| Literature DB >> 28787907 |
Sen Guo1, Jingwei He2, Weixun Luo3, Fang Liu4.
Abstract
A series of pyridinol-blocked isophorone isocyanates, based onEntities:
Keywords: blocked isocyanate, deblocking temperature, thermal decomposition, reaction kinetics, mechanism function, polyurethane
Year: 2016 PMID: 28787907 PMCID: PMC5456470 DOI: 10.3390/ma9020110
Source DB: PubMed Journal: Materials (Basel) ISSN: 1996-1944 Impact factor: 3.623
Scheme 1Overall reaction of blocked isocyanates.
Figure 1FTIR spectra of blocked isocyanates at different temperatures.
Deblocking temperatures of blocked isocyanates.
| Blocking Agent | Deblocking Temperature/°C | ||
|---|---|---|---|
| TGA | DSC | CO2 | |
| 2-hydroxypyridine | 73 | 69 | 76 |
| 3-hydroxypyridine | 76 | 72 | 78 |
| 4-hydroxypyridine | 71 | 71 | 77 |
Figure 2DSC thermograms of blocked isocyanates.
Figure 3TGA-DTG thermograms of blocked isocyanates.
Figure 4TGA curves of the blocked isocyanate at different heating rates.
Basis kinetic data of the blocked isocyanate.
| Max mass loss/% | |||
|---|---|---|---|
| 5 | 78 | 139.7 | 36.2 |
| 10 | 79 | 142.2 | 37.5 |
| 15 | 81 | 145.5 | 32.5 |
| 20 | 83 | 152.4 | 30.5 |
| 25 | 85 | 167.6 | 24.8 |
Notes: a β is the heating rate; b Ti is the initial temperature; c Tp is the peak temperature.
Temperatures at the same degree of conversion at different heating rates.
| α | T/K | ||||
|---|---|---|---|---|---|
| β = 5 K·min−1 | β = 10 K·min−1 | β = 15 K·min−1 | β = 20 K·min−1 | β = 25 K·min−1 | |
| 0.10 | 419.4 | 425.7 | 428.3 | 431.3 | 434.6 |
| 0.11 | 426.2 | 434.9 | 440.8 | 444.4 | 445.9 |
| 0.12 | 438.8 | 448.7 | 452.6 | 455.5 | 460.5 |
| 0.13 | 455.7 | 466.9 | 473.5 | 475.3 | 478.3 |
| 0.14 | 465.1 | 476.9 | 481.9 | 487.2 | 491.4 |
| 0.15 | 474.5 | 487.0 | 490.8 | 493.5 | 499.6 |
Figure 5Fitting curves based on FRL (A) and FWO (B) methods.
Activation energy based on FRL and FWO methods.
| α | FRL equation | FWO equation | ||
|---|---|---|---|---|
| E/kJ·mol−1 | r | E/kJ·mol−1 | r | |
| 0.10 | 122.0 | 0.9832 | 147.1 | 0.9949 |
| 0.11 | 129.4 | 0.9821 | 118.6 | 0.9969 |
| 0.12 | 133.8 | 0.9837 | 123.2 | 0.9937 |
| 0.13 | 149.4 | 0.9809 | 120.5 | 0.9817 |
| 0.14 | 134.7 | 0.9909 | 122.4 | 0.9888 |
| 0.15 | 138.2 | 0.9808 | 125.5 | 0.9888 |
Part of the results from the linear least squares method at different kinetic mechanisms of thermal decomposition.
| T/K | Function | ||
|---|---|---|---|
| Valensi | −0.6721 | 0.9231 | |
| 403.2 | Jander | −0.9879 | 0.9941 |
| Mampel Power | −0.7258 | 0.9152 | |
| Valensi | −0.4315 | 0.8956 | |
| 423.2 | Jander | −0.9731 | 0.9965 |
| Mampel Power | −0.6532 | 0.9972 | |
| Valensi | −0.7635 | 0.9466 | |
| 443.2 | Jander | −1.0245 | 0.9895 |
| Mampel Power | −2.0615 | 0.9358 | |
| Valensi | −0.8527 | 0.9911 | |
| 463.2 | Jander | −0.9851 | 0.9953 |
| Mampel Power | −1.4627 | 0.9512 | |
| Valensi | −0.7855 | 0.9263 | |
| 483.2 | Jander | −0.9758 | 0.9910 |
| Mampel Power | −1.1284 | 0.9599 |
Reaction order based on the Crane equation.
| α | n | r |
|---|---|---|
| 0.10 | 1.25 | 0.9974 |
| 0.11 | 1.23 | 0.9889 |
| 0.12 | 1.28 | 0.9934 |
| 0.13 | 1.24 | 0.9888 |
| 0.14 | 1.27 | 0.9961 |
| 0.15 | 1.25 | 0.9983 |