C O M M U N I C A T I O N S
Scheme 1. Phase Transfer and NP Hydrolysis in the Cyclohexane/
Water System
°C, and that value increases with increasing temperature (see SI
for thermodynamic details).
The present findings imply that the distribution coefficient of
phosphate esters from water to wet cyclohexane increases greatly
as they proceed from the ground state to the transition state in their
hydrolysis. As has been suggested for nucleophilic displacement
reactions in the vapor phase,12 it seems likely that the present
solvent effects arise in part from greater delocalization of charge
in the transition state than in the ground state. Possible changes in
transition state structure, and the extent to which water molecules
remain associated with phosphate esters when they are transferred
from water to cyclohexane, remain to be determined.
Figure 2. Effect of water concentration on rate of NP2- hydrolysis in
cyclohexane at 90 or 100 °C. Water concentration was adjusted by mixing
wet cyclohexane (4.3 × 10-3 M H2O) with dry cyclohexane. Values are
normalized relative to the rate of hydrolysis in water-saturated cyclohexane
at the appropriate temperature.
Table 1. Rate Constants and Thermodynamics of Activation for
Hydrolysis of NP2- in Water1 and Cyclohexane (Thermodynamic
Parameters in kcal/mol)
∆G‡
∆H‡
T∆S‡
k25 (s-1
)
k25 (s-1 M-1
)
H2O
CHX
44.3
32.9 ( 0.53
47.0
47.6
2.7
14.7
2.0 × 10-20
3.6 × 10-22
3.8 × 10-12
8.8 × 10-10
These rate enhancements approach or surpass the rate enhance-
ments produced by many hydrolytic enzymes and accord with the
possibility that desolvation plays a substantial role in the action of
phosphate monoesterases.
ionized form of NP that had been present in the aqueous phase
(Table 2). Distribution coefficients observed for NPH2, NPH-/
TBA+, and NP2-/2TBA+ were found to be similar, and their rate
constants for hydrolysis in wet cyclohexane were distributed over
a surprisingly narrow range (Table 2).
Acknowledgment. We thank N. H. Williams, A. J. Kirby, and
A. C. Hengge for helpful discussions and N. H. Williams for a gift
of neopentyl phosphate used during the initial stages of this work.
We are grateful to the National Institute of General Medical
Sciences (Grant No. GM-18325) for financial support.
Table 2. Rate Constants for Hydrolysis and Coefficients for
Transfer of NP2-, NPH-, and NPH2 from Water to Cyclohexane
Supporting Information Available: Detailed kinetic methods; van’t
Hoff analysis of equilibria for transfer of NP2- and NPH- from water
to cyclohexane; effect of ester concentration on distribution coefficients
observed for transfer of NP2-, NPH-, and NPH2 from water to
cyclohexane; error analysis for distribution coefficients and rate
constants; estimation of ∆H‡ values for phase transfer catalysis. This
pH (aq.)
TBAc /NPc
species (CHX)
K1
k90 (s-1
)
0
0
NPH2
9.9 × 10-5
5.0 × 10-5
4.7 × 10-6
3.6 × 10-6
7.0 × 10-6
3.6 × 10-6
6.8 × 10-6
1.1 × 10-5
1.8 × 10-5
1.0 × 10-5
1.8
5.5
6.8
12.0
0.09
1.12
1.49
2.0
NPH2 + NPH-
NPH-
NPH- + NP2-
NP2-
In wet cyclohexane, the concentration of water (4.2 × 10-3 M)
is considerably higher than the concentrations of the neopentyl esters
that were present in these experiments (∼10-6 M). Thus, one might
question whether the unexpectedly high apparent reactivity of
monoester dianions in wet cyclohexane arises from a small
population of monoanions that reacts relatively rapidly and that
can be replenished by protons donated by H2O. The similarity of
the observed rate constants for hydrolysis of NPH2, NPH-, and
NP2- in wet cyclohexane seems to render that explanation unlikely.
Transfer to cyclohexane may level the observed rate constants by
removing the intervening water molecules that have been postulated
to participate in intramolecular general acid catalysis,11 tending to
eliminate the special reactivity of monoester monoanions.
For an enzyme acting by desolvation effects, substrate binding
might be compared to solvent transfer in the presence of a phase
transfer catalyst. Scheme 1 shows that for such a catalyst to be
effective, K1 ·K2 ·kCHX must exceed the value of kH2O. In the reactions
described here, the resulting “phase transfer rate enhancement,” as
defined in Scheme 1, is 1.3 × 103-fold for NP2- hydrolysis at 25
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