| Literature DB >> 36092635 |
Abstract
Capillary flow techniques have been used to determine the translational diffusion constant, D, of squalene in seven alkanes and five cyclohexanes. The alkanes are n-hexane, n-octane, n-decane, n-dodecane, n-tetradecane, 2,2,4,4,6,8,8-heptamethylnonane (isocetane), and 2,6,10,14-tetramethylpentadecane (pristane). The cyclohexanes are cyclohexane, n-butylcyclohexane, n-hexylcyclohexane, n-octylcyclohexane, and n-dodecylcyclohexane. When combined with published data in CD2Cl2, ethyl acetate, n-hexadecane, squalane, n-octane-squalane mixtures, and supercritical CO2, the 35 diffusion constants and viscosities, η, vary by factors of ∼230 and ∼500, respectively. A fit to the modified Stokes-Einstein equation (MSE, D/T = A SE/η p ) gives an average absolute percentage difference (AAPD) of 7.72% between the experimental and calculated D values where p and A SE are constants, T is the absolute temperature, and the AAPD is the average value of (102) (|D calcd - D exptl|/D exptl). Two other MSE fits using subsets of the 35 diffusion constants may be useful for (a) estimating the viscosity of the hydrophobic core of lipid droplets, where squalene is a naturally occurring component, and (b) providing estimates of the D values needed to design extraction processes by which squalene is obtained from plant oils. The Wilke-Chang equation also was considered and found to give larger AAPDs than the corresponding MSE fits.Entities:
Year: 2022 PMID: 36092635 PMCID: PMC9454272 DOI: 10.1021/acsomega.2c03842
Source DB: PubMed Journal: ACS Omega ISSN: 2470-1343
Figure 1Structure of squalene.
Squalene Diffusion Constants
| % difference | |||||||
|---|---|---|---|---|---|---|---|
| solvent | 106 | 102η, P | r, Å | no CO2 | no HPSM | all 35 | |
| 23.0 | 16.50 | 0.306 | 4.30 | –11.2 | –4.51 | –4.51 | |
| 24.0 | 10.07 | 0.514 | 4.20 | –4.99 | –1.88 | 0.17 | |
| 24.0 | 6.27 | 0.850 | 4.08 | 0.70 | –0.006 | 4.15 | |
| 24.0 | 4.18 | 1.41 | 3.70 | –0.52 | –5.01 | 0.95 | |
| 24.0 | 2.91 | 2.14 | 3.50 | 1.28 | –6.38 | 1.15 | |
| 22.75 | 2.10 | 3.18 | 3.24 | 0.38 | –10.0 | –1.26 | |
| 22.5 | 2.36 | 2.97 | 3.08 | –5.62 | –15.0 | –6.92 | |
| 22.75 | 1.11 | 7.24 | 2.69 | –3.77 | –19.1 | –8.25 | |
| 22.5 | 0.670 | 13.8 | 2.35 | –6.28 | –25.1 | –12.8 | |
| squalane | 23.0 | 0.336 | 30.3 | 2.13 | –2.39 | –26.6 | –11.8 |
| pristane | 22.25 | 1.25 | 7.28 | 2.38 | –14.9 | –28.5 | –18.8 |
| HPMN | 24.0 | 1.64 | 3.52 | 3.71 | 17.0 | 4.07 | 14.7 |
| cyclohexane | 24.0 | 5.88 | 0.910 | 4.06 | 1.39 | 0.15 | 4.59 |
| 24.0 | 4.48 | 1.23 | 3.96 | 4.09 | –7.77 | 6.17 | |
| 24.5 | 2.85 | 2.02 | 3.79 | 8.50 | 0.74 | 8.60 | |
| 23.25 | 1.84 | 3.24 | 3.64 | 13.3 | 1.36 | 11.4 | |
| 24.0 | 1.10 | 6.53 | 3.04 | 6.71 | –9.51 | 2.21 | |
| CD2Cl2 | 10.0 | 9.82 | 0.482 | 4.38 | –2.10 | 1.61 | 3.46 |
| CO2, 18 MPa | 41.35 | 68 | 0.0728 | 4.65 | –25.0 | –9.83 | –14.8 |
| CO2, 17 MPa | 41.35 | 71 | 0.0709 | 4.58 | –26.6 | –11.5 | –16.5 |
| CO2, 16 MPa | 41.35 | 66 | 0.0688 | 5.07 | –19.0 | –2.24 | –7.87 |
| CO2, 15 MPa | 41.35 | 71 | 0.0665 | 4.88 | –22.5 | –6.24 | –11.8 |
| CO2, 13 MPa | 41.35 | 78 | 0.0602 | 4.91 | –23.5 | –6.59 | –12.4 |
| EtOAc, 1 bar | 30.0 | 11.71 | 0.399 | 4.75 | 2.78 | 8.26 | 9.41 |
| EtOAc, 75 bar | 30.0 | 10.98 | 0.433 | 4.67 | 2.45 | 7.22 | 8.72 |
| EtOAc, 150 bar | 30.0 | 10.52 | 0.464 | 4.55 | 1.00 | 5.13 | 6.89 |
| EtOAc, 1 bar | 40.0 | 13.38 | 0.359 | 4.77 | 1.41 | 7.69 | 8.39 |
| EtOAc, 75 bar | 40.0 | 12.65 | 0.390 | 4.65 | 0.16 | 5.68 | 6.70 |
| EtOAc, 150 bar | 40.0 | 11.88 | 0.419 | 4.61 | 0.51 | 5.46 | 6.79 |
| EtOAc, 1 bar | 50.0 | 15.14 | 0.325 | 4.81 | 0.42 | 7.46 | 7.72 |
| EtOAc, 75 bar | 50.0 | 14.19 | 0.354 | 4.71 | –0.17 | 6.12 | 6.75 |
| EtOAc, 150 bar | 50.0 | 13.38 | 0.381 | 4.64 | –0.37 | 5.31 | 6.24 |
| EtOAc, 1 bar | 60.0 | 17.22 | 0.295 | 4.80 | –1.38 | 6.34 | 6.18 |
| EtOAc, 75 bar | 60.0 | 16.03 | 0.323 | 4.71 | –1.72 | 5.23 | 5.46 |
| EtOAc, 150 bar | 60.0 | 15.00 | 0.348 | 4.67 | –1.25 | 5.11 | 5.65 |
From the refs in the Experimental Methods section.
Calculated from the D values using eq .
Percentage differences between 30 calculated and experimental D values using fit to eq excluding CO2 data.
Same as footnote c using fit to eq for 29 D values excluding HPSM data.
Same as footnote c using fit to eq for all 35 experimental D values.
From ref (5) (xi = mole fraction squalane in n-C8–squalane mixed solvents).
From ref (12).
All CO2D values are from ref (14).
All EtOAc D values are from ref (13).
Values of p, −Log ASE, and R2 for the Fits of Squalene’s D Values to eq
| solvents | –log | ||
|---|---|---|---|
| all 35 | 0.865 ± 0.007 | 9.449 ± 0.017 | 0.995 |
| no CO2 | 0.827 ± 0.009 | 9.385 ± 0.021 | 0.997 |
| no HPSMs | 0.905 ± 0.008 | 9.549 ± 0.018 | 0.997 |
All 35 of the D values in Table are included.
The five D values in CO2 are excluded.
The six D values in the HPSMs are excluded.
AAPD between Experimental and Calculated Diffusion Constants for the Three Fits to eq
| solvent type | no. of solvents | no CO2 | no HPSMs | all |
|---|---|---|---|---|
| HPSM | 6 | 8.33 | 19.7 | 12.2 |
| CO2 | 5 | 23.3 | 7.28 | 12.7 |
| 6 | 3.18 | 4.63 | 2.03 | |
| cyclohexanes | 5 | 6.80 | 3.91 | 6.59 |
| CD2Cl2 | 1 | 2.10 | 1.61 | 3.46 |
| EtOAc | 12 | 1.135 | 6.25 | 7.075 |
| AAPD for included | 3.96 | 5.53 | 7.72 |
AAPD between experimental and calculated D values for each solvent group.
AAPD for 30 solvents excluding CO2 data.
AAPD for 29 solvents excluding HPSM data.
AAPD for all 35 solvents.
Figure 2Plot of log(D/T) vs. log η for squalene. D is in cm2 s–1 and η in P. The line is drawn using the fit to eq for all 35 of squalene’s D values.
Figure 3Plot of calculated vs. experimental diffusion constants for squalene. The calculated values were obtained using the MSE fit to eq for all 35 of squalene’s D values.
Viscosity Calculations for Squalene’s Solvents
| % difference | |||||
|---|---|---|---|---|---|
| solvent | 102η,
P | no CO2 | no HPSM | all 35 | |
| 23.0 | 0.306 | –13.4 | –4.97 | –5.19 | |
| 24.0 | 0.514 | –6.00 | –2.08 | 0.195 | |
| 24.0 | 0.850 | 0.841 | –0.007 | 4.81 | |
| 24.0 | 1.41 | –0.611 | –5.51 | 1.11 | |
| 24.0 | 2.14 | 1.55 | –7.02 | 1.34 | |
| 22.75 | 3.18 | 0.472 | –11.0 | –1.43 | |
| 22.5 | 2.97 | –6.75 | –16.4 | –7.95 | |
| 22.75 | 7.24 | –4.54 | –20.9 | –9.47 | |
| 22.5 | 13.8 | –7.55 | –27.3 | –14.6 | |
| squalane | 23.0 | 30.3 | –2.87 | –28.9 | –13.6 |
| pristane | 22.25 | 7.28 | –17.7 | –30.9 | –21.4 |
| HPMN | 24.0 | 3.52 | 21.0 | 4.51 | 17.2 |
| cyclohexane | 24.0 | 0.910 | 1.67 | 0.154 | 5.32 |
| 24.0 | 1.23 | 4.97 | 0.514 | 7.18 | |
| 24.5 | 2.02 | 10.3 | 0.753 | 9.94 | |
| 23.25 | 3.24 | 16.3 | 1.50 | 13.2 | |
| 24.0 | 6.53 | 8.25 | –10.5 | 2.57 | |
| CD2Cl2 | 10.0 | 0.482 | –2.61 | 1.71 | 3.94 |
| CO2, 18 MPa | 41.35 | 0.0728 | –29.4 | –10.8 | –17.0 |
| CO2, 17 MPa | 41.35 | 0.0709 | –31.1 | –12.6 | –18.8 |
| CO2, 16 MPa | 41.35 | 0.0688 | –22.5 | 2.47 | –9.04 |
| CO2, 15 MPa | 41.35 | 0.0665 | –26.6 | –6.85 | –13.5 |
| CO2, 13 MPa | 41.35 | 0.0602 | –27.6 | –7.27 | –14.3 |
| EtOAc, 1 bar | 30.0 | 0.399 | 3.57 | 9.17 | 11.0 |
| EtOAc, 75 bar | 30.0 | 0.433 | 3.17 | 8.03 | 10.2 |
| EtOAc, 150 bar | 30.0 | 0.464 | 1.37 | 5.67 | 7.99 |
| EtOAc, 1 bar | 40.0 | 0.359 | 1.90 | 8.54 | 9.75 |
| EtOAc, 75 bar | 40.0 | 0.390 | 0.390 | 6.31 | 7.81 |
| EtOAc, 150 bar | 40.0 | 0.419 | 0.790 | 6.04 | 7.88 |
| EtOAc, 1 bar | 50.0 | 0.325 | 0.702 | 8.29 | 8.99 |
| EtOAc, 75 bar | 50.0 | 0.354 | –0.028 | 6.79 | 7.84 |
| EtOAc, 150 bar | 50.0 | 0.381 | –0.280 | 5.87 | 7.23 |
| EtOAc, 1 bar | 60.0 | 0.295 | –1.49 | 7.02 | 7.17 |
| EtOAc, 75 bar | 60.0 | 0.323 | –1.89 | 5.79 | 6.33 |
| EtOAc, 150 bar | 60.0 | 0.348 | –1.34 | 5.66 | 6.56 |
From the refs in the Experimental Methods section.
Percentage differences between calculated and experimental viscosities using fit to eq excluding CO2 data.
Same as footnote c using fit to eq excluding HPSM data.
Same as footnote c using fit to eq for all 35 experimental D values.
From ref (5) (xi = mole fraction squalane in n-C8–squalane mixed solvents).
From ref (12).
All CO2D values are from ref (14).
All EtOAc D values are from ref (13).
AAPD between Experimental and Calculated Viscosities for the Three Fits to eq
| solvent type | no. of solvents | no CO2 | no HPSMs | all |
|---|---|---|---|---|
| HPSM | 6 | 10.1 | 21.5 | 14.0 |
| CO2 | 5 | 27.4 | 8.00 | 14.5 |
| 6 | 3.81 | 5.10 | 2.35 | |
| cyclohexanes | 5 | 8.30 | 2.68 | 7.64 |
| CD2Cl2 | 1 | 2.61 | 1.71 | 3.94 |
| EtOAc | 12 | 1.41 | 6.93 | 8.23 |
| AAPD for included | 4.82 | 5.82 | 8.90 |
AAPD between experimental and calculated viscosities for each solvent group.
AAPD for 30 solvents excluding CO2 data.
AAPD for 29 solvents excluding HPSM data.
AAPD for all 35 solvents.
Figure 4Plot of calculated vs. experimental viscosities for squalene’s solvents. The calculated values were obtained using the fit that omitted squalene’s D values in supercritical CO2.
AAPD between Experimental and Calculated Diffusion Constants for the WCE and MSE Correlations by the Solvent Group
| solvent type | no. of solvents | WCE | MSE |
|---|---|---|---|
| HPSM | 6 | 10.9 | 12.2 |
| CO2 | 5 | 32.4 | 12.7 |
| 6 | 5.53 | 2.03 | |
| cyclohexanes | 5 | 7.24 | 6.59 |
| CD2Cl2 | 1 | 13.6 | 3.46 |
| EtOAc | 12 | 6.77 | 7.075 |
| all solvents | 35 | 11.2 | 7.72 |
| without CO2 | 30 | 7.65 | 3.96 |
AAPDs for this column are from the “all” column” in Table except for the “without CO2” entry which is the “AAPD for included” entry in the “no CO2” column in Table .
Figure 5Plot of calculated vs. experimental diffusion constants (in cm2 s–1) for squalene. The calculated values were obtained using the Wilke–Chang correlation, eq , for all 35 of squalene’s D values.