Heat recovery Process Flowsheets & Simulations
Explore 2 validated, solved Heat recovery simulation flowsheets in MaximaLabs — real components: n2, oxygen, co2, water, loaded_sorbent, regenerated_sorbent. Open any one directly in your browser.
Solved via: COOLPROP, PENG-ROBINSON.
Solid-sorbent fluidized-bed DAC with compression heat recovery
A second, lower-temperature DAC pathway alongside the liquid-KOH + rotary-kiln example: the captured CO₂ loads onto a solid sorbent, which regenerates in an indirectly-heated fluidized bed (real Wen-Yu minimum-fluidization sizing + Arrhenius desorption kinetics, the FluidizedBed) at 120 degC — the real low-temperature regime solid amine/physisorbent DAC sorbents actually use, versus the other example's ~977 degC calcination. The bed is fluidized by a recycled CO₂ sweep (self-sweep with product gas, a real design choice that sidesteps needing a steam-condensate knockout step). The desorbed CO₂ is compressed toward liquefaction pressure in one adiabatic stage — hot enough (~780 K discharge) that routing it through a heat exchanger against process utility water genuinely converts that water from subcooled liquid to a boiling mixed-phase stream before the CO₂ continues on to the same real liquefaction physics as the other DAC example.
14 unit ops • COOLPROP
222 0
View & openDesiccant rotor HVAC — three-stage low-grade heat recovery
A desiccant dehumidification rotor whose regeneration air is preheated by three low-grade heat sources in ascending temperature order: a PVT (photovoltaic-thermal) collector loop at 40 °C, condenser heat rejected by the chiller at 50 °C, and a district-heating return at 55 °C. Cascading them warmest-last is the whole point — each coil lifts the air as far as its own source can reach, so the 55 °C district return is spent only on the final lift instead of being wasted on air that is still at ambient. Every coil leaves a 5 K approach at its hot end, which is what makes this solvable: a cold stream can never leave an exchanger hotter than the hot stream entering it, and in a series train each coil's outlet is the next one's inlet, so a target that looks reasonable in isolation becomes impossible two units downstream. The hot-side flows are sized so the water gives up its duty over a modest ΔT and stays above the air at the cold end as well — specifying the approach alone is not enough if the heat-capacity flow rates don't support it. The rotor's two halves are custom_block equation blocks (the regen side and the process side), and the process air is finished to a 16 °C supply condition by the evaporator coil.
16 unit ops • PENG-ROBINSON
118 1
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