Substrate-Induced Dimerization of Mpro
1329
where K0 is a constant that relates to the dissociation constant and h is the
Hill constant.
of enzyme was performed in parallel to correct for the dilution of heat. The
data were then analyzed by integrating the heat effects normalized to the
amount of injected proteins using curve fitting based on a 1:1 binding model.
This involved the use of Digitam software (TA instruments).
The dependence of the proteolytic activity on enzyme concentration was
investigated for the wild-type Mpro and R298A/L mutants, at a substrate
concentration of 600 mM TQ6-pNA. The initial velocity of the reaction at
various concentrations of each enzyme was determined and fitted to the
nonlinear dependence equation (Eq. 3):
RESULTS AND DISCUSSION
ꢀ
ꢁ
qffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffi
.
Cooperative effect of initial velocity curves
of R298A and R298L mutants
n0 ¼ kcat Kd þ 4½Eꢂ ꢃ Kd2 þ 8Kd½Eꢂ
where Kd is the monomer-dimer dissociation constant.
Analytical ultracentrifugation analysis
8;
(3)
To measure the activity of Mpro and its mutants, we used the
6-mer substrate peptide (TSAVLQ) attached to a pNA group
(23). This peptide is specifically cleaved by SARS-CoV
Mpro at the designated site (Gln-pNA) to release free
pNA, which results in an increased absorbance at 405 nm.
Besides wild-type Mpro as a dimeric target, two single
mutants, R298A and R298L, and one double mutant,
R298A/Q299A, were chosen as the monomeric targets. Ac-
cording to previous studies (19), mutation of R298 or Q299
will induce dimer dissociation and result in an ~10-fold
decrease in proteolytic activity (18). When R298 and Q299
are both mutated, the enzyme activity decreases by 100-fold.
Other studies also suggest that the monomeric Mpro by other
mutations shows very low or no proteolytic activity
(16–21,31). Indeed, in this study, we were not able to detect
any enzyme activity associated with the R298A/Q299A
double mutant. However, for the single mutants, R298A or
R298L, the initial velocity pattern at various substrate
concentrations displayed a sigmoid curve (Fig. 2, B and C).
The dimeric Mpro, on the other hand, exhibited a classical
saturation curve (Fig. 2 A). These results were then fitted
to the Michaelis-Menten or Hill equations to evaluate the
kinetic parameters. The best-fit results are shown in Table 1.
The Km (223 mM) and kcat (0.63 sꢃ1) of wild-type Mpro with
TQ6-pNA substrate are close to observations from other
laboratories (23,32). After fitting to the Hill equation, the
kcat of R298A was sixfold lower than that of the wild-type
enzyme. In contrast, R298L showed a kcat close to that of
the wild-type enzyme. The Hill constants of R298A and
R298L were 2.0 and 1.8, respectively. This nonunity number
suggested that there is a strong positive cooperativity among
the Mpro protomers. However, since the cooperativity
phenomenon is not compatible with a monomeric form, we
sought other evidence to examine the possibility of dimeric
Mpro formation during the catalytic process.
The analytical ultracentrifugation (AUC) experiments were performed on an
XL-A analytical ultracentrifuge (Beckman, Fullerton, CA) with an An-50 Ti
rotor (17). The sedimentation velocity (SV) experiments were performed in
a double-sector epon charcoal-filled centerpiece at 20ꢀC with a rotor speed
of 42,000 rpm. The sample (330 ml) and reference (370 ml) solutions with or
without different concentrations of TQ6-pNA substrate were loaded into the
centerpiece. We found that the TQ6-pNA was cleaved and free pNA was
released in the process of centrifugation (detected by absorbance at
405 nm). The absorbance spectrum of free pNA interfered with protein
absorbance at 280 nm. Therefore, absorbance at 250 nm was chosen to
detect the protein, which was monitored in a continuous mode with a time
interval of 480 s and a step size of 0.003 cm. Three different protein concen-
trations (from 1.4 to 57.2 mM) were used to estimate the dynamic monomer-
dimer content. Multiple scans at different time intervals were then fitted to a
continuous c(s) distribution model using the SEDFIT program (25,26). The
partial specific volume of Mpro, the solvent density, and the viscosity were
(cited Oct. 20, 2009).
The sedimentation equilibrium (SE) experiments were performed in a six-
channel centerpiece. Three different samples (0.10–0.12 ml) were loaded
into the sample channels and 0.11–13 ml buffers were loaded into the refer-
ence channels. The cells were then loaded into the rotor and run at multi-
speeding (8000, 12,000, and 15,000 rpm), each for 12 h at 20ꢀC. Ten scans
of absorbance at 250 nm at time intervals of 10 min were measured for every
rotor speed to check the status of SE. In our studies, all Mpro and its mutants
were able to achieve equilibrium state after 12 h. The SV results at three
protein concentrations and the multispeed SE data were then globally
analyzed using a monomer-dimer equilibrium model by the SEDPHAT
program (27), which gives a precise measurement for Kd and the dissociation
rate constant (koff) (18,28,29).
Analytical size-exclusive chromatography
Size-exclusive chromatographic experiments were performed using a GE
¨
Healthcare AKTA purifier system (Pittsburgh, PA) with a Superose 12
(10/300) column preequilibrated with phosphate-buffered saline (pH 7.6).
Mpro and its mutants without or with 600 mM of substrate preincubation
for 20 min were injected into the column separately. The elution was carried
out at a flow rate of 0.5 ml/min and the absorbance at 280 nm was monitored
continuously.
Nonlinear dependence of initial velocity
on protease concentration
Isothermal titration calorimetry
The dependence of the initial velocity on protease concentra-
tion was analyzed (Fig. 2, D–F). If the monomeric Mpro has
an activity identical to that of the dimeric one, a linear pattern
should be obtained (28). However, a nonlinear positive
correlation was observed for the wild-type and R298A/L
monomeric mutants. After fitting to the nonlinear depen-
dence equation (Eq. 3), the kcat (Table 1) and Kd for the
monomer-dimer equilibrium (Table 2) were calculated.
The isothermal titration calorimetry (ITC) protocol followed was that of
Sondermann et al. (30) with some modifications. Apparent dissociation
constants and stoichiometry of the enzyme-ligand interactions were
measured by a thermal activity monitor (2277, TA instruments, New Castle,
DE). Calorimetric titrations of the peptide substrate TQ6-pNA (1 mM in
a 250-ml syringe) and Mpro (5.7 mM for wild-type and 28.6 mM for mutants
in a 4-ml ampoule) were carried out at 25ꢀC in 10 mM phosphate buffer
(pH 7.6). The peptides were titrated into the enzyme in 10-ml aliquots per
injection with a time interval of 20 min. A control experiment in the absence
Biophysical Journal 98(7) 1327–1336