Difference between revisions of "Keywords and settings new"
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=== Selectivity block === | === Selectivity block === | ||
− | [[Image: | + | [[Image:Mkmcxx2.15.3.png]] |
Inside the selectivity block, you can specify mole balances on which basis you calculate selectivity and degree of selectivity control graphs. You need to specify a name, a key component and one or more products (typically more than one, else the concept of selectivity is rather trivial). The name will be used in the generation of the corresponding graph file, so please use a safe name (i.e. no spaces and no special characters!) | Inside the selectivity block, you can specify mole balances on which basis you calculate selectivity and degree of selectivity control graphs. You need to specify a name, a key component and one or more products (typically more than one, else the concept of selectivity is rather trivial). The name will be used in the generation of the corresponding graph file, so please use a safe name (i.e. no spaces and no special characters!) | ||
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<pre> | <pre> | ||
&selectivity | &selectivity | ||
− | carbon_balance; {CO}; {CH4}, 2{CH2CH2}, 2{CH3CH3}, 3{CH3CH2CH3}, 3{CH2CHCH3} | + | carbon_balance; {CO}; {CH4}, 2{CH2CH2}, 2{CH3CH3}, 3{CH2CHCH3}, 3{CH3CH2CH3} |
+ | </pre> | ||
+ | |||
+ | For complex systems like the Fischer-Tropsch synthesis reaction the number of products can be quite large. To help prevent very long lines in the input file we allow the selectivity definition to be separated over multiple lines. These lines are additive, meaning that the example above can also be written as follows: | ||
+ | |||
+ | <pre> | ||
+ | &selectivity | ||
+ | carbon_balance; {CO}; {CH4} | ||
+ | carbon_balance; {CO}; 2{CH2CH2}, 2{CH3CH3} | ||
+ | carbon_balance; {CO}; 3{CH2CHCH3}, 3{CH3CH2CH3} | ||
+ | </pre> | ||
+ | |||
+ | Or: | ||
+ | |||
+ | <pre> | ||
+ | &selectivity | ||
+ | carbon_balance; {CO}; {CH4} | ||
+ | carbon_balance; {CO}; 2{CH2CH2} | ||
+ | carbon_balance; {CO}; 2{CH3CH3} | ||
+ | carbon_balance; {CO}; 3{CH2CHCH3} | ||
+ | carbon_balance; {CO}; 3{CH3CH2CH3} | ||
+ | </pre> | ||
+ | |||
+ | Multiple selectivity balances may be defined in the same selectivity group, e.g.: | ||
+ | &selectivity | ||
+ | carbon_balance; {CO}; {CH4} | ||
+ | carbon_balance; {CO}; 2{CH2CH2}, 2{CH3CH3} | ||
+ | carbon_balance; {CO}; 3{CH2CHCH3}, 3{CH3CH2CH3} | ||
+ | ethylene_vs_ethane; {CO}; 2{CH2CH2}, 2{CH3CH3} | ||
+ | propylene_vs_propene; {CO}; 3{CH2CHCH3}, 3{CH3CH2CH3} | ||
</pre> | </pre> |
Revision as of 10:31, 25 March 2020
Settings block
The list below is an overview of all the keywords that can be placed inside the &settings
block. All keywords have a default value, so if these are not specified within the block, then the default value is used.
Keyword | Explanation | Default value | Possible values |
---|---|---|---|
TYPE | The type of MKMCXX run.
|
string | SEQUENCERUN, SSITKA, TPD, REACTOR |
PRESSURE | The total pressure in the gas phase.
|
-1 (Take starting pressures) | float > 0 or negative value |
CSTR_RES | Residence time of the gas phase in seconds. Defined as the reactor volume divided by the volumetric flow rate into the reactor. This parameter effectively sets the input flow rate. The actual residence time may differ if the overall reaction includes expansion or contraction of the gas volume.
|
-1 (Fixed gas phase) | float > 0 or negative value |
CSTR_LOAD | Sets the amount of sites (in mole) in the open reactor volume (in m^3).
|
1e-4 | float > 0 |
USETIMESTAMP | Whether to place the output in a new folder which name is based on the current time stamp.
|
1 | 0 or 1 |
ORDERS | Whether to calculate the reaction orders.
|
0 | 0 or 1 |
EACT | Whether to calculate the apparent activation energy.
|
0 | 0 or 1 |
DRC | Whether to perform a degree of rate control analysis.
|
0 | 0-2 (int) |
TDRC | Whether to perform a thermodynamic degree of rate control analysis.
|
0 | 0 or 1 |
REAGENTS | List of reagents for which the reaction orders will be calculated. | NULL | {<Cmp1>},{<Cmp2>},... |
KEYCOMPONENTS | List of compounds on which the reaction orders, apparent activation energy, DRC, DSC and/or TDRC analysis should be based. | NULL | x{<Cmp1>},x{<Cmp2>},... |
PDRC | Whether to include DRC results for every selectivity-component.
|
1 | 0 or 1 |
DSC | Whether to include DSC results for every selectivity-component.
|
1 | 0 or 1 |
DCGC | Whether to include DCGC results for every ASF block.
|
1 | 0 or 1 |
NPAR | Maximum number of CPU threads to use (if available).
|
0 | int >= 0 |
TRANSIENT | Define the level of detail at which transient results should be stored.
|
1 | int >= 0 |
GRAPHDATA | Include data files that contain all data points that are plotted in the graphs.
|
0 | 0 or 1 |
GRAPHFILTER | Apply a filter to graph data that omits small values.
|
1 | 0 or 1 |
Keyword | Explanation | Default value | Possible values |
---|---|---|---|
DEBUG | Output additional debug statements.
|
0 | 0-4 (int) |
CSTR_REPLACE | Replaces starting gas-phase compounds by some other component. E.g. "{He};{CO},{H2}" replaces CO and H2 with He. This does not change inflow concentrations. | NULL | {<ReplaceCmp>};{<Cmp1>},{<Cmp2>} |
RERUN_OUTPUT | Define the folder used for re-running sensitivity analysis and graphs. | run | string |
RERUN_GRAPH | Whether to re-run graphs from the RERUN_OUTPUT folder.
|
0 | 0 or 1 |
CACHE_WORKPOINT | Reuse the sequencerun results as a workpoint in additional routines like DRC.
|
1 | 0 or 1 |
NUMDIFF | Resolution of perturbations at each side of the workpoint. | 2 | int >= 1 |
ORDERSDIFF | Step size used in the linear fitting of reaction orders (fractional pressure).
|
0.01 | float > 0 |
EACTDIFF | Step size used in the linear fitting of the apparent activation energy (fractional temperature).
|
0.0001 | float > 0 |
DRCDIFF | Step size used in the linear fitting for the degree of rate control analysis (fractional k).
|
0.01 | float > 0 |
TDRCDIFF | Step size used in the linear fitting for the thermodynamic DRC analysis (absolute dG in J/mol).
|
1 | float > 0 |
BOOSTER | Multiplier used to speed-up reaction rates; sometimes leads to faster convergence towards the steady-state solution (time is scaled inversely to compensate). | 1.0 (regular speed) | float > 0 |
SOLVERTYPE | Type of integration method to use for solving the system of ordinary differential equations.
|
1 (BDF) | 1 or 2 (int) |
SOLSTOPTIME | Specificies when the solver should force re-evaluation of dydt/jac.
|
2 | 0-2 (int) |
SOLMAXSTEP | Maximum number of internal steps the solver is allowed to take. | 5000 | int > 0 |
SOLTESTFAIL | Maximum number of test failures before the solver gives up. | 70 | int > 0 |
SOLCONVFAIL | Maximum number of convergence failures before the solver gives up. | 100 | int > 0 |
PRECISION | Amount of significant digits to use in output. | 10 | int > 0 |
SEQAL | Use the output concentrations from completed runs as input for new runs.
|
0 | 0 or 1 |
DRCBIN | Store binary data of sequencerun to allow re-plotting data.
|
0 | 0 or 1 |
MAKEPLOTS | Whether to create .png and .pdf files of plots.
|
1 | 0 or 1 |
HEATMAP | Whether to create heatmap graphs for DRC/DSC results.
|
1 | 0 or 1 |
COLORBLIND | Change the order of the graph-coloring for (slightly) improved readability.
|
0 | 0 or 1 |
PRINTLIST | Generate some extra debug lines with the initial and final concentrations.
|
1 | 0 or 1 |
WERROR | Interpret input warnings as errors.
|
0 | 0 or 1 |
RELDERIV | Plot relative derivatives.
|
0 | 0 or 1 |
SELECTIVITY_CAP | Force upper limit for selectivity data to prevent unreadable selectivity graphs. | NULL | float > 0 |
MINIMUM_BAR | Set a minimum reaction barrier height based on max(Ef,Eb). | NULL | float > 0 |
MAXIMUM_BAR | Set a maximum reaction barrier height based on max(Ef,Eb). | NULL | float > 0 |
SIMPLE_LAT_FAC | Scaling factor for lateral interactions. | 1.0 | float |
SIMPLE_LAT_CLAMP | Upper bound for the change in barrier height (J/mol) from lateral interactions. | 250e3 | float |
SIMPLE_LAT_DIFF | Convert supplied integral simple_lat to differential_lat.
|
0 | 0 or 1 |
Keyword | Explanation | Default value | Possible values |
---|---|---|---|
POTAXIS | Sets the x-axis for the SEQUENCERUN range plot.
|
0 | 0 or 1 |
pH | Sets the pH that is used to determine the RHE potential. | 0 | float |
DIFF | Whether to generate plots of diffusion layer concentrations.
|
0 | 0 or 1 |
NdX | Number of discretized layers in diffusion layer
|
100 | float > 0 |
dX | Thickness of one discretized diffusion layer
|
1e-8 | float > 0 |
DIFF_LOAD | Conversion factor for diffusion-surface interface (mol sites / m2) | 1e-5 | float > 0 |
DIFF_START_ZERO | Whether to initialize diffusion layers to zero or use bulk.
|
0 : initialize to zero | 0 or 1 |
DIFF_POT | Extra potential over diffusion layer that influences diffusion of charged particles
|
0 | float |
DIFF_PHASE | Set the phase of the diffusion layer (influences boundary conditions).
|
LIQUID | LIQUID, GAS |
Keyword | Explanation | Default value | Possible values |
---|---|---|---|
NETWORK | Allow creation of network graphs.
|
1 | 0 or 1 |
NETWORK_RATES | Also print forward and backward rates in the network graphs.
|
0 | 0 or 1 |
NETWORK_STRICT | Merge multiple edges between nodes into one edge.
|
1 | 0 or 1 |
NETWORK_FLUX | Generate dedicated flux output.
|
0 | 0 or 1 |
NETWORK_NODAL_PROD | Show connected products in nodal-recall chain.
|
0 | 0 or 1 |
GIBBS | Calculate gibbs free energy barriers at the start and at the end coverages
|
0 | 0 or 1 |
Keyword | Explanation | Default value | Possible values |
---|---|---|---|
ABSTOL | Set the absolute tolerance for a TPD run. | 1e-12 | float > 0 |
RELTOL | Set the relative tolerance for a TPD run. | 1e-8 | float > 0 |
TIME | Set the simulation time for a TPD run. | NULL | float > 0 |
TSTART | Starting temperature for a TPD run. | NULL | float > 0 |
TEND | Temperature reached at the end of the TPD run. | NULL | float > 0 |
TPD_EQ | Try to equilibrate the system before starting the TPD run.
|
0 | 0 or 1 |
Keyword | Explanation | Default value | Possible values |
---|---|---|---|
F_MOLE | In-flow of a PFR type reactor. | NULL | float > 0 |
A_REAC | Cross-sectional area of a PFR type reactor in m^2. | NULL | float > 0 |
L_REAC | Length of a PFR type reactor in m. | NULL | float > 0 |
RHO_SITES | Site density in mole sites / m^2 | NULL | float > 0 |
BET | Surface area in m^2 / g | NULL | float > 0 |
CATALYST_LOADING | Ratio of active catalyst material on support kg/kg | NULL | float > 0 |
CATALYST_DENSITY | Density of the catalyst bed in kg / m^3 | NULL | float > 0 |
VOID_FRACTION | Void fraction of the reactor | NULL | float > 0 |
REACNRSTEPS | Number of discrete slabs in the PFR. | 30 | int > 0 |
Keyword | Explanation |
---|---|
GNUPLOT | Whether to output GNUPlot-style graphs. |
CSTR | Whether to use the CSTR module or not.
|
JACOBIAN | Whether to use the custom MKMCXX JACOBIAN.
|
DAMPENING | Whether to enable dampening to old implementation of lateral interactions.
|
DAMPENING | Lower coverage bound for old implementation of lateral interactions.
|
DEFAULT_LAT | Allows old lateral repulsion parameters A and B to be set for all compounds.
|
MAXIMUM_RATE | Set a maximum reaction rate. (in s-1 - e.g. 1e6)
|
Graphs block
Inside the graphs block, you can set the colors used in the non-GNUPLOT graphs for specific components. On each line, you place the compound between curly brackets followed by the RGB color code. For example:
&graphs # fix colors for particular compounds {A*} E74C3D {B*} F29C1F {C*} 287FB9 {*} 15A086
Selectivity block
Inside the selectivity block, you can specify mole balances on which basis you calculate selectivity and degree of selectivity control graphs. You need to specify a name, a key component and one or more products (typically more than one, else the concept of selectivity is rather trivial). The name will be used in the generation of the corresponding graph file, so please use a safe name (i.e. no spaces and no special characters!)
&selectivity species_balance; {A}; {E},{F}
In the above example, the name of the mole balance block is "species_balance", the key component is A and the products of interest are E and F. A detailed example on how to use this block is explained here.
Stoichiometry
Often, the stoichiometry of the key component and the products is not simply a 1:1 ratio. To account for this difference, you need to put the stoichiometric coefficient in front the compound. The stoichiometric coefficient is simply the number of key components which need to be consumed to produce one product. To illustrate this, below an example for CO hydrogenation towards C1-C3 hydrocarbons is provided.
&selectivity carbon_balance; {CO}; {CH4}, 2{CH2CH2}, 2{CH3CH3}, 3{CH2CHCH3}, 3{CH3CH2CH3}
For complex systems like the Fischer-Tropsch synthesis reaction the number of products can be quite large. To help prevent very long lines in the input file we allow the selectivity definition to be separated over multiple lines. These lines are additive, meaning that the example above can also be written as follows:
&selectivity carbon_balance; {CO}; {CH4} carbon_balance; {CO}; 2{CH2CH2}, 2{CH3CH3} carbon_balance; {CO}; 3{CH2CHCH3}, 3{CH3CH2CH3}
Or:
&selectivity carbon_balance; {CO}; {CH4} carbon_balance; {CO}; 2{CH2CH2} carbon_balance; {CO}; 2{CH3CH3} carbon_balance; {CO}; 3{CH2CHCH3} carbon_balance; {CO}; 3{CH3CH2CH3}
Multiple selectivity balances may be defined in the same selectivity group, e.g.: &selectivity carbon_balance; {CO}; {CH4} carbon_balance; {CO}; 2{CH2CH2}, 2{CH3CH3} carbon_balance; {CO}; 3{CH2CHCH3}, 3{CH3CH2CH3} ethylene_vs_ethane; {CO}; 2{CH2CH2}, 2{CH3CH3} propylene_vs_propene; {CO}; 3{CH2CHCH3}, 3{CH3CH2CH3} </pre>