mean_field_driver.py Command Help

Command: $SCHRODINGER/run microkinetics_gui_dir/mean_field_driver.py

usage: $SCHRODINGER/run microkinetics_gui_dir/mean_field_driver.py
       [-h] -rxn_network_file RXN_NETWORK_FILE [-temperature TEMPERATURE]
       [-catalyst_info catalyst_name,mass,specific_surface_area,adsorption_site_density [catalyst_name,mass,specific_surface_area,adsorption_site_density ...]]
       [-gas_info gas_name1,partial_pressure1,mol_mass1,(optional:variable_pressure1) [gas_name2,partial_pressure2,mol_mass2,(optional:variable_pressure2) ...]]
       [-bulk_info bulk_name1 [bulk_name2 ...]]
       [-reactor_flow_rate REACTOR_FLOW_RATE] [-reactor_volume REACTOR_VOLUME]
       [-deg_rate_control] [-deg_selectivity_control] [-rxn_order]
       [-convergence_tol CONVERGENCE_TOL]
       [-max_integration_time MAX_INTEGRATION_TIME]
       [-ode_solver {RK45,RK23,DOP853,Radau,BDF,LSODA}]
       [-epsilon_pct EPSILON_PCT]
       [-max_integration_time_step MAX_INTEGRATION_TIME_STEP]
       [-coverage_file COVERAGE_FILE]
       [-max_integration_wall_clock_time MAX_INTEGRATION_WALL_CLOCK_TIME]
       [-stages STAGES] [-jacobian {numerical,analytical}]
       [-interaction {simple_quadratic}] [-atol ATOL] [-rtol RTOL]
       [-electrode_potential ELECTRODE_POTENTIAL]
       [-transfer_coeff_method {fixed,hammond}] [-D]

Driver for mean field microkinetic modeling. Copyright Schrodinger, LLC. All
rights reserved.

options:
  -h, -help             Show this help message and exit.
  -rxn_network_file RXN_NETWORK_FILE
                        A comma-separated-value (CSV) file containing the
                        reaction network information. See /opt/schrodinger/sui
                        tes2026-3/mmshare-
                        v7.5/python/scripts/microkinetics_gui_dir/example_rxn_
                        network_file.csv for an example. One header should be
                        labeled Reactions. Its rows should contain the name of
                        each reaction, and each reaction name should be
                        unique. More headers should be labeled Forward
                        Reaction Barrier (eV) and Reverse Reaction Barrier
                        (eV). Their rows should be the reaction barriers of
                        the forward and reverse reactions, respectively. There
                        should be a forward and reverse barrier for a given
                        reaction. Unlisted barriers are assumed to be
                        zero.Another optional header is Collision Factor whose
                        rows give the type of pre-exponential collision factor
                        (1/s) to use when computing rate constants for the
                        given reaction in either direction. Current supported
                        types are a fixed positive numerical value, Eyring and
                        Hertz-Knudsen. Eyring is default.Use the optional
                        column TS Lateness Parameter to define a transition
                        state lateness parameter for each reaction. This is a
                        number in [0.0, 1.0] where a value of 0.0 means the
                        transition state geometry resembles that of the
                        reactants while a value of 1.0 means it resembles
                        products. This is used when partitioning the
                        adsorbate-adsorbate lateral interaction correction to
                        the reaction energy into corrections to the forward
                        and reverse reaction barriers according to the
                        Brønsted–Evans–Polanyi (BEP) scaling relation. It has
                        a default value of 0.5.Another optional header is
                        Notes. This column is meant to be used to store
                        reference information, and it will be ignored by this
                        driver. All remaining headers will be assumed to be
                        the names of intermediate species involved in the
                        microkinetic model. The empty site should be named as
                        *:catalyst_name by the user. The catalyst_name should
                        be exactly same as the name in provided in
                        -catalyst_info. Each intermediate name should be
                        unique. The rows for each of these columns should be
                        the stoichiometric coefficients of the intermediates.
                        Positive coefficients indicate that the intermediate
                        is a product, and negative coefficients indicate that
                        intermediate is a reactant in the reaction.Additional
                        options for electrocatalytic reactions: Transfer
                        Coefficient is a unitless quantity representing the
                        fraction of the electrical driving force
                        (overpotential) that lowers the activation barrier for
                        an electrochemical reaction. Reaction Type determines
                        the reaction type. Accepted values are 'thermo' (or
                        'thermocatalytic') and 'electro' (or
                        'electrocatalytic'). If absent, the default is
                        thermocatalytic. Butler-Volmer correction is applied
                        to all electrocatalytic reactions. Electrons
                        Transferred determines the number of electrons
                        transferred during the reaction. The electron count is
                        used directly in the Butler-Volmer equation. For each
                        electrocatalytic reaction, n_electron must be non-
                        zero. (default: None)
  -temperature TEMPERATURE
                        Temperature (in K). (default: 298.15)
  -catalyst_info catalyst_name,mass,specific_surface_area,adsorption_site_density [catalyst_name,mass,specific_surface_area,adsorption_site_density ...]
                        The information for the catalysts you want to model.
                        The first piece of information should be the exact
                        name of the catalyst. The second piece of information
                        should be the mass of catalyst added to the reactor,
                        in units of grams. The third piece of information
                        should be the specific surface area of the catalyst,
                        in units of m^2/g. The fourth piece of information
                        should be the adsorption site density of the catalyst,
                        in units of sites/cm^2. (default: None)
  -gas_info gas_name1,partial_pressure1,mol_mass1,(optional:variable_pressure1) [gas_name2,partial_pressure2,mol_mass2,(optional:variable_pressure2) ...]
                        The information for each gaseous/solvated intermediate
                        in the reaction network. The first piece of
                        information should be the exact name of the
                        intermediate, as written in the headers of the
                        -rxn_network_file file (note: these names are case-
                        sensitive). The second piece of information should be
                        the partial pressure of the gas/solute in the inlet
                        stream, in units of bar. The third piece of
                        information should be the molecular mass of the
                        gas/solute molecule, in units of Daltons. The fourth,
                        and optional, piece of information should be a
                        boolean: True to enable variable partial pressure of
                        the gas/solute molecule or False to keep it constant
                        (defaults to False). (default: None)
  -bulk_info bulk_name1 [bulk_name2 ...]
                        The information for any bulk materials. Since bulk
                        materials have unlimited sites the rates of reactions
                        involving them are zeroth order in the empty site
                        and/or absorbed species coverage. (default: None)
  -reactor_flow_rate REACTOR_FLOW_RATE
                        The flowrate of fluid in/out of the reactor (in
                        liters/second) (default: 1.0)
  -reactor_volume REACTOR_VOLUME
                        The volume of the reactor (in liters). (default: 10.0)
  -deg_rate_control     Calculate the degrees of rate control. (default:
                        False)
  -deg_selectivity_control
                        Calculate the degrees of selectivity control.
                        (default: False)
  -rxn_order            Calculate the reaction orders. (default: False)
  -convergence_tol CONVERGENCE_TOL
                        If seeking a steady state then this is the absolute
                        tolerance of the time derivative (1/s) of coverages
                        and pressures used to determine if the system has
                        reached a steady state. Otherwise pass "none" to
                        indicate that no steady state is being sought.
                        (default: 1e-05)
  -max_integration_time MAX_INTEGRATION_TIME
                        The maximum integration time in seconds. (default:
                        1000000.0)
  -ode_solver {RK45,RK23,DOP853,Radau,BDF,LSODA}
                        The ODE solver to use. Choices are
                        RK45,RK23,DOP853,Radau,BDF,LSODA. (default: LSODA)
  -epsilon_pct EPSILON_PCT
                        When calculating degrees of rate control or reaction
                        orders net rates are differentiated with respect to
                        either rate constants or pressures, respectively. This
                        is done using finite difference where the
                        perturbations have relative magnitudes. For degree of
                        rate control the rate constant perturbations are
                        calculated from this percentage of reaction barriers.
                        For reaction orders the pressure perturbations are
                        calculated from this percentage of pressures.
                        (default: 0.1)
  -max_integration_time_step MAX_INTEGRATION_TIME_STEP
                        The maximum integration time step in seconds.
                        (default: 100000.0)
  -coverage_file COVERAGE_FILE
                        An input csv file specifying parameters of empty sites
                        and adsorbates on catalysts. The column header
                        'Species' is required and specifies the species. Use
                        the column header 'Coverage' to optionally specify
                        initial coverages. By default initial coverages will
                        be 1 for empty sites and 0 for adsorbates. Use the
                        column header 'Lateral Scaling Parameter (eV)' to
                        optionally specify scaling parameters used to
                        calculate the lateral interaction corrections to the
                        reaction energies. Parameters for adsorbate pairs will
                        be calculated using the geometric mean combination
                        rule. By default parameters are 1.0 eV. (default:
                        None)
  -max_integration_wall_clock_time MAX_INTEGRATION_WALL_CLOCK_TIME
                        The maximum integration wall clock time in seconds.
                        (default: 1800)
  -stages STAGES        An input csv file specifying subsequent stages.
                        Columns are stage properties, and rows are stages.
                        Coverages for each adsorbate, and
                        pressures/concentrations for each gas/solute, must be
                        specified for each subsequent stage. The name of the
                        adsorbate or gas/solute is the column name for the
                        respective value. In addition, values for
                        -temperature, -max_integration_time,
                        -deg_rate_control, -deg_selectivity_control,
                        -rxn_order must be specified. -electrode_potential may
                        optionally be specified to override the applied
                        voltage per stage for electrocatalytic reactions. The
                        column names should match with the flag names. If it
                        is desired to use the final value from the previous
                        stage as the initial value for the subsequent stage,
                        then the value should be specified as 'PS' (previous
                        stage) (default: None)
  -jacobian {numerical,analytical}
                        The Jacobian for the ODE solver to use. Choices are
                        numerical,analytical. Each element of the Jacobian is
                        a derivative of an ODE, dC_i/dt ( concentration of i),
                        with respect to C_j (concentration of j),
                        d^2C_i/dC_jdt. (default: analytical)
  -interaction {simple_quadratic}
                        Adsorbate-adsorbate interactions. 'simple_quadratic'
                        specifies a simple second-order dependence on the
                        coverage. The default is 'none', in which the barriers
                        are independent of coverage. (default: None)
  -atol ATOL            Absolute tolerance, or the number of correct decimal
                        places, used in the ODE solver to maintain local error
                        estimates less than atol + rtol * abs(y), where y is
                        the solution whose accuracy is being controlled. See
                        scipy.integrate.solve_ivp documentation (https://docs.
                        scipy.org/doc/scipy/reference/generated/scipy.integrat
                        e.solve_ivp.html) for more details. We are using their
                        recommended defaults. Set atol to be smaller than the
                        smallest value that can be expected from rtol *
                        abs(y). If atol is larger than rtol * abs(y) the
                        number of correct digits is not guaranteed. (default:
                        1e-06)
  -rtol RTOL            Relative tolerance, or the number of correct digits,
                        used in the ODE solver to maintain local error
                        estimates less than atol + rtol * abs(y), where y is
                        the solution whose accuracy is being controlled. See
                        scipy.integrate.solve_ivp documentation (https://docs.
                        scipy.org/doc/scipy/reference/generated/scipy.integrat
                        e.solve_ivp.html) for more details. We are using their
                        recommended defaults. Set rtol such that rtol * abs(y)
                        is always smaller than atol. (default: 0.001)
  -electrode_potential ELECTRODE_POTENTIAL
                        Fixed electrode potential in Volt with respect to
                        standard hydrogen electrode (SHE). Value can be
                        positive or negative. (default: None)
  -transfer_coeff_method {fixed,hammond}
                        Method for determining transfer coefficient α when not
                        provided in CSV. 'fixed' (default): Uses symmetric
                        value α = 0.5, treating the reaction as equally
                        sensitive to overpotential in forward and reverse
                        directions. 'hammond': Calculates α from barrier ratio
                        using Hammond postulate (Marcus/BEP model): α =
                        Ea_fwd/(Ea_fwd+Ea_rev). This gives α → 0 for strongly
                        exergonic reactions (early TS) and α → 1 for strongly
                        endergonic ones (late TS). User-provided values in the
                        reaction network CSV always take precedence over this
                        setting. (default: fixed)

Job Control Options:
  -D, -DEBUG            Show details of Job Control operation. (default:
                        False)