Chemkin-Pro List of Figures
© 2017 ANSYS 16 CK-TU-15181-1704-UG-1
2-156 Batch Reactor with Particle Aggregation—Complete Aggregation: Aggregate number density as a
function of the volume equivalent section diameter.
...................................................................................................196
2-157 Batch Reactor with Particle Aggregation—Evolution of the primary particle diameter................................................197
2-158 Batch Reactor with Particle Aggregation—Number density distributions obtained without aggregation. ..................198
2-159 Batch Reactor with Particle Aggregation—Collision diameter as a function of (volume equivalent)
section diameter.
.........................................................................................................................................................199
2-160 Batch Reactor with Particle Aggregation—Comparison of the total particle number and surface area
densities as a function of time with and without aggregation model
...........................................................................200
2-161 Coal Gasifier—A PSR-PFR network as a simplified representation of a coal gasifier. ..............................................202
2-162 Coal Gasifier—Entering coal particle number density and coal mass flow rate on the Inlet Stream
Properties panel for the inlet to PSR #2. The particle volume fraction or particle mass density will
be calculated internally for coal particles.
....................................................................................................................202
2-163 Coal Gasifier—Mole fraction profiles of major syngas species (a) & (b); and gaseous tar species,
such as pyrene (c).
......................................................................................................................................................206
2-164 Coal Gasifier—Predicted profiles of gas and coal particle mass flow rates (a); and the average coal
particle diameter (b).
..................................................................................................................................................207
2-165 Coal Gasifier—Schematic of the labile bridge scission sequence of the CPD model.................................................207
2-166 Coal Gasifier—Predicted concentration profiles of coal structural Functional Group Species: Aromatic
Core (core(B)), Labile Bridge (lbrdg(B)), Activated Labile Bridge (lbrdg*(B)), and Char Link (clink(B)).
The scaling factor for model bridge/link FG species is 12.5.
......................................................................................208
2-167 Stirred Reactor with Uncertainty Analysis—Setting up an uncertainty analysis for heat loss.....................................210
2-168 Stirred Reactor with Uncertainty Analysis—Setting up the uncertainty distribution for heat loss................................210
2-169 Stirred Reactor with Uncertainty Analysis—Probability density function of NO..........................................................211
2-170 Example validation comparisons for PRF blends. Model predictions are depicted with lines, and
experimental data with symbols in all the figures. The experimental data are from the references
listed in Table 2-17.
....................................................................................................................................................219
3-1 Two-stage Catalytic Combustor—Turbine Flow Capacity...........................................................................................222
3-2 Two-Stage Catalytic Combustor—Diagram View .......................................................................................................225
3-3 Catalytic Pre-combustor (C1_)—Honeycomb Monolith, Catalyst sub-tab .................................................................225
3-4 Catalytic Pre-combustor (C1_)—Honeycomb Monolith, Honeycomb sub-tab ...........................................................226
3-5 Homogeneous Stage Combustor (C3_)—Reactor Physical Property ........................................................................226
3-6 Two-Stage Catalytic Combustor—Excess_Air_Dilution (Cluster 4) Output Results ...................................................227
3-7 Two-Stage Catalytic Combustor—Temperature Comparison.....................................................................................229