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BOG recondenser simulation

boil-off vapour + subcooled LNG -> recondensed liquid (+ surplus vapour)

Governing equations

The exact equations the solver works for a bog recondenser — the same math shown in the app's "Theory" panel, not a black box.

n˙LNGΔhsubn˙BOGΔhcond\dot n_{LNG}\,\Delta h_{sub} \ge \dot n_{BOG}\,\Delta h_{cond}
(n˙LNGn˙BOG)min=ΔhcondΔhsub\left(\frac{\dot n_{LNG}}{\dot n_{BOG}}\right)_{min} = \frac{\Delta h_{cond}}{\Delta h_{sub}}
Δhsub=hL(Tbub,P)hL(TLNG,P)\Delta h_{sub} = h_L(T_{bub}, P) - h_L(T_{LNG}, P)
n˙LNG\dot n_{LNG}
subcooled send-out LNG [mol/s]
n˙BOG\dot n_{BOG}
boil-off vapour to be condensed [mol/s]
Δhsub\Delta h_{sub}
subcooling available per mole of LNG [J/mol]
Δhcond\Delta h_{cond}
heat the vapour must give up to condense [J/mol]
hLh_L
liquid molar enthalpy [J/mol]
TLNGT_{LNG}
subcooled LNG temperature [K]
TbubT_{bub}
bubble point at the recondenser pressure [K]
PP
pressure [Pa]

Parameters

puts boil-off back into the liquid instead of flaring it: the subcooling in the send-out LNG condenses the vapour. Two inlets (BOG vapour + subcooled LNG, told apart by phase). Reports lng_to_bog_ratio against the minimum_ratio the energy balance demands; below it the surplus vapour leaves as a SECOND outlet rather than being silently condensed

Example flowsheets that use it

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