A general package for linearly defining and solvig microkinetic catalytic systems.
Project description
mkin4py
mkin(microkinetics) 4 py(thon)
A general package for linearly defining and solvig microkinetic catalytic systems.
Description
A microkinetic package tranlated from Linearized Microkinetic Catalytic System Solver
By the author:
Gabriel S. Gusmão <gusmaogabriels@gmail.com> under Dr. Phillip Christopher <christopher@engr.ucr.edu> advisement.
For detailed information, refer to code comments or associated publication. Gusmão, G. S. & Christopher, P., A general and robust approach for defining and solving microkinetic catalytic systems. AIChE J. 00, (2014).; http://dx.doi.org/10.1002/aic.14627
The 17-Step Ethylene Epoxidation by Stegelmann et al. has been used as example. Stegelmann, C., Schiødt, N. C., Campbell, C. T. & Stoltze, P. Microkinetic modeling of ethylene oxidation over silver. J. Catal. 221, 630–649 (2004).
Set-up the environment conditions (temperature, pressure, gas constant)
Create a MK (microkinetic model object) - Define its dimensions: number of reactants (rows) and elementary reactions (columns) involved in the stoichiometry matrix, and parse the rows that refer to free-species (non-adsorbed) - Parse the stoichiometry matrix (must be of size number of reactants × number of elementary reactions) - Set the kinetic parameters: Activation Energies and Pre-exponential factors (must be of the size of the involved elementary reactions) - Set the fixed concentration of free-species (molar fraction in non-adsorbed phase) - Parse the string-labels of involved species (array of size of number of species)
Solve the ensuing LP (linear problem) - For now, there is only a Newton-type method available. - Standard iterative-procedure adopted for solving the inner-loop LP (Quasi-minimum residue)
The convergence parameters are set as default in the module solver in .params
Features
Linearization
The project makes use of explicit routines for the calculation of the MK model derivatives
Jacobian: Available as standard.
Hessian: Used in the convex two-step method (details in the aforementioned reference)
On the way
Additional LP solvers in “switchable” fashion.
Evolutionary methods for the definition of best convergence parameters for stiff problems (when TOF`s are close to the machine precision)
Instructions
Installation
pip install mkin4py==version_no
Example: Stoltze’s 17-Step Ethylene Epoxidation MK system
import mkin4py import numpy as np # Environment Conditions T = 500; #K P = 2; #bar gas_constant = 8.31456e-3 # Gas Constant - kJ/(mol×K) # Set the environment conditions mkin4py.environment.set_temperature(T) mkin4py.environment.set_gas_constant(gas_constant) mkin4py.environment. set_pressure(P) # Stoichsiometric Matrix ms = [ [-1, 1, 0, 0,-1, 1, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0],\ [ 0, 0, 0, 0, 0, 0,-1, 1, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0,-1, 1, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0],\ [ 0, 0, 0, 0, 0, 0, 0, 0, 0, 0,-1, 1, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0],\ [ 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 1,-1, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0],\ [ 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 1,-1, 0, 0],\ [ 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 1,-1],\ [-1, 1,-1, 1, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 1,-1,-1, 1, 1,-1, 0, 0, 1,-1, 0, 0, 1,-1, 1,-1],\ [ 1,-1,-1, 1, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0],\ [ 0, 0, 2,-2,-2, 2,-1, 1, 1,-1,-1, 1, 0, 0, 0, 0, 1,-1,-6, 6, 0, 0,-1, 1,-1, 1,-5, 5, 1,-1, 0, 0, 0, 0],\ [ 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 4,-4, 0, 0, 0, 0, 1,-1, 3,-3,-2, 2, 0, 0, 0, 0],\ [ 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 1,-1, 0, 0,-1, 1],\ [ 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 2,-2, 0, 0, 0, 0, 0, 0, 2,-2, 0, 0,-1, 1, 0, 0],\ [ 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 1,-1, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0],\ [ 0, 0, 0, 0, 2,-2, 0, 0,-1, 1, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0],\ [ 0, 0, 0, 0, 0, 0, 1,-1,-1, 1, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0,-1, 1, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0],\ [ 0, 0, 0, 0, 0, 0, 0, 0, 1,-1, 0, 0,-1, 1,-1, 1, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0],\ [ 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 1,-1, 1,-1, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0],\ [ 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 1,-1,-1, 1,-1, 1, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0],\ [ 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 1,-1,-1, 1, 0, 0, 0, 0, 0, 0, 0, 0],\ [ 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 1,-1,-1, 1, 0, 0, 0, 0, 0, 0],\ ]; nreac = [0, 1] # Reactant Rows in mS nprod = [2, 3, 4, 5] # Product Rows in mS stoichs = np.concatenate((nreac,nprod)) # Reactants and Products are not under PSSA mkin4py.mkmodel.create(np.shape(ms)[0],np.shape(ms)[1],stoichs) # Initialize the model # Species labels splabels = ['O2','C2H4','C2H4O','CH3CHO','CO2','H2O','*','O2*','O*','OH*',\ 'H2O*','CO2*','C2H4*','O·O*','C2H4·O*','CH2CH2O·O*','C2H4O·O*','CH3CHO·O*',\ 'CH2CHOH·O*','CH2CHO·O*'] mkin4py.mkmodel.set_splabels(splabels) # Set species labels # Pre-exponential Factors of Eelementary Reactions (1/s) va =[2.71e5, 1.1e12, 4.0e12, 8.0e14, 2.0e7, 1.3e15, 7.2e7,\ 2.2e11, 9.0e14, 5.3e14, 1.95e8, 4.8e12, 1.13e13, 2.11e12,\ 9.0e12, 4.5e10, 2.9e13, 2.6e9, 2.0e20, 5.3e13, 7.2e7, 2.2e11,\ 4.0e11, 3.1e14, 2.6e13, 1.3e9, 1.0e20, 5.5e13, 1.4e10, 1.0e11,\ 3.6e14, 1.0e8, 5.9e14, 1.4e9] # Activation Barriers for Elementary ReactionS (kJ/mol) vea = [5.7000, 47.3000, 75.0000, 157.5000, 20.0000, 96.9000, 0, 37.1000, 112.0000,\ 183.3000, 0, 39.1000, 95.0000, 93.5000, 95.0000, 204.3000, 41.9000, 4.4000,\ 11.0000, 791.6000, 0, 30.1000, 32.0000, 42.8000, 86.0000, 106.1000, 0, 906.6000,\ 65.6000, 50.0000, 38.9000, 0, 46.6000, 0] # Set the kinetic parameters mk4py.mkmodel.set_kinetic_params(np.array(va,ndmin=2).T,np.array(vea,ndmin=2).T) y = [0.5, 0.5, 0, 0, 0, 0] # Reactants and Products Initial Fraction mkin4py.mkmodel.set_concentrations(y) # Set the *free*-species concentrations
Evaluation:
sol = mkin4py.solver.solve.rk4() # 4th-order Runge-Kutta method coupled within the LP solved via QMR # Outupts print '...' print sol['msg'], 'time: ', sol['time'] print 'Coverage' print sol['coverage'] print 'Rates' print sol['rates']
Output:
... Convergence achieved time: 2.25999999046 Coverage [[ 5.00000000e-01] [ 5.00000000e-01] [ 0.00000000e+00] [ 0.00000000e+00] [ 0.00000000e+00] [ 0.00000000e+00] [ 4.39342950e-01] [ 1.19743307e-03] [ 1.07992516e-01] [ 1.10447591e-01] [ 2.99730332e-09] [ 7.70711567e-10] [ 1.00256049e-01] [ 9.78269843e-02] [ 1.32727193e-01] [ 9.64368428e-03] [ 3.28419897e-08] [ 4.59118359e-13] [ 5.65562897e-04] [ 1.12150752e-15]] Rates [[ -4.24252190e+01] [ -2.49532633e+01] [ 1.29732696e+01] [ 5.58723011e-04] [ 2.39588699e+01] [ 2.39588699e+01] [ 0.00000000e+00] [ 3.65929509e-13] [ 0.00000000e+00] [ 4.32857086e-11] [ 2.76796815e-16] [ 2.87485591e-11] [ 0.00000000e+00] [ -2.27373675e-13] [ -4.65661287e-10] [ 9.86479981e-16] [ 0.00000000e+00] [ -1.60491195e-13] [ 4.65661287e-10] [ -1.42115222e-11]]