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STAR
Cal STAR — firmware, DAQ server, and engine design
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Variables | |
| ROOT = Path(__file__).resolve().parents[1] | |
| float | PSI = 6894.757 |
| float | D_TUBE = 0.010922 |
| float | A_TUBE = math.pi / 4.0 * D_TUBE ** 2 |
| float | D_NPT = 0.5 * 0.0254 |
The feed line's velocity head is lost where it dumps into the injector manifold, and one
flow area serves the loss model and the chug inertance alike.
Exit loss. From a still tank to a still manifold,
P_tank - P_manifold = (K_entrance + f L/D + K_exit) q_line,
and a line discharging into a plenum loses its whole velocity head: Borda-Carnot
K = (1 - A_line/A_manifold)^2 -> 1, Crane TP-410 "pipe exit" K = 1.0. The shipped K0 values
(scripts/feed_line_K.py) end at the last fitting, so P_injector was the stagnation pressure of
flow still moving at ~15 m/s, and every orifice was credited one line q too much.
Area. ``A_hydraulic`` is the passage; ``d_inlet`` used to win whenever it was set (it always
is), so a twin line or non-circular passage lost 4x too much in performance while the chug
model used the declared area.
Expected values are hand arithmetic.
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Definition at line 84 of file test_feed_exit_loss.py.
Referenced by test_injector_sees_the_manifold_not_the_line_stagnation().
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The authoritative Python path; engine/accel mirrors it and test_numba_ab_parity holds the two together.
Definition at line 35 of file test_feed_exit_loss.py.
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Definition at line 48 of file test_feed_exit_loss.py.
Referenced by test_area_alone_is_a_valid_feed_passage(), test_exit_loss_defaults_to_one_line_velocity_head(), test_exit_through_a_wider_fitting_is_referred_to_the_line(), test_injector_sees_the_manifold_not_the_line_stagnation(), and test_twin_line_area_is_used().
| test_feed_exit_loss.test_area_alone_is_a_valid_feed_passage | ( | ) |
feed_loss.py's own recipe: give A_hydraulic with d_inlet omitted.
Definition at line 76 of file test_feed_exit_loss.py.
References _q().
| test_feed_exit_loss.test_exit_loss_defaults_to_one_line_velocity_head | ( | ) |
Definition at line 53 of file test_feed_exit_loss.py.
References _q().
| test_feed_exit_loss.test_exit_through_a_wider_fitting_is_referred_to_the_line | ( | ) |
Tube into a 1/2" NPT bore, then the dump: K at the tube is (A_tube/A_npt)^2 = (0.430/0.500)^4.
Definition at line 59 of file test_feed_exit_loss.py.
References _q().
| test_feed_exit_loss.test_injector_sees_the_manifold_not_the_line_stagnation | ( | ) |
Definition at line 96 of file test_feed_exit_loss.py.
References _evaluate(), and _q().
| test_feed_exit_loss.test_twin_line_area_is_used | ( | ) |
Two 1/2" tubes: A = 2 x bore area. 1.118 kg/s of ethanol at K0 2.019 -> 6.61 psi, not 26.4.
Definition at line 67 of file test_feed_exit_loss.py.
References _q().
| float test_feed_exit_loss.A_TUBE = math.pi / 4.0 * D_TUBE ** 2 |
Definition at line 30 of file test_feed_exit_loss.py.
| float test_feed_exit_loss.D_NPT = 0.5 * 0.0254 |
Definition at line 31 of file test_feed_exit_loss.py.
| float test_feed_exit_loss.D_TUBE = 0.010922 |
Definition at line 29 of file test_feed_exit_loss.py.
| float test_feed_exit_loss.PSI = 6894.757 |
Definition at line 28 of file test_feed_exit_loss.py.
| test_feed_exit_loss.ROOT = Path(__file__).resolve().parents[1] |
Definition at line 27 of file test_feed_exit_loss.py.