| Literature DB >> 35936486 |
Chao-Tun Cao1, Chenzhong Cao1.
Abstract
Changes in various physicochemical properties (P (n)) of organic compounds with the number of carbon atoms (n) can be roughly divided into linear and nonlinear changes. To date, there has been no general equation to express nonlinear changes in the properties of organic homologues. This study proposes a general equation expressing nonlinear changes in the physicochemical properties of organic homologues, including boiling point, viscosity, ionization potential, and vapor pressure, named the "NPOH equation", as follows: P (n) = P (1) α n - 1 e ∑i=2 n(β/(i - 1)) where α and β are adjustable parameters, and P (1) represents the property of the starting compound (pseudo-value at n = 1) of each homologue. The results show that various nonlinear changes in the properties of homologues can be expressed by the NPOH equation. Linear and nonlinear changes in the properties of homologues can all be correlated with n and the "sum of carbon number effects", ∑i=2 n(1/i - 1). Using these two parameters, a quantitative correlation equation can be established between any two properties of each homologue, providing convenient mutual estimation of the properties of a homologue series. The NPOH equation can also be used in property correlation for structures with functionality located elsewhere along a linear alkyl chain as well as for branched organic compounds. This work can provide new perspectives for studying quantitative structure-property relationships.Entities:
Year: 2022 PMID: 35936486 PMCID: PMC9352247 DOI: 10.1021/acsomega.2c02828
Source DB: PubMed Journal: ACS Omega ISSN: 2470-1343
Figure 1(a) Relationship of boiling point (Tb), (b) viscosity (μ), and (c) ionization potential (Ip) with the carbon atom number (n) of n-paraffins.
Number of Repeating Structural Units, n, and SCNE Values
| 1 | 0 | 26 | 25 | 3.8160 | 51 | 50 | 4.4992 | 76 | 75 | 4.9014 | |
| 2 | 1 | 1.0000 | 27 | 26 | 3.8544 | 52 | 51 | 4.5188 | 77 | 76 | 4.9145 |
| 3 | 2 | 1.5000 | 28 | 27 | 3.8915 | 53 | 52 | 4.5380 | 78 | 77 | 4.9275 |
| 4 | 3 | 1.8333 | 29 | 28 | 3.9272 | 54 | 53 | 4.5569 | 79 | 78 | 4.9403 |
| 5 | 4 | 2.0833 | 30 | 29 | 3.9617 | 55 | 54 | 4.5754 | 80 | 79 | 4.9530 |
| 6 | 5 | 2.2833 | 31 | 30 | 3.9950 | 56 | 55 | 4.5936 | 81 | 80 | 4.9655 |
| 7 | 6 | 2.4500 | 32 | 31 | 4.0272 | 57 | 56 | 4.6115 | 82 | 81 | 4.9778 |
| 8 | 7 | 2.5929 | 33 | 32 | 4.0585 | 58 | 57 | 4.6290 | 83 | 82 | 4.9900 |
| 9 | 8 | 2.7179 | 34 | 33 | 4.0888 | 59 | 58 | 4.6463 | 84 | 83 | 5.0021 |
| 10 | 9 | 2.8290 | 35 | 34 | 4.1182 | 60 | 59 | 4.6632 | 85 | 84 | 5.0140 |
| 11 | 10 | 2.9290 | 36 | 35 | 4.1468 | 61 | 60 | 4.6799 | 86 | 85 | 5.0257 |
| 12 | 11 | 3.0199 | 37 | 36 | 4.1746 | 62 | 61 | 4.6963 | 87 | 86 | 5.0374 |
| 13 | 12 | 3.1032 | 38 | 37 | 4.2016 | 63 | 62 | 4.7124 | 88 | 87 | 5.0489 |
| 14 | 13 | 3.1801 | 39 | 38 | 4.2279 | 64 | 63 | 4.7283 | 89 | 88 | 5.0602 |
| 15 | 14 | 3.2516 | 40 | 39 | 4.2535 | 65 | 64 | 4.7439 | 90 | 89 | 5.0715 |
| 16 | 15 | 3.3182 | 41 | 40 | 4.2785 | 66 | 65 | 4.7593 | 91 | 90 | 5.0826 |
| 17 | 16 | 3.3807 | 42 | 41 | 4.3029 | 67 | 66 | 4.7744 | 92 | 91 | 5.0936 |
| 18 | 17 | 3.4396 | 43 | 42 | 4.3267 | 68 | 67 | 4.7894 | 93 | 92 | 5.1044 |
| 19 | 18 | 3.4951 | 44 | 43 | 4.3500 | 69 | 68 | 4.8041 | 94 | 93 | 5.1152 |
| 20 | 19 | 3.5477 | 45 | 44 | 4.3727 | 70 | 69 | 4.8186 | 95 | 94 | 5.1258 |
| 21 | 20 | 3.5977 | 46 | 45 | 4.3949 | 71 | 70 | 4.8328 | 96 | 95 | 5.1363 |
| 22 | 21 | 3.6454 | 47 | 46 | 4.4167 | 72 | 71 | 4.8469 | 97 | 96 | 5.1468 |
| 23 | 22 | 3.6908 | 48 | 47 | 4.4380 | 73 | 72 | 4.8608 | 98 | 97 | 5.1571 |
| 24 | 23 | 3.7343 | 49 | 48 | 4.4588 | 74 | 73 | 4.8745 | 99 | 98 | 5.1673 |
| 25 | 24 | 3.7760 | 50 | 49 | 4.4792 | 75 | 74 | 4.8880 | 100 | 99 | 5.1774 |
Correlation Equations of Properties for n-Paraffins H–(CH2)–H (Model Equation: ln(P() = a + b(n – 1) + cSCNE)
| no. | property | range of | ref | |||||||
|---|---|---|---|---|---|---|---|---|---|---|
| 1 | 2–100 | ( | 4.6973 | –0.004569 | 0.51040 | 0.9999 | 0.0057 | 34 | 73 691.18 | |
| 2 | 2–20 | ( | 5.2972 | –0.008981 | 0.42758 | 0.9999 | 0.0030 | 19 | 65 747.43 | |
| 3 | 2–20 | ( | 1.9097 | –0.050147 | –0.24698 | 0.9992 | 0.0191 | 19 | 5084.85 | |
| 4 | 4–16 | ( | 3.6382 | 0.025666 | 0.66368 | 0.9997 | 0.0099 | 11 | 7888.46 | |
| 5 | λ | 5–16 | ( | –2.7579 | –0.014647 | 0.30762 | 0.9944 | 0.0101 | 7 | 177.44 |
| 6 | 5–16 | ( | 1.1369 | –0.048077 | 0.86717 | 0.9990 | 0.0108 | 7 | 978.56 | |
| 7 | μ | 5–35 | ( | –5.6286 | 0.043485 | 1.79992 | 0.9996 | 0.0448 | 28 | 14 301.74 |
| 8 | 4–20 | ( | 0.15997 | –0.003447 | 0.076226 | 0.9987 | 0.0012 | 16 | 2534.24 | |
| 9 | 2–16 | ( | 7.4528 | –0.461790 | –0.36834 | 1.0000 | 0.0103 | 15 | 347 794.19 | |
| 10 | ω | 2–20 | ( | –3.2314 | –0.005694 | 0.90514 | 0.9997 | 0.0158 | 19 | 13 904.65 |
| 11 | 2–11 | ( | 2.5643 | 0.004981 | –0.12156 | 0.9996 | 0.0020 | 10 | 4094.40 | |
| 12 | 5–16 | ( | –1.0445 | –0.016174 | 0.30966 | 0.9994 | 0.0025 | 12 | 3850.05 | |
| 13 | 3–16 | ( | 4.4783 | 0.000031 | 0.45456 | 0.9970 | 0.0213 | 14 | 915.62 | |
| 14 | 2–8 | ( | 1.1261 | 0.536478 | 0.12495 | 0.9990 | 0.0716 | 6 | 736.35 |
Tb, boiling point (K); Tc, critical temperature (K); Pc, critical pressure (MPa); Cp, heat capacity (J·mol–1·K–1); λ, thermal conductivity (W·m–1 K–1); ST, surface tension (mN·m–1); μ, liquid viscosity [μm Pa·s(300 K)]; nD, refractive Index; Pv, vapor pressure (regression in the form of log Pv); ω, acentric factor; Ip, ionization potential (eV); D, liquid density (g·cm3); TF, flash point (K); and Pw, partition coefficient (regression in the form of log Pw). These properties data are listed in the Supporting Information.
Carbon atom number range.
Number of data points.
Correlation Equations of Properties for Cycloalkanes, Alkenes, Alkynes, Alcohols, 2-Methylparaffins, 2,2-dimethylparaffins, 2,3-Dimethylparaffins, and 1-Cyclopentylparaffins (Model Equation: ln(P() = a + b(n – 1) + cSCNE)
Pw, partition coefficient (regression in the form of logPw); other symbols are defined in Table . These properties data are listed in the Supporting Information.
Carbon atom number range.
Number of data points.
Experimental and Calculated Critical Temperature, Tc (K), for n-Paraffins H–(CH2)–H
| 2 | 184.55 | 305.6 | 307.84 | 13 | 508.29 | 676.1 | 678.36 | 24 | 664.29 | 793.90 | |
| 3 | 231.05 | 369.2 | 368.85 | 14 | 526.69 | 693.1 | 694.86 | 25 | 674.29 | 798.76 | |
| 4 | 272.65 | 425.2 | 421.91 | 15 | 543.59 | 708.1 | 709.23 | 26 | 685.19 | 804.63 | |
| 5 | 309.25 | 469.9 | 466.84 | 16 | 559.99 | 722.1 | 722.82 | 27 | 695.09 | 809.28 | |
| 6 | 342.15 | 507.7 | 505.80 | 17 | 574.79 | 734.1 | 734.23 | 28 | 704.59 | 813.41 | |
| 7 | 371.55 | 540.7 | 539.25 | 18 | 589.09 | 747.1 | 744.90 | 29 | 713.79 | 817.16 | |
| 8 | 398.85 | 568.9 | 569.35 | 19 | 601.99 | 755.4 | 753.71 | 30 | 722.69 | 820.52 | |
| 9 | 423.92 | 594.6 | 596.00 | 20 | 615.99 | 767.6 | 763.81 | 31 | 731.69 | 823.96 | |
| 10 | 447.27 | 617.8 | 620.00 | 21 | 629.49 | 773.20 | 32 | 740.09 | 826.68 | ||
| 11 | 468.79 | 639.1 | 641.24 | 22 | 641.59 | 780.77 | |||||
| 12 | 489.29 | 658.2 | 660.90 | 23 | 653.19 | 787.67 |
Number of carbon atoms.
Experimental boiling point (K), from ref (17).
Experimental critical temperature (K), from ref (20).
Critical temperature calculated using eq .
Figure 2Plot of calculated (solid line) and experimental (open circle) critical temperature (Tc) values versus experimental boiling point (Tb) of n-paraffins (n = 2–32).
Correlation Equations between the Boiling Point, Tb, and Other Properties of n-Paraffins (Model Equations 23 and 24)
| no. | property | range of | |||||||
|---|---|---|---|---|---|---|---|---|---|
| 1 | 2–20 | 0.593807 | –0.0056465 | –0.07651 | 0.9989 | 0.0042 | 19 | 3715.10 | |
| 2 | 2–20 | –2.79364 | –0.0468120 | –0.75107 | 0.9996 | 0.0235 | 19 | 10 289.86 | |
| 3 | 4–16 | –1.01102 | 0.0314657 | 0.13146 | 0.9988 | 0.0095 | 11 | 1670.97 | |
| 4 | λ | 5–16 | –7.39959 | –0.0084513 | –0.22859 | 0.9979 | 0.0104 | 7 | 476.21 |
| 5 | 5–16 | (5.77866) | (−0.0542733) | (1.40338) | 0.9998 | 0.0106 | 7 | 4300.28 | |
| 6 | μ | 5–32 | –10.2984 | 0.0487215 | 1.27732 | 0.9992 | 0.0475 | 25 | 6681.44 |
| 7 | 4–20 | –4.48113 | 0.0030487 | –0.46118 | 1.0000 | 0.0019 | 16 | 98 646.53 | |
| 8 | 2–16 | 2.737019 | –0.4605237 | –0.86135 | 1.0000 | 0.0119 | 15 | 339 306.10 | |
| 9 | ω | 2–10 | –7.934717 | –0.0023596 | 0.401052 | 0.9991 | 0.0126 | 19 | 4279.41 |
| 10 | 2–11 | –2.172143 | 0.0013372 | –0.593327 | 0.9999 | 0.0056 | 10 | 19 231.41 | |
| 11 | 5–16 | –5.686163 | –0.0099647 | –0.226592 | 0.9998 | 0.0026 | 12 | 12752.15 | |
| 12 | 3–16 | (9.143340) | (−0.0048236) | (0.977959) | 0.9993 | 0.0206 | 14 | 4213.98 | |
| 13 | 2–8 | –3.631401 | 0.5256402 | –0.321655 | 0.9985 | 0.0686 | 6 | 487.63 |
Symbols are defined in Table , obtained using model equation 23 except when noted otherwise.
Obtained using model equation 24.
Figure 3Plot of calculated (−) and experimental (△) liquid viscosity, μ, values versus experimental boiling point, Tb, of n-paraffins (n = 5–32).
Figure 4Plot of exp(SCNE) versus the parameter c(G) of ref (27) for n-paraffins (n = 4–14).