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f2fc925 | 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60 61 62 63 64 65 66 67 68 69 70 71 72 73 74 75 76 77 78 79 80 81 82 83 84 85 86 87 88 89 90 91 92 93 94 95 96 97 98 99 100 101 102 103 104 105 106 107 108 109 110 111 112 113 114 115 116 117 118 119 120 121 122 123 124 125 126 127 128 129 130 131 132 133 134 135 136 137 138 139 140 141 142 143 144 145 146 147 148 149 150 151 152 153 154 155 156 157 158 159 160 161 162 163 164 165 166 167 168 169 170 171 172 173 174 175 176 177 178 179 180 181 182 183 184 185 186 187 188 189 190 191 192 193 194 195 196 197 198 199 200 201 202 203 204 205 206 207 208 209 210 211 212 213 214 215 216 217 218 219 220 221 222 223 224 225 226 227 228 229 230 231 232 233 234 235 236 237 238 239 240 241 242 243 244 245 246 247 248 249 250 251 252 253 254 255 256 257 258 259 260 261 262 263 264 265 266 267 268 269 270 271 272 273 274 275 276 277 278 279 280 281 282 283 284 285 286 287 288 289 290 291 292 293 294 295 296 297 298 299 300 301 302 303 304 305 306 307 308 309 310 311 312 313 314 | """Transient downstream piping simulation β Euler integration.
Components (in flow order):
1. Cryogenic reciprocating pump (2-D LUT: motor% x back-pressure -> mdot, T)
2. Snubber volume (pulsation dampener, single state = mass)
3. Control valve 2 (variable 0-100%, liquid/dense-fluid equation)
4. Pipe 2 (vents to atmosphere or discharges into tank)
Ported from HuggingFace Space csh2/process_sim.
"""
from __future__ import annotations
import math
import numpy as np
try:
import CoolProp.CoolProp as CP
except ImportError as e:
raise ImportError("CoolProp is required. Install with: pip install CoolProp") from e
# ββ Constants ββββββββββββββββββββββββββββββββββββββββββββββββββββββββββββββββ
FLUID = "Hydrogen"
R_H2 = 4124.2
BAR2PA = 1.0e5
IN2M = 0.0254
FT2M = 0.3048
PSI2PA = 6894.76
MAX_STEPS = 500_000 # hard cap
SIM_MODE_VALVE = "Pressure Build through Valve"
SIM_MODE_FILL = "Simulated Fill"
SIM_MODES = [SIM_MODE_VALVE, SIM_MODE_FILL]
# ββ Density β Pressure LUT (1-D, fixed T) βββββββββββββββββββββββββββββββββββ
class _RhoToPressureLUT:
"""Pre-built 1-D lookup: density β pressure at fixed temperature.
Replaces per-step CoolProp calls with np.interp (~1000x faster).
Built once before the integration loop.
"""
N_PTS = 2000
def __init__(self, T: float, rho_min: float, rho_max: float, fluid: str = FLUID):
rho_min = max(rho_min * 0.1, 1e-4)
rho_max = rho_max * 1.5
self.rho_pts = np.geomspace(rho_min, rho_max, self.N_PTS)
self.P_pts = np.empty(self.N_PTS)
for i, rho in enumerate(self.rho_pts):
try:
self.P_pts[i] = CP.PropsSI("P", "D", rho, "T", T, fluid)
except Exception:
self.P_pts[i] = rho * R_H2 * T
def __call__(self, rho: float) -> float:
return float(np.interp(rho, self.rho_pts, self.P_pts))
# ββ Simulation Engine ββββββββββββββββββββββββββββββββββββββββββββββββββββββββ
class Simulation:
"""Euler integration engine β mass-only state variable with 1-D P(rho) LUT."""
def __init__(self, p: dict):
self.p = p
def _friction(self, Re: float, D: float, eps: float) -> float:
if Re < 1.0:
return 0.0
if Re < 2300.0:
return 64.0 / Re
term = eps / (3.7 * D) + 5.74 / Re**0.9
if term <= 0:
return 0.02
return 0.25 / math.log10(term) ** 2
def _pipe_dp(self, mdot, rho, mu, D, L, A_pipe, fLD_cache, eps):
if mdot <= 0 or rho < 1e-10:
return 0.0
v = mdot / (rho * A_pipe)
Re = rho * abs(v) * D / mu if mu > 1e-15 else 1e6
f = self._friction(Re, D, eps)
return f * fLD_cache * 0.5 * rho * v * v
@staticmethod
def _valve_mdot_liq(P1, rho1, P2, Cv_eff):
if P1 <= P2 or Cv_eff <= 0:
return 0.0
dP_psi = (P1 - P2) / PSI2PA
SG = rho1 / 999.0
if SG <= 0:
return 0.0
q_gpm = Cv_eff * math.sqrt(dP_psi / SG)
return q_gpm * rho1 * 6.309e-5
@staticmethod
def _profile_lookup(t, profile_times, profile_values, default):
if profile_times is None or len(profile_times) == 0:
return default
idx = np.searchsorted(profile_times, t, side="right") - 1
idx = max(0, min(idx, len(profile_values) - 1))
return profile_values[idx]
def run(self, cb=None) -> dict:
p = self.p
dt = p["dt"]
dur = p["duration"]
N = int(dur / dt)
P_atm = p["P_atm_bar"] * BAR2PA
use_profiles = p.get("use_profiles", False)
prof_times = p.get("profile_times", None)
prof_motor = p.get("profile_motor", None)
prof_valve2 = p.get("profile_valve2", None)
pump_lut = p.get("pump_lut", None)
sim_mode = p.get("sim_mode", SIM_MODE_VALVE)
fill_mode = sim_mode == SIM_MODE_FILL
D2 = p["p2_id_in"] * IN2M
L2 = p["p2_len_ft"] * FT2M
eps = p["roughness_mm"] * 1e-3
A2 = math.pi / 4.0 * D2 * D2
fLD2 = L2 / D2
static_motor_pct = p["motor_pct"]
static_v2_pct = p["v2_pct"]
T_out = p["pump_T_out"]
V_snub = p["snub_V_L"] * 1e-3
V_snub_inv = 1.0 / V_snub
P_snub0 = p["snub_P0_bar"] * BAR2PA
T_snub = p["snub_T0_K"]
try:
rho_s0 = CP.PropsSI("D", "P", P_snub0, "T", T_snub, FLUID)
except Exception:
rho_s0 = P_snub0 / (R_H2 * T_snub)
m_snub = rho_s0 * V_snub
Cv2 = p["v2_cv"]
P_ref = max(P_snub0, 2.0 * P_atm)
try:
mu_g = CP.PropsSI("V", "P", P_ref, "T", T_out, FLUID)
except Exception:
mu_g = 5.0e-6
pulsation = p["pulsation"]
cpm_max = p.get("pump_cpm_max", 500.0)
omega_max = 2.0 * math.pi * cpm_max / 60.0
pi_val = math.pi
if cb:
cb(0.0)
if pump_lut is not None:
mdot_max_est = float(np.nanmax(pump_lut.mdot_grid))
else:
mdot_max_est = 0.05
rho_max_est = max((m_snub + mdot_max_est * dur) * V_snub_inv, 200.0)
rho_min_est = max(rho_s0 * 0.1, 1e-4)
P_lut = _RhoToPressureLUT(T_out, rho_min_est, rho_max_est)
# ββ Tank setup (Fill mode only) ββ
if fill_mode:
V_tank = p["tank_V_L"] * 1e-3
V_tank_inv = 1.0 / V_tank
P_tank0 = p["tank_P0_bar"] * BAR2PA
tank_dT = p.get("tank_dT_K", 20.0)
if pump_lut is not None:
if use_profiles and prof_motor is not None and len(prof_motor) > 0:
init_motor = float(prof_motor[0])
else:
init_motor = static_motor_pct
try:
_, T_pump_init = pump_lut.lookup(init_motor, p["snub_P0_bar"])
except Exception:
T_pump_init = T_out
else:
T_pump_init = T_out
T_tank = T_pump_init + tank_dT
try:
rho_t0 = CP.PropsSI("D", "P", P_tank0, "T", T_tank, FLUID)
except Exception:
rho_t0 = P_tank0 / (R_H2 * T_tank)
m_tank = rho_t0 * V_tank
rho_tank_max_est = max(
(m_tank + mdot_max_est * dur) * V_tank_inv, rho_t0 * 5.0
)
rho_tank_min_est = max(rho_t0 * 0.1, 1e-4)
P_tank_lut = _RhoToPressureLUT(T_tank, rho_tank_min_est, rho_tank_max_est)
else:
V_tank = V_tank_inv = P_tank0 = T_tank = 0.0
m_tank = 0.0
P_tank_lut = None
if cb:
cb(0.05)
t_arr = np.linspace(0, dur, N + 1)
P_snub_arr = np.zeros(N + 1)
mdot_pump_arr = np.zeros(N + 1)
mdot_out_arr = np.zeros(N + 1)
mdot_net_arr = np.zeros(N + 1)
motor_pct_arr = np.zeros(N + 1)
valve2_pct_arr = np.zeros(N + 1)
T_pump_arr = np.zeros(N + 1)
P_tank_arr = np.zeros(N + 1) if fill_mode else None
m_tank_arr = np.zeros(N + 1) if fill_mode else None
rpt = max(N // 100, 1)
mdot_out_prev = 0.0
_sin = math.sin
_max = max
_min = min
for i in range(N + 1):
t = i * dt
if use_profiles and prof_times is not None:
motor_pct = self._profile_lookup(t, prof_times, prof_motor, static_motor_pct)
v2_pct = self._profile_lookup(t, prof_times, prof_valve2, static_v2_pct)
else:
motor_pct = static_motor_pct
v2_pct = static_v2_pct
speed_frac = _max(0.0, _min(motor_pct * 0.01, 1.0))
f2 = _max(0.0, _min(v2_pct * 0.01, 1.0))
rho_s = _max(m_snub * V_snub_inv, 1e-6)
P_snub = P_lut(rho_s)
P_snub_bar = P_snub / BAR2PA
# Downstream boundary
if fill_mode:
rho_t = _max(m_tank * V_tank_inv, 1e-6)
P_tank = P_tank_lut(rho_t)
P_downstream = P_tank
else:
P_tank = 0.0
P_downstream = P_atm
if pump_lut is not None and speed_frac > 0:
mdot_avg, T_pump = pump_lut.lookup(motor_pct, P_snub_bar)
if pulsation:
omega = speed_frac * omega_max
phase = _sin(omega * t)
mdot_p = mdot_avg * pi_val * _max(phase, 0.0)
else:
mdot_p = mdot_avg
else:
mdot_p = 0.0
T_pump = T_out
Cv2_eff = Cv2 * f2
mdot_o = mdot_out_prev
for _iter in range(3):
P_avg2 = _max((P_snub + P_downstream) * 0.5, P_downstream)
rho_g2 = P_avg2 / (R_H2 * T_out)
dp_pipe2 = self._pipe_dp(mdot_o, rho_g2, mu_g, D2, L2, A2, fLD2, eps)
P_back = P_downstream + dp_pipe2
mdot_o = self._valve_mdot_liq(P_snub, rho_s, P_back, Cv2_eff)
P_snub_arr[i] = P_snub
mdot_pump_arr[i] = mdot_p
mdot_out_arr[i] = mdot_o
mdot_net_arr[i] = mdot_p - mdot_o
motor_pct_arr[i] = motor_pct
valve2_pct_arr[i] = v2_pct
T_pump_arr[i] = T_pump
if fill_mode:
P_tank_arr[i] = P_tank
m_tank_arr[i] = m_tank
if i < N:
m_snub += (mdot_p - mdot_o) * dt
m_snub = _max(m_snub, 1e-15)
if fill_mode:
m_tank += mdot_o * dt
m_tank = _max(m_tank, 1e-15)
mdot_out_prev = mdot_o
if cb and i % rpt == 0:
cb(0.05 + 0.95 * i / N)
if cb:
cb(1.0)
out = {
"time": t_arr,
"P_snub_bar": P_snub_arr / BAR2PA,
"mdot_pump": mdot_pump_arr * 60.0,
"mdot_out": mdot_out_arr * 60.0,
"mdot_net": mdot_net_arr * 60.0,
"motor_pct": motor_pct_arr,
"valve2_pct": valve2_pct_arr,
"T_pump_K": T_pump_arr,
"sim_mode": sim_mode,
}
if fill_mode:
out["P_tank_bar"] = P_tank_arr / BAR2PA
out["m_tank_kg"] = m_tank_arr
out["T_tank_K"] = T_tank
return out
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