Template:Electric Power per O2 Effluent Impurity Recycler (W/liquefactor)

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232.52348851531

Model

Specific energy cost to liquefy NH3 at ambient (J/kg) * Oxygen Effluent Impurity Rate Per Area (kg/s/photobioreactor) * ( 1 + 1/Growth Medium Gas Tolerable O2 Fraction )

Comment

Deriving gas flow to be reduced to NH3 liquefaction temperature sufficient to extract the O2 production rate from the photobioreactor.

Notes

It may be that graphene will prove useful in this process: http://www.manchester.ac.uk/research/news/display/?id=7895