| Literature DB >> 25550724 |
Eléonore Bertaut1, David Landy1.
Abstract
The study of 1:1 cyclodextrin inclusion compounds by isothermal titration calorimetry was explored in a theoretical and experimental point of view to compare the efficiency of conventional and non-conventional experiments. All direct and competitive protocols were described and evaluated in terms of accuracy on both binding constant and inclusion enthalpy. Significant improvement in the calorimetric characterization may be obtained by means of the global analysis of non-conventional experiments coupled to the standard titration protocol. While the titration-release approach proved to be the most accurate strategy for classical complexations, the valuable contribution of other non-conventional experiments was demonstrated for issues concerning weak stability, enthalpy, or solubility.Entities:
Keywords: cyclodextrins; global analysis; inclusion compounds; isothermal titration calorimetry; non-conventional experiments
Year: 2014 PMID: 25550724 PMCID: PMC4273236 DOI: 10.3762/bjoc.10.275
Source DB: PubMed Journal: Beilstein J Org Chem ISSN: 1860-5397 Impact factor: 2.883
Figure 1Non-competitive ITC isotherms for the β-CD-IBU complex at 298 K. Each protocol (from A to H) is defined by the respective content of syringe (top) and cell (bottom). Ø indicates the buffer solution. Lines and dots correspond to theoretical and experimental data, respectively. The x-axis corresponds to the injection number (10 injections per isotherm).
Theoretical uncertainties of K and ΔH for the eight non-competitive ITC protocols with a guest solubility equal to 2 mM.
| 100 M−1 | 1000 M−1 | 10000 M−1 | 100000 M−1 | |||||
| Protocol | ||||||||
| A | >100% | >100% | 11% | 6% | 5% | 1% | 5% | 1% |
| B | >100% | 75% | 12% | 7% | >100% | 4% | >100% | 4% |
| C | 35% | 19% | 6% | 1% | 19% | 7% | 45% | 26% |
| D | >100% | 48% | >100% | 61% | >100% | >100% | >100% | >100% |
| E | >100% | >100% | 38% | 12% | 8% | 1% | 9% | 1% |
| F | >100% | >100% | 43% | 2% | >100% | 66% | >100% | >100% |
| G | >100% | >100% | >100% | >100% | >100% | >100% | >100% | >100% |
| H | >100% | >100% | >100% | >100% | >100% | >100% | >100% | >100% |
Figure 2Theoretical uncertainty on K (left) and ΔH (right) as a function of log K for titration (red curve) and release (black curve) protocols given an aqueous guest solubility equal to 2 mM and for an inclusion enthalpy equal to −3000 cal·mol−1.
Figure 3Theoretical uncertainty on K (left) and ΔH (right) as a function of Log K for titration-titration (red curve) and titration-release (black curve) approaches given an aqueous guest solubility equal to 2 mM and for an inclusion enthalpy equal to −3000 cal·mol−1.
Figure 4Competitive ITC isotherms for the HPβ-CD-β-CD-IBU system at 283 K. Each protocol (from I to P) is defined by the respective content of syringe (top) and cell (bottom). Ø indicates the buffer solution. Lines and dots correspond to theoretical and experimental data, respectively. The x axis corresponds to the injection number (10 injections per isotherm).
Theoretical uncertainties of K for an individual analysis of the eight competitive ITC protocols described in Figure 4, in the case of the HPβ-CD-IBU complex at 283 K (total concentrations are considered as perfectly known).
| Protocol | I | J | K | L | M | N | O | P |
| 16% | 15% | 10% | 6% | 9% | >100% | 88% | >100% | |
Thermodynamic data for the HPβ-CD-IBU complex obtained by a global analysis of the competitive approach and the titration-release approach (considering a 5% uncertainty on each total concentration). Data for the β-CD-IBU complex correspond to the global analysis of titration-release experiments.
| HPβ-CD-IBU | β-CD-IBU | |||||
| Competitive | Titration-release | Titration-release | ||||
| Δ | Δ | Δ | ||||
| 283.0 K | 5457 ± 648 | −9 ± 21 | 5566 ± 252 | −2 ± 15 | 11985 ± 595 | −1954 ± 64 |
| 290.5 K | 5360 ± 637 | −786 ± 32 | 5452 ± 248 | −921 ± 33 | 10804 ± 536 | −2576 ± 84 |
| 298.0 K | 5076 ± 603 | −1733 ± 65 | 5146 ± 234 | −1750 ± 59 | 9502 ± 471 | −3329 ± 110 |
| 305.5 K | 4637 ± 551 | −2649 ± 100 | 4713 ± 215 | −2502 ± 85 | 8153 ± 405 | −4069 ± 137 |
| 313.0 K | 4118 ± 489 | −3387 ± 130 | 4188 ± 191 | −3505 ± 120 | 6855 ± 340 | −4726 ± 163 |
| Δ | −114 cal·mol−1·K−1 | −115 cal·mol−1·K−1 | −94 cal·mol−1·K−1 | |||