Tutorials Manual

List of Figures
Tutorials Manual
2-50 Peaking of NO Concentration Dependent on Temperature in a PFR with an Approximated Mixing Region. ..............72
2-51 Confined Co-flowing Annular Jet Configuration. ...........................................................................................................73
2-52 Preferences Panel Showing the Display User Routine Options Is Enabled..................................................................74
2-53 Get Initial Solution Profile from User Routine Check box..............................................................................................75
2-54 Visualization of Full Computational Domain Can Be Acquired by Selecting Proper Reflect Contour Data Option in the
Chemkin Post-Processor Panel. ...................................................................................................................................76
2-55 Contour Plot Window Showing the Pull-down List Selections of the Insert Menu........................................................77
2-56 Colorbar Property Panel................................................................................................................................................77
2-57 Final 3-D Temperature Contours of the Entire Physical Domain with Vertical Contour Legend (Colorbar)..................78
2-58 A schematic of the JSR/PFR reactor configuration used by Marr 23 ..............................................................................79
2-59 Diagram View of the CHEMKIN 4.1 Project Used to Simulate the JSR/PFR Experiment ...............................................80
2-60 Specifying Particle Tracking Module Parameters and Initial Conditions of Particle Size Moments in the Reactor ......80
2-61 Surface Area Fraction of the Particle Material Must Be Set to Zero in the Material-specific Data Tab. The Default Value
of Surface Area Fraction Is One. ..................................................................................................................................81
2-62 Dispersed Phase Tab for Specifying Particle Size Moments in Inlet Streams .............................................................81
2-63 Tolerances for Particle Size Moments Can Be Given Explicitly in the Solver Window .................................................81
2-64 Comparisons of Mole Fraction Profiles of Selected Gas Phase Species Inside the PFR for the 1630K and F = 2.2 Case
of the C 2 H 4 /O 2 /N 2 JSR/PFR Experiment by Marr 23 . Symbols: data; Solid lines: predictions with HACA and PAH
condensation growth mechanisms................................................................................................................................83
2-65 Comparisons of Soot Mass Concentration Profiles Inside the PFR for the 1630K and F = 2.2 Case of the C 2 H 4 /O 2 /N 2
JSR/PFR Experiment by Marr 23 . Symbols: data; Solid line: prediction with both HACA and PAH condensation growth
mechanisms; Dash-dot line: prediction with HACA growth mechanism only ...............................................................84
2-66 Comparison of Contributions of Different Soot Mass Growth Mechanisms by Using the Rate-Of-Production Analysis...
84
2-67 The Particle Diameter Evolution Inside the PFR Predicted by the Present Soot Module for the 1630K and F = 2.2 case
of the C 2 H 4 /O 2 /N 2 JSR/PFR Experiment by Marr 23 (see p. 78) ......................................................................................85
3-1 Turbine Flow Capacity...................................................................................................................................................92
3-2 Two-Stage Catalytic Combustor—Diagram View .........................................................................................................95
3-3 Catalytic Pre-combustor (C1_)—Honeycomb Monolith, Catalyst sub-tab ...................................................................95
3-4 Catalytic Pre-combustor (C1_)—Honeycomb Monolith, Honeycomb sub-tab .............................................................96
3-5 Homogeneous Stage Combustor (C3_)—Reactor Physical Property ..........................................................................96
3-6 Two Stage Catalytic Combustor—Excess_Air_Dilution (Cluster 4) Output Results .....................................................97
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