J. W. Dingee, A. B. Anton / Carbohydrate Research 345 (2010) 2507–2515
2513
4.4. Kinetics model—comparison to pNP-reporter data
5. Conclusions
Data were collected in a region of parameter space where
, that is, where the transglycosylation yield varied consid-
Nitrophenyl glycosides are commonly used substrates for
studying the reactivity of retaining glycosyl hydrolases, yet the
deceptively simple kinetics of nitrophenol formation can be com-
plicated by concurrent transglycosylation pathways. Herein we
propose a two-pathway mechanism for the hydrolysis and trans-
glycosylation of pNP-G2 by Cel5Acd, and from it we develop a rate
expression for reporter formation. We provide quantitative justifi-
cation for using the QSSA for three intermediate complexes when
integrating the rate expression, and we fit the integral form of
the rate to pNP-versus-time data to extract values of several
lumped kinetics parameters. One parameter, which emerges from
the integration and is quantified very precisely by the curve-fits
we present, uniquely determines the variation of hydrolysis versus
transglycosylation selectivity as a function of initial substrate con-
centration. We demonstrate that when the substrate composition
is sufficiently low, the two-pathway mechanism predicts simple
MM kinetics for hydrolysis, even though three intermediate com-
plexes are involved in the reaction. Our kinetics model and mech-
anistic explanation should be useful for interpreting results for
other retaining glycosyl hydrolase systems where competing
hydrolysis and transglycosylation are evident.
ST
ffi
x
erably with ST. All 104 data points for reporter concentration ver-
sus time in Figure 1 (with their sample standard deviations)
were fit simultaneously with Eqs. 4a and 4b using a non-linear,
weighted least-squares approach, as described in the Section 2.
The best-fit values, standard deviations, and relative precisions
~
~
~
for the fit-parameters kcat, Km, Km;2, and
x are presented in Table 1.
~
We also calculate and present the dependent parameter kcat;2
cat=2x for comparison, since this parameter appears naturally in
¼
~
k
the differential form of the mass balance for RðtÞ, Eq. 2a, used by
others for initial-rate analysis in similar systems.7,8,19 The solid
lines in Figure 1 represent the kinetics-model solution with these
parameters. The fit to the data for ET = 1.4
lent, as evidenced by the fact that the fit-curves pass within the
error bars ðÆ1 Þ for all but three of the 52 data points. The same
fit appears less good but still convincing when compared to the
data for ET = 4.0 M in Figure 1b. The fit-curve for ST = 1.0 mM
lM in Figure 1a is excel-
r
l
lies below the data for t P 40 min, and the fit-curve for
ST = 2.5 mM passes above the data points for all times. These devi-
ations may be an evidence that the measurements in Figure 1b
include systematic errors that increasing ET to 4.0
into a range of parameter-space where the QSSA for complex C3
is beginning to fail (cf. Appendix, 3 >0 in Eq. A4c), or that other
lM moves one
Acknowledgments
e
mechanistic complications, unaccounted for in our model, enter
the picture at high ET and ST. (Transglycosylation of G3, e.g., see
Section 4.1.) We have no information to discriminate among these
possibilities.
This project was supported by the Initiative for Future Agricul-
ture and Food Systems Grant no. 2001-52104-11484 from the
USDA Cooperative State Research, Education, and Extension Ser-
vice. The authors thank Dr. David Wilson, his staff, and his students
at Cornell University for their assistance and advice throughout the
experimental portion of this study.
Irwin et al. investigated the hydrolysis of pNP-G2 by Cel5Acd
as part of a larger, comparative study of cellulase enzymes.13
They report an activity of 14.4
sured at t = 30 min with ST = 2.5 mM. For comparison, the data
for ET = 1.4
M in Figure 1a give an activity of 12:0 Æ 0:4 at
t = 30 min, and the data for ET = 4.0 in Figure 1b give
15:7 Æ 1:4. A small deviation from Irwin’s result is not surpris-
ing, since t = 30 min penetrates the portion of the curves where
the hydrolysis yield varies nonlinearly with ET and ST (vide
infra).
lmol G2/min/lmol protein, mea-
Appendix
l
l
M
The QSSA is a versatile method for finding approximate solu-
tions to the mass balances for some kinetics problems.37,38 The
QSSA assumes that in a specific region of parameter space and
time, the rates of formation and destruction of a particular chem-
ical species are effectively equal, such that the time derivative of
its concentration is nearly zero. This simplifies that mathematical
problem at hand by reducing an ODE to an algebraic equation,
but at the expense of completeness, because when a concentra-
tion-derivative is lost, the solution of the remaining equations can-
not meet the initial condition for the species in question.
It is often assumed that the QSSA is valid for any intermediate,
that is, any species that is produced after a reaction starts and dis-
appears before the reaction finishes. Indeed, several analyses of
transglycosylation kinetics that precede this one present rate func-
tions that were derived with multiple QSSAs without pausing to
consider their validity.7,8,19 The QSSA is valid for intermediate com-
plexes in many but certainly not all enzymatic biochemical reac-
Eq. 4a reveals that the long-time amplitude of the RðtÞ curves
is a function of the single parameter
x. The copious long-time
data in the right panel of Figure 1 ensure that
x can be specified
to very high precision ( 2.3%, cf. Table 1) by curve-fits to the data
~
~
~
~
of Figure 1. Conversely, the parameters kcat, kcat;2, Km, and Km;2
cannot be determined with rewardingly high precision ( 20–
50%, cf. Table 1). These parameters only affect the shape of RðtÞ
where it rises from zero and bends toward its long-time, stea-
dy-state value, and there are fewer data points in this regime.
Extracting more parameters from fewer data ensures lower statis-
tical precision.
The most important quantitative result of the integral curve-
fits is the value of the selectivity-determining parameter
x
¼
tions, so one should be wary. Here we outline
a rigorous
1:30 Æ 0:03 mM, since it can be used in Eq. 6 to predict the final
product distribution as a function of initial substrate concentra-
tion. For example, reducing the substrate concentration to
ST = 0.10 mM would give f ¼ 0:98, that is, almost pure hydrolysis
procedure for re-scaling Eqs. 1a–e to delimit the validity of the
QSSA for the complexes in the reaction mechanism we propose,
and we use the QSSA to derive the mathematical model for hydro-
lysis kinetics we presented earlier as Eqs. 4a and 4b. We demon-
strate the scaling method not only to support our own work, but
with a hope that others will use the QSSA for biochemical kinetics
cautiously and pause to investigate whether it is valid.
Bowne, Acrivos, and Oppenheim were the first to recognize the
analogy between the QSSA of chemical kinetics and the ‘singular
perturbation theory’ of differential equations.41 This analogy pro-
vides a rigorous prescription for identifying when a QSSA is valid.42
One must first re-scale the problem carefully to a dimensionless
products, and since ST =
tions, the pNP-versus-time curves would evidence simple MM
x
¼ 0:10=1:30 ffi 0:08 under these condi-
kinetics according to Eqs. 7a and 7b. The apparent catalytic rate
constant and MM constant would be kcat ¼ 65:5 minꢀ1 and
ꢀ
ꢀ
Km ¼ 3:08 mM according to Eqs. 8a and 8b. Conversely, very high
substrate concentrations are required to achieve a near-maximum
yield of transglycosylation products for this system; for example,
ST ffi 50 mM is required to achieve f ffi 0:55.