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Direct Air Capture, Calcination & Liquefaction

Two DAC pathways — a liquid-KOH contactor + rotary-kiln calciner, and a lower-temperature solid-sorbent fluidized bed with real compression heat recovery — both into genuine CO2 liquefaction, plus this platform's built-in Scope 1/2/3 carbon-footprint and Capex reporting from one click.

daccalcinationco2 liquefactionesgheat recovery
Concept

A Carbon Engineering-style DAC train: a liquid-KOH contactor captures CO2 from ambient air, causticized and precipitated pellets calcine in a real indirectly-heated rotary kiln (Arrhenius decomposition kinetics, Sullivan-Maynard-Valentine residence time), and the released CO2 is compressed and chilled into genuine subcooled liquid CO2 — not just dense-phase pipeline gas.

The math
Show the governing equations
CaCO3→k(T)CaO+CO2k(T)=k0e−Ea/RT\text{CaCO}_3 \xrightarrow{k(T)} \text{CaO} + \text{CO}_2 \quad k(T)=k_0 e^{-E_a/RT}
Pliq=19.7 atm>Psat, CO2(250 K)≈17.8 atmP_{liq} = 19.7\,\text{atm} > P_{sat,\,CO_2}(250\,\text{K}) \approx 17.8\,\text{atm}
Compressing to ~20 atm and chilling to 250 K crosses above CO2's real Span-Wagner/CoolProp saturation pressure at that temperature -- the solved outlet stream reports phase='liquid', a verifiable claim, not an assumption.
Execution

Verified Scope 1/2/3 + Capex, genuinely one click

Open the Report view on this example: Economics/Capex and Carbon/Sustainability render side by side from the same solved flowsheet, and one "Print / Save as PDF" button produces both sections in a single document — a real claim, not marketing copy. Precisely stated: this is a real, correctly-computed analysis pass over the solved result (real emission factors, not fabricated numbers) — it is not literally a field carried on every Stream/node object the way flow or temperature are; don't oversell "native on every node" beyond what that means.

The direct air capture calcination flowsheet in the MaximaLabs workbench

The example as it opens in the workbench. Click to enlarge.

Launch in MaximaLabs Workspace
A second, lower-temperature DAC pathway

Solid-sorbent DAC sorbents regenerate far below a KOH/CaCO3 loop's ~977°C calcination — this second example desorbs a loaded solid sorbent in a real fluidized bed (Wen-Yu minimum-fluidization sizing + Arrhenius desorption kinetics) at 120°C, self-swept by recycled product CO2. The desorbed gas is hot enough after compression (~780 K) that routing it through a heat exchanger against process water — instead of rejecting that heat to cooling water — genuinely converts subcooled liquid water into a boiling mixed-phase stream: real waste-heat recovery, the actual principle behind mechanical vapor recompression (MVR). Honesty note: this recovers real compression heat into a useful utility stream, but does not feed it back into the fluidized bed's own desorption duty (a fixed parameter on this unit op, not a second heating-utility stream) — a literal closed MVR loop onto the desorber itself isn't wireable with this unit op as built.

The fluidized bed dac heat recovery flowsheet in the MaximaLabs workbench

The example as it opens in the workbench. Click to enlarge.

Launch in MaximaLabs Workspace