/mol×K | 298.15 | Enthalp... |
| Cp,solid | 686.90 | J/mol×K | 300.00 | Enthalp... |
| Cp,solid | 700.30 | J/mol×K | 305.00 | Enthalp... |
| Cp,solid | 715.30 | J/mol×K | 310.00 | Enthalp... |
| Cp,solid | 728.40 | J/mol×K | 315.00 | Enthalp... |
| Cp,solid | 741.60 | J/mol×K | 320.00 | Enthalp... |
| Cp,solid | 755.50 | J/mol×K | 325.00 | Enthalp... |
| Cp,solid | 769.90 | J/mol×K | 330.00 | Enthalp... |
| Cp,solid | 783.30 | J/mol×K | 335.00 | Enthalp... |
| Cp,solid | 797.00 | J/mol×K | 340.00 | Enthalp... |
| Cp,solid | 811.50 | J/mol×K | 345.00 | Enthalp... |
| Cp,solid | 826.40 | J/mol×K | 350.00 | Enthalp... |
| Cp,solid | 844.90 | J/mol×K | 355.00 | Enthalp... |
| Cp,solid | 868.20 | J/mol×K | 360.00 | Enthalp... |
| η | [4.4800360e-10; 0.0000003] | Pa×s | [690.12; 1282.48] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 5.00e-8 1.00e-7 1.50e-7 2.00e-7 2.50e-7 3.00e-7 3.50e-7 800 1000 1200 | ||||
| η | 0.0000003 | Pa×s | 690.12 | Joback Calculated Property |
| η | 5.3958678e-08 | Pa×s | 788.85 | Joback Calculated Property |
| η | 1.3512811e-08 | Pa×s | 887.57 | Joback Calculated Property |
| η | 4.4648933e-09 | Pa×s | 986.30 | Joback Calculated Property |
| η | 1.8046668e-09 | Pa×s | 1085.03 | Joback Calculated Property |
| η | 8.4840951e-10 | Pa×s | 1183.75 | Joback Calculated Property |
| η | 4.4800360e-10 | Pa×s | 1282.48 | Joback Calculated Property |
| Pvap | [0.03; 0.27] | kPa | [545.00; 595.00] |
|
|
T(K) Vapor pressure (kPa) 0.05 0.1 0.15 0.2 0.25 560 580 | ||||
| Pvap | 0.04 | kPa | 545.00 | Enthalp... |
| Pvap | 0.03 | kPa | 545.00 | Enthalp... |
| Pvap | 0.03 | kPa | 545.00 | Enthalp... |
| Pvap | 0.04 | kPa | 550.00 | Enthalp... |
| Pvap | 0.04 | kPa | 550.00 | Enthalp... |
| Pvap | 0.04 | kPa | 550.00 | Enthalp... |
| Pvap | 0.05 | kPa | 555.00 | Enthalp... |
| Pvap | 0.05 | kPa | 555.00 | Enthalp... |
| Pvap | 0.05 | kPa | 555.00 | Enthalp... |
| Pvap | 0.07 | kPa | 560.00 | Enthalp... |
| Pvap | 0.06 | kPa | 560.00 | Enthalp... |
| Pvap | 0.06 | kPa | 560.00 | Enthalp... |
| Pvap | 0.08 | kPa | 565.00 | Enthalp... |
| Pvap | 0.08 | kPa | 565.00 | Enthalp... |
| Pvap | 0.08 | kPa | 565.00 | Enthalp... |
| Pvap | 0.09 | kPa | 570.00 | Enthalp... |
| Pvap | 0.09 | kPa | 570.00 | Enthalp... |
| Pvap | 0.10 | kPa | 570.00 | Enthalp... |
| Pvap | 0.12 | kPa | 575.00 | Enthalp... |
| Pvap | 0.12 | kPa | 575.00 | Enthalp... |
| Pvap | 0.12 | kPa | 575.00 | Enthalp... |
| Pvap | 0.14 | kPa | 580.00 | Enthalp... |
| Pvap | 0.15 | kPa | 580.00 | Enthalp... |
| Pvap | 0.14 | kPa | 580.00 | Enthalp... |
| Pvap | 0.18 | kPa | 585.00 | Enthalp... |
| Pvap | 0.18 | kPa | 585.00 | Enthalp... |
| Pvap | 0.19 | kPa | 585.00 | Enthalp... |
| Pvap | 0.22 | kPa | 590.00 | Enthalp... |
| Pvap | 0.22 | kPa | 590.00 | Enthalp... |
| Pvap | 0.21 | kPa | 590.00 | Enthalp... |
| Pvap | 0.27 | kPa | 595.00 | Enthalp... |
| Pvap | 0.26 | kPa | 595.00 | Enthalp... |
| Pvap | 0.27 | kPa | 595.00 | Enthalp... |
Similar Compounds
Find more compounds similar to dibenzo-30-crown-10.
Sources
- Crippen Method
- Crippen Method
- Enthalpies of fusion, vaporisation and sublimation of crown ethers determined by thermogravimetry and differential scanning calorimetry
- Joback Method
- McGowan Method
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.