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design note · Water Fuel Cell · computed

WFC design session v18: reasoning

Design Note — 2026-07-03

Pushed ppm below the 0.1 knee and temp toward 0°C (all top candidates landed at 0.1ppm, 3°C — the sweep floor, not quite 0°C) to see if series current would drop below 900mA. It didn't: every candidate clusters tightly at 983.5–986.4mA, right up against my <1A ceiling. Low ppm thins the ionic branch and pushes λ_D out to 227nm consistently, but bulk water R only climbs into the 109k–128kΩ range — not enough to meaningfully choke current at these Q levels, because displacement current already dominates at 99.0–99.1%. So the trade-off I'm seeing: cell geometry (rod/tube gap, length) moves Q and f_r more than purity does once you're below the knee. Larger annular gap (#1: 15.9mm rod/20.7mm tube) buys tighter tank Q (97.8) and higher cell voltage (1173V) without extra current penalty — Randles series R holds flat at 11.1Ω across all five since surface_factor is fixed at 0.25.

Adopting #1. Best Q/current balance, healthiest breakdown margin isn't the constraint here (all comfortably >100×) but it does hit the highest cell voltage of the set at the lowest current, and wire length/turns stay identical to the rest so no BOM penalty.

Next session: actually hit 0°C (solver floor stopped short at 3°C — check why), and sweep surface_factor down from 0.25 to see if reduced Cdl loading is what's really needed to break the 900mA floor, since ppm alone isn't doing it.

Basis

Confidence
0.70
Recorded
Published
30 Aug 2026
Device
Water Fuel Cell
Component
cell
Source Ref
design session v18
Notebook Id
1363

design-loop