| Literature DB >> 21541050 |
Malcolm J D'Souza1, Shannon E Carter, Dennis N Kevill.
Abstract
The specific rates of solvolysis of neopentyl chloroformate (1) have been determined in 21 pure and binary solvents at 45.0 °C. In most solvents the values are essentially identical to those for ethyl and n-propyl chloroformates. However, in aqueous-1,1,1,3,3,3-hexafluoro-2-propanol mixtures (HFIP) rich in fluoroalcohol, 1 solvolyses appreciably faster than the other two substrates. Linear free energy relationship (LFER) comparison of the specific rates of solvolysis of 1 with those for phenyl chloroformate and those for n-propyl chloroformate are helpful in the mechanistic considerations, as is also the treatment in terms of the Extended Grunwald-Winstein equation. It is proposed that the faster reaction for 1 in HFIP rich solvents is due to the influence of a 1,2-methyl shift, leading to a tertiary alkyl cation, outweighing the only weak nucleophilic solvation of the cation possible in these low nucleophilicity solvents.Entities:
Keywords: 1,2-methyl shift; Grunwald-Winstein equations; LFER; addition-elimination; ionization; neopentyl chloroformate; solvolysis
Mesh:
Substances:
Year: 2011 PMID: 21541050 PMCID: PMC3083697 DOI: 10.3390/ijms12021161
Source DB: PubMed Journal: Int J Mol Sci ISSN: 1422-0067 Impact factor: 5.923
Figure 1.Molecular structures of neopentyl chloroformate (1), phenyl chloroformate (2), and n-propyl chloroformate (3).
Scheme 1.Stepwise addition-elimination mechanism through a tetrahedral intermediate for chloroformate esters.
Scheme 2.Possible unimolecular solvolytic pathways for chloroformate esters.
Specific rates of solvolysis (k) of 1, in several pure and binary solvents at 45.0 °C, and literature values for NT and YCl.
| 100% MeOH | 47.9 ± 0.3 | 0.17 | −1.2 |
| 90% MeOH | 77.6 ± 0.6 | −0.01 | −0.20 |
| 80% MeOH | 91.3 ± 0.6 | −0.06 | 0.67 |
| 100% EtOH | 16.3 ± 0.3 | 0.37 | −2.50 |
| 90% EtOH | 27.7 ± 0.1 | 0.16 | −0.90 |
| 80% EtOH | 34.3 ± 0.1 | 0.00 | 0.00 |
| 90% Acetone | 0.804 ± 0.005 | −0.35 | −2.39 |
| 80% Acetone | 2.99 ± 0.04 | −0.37 | −0.80 |
| 70% Acetone | 7.81 ± 0.01 | −0.42 | 0.17 |
| 60% Acetone | 11.7 ± 0.1 | −0.52 | 1.00 |
| 97% TFE (w/w) | 0.697 ± 0.002 | −3.30 | 2.83 |
| 90% TFE (w/w) | 1.14 ± 0.01 | −2.55 | 2.85 |
| 70% TFE (w/w) | 4.07 ± 0.02 | −1.98 | 2.96 |
| 50% TFE (w/w) | 7.89 ± 0.07 | −1.73 | 3.16 |
| 80T-20E | 0.455 ± 0.002 | −1.76 | 1.89 |
| 40T-60E | 4.44 ± 0.08 | −0.34 | −0.48 |
| 20T-80E | 11.3 ± 0.1 | 0.08 | −1.42 |
| 97% HFIP (w/w) | 14.5 ± 0.1 | −5.26 | 5.17 |
| 90% HFIP (w/w) | 8.48 ± 0.01 | −3.84 | 4.41 |
| 70% HFIP (w/w) | 4.09 ± 0.01 | −2.94 | 3.83 |
| 50% HFIP (w/w) | 5.48 ± 0.02 | −2.49 | 3.80 |
Substrate concentration of ca. 0.0052 M; binary solvents on a volume-volume basis at 25.0 °C, except for TFE-H2O and HFIP-H2O solvents which are on a weight-weight basis. T-E are TFE-ethanol mixtures;
With associated standard deviation;
Refs [28,29];
Refs [24,26].
Correlation of the specific rates of solvolysis of neopentyl chloroformate (this study) and several other chloroformate esters (values from the literature), using the extended Grunwald-Winstein equation (Equation 3).
| neoPOCOCl | 13 | 1.76 ± 0.14 | 0.48 ± 0.06 | 0.14 ± 0.08 | 3.67 | 0.977 | 226 | A-E |
| 8 | 0.36 ± 0.10 | 0.81 ± 0.14 | −2.79 ± 0.33 | 0.44 | 0.938 | 18 | I | |
| 22 | 1.57 ± 0.12 | 0.56 ± 0.06 | 0.15 ± 0.08 | 2.79 | 0.947 | 83 | A-E | |
| 6 | 0.40 ± 0.12 | 0.64 ± 0.13 | −2.45 ± 0.27 | 0.63 | 0.942 | 11 | I | |
| 8 | 0.66 ± 0.14 | 0.91 ± 0.19 | −2.61 ± 0.44 | 0.73 | 0.912 | 12 | I | |
| EtOCOCl | 28 | 1.56 ± 0.09 | 0.55 ± 0.03 | 0.19 ± 0.24 | 2.84 | 0.967 | 179 | A-E |
| 7 | 0.69 ± 0.13 | 0.82 ± 0.16 | −2.40 ± 0.27 | 0.84 | 0.946 | 17 | I | |
| MeOCOCl | 19 | 1.59 ± 0.09 | 0.58 ± 0.05 | 0.16 ± 0.07 | 2.74 | 0.977 | 171 | A-E |
| PhOCOCl | 49 | 1.66 ± 0.05 | 0.56 ± 0.03 | 0.15 ± 0.07 | 2.95 | 0.980 | 568 | A-E |
| BzOCOCl | 11 | 0.25 ± 0.05 | 0.66 ± 0.06 | −2.05± 0.11 | 0.38 | 0.976 | 80 | I |
| 9 | 1.35 ± 0.22 | 0.40 ± 0.05 | 0.18 ± 0.07 | 3.38 | 0.960 | 35 | A-E | |
| 16 | 0.28 ± 0.04 | 0.59 ± 0.04 | −0.32 ± 0.06 | 0.47 | 0.982 | 176 | I | |
| 2-AdOCOCl | 19 | 0.03 ± 0.07 | 0.48 ± 0.04 | −0.10 ± 0.09 | 0.06 | 0.971 | 130 | I |
| 1-AdOCOCl | 11 | 0.08 ± 0.20 | 0.59 ± 0.05 | 0.06 ± 0.08 | 0.14 | 0.985 | 133 | I |
n is the number of solvents;
With associated standard error;
Multiple Correlation Coefficient;
F-test value;
Addition-elimnation;
Ionization;
See text for references giving the source of this data;
Calculated for the same eight solvents as are used in the parallel treatment of neopentyl chloroformate solvolyses.
Figure 2.The plot of log(k/k) for solvolyses of neopentyl chloroformate (1) at 45.0 °C against log(k/ko) values for solvolyses of phenyl chloroformate (2) at 25.0 °C.
Figure 3.The plot of log(k/k) values for solvolyses of neopentyl chloroformate (1) at 45.0 °C against log(k/ko) values for solvolyses of n-propyl chloroformate (3) at 25.0 °C.
Figure 4.The plot of log(k/k) values for solvolyses of neopentyl chloroformate (1) at 45.0 °C against 1.76 N + 0.48 Y. The points for HFIP-H2O and TFE-H2O mixtures are not included in the correlation. They are shown in the figure to demonstrate their appreciable deviations from the correlation line.
Figure 5.The plot of log(k/k) values for solvolyses of neopentyl chloroformate (1) against at 45.0 °C against (0.36 NT + 0.81 YCl) for HFIP-H2O and TFE-H2O mixtures.