Dipole Formation/SolVent Electrostriction in Subtilisin Catalysis
J. Am. Chem. Soc., Vol. 119, No. 40, 1997 9333
air oven (Blue M Corp, Blue Island, IL). The suspension was
maintained by sonication during sampling of the stock enzyme solution.
The transesterification reaction of acetyl-L-phenylalanine ethyl ester
(APEE) was then initiated by adding 75 µL of a freshly prepared stock
solution of APEE in n-propanol. The final concentrations of the
substrates were 1 M n-propanol and 5-40 mM APEE in a 1 mL total
liquid volume. Pressurization was achieved with oxygen-free helium
and was complete within 20-30 s of the substrate being added to the
pressure bomb. In a control experiment to investigate potential heating
upon pressurization, pressurization of the water-filled bomb to 500 atm
over 5 s caused a temperature rise of less than 1 °C, measured with a
high-pressure thermocouple.
Samples were periodically withdrawn from the reactor, and the
formation of acetyl-L-phenylalanine propyl ester was followed by GC-
MS using a 25 m, 95% methyl-5% biphenyl capillary column (Hewlett-
Packard). There was no measurable reaction in hexane in the absence
of enzyme and hence no detectable product. Therefore, a lower limit
of the enzymatic rate enhancement relative to the uncatalyzed reaction
Figure 1. Catalytic efficiency of subtilisin Carlsberg measured for
transesterification in hexane as a function of pressure. The curve
represents a quadratic fit to the data. The activation volume was
calculated from the slope of the quadratic at 1 bar.
at room temperature was determined by dividing kcat/Km (4.6 M-1 s-1
)
APEE are plotted against (∂q/∂P) in Figure 2.28 Values of (∂q/
∂P) were calculated from literature data for the dependence of
the solvent dielectric constant on pressure.29-32 As shown by
the plot, pressurization of subtilisin Carlsberg significantly
increased or decreased catalytic efficiencies for transesterifica-
tion, depending on the solvent. For example, kcat/Km in propyl
ether increased from 0.44 M-1‚s-1 at ambient pressure to 4.6
M-1‚s-1 at 1000 bar (i.e., ∆Vq) -55 mL/mol), a factor of
greater than 10. In contrast, the apparent activation volume in
acetone is 58 mL/mol, which corresponds to a 10-fold reduction
in kcat/Km at 1000 bar.
The good linear correlation between ∆Vq and (∂q/∂P) for the
various solvents demonstrates the strong participation of
electrostatic effects during the formation of the transition state.
From eq 3, the slope of the line equals -NA∆(µ2/r3). Estimating
the value of r from the known geometry of the transition state
thus enables one to calculate the apparent change of polarity
for the formation of the transition-state acyl-enzyme complex
(eq 4). The most likely source of this polarity change, based
on the widely accepted charge-transfer mechanism of serine
proteases in water, is the developing charge on both His64 and
the substrate carboxyl group during formation of the transition
state.
by the rate constant for the uncatalyzed reaction estimated from the
measured detection limit of the gas chromatograph for acetyl-L-
phenylalanine propyl ester (2.2 × 10-10 M-1 s-1). The estimated lower
limit of the rate enhancement was thus ca. 2.1 × 1010.24
The initial rates increased linearly with substrate concentration,
indicating that the reaction followed first-order kinetics over the
substrate range tested (5-40 mM). To convert the reaction velocities
into the kinetic parameter kcat/Km, the fraction of active sites available
in the suspended subtilisin powders (which were prepared exactly the
same way for all experiments) was assumed to be 15%, independent
of pressure. This value is based upon our previous active-site titration
measurements for this enzyme in a variety of solvents and is in
agreement with the results of Affleck et al.3 for the same lyophilization
procedure. The relatively low fraction of competent active sites is
reportedly due to the irreversible (in organic solvents) partial unfolding
of the native enzyme structure during the lyophilization process.25,26
Once the sonicated powders are suspended in organic solvent, no
treatment, including pressurization, has been shown to induce irrevers-
ibly denatured enzyme to refold to the native and active form. Hence
the assumption that the competent active-site concentration is inde-
pendent of pressure.
Because the kcat/Km values are reported in pressure-dependent units
of M-1‚s-1, compression of solvent must be accounted for by correcting
the calculated activation volumes by RTâT, where âT is the isothermal
compressibility of the solvent.27 For subtilisin-catalyzed transesteri-
fication in organic solvents, this adjustment typically resulted in a
correction of 3-4 cm3/mol.
In eq (4), the term µs2/rs3 can be calculated for the substrate
in its ground state using standard computational methods.33 For
APEE in organic solvents, a radius of 3.9 Å was calculated
from a van der Waals volume of 184 Å3.34 Optimizing the
structure of APEE by molecular simulation in a low dielectric
and calculating its dipole moment using the method of Pullman
Results and Discussion
Figure 1 plots the catalytic efficiencies in hexane versus
pressure. As is often the case, this plot exhibits slight curvature,
which is typically described by a quadratic series in pressure.12
The value for ∆Vq in hexane was obtained from Figure 1 by
evaluating the slope of this quadratic at 1 bar.12,13 The
uncatalyzed reaction was very slow at room temperature (no
measurable product in hexane after 48 h). However, cursory
rate measurements of the uncatalyzed reaction in hexane at 150
°C provided an upper limit for the reaction rate of ∼0.4 µM/h
and showed very little effect of pressure (∆Vq∼ -5 mL/mol at
100 °C based on a comparison of the uncatalyzed reaction rates
at 1 and 500 bar).
(28) We did not compare ester hydrolysis in aqueous solution to
transesterification in organic solvents for two primary reasons. First, the
two types of reactions have different rate-limiting steps. The rate-controlling
step for subtilisin-catalyzed ester hydrolysis is deacylation (Bonneau, P.
R.; Graycar, T. P.; Estell, D. A.; Jones, B. J. J. Am. Chem. Soc. 1991, 113,
1026), whereas the rate-controlling step for transesterification in organic
solvents is acylation (Wangikar, P. P.; Graycar, T. P.; Estell, D. A.; Clark,
D. S.; Dordick, J. S. J. Am. Chem. Soc. 1993, 115, 12231. Chatterjee, S.;
Russell, A. J. Biotechnol. Bioeng. 1992, 40, 1069.) Moreover, water differs
in its mechanism of electrostatic solvation compared with more apolar
solvents (Whalley, E. J. Chem Phys., 1963, 38, 1400.) and commonly
engages in nonelectrostrictive interactions. These effects often cause
deviations from the Kirkwood model for electrostriction (Isaacs, N. Liquid
Phase High Pressure Chemistry; John Wiley & Sons: Chichester, 1981 pp
181-343. Hamann, S. D. Mod. Asp. Electochem. 1972, 9, 47.).
(29) Brazier, D. W.; Freeman, G. R. Canadian J. Chem. 1969, 47, 893.
(30) Owen, B. B.; Stuart R. Brinkley, J. Phys. ReV. 1943, 64, 32.
(31) Schornack, L. G.; Eckert, C. A. J. Phys. Chem. 1970, 74, 3014.
(32) Skinner, J. F.; Cussler, E. L.; Fuoss, R. M. J. Phys. Chem. 1968,
72, 1057.
Effective activation volumes for the transesterification of
(24) This estimate, while only approximate, is comparable to the value
reported previously for a similar transesterification reaction catalyzed by
subtilisin in octane (Zaks, A.; Klibanov, A. M. J. Biol. Chem. 1988, 263,
3194).
(25) Desai, U. R.; Osterhout, J. J.; Klibanov, A. M. J. Am. Chem. Soc.
1994, 116, 9420.
(33) Clark, M.; Cramer, R. D.; van Opdenbosch, N. J. Comput. Chem.
1989, 10, 982.
(34) Cox, P. J. J. Chem. Educ. 1982, 59, 275.
(26) Desai, U. R.; Klibanov, A. M. J. Am. Chem. Soc. 1995, 117, 3940.
(27) le Noble, W. J. ReV. Phys. Chem. Jpn. 1980, 50, 207.