LCOE = P.mean + (C.fix - P.std f(z))/F(z)
C.fix is fixed costs MW capacity allocated per hour.
F and f are the standard normal cdf and pdf.
Z = (P - P.mean)/P.std
F(z) is also the capacity factor operating whenever X <= x.
C.fix / P.std = z F(z) + f(z)
When cost to volatility is 1, LCOE is minimized at 81.6% CF, z = 0.90.
At a ratio of 0.5, 57.5% CF, z = 0.19.
At a ratio of 0.25, 36.7% CF, z = -0.34
Decreasing capex also leads to obtaining minimal LCOE at lower CF.
NV = (V.h - LCOE) F(z)
= (V.hy - P.mean) F(z) + P.std f(z) - C.fix
The option theoretic value of an electrolyzer is obtained by maximizing NV.
V.hy = $40/MWh = $2.00/kg
C.fix = $10/MWh ~ $876/kW capex
P.mean = $30/MWh
At 100% CF this is breakeven, NV = $0/MWh. We can do better.
MaxNV = $0.83/MWh at CF 84%
MinLCOE = $38.99/MWh at CF 82%
Electrolyzer NPV = $73/kW
MaxNV = $3.96/MWh at CF 69%
MinLCOE = $33.76/MWh at CF 57%
Electrolyzer NPV = $347/kW
MaxNV = $7.63/MWh at CF 59%
MinLCOE = $25.83/MWh at CF 33%
Electrolyzer NPV = $668/kW
en.m.wikipedia.org/wiki/Truncated…
Note also that combined CF is 100%, indication that the electrolyzer kicks in when generation becomes marginally unprofitable and vice versa.
Second, build our 3MW electrolyzer for 1 MW gas.
The first substantially boosts the ROi of electrolyzers which would induce more investment in more capacity.
Next, I will argue that battery storage will be of little help to stop value erosion of thermal fleets.