Hi Charles,
There are no functions for providing this information via the Matlab toolbox or any of the other interfaces. The reason for this is, in part, because the modified Arrhenius rate expression is not general, and is not the only reaction rate parameterization supported by Cantera. For example, what would you expect such methods to return for a pressure-dependent "falloff" reaction? One approach you might consider would be to calculate locally-equivalent Arrhenius parameters indirectly by evaluating derivatives of the rate constants. Assume that k(T) has the form:
k(T) = A * T**b * exp(-Ta/T)
where (A,b,Ta) are the parameters for the modified Arrhenius equation. Then let:
F = 1/k * dk/dT = (b*T + Ta) / T
G = 1/k * d2k/dT2 = ((b-1)*b*T**2 + 2*(b-1)*T*Ta + Ta**2)/T**4
We can solve these two equations for Ta and b:
Ta = T**2*(F**2*T- F -G*T)
b = T*(2*F - F**2*T + G*T)
A = k / (T**b * exp(-Ta/T))
F and G can be computed by finite difference (here using the Cantera Python module):
T = 1000.0
dT = 0.1
R = 1.9872041 # cal/mol-K
gas.TP = T, 101325
k = gas.forward_rate_constants
gas.TP = T+dT, None
kp = gas.forward_rate_constants
gas.TP = T-dT, None
km = gas.forward_rate_constants
F = (kp-km) / (k*2*dT)
G = (kp-2*k+km) / (dT**2*k)
Ea = T**2 * (F**2 * T - F - G*T) * R
b = T * (2*F - F**2*T + G*T)
A = k * T**-b * np.exp(Ea/(R*T))
Using dT = 0.1 seems to work better than smaller values, and gives about 5 significant figures, at least for the reactions in h2o2.xml. Working out the equivalent Matlab code should be straightforward.
Regards,
Ray