Experiment 0 is the cheap water-sealed bell side-bench. The first five are staged parent/kill-test builds before integrated hybrid claims.
0raw rank 17 · score 67.9
Water-sealed bell / siphon-primer bench
Experiment 0 / flooded-cup primer side-bench · Siphon helper · VERY_LOW (€50–€250) · ~1 days
Question: Does an inverted water-filled cup/bell over a hose inlet reduce priming loss, prevent air ingestion, and improve shallow-water pickup versus a bare hose?
Measure
- start success rate
- time to prime
- flow rate Q liters/min
- outlet head Δh
- minimum water depth before prime loss
- air ingestion rate / visible bubbles
- pressure drop / loss coefficient
- remaining water depth after drain
- debris clogging tendency
Kill criteria
- loses prime easily
- flow rate too low
- adds more hydraulic loss than it saves
- clogs or fouls too easily
- requires too much manual setup
- does not reduce pump-start energy or transfer J/cycle
- only works in shallow demo conditions but fails under repeated cycling
Accounting: HELPER_ONLY: WATER_SEALED_BELL_INTAKE is a passive hydraulic helper; source_credit_kw=0; credit only saved loss/J after added loss and complexity. source_credit_kw=0: this primitive is never an energy source. | Credit only reduced priming loss, reduced pump-start energy, reduced air-ingestion loss, or reduced transfer J/cycle. | A candidate only benefits when net_helper_value = saved_loss_or_saved_J - added_loss - added_complexity_penalty is positive. | Do not let this primitive improve product gate by itself; repeated-cycle reliability must pass first.
1raw rank 1 · score 85.1
Transparent HTH / trompe channel
minimum clear-pipe velocity ramp · HTH / trompe · VERY_LOW (€50–€250) · ~2 days
Question: What velocity/head first creates stable entrainment and positive separator pressure?
Measure
- flow velocity
- entrainment threshold
- bubble survival distance
- separator pressure
- air flow rate
- water head / depth
- net pneumatic power
- hydraulic/parasitic losses
Kill criteria
- no stable entrainment below practical velocities
- separator pressure too low for useful air output
- parasitic losses exceed useful pneumatic output
- bubble transport collapses before separator
Accounting: EXTERNAL_RESOURCE: river/current/depth head measured; no gravity/buoyancy free-source credit. External energy is river/current/depth head, not gravity as free source. | Report pneumatic output after water-flow and separator losses. | Do not credit downstream water flow twice if an air turbine is measured.
2raw rank 6 · score 74.5
MGHB wave tank cell
piston-only baseline · MGHB / wave · LOW (€250–€900) · ~5 days
Question: What fraction of incoming wave energy can a guided piston convert without pneumatic hybrid complexity?
Measure
- incoming wave height
- outgoing wave height
- piston stroke
- piston force
- generator/load output
- damping setting
- water leakage/slam
- wave period
- absorbed wave fraction
Kill criteria
- wave reduction poor
- useful work fraction too low
- mechanical loads too high
- hybrid complexity worse than piston-only or pneumatic-only
- storm/surge mode cannot fail safe
Accounting: EXTERNAL_RESOURCE: incoming wave energy measured and normalized against wave reduction/output. External source is wave energy crossing the cell, not buoyancy alone. | Credit either piston output or OWC pneumatic output separately before hybrid sum. | Compare against passive breakwater wave reduction and piston-only baseline.
3raw rank 5 · score 77.3
Pure DGTE rotary/starwheel crossover rig
single pocket dye/carry-over test · Pure DGTE · VERY_LOW (€50–€250) · ~3 days
Question: Can a wetted starwheel transfer capsules with low carry-over?
Measure
- transfer J/cycle
- carry-over fluid mass
- leakage
- torque/current per transfer
- pressure balance stability
- cycle rate
- jam rate
- seal friction
Kill criteria
- transfer work exceeds expected stroke gain
- carry-over too high
- sealing friction too high
- cycle rate too low
- pressure-balanced pockets cannot stay repeatable
Accounting: THERMAL_CLOSURE: P_net=min(P_thermal_gross,P_PTO_path)-transfer-auxiliary. Crossover does not create energy; it must reduce losses enough for thermal stroke to matter. | Measured J/transfer must be compared against expected per-cycle stroke work. | Carry-over heat/fluid penalty must be included.
4raw rank 11 · score 69.9
Hydraulic balanced lock rig
empty lock equalization baseline · Pure DGTE · VERY_LOW (€50–€250) · ~3 days
Question: What is the minimum pressure-equalization cost before capsules are added?
Measure
- pressure equalization energy
- lock leakage
- valve losses
- throughput
- J/transfer
- fouling sensitivity
- timing jitter
Kill criteria
- lock overhead kills net power
- fouling or complexity too high
- valve losses dominate
- throughput too low for useful cycle rate
Accounting: THERMAL_CLOSURE: P_net=min(P_thermal_gross,P_PTO_path)-transfer-auxiliary. Pressure equalization is not free; count valve and timing losses. | Lock only survives if it reduces transfer loss below stroke-gain budget. | No product claim until fouling and repeatability are tested.
5raw rank 27 · score 63.3
Integrated DGTE thermal slice
controlled heater closure · Pure DGTE · MEDIUM (€900–€2800) · ~6 days
Question: Can a DGTE slice close thermal-to-mechanical accounting with a known heat input?
Measure
- hot/cold temperatures
- thermal input
- real ΔT
- cycle work
- transfer losses
- auxiliary pumping
- net electrical output
- heat exchanger area
- recuperator effectiveness
Kill criteria
- thermal-to-mechanical closure fails
- required heat exchanger area too large
- low-grade waste heat insufficient
- auxiliary pumping exceeds generated work
- cycle rate too low
Accounting: THERMAL_CLOSURE: P_net=min(P_thermal_gross,P_PTO_path)-transfer-auxiliary. Use P_net = min(P_thermal_gross, P_mechanical_or_PTO_path_gross) - transfer losses - auxiliaries. | Waste heat must pay exergy/temperature limit. | Heat source and sink must be measured as a pair.