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Parameter reference
These are the variables the UI exposes. They live in each example's
in.sdpd_phase.2d as variable NAME equal X lines and are patched at run
time when the user (or agent) supplies overrides.
Run
| Name | Type | Meaning | Sensible range |
|---|---|---|---|
prodRun |
int | Production-phase timesteps | 100 (smoke) — 250 000 (publication) |
preRun |
int | Equilibration timesteps before production | 0 — 20 000 |
preRunTemp |
int | Initial temperature-equilibration steps | 0 — 1000 |
dt |
float | Integration timestep | 1e-5 — 1e-3, smaller for stiffer EOS / smaller dh |
Output
| Name | Type | Meaning |
|---|---|---|
fqTher |
int | Print thermo line every N steps |
fqDump |
int | Write trajectory dump every N steps |
fqRes |
int | Write restart file every N steps |
fqV |
int | Re-apply velocity boundary conditions every N steps |
For a 100-step smoke test use fqTher=10, fqDump=50 so you actually get
some output. For a 250 000-step production run, fqTher=1000, fqDump=5000
keeps disk usage in check.
Geometry
| Name | Type | Meaning |
|---|---|---|
dim |
int | 2 or 3 (every bundled example is 2) |
dh |
float | Particle spacing in lattice units. Smaller = finer = slower |
coreL |
float | Edge length of the simulation box |
dhN |
int | dh × dhN = sphere/droplet radius |
diaNx, diaNy |
int | Droplet diameter multipliers in X/Y |
squareL |
float | Half-length of a square sub-region |
lenNx |
int | Length-times multiplier for square regions |
The kernel cutoff h = 4·dh is hard-coded. If you halve dh (×2 resolution)
expect ~16× more particles in 2D and 4× more neighbours per particle.
Fluid properties
| Name | Type | Meaning |
|---|---|---|
rho |
float | Reference fluid density |
T |
float | kBT — thermal noise. Validation cases use ~1e-18 (effectively zero) |
Tbuf |
float | Temperature in buffer / reservoir regions |
Multi-phase / Surface tension
| Name | Type | Meaning |
|---|---|---|
sigmao |
float | Reference interfacial tension for the multi-phase term |
F |
int (1, 2, or 3) | Selector for the multi-phase free-energy functional |
fluid_type |
int | Phase identifier passed to the SDPD-mf pair style |
f2Frac |
float (0–1) | Volume fraction of phase 2 (the dispersed phase) |
randPos |
int (0/1/2) | 0=single droplet, 1=random, 2=square block |
For a Young–Laplace droplet test, vary sigmao and the droplet size
(dhN/diaNx); the pressure jump should follow Δp = σ/r in 2D.
Boundary / driving
| Name | Type | Meaning |
|---|---|---|
dVx, dVy |
float | Imposed wall velocities (Couette/Poiseuille setup) |
dSSx, dSSy |
float | Imposed shear strains |
What's NOT exposed in the UI yet
These live in each example's micro file (or eta_input / pair_input /
s_input / thixo_input for cases that read them from data files):
eta11,eta22,eta12— viscosity per type-pairksai11,ksai12— multi-phase coupling constantss11,s22,s12— strength factorswall_index*— wall non-slip flag per type-paira_thixo,b_thixo,alpha_thixo,f0_thixo— thixotropy coefficients
To change these, edit Numerical examples/<case>/micro directly (or its
*_input files) before running.
What to vary in an optimization
Good choices for sweeps:
dh(resolution) — affects accuracy and runtimesigmao(surface tension) — drives droplet shape recoverydt(timestep) — affects stability marginf2Frac,randPos— initial phase distribution
Not great choices:
prodRun— varying it changes runtime, not physicsdim,fluid_type,F— categorical selectors, only meaningful at specific values; use them ascategoricalnotintin search space