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design note · Water Fuel Cell · computed

WFC design session v12: reasoning

Lab note, 7/3/26.

This sweep confirms what I suspected: at fixed geometry (21.8mm rod/26.8mm tube, 60mm) and 0.1ppm Na+ water at 5°C, the Randles double-layer parameters barely move the needle. Candidates #1-4 are identical electrically — same C_eff (1.39nF), same bulk R, same tank Q (91.2), same 915.8mA current, same 1094V output. Surface_factor sweeping from ×0.5 to ×4 only changes C_dl (3.8µF→30.1µF) without touching resonance, because at 96kHz the double-layer impedance is so low relative to the bulk/geometric branch that Cdl just isn't in the current path — displacement current stays pinned at 99.0%. So surface treatment, at least in this ppm/temp regime, is not a lever for Q or current headroom. That's useful negative information — it tells me the ionic branch is already dominated by bulk R, not electrode kinetics.

Comparing #1 to #5: going to 2 parallel cells drops Q (91.2→70.6) and f_r (96→74kHz) while current rises toward the 1A ceiling (923.6mA) despite better breakdown margin. Confirms the Q-vs-current-vs-cell-count trade I've logged before — cell count is a bigger lever than surface finish.

Adopting #1: best score, lowest current (915.8mA, more headroom under 1A cap), highest breakdown margin at single-cell simplicity, and surface ×0.5 means less electrode prep — cheapest build for the same performance as #2-4.

Next session: sweep ppm and temperature independently (not just surface_factor) to see if bulk R — the actual dominant term — can be pushed lower without wrecking breakdown margin.

Basis

Confidence
0.70
Recorded
Published
30 Aug 2026
Device
Water Fuel Cell
Component
cell
Source Ref
design session v12
Notebook Id
1350

design-loop