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Capturing CO2 from ambient air - David Keith

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F Liquid flow rate in the contactor [m 3 /s]<br />

g Gravitational constant [m 2 /s]<br />

H Height of the contactor [m]<br />

h Vertical coordinate (height) within contactor [m]<br />

K Collection kernel for colliding drops [cm 3 /s]<br />

kg Gas-side mass transfer coefficient<br />

kspray Empirical spray constant: <strong>CO2</strong> absorption per unit surface area per unit time<br />

kv Empirical constant for calculating the terminal velocity of a drop<br />

˙M Rate of <strong>CO2</strong> absorption by the contactor<br />

O&M Operating costs excluding energy [US$/yr]<br />

[OH − ] Concentration of hydroxide ions in solution [mol/L]<br />

pelec Price of carbon-neutral electricity [US$/GJ]<br />

ptherm Price of thermal energy (natural gas equivalent) [US$/GJ]<br />

Q Rate of <strong>CO2</strong> absorption by a drop [mol/s]<br />

R Gas constant<br />

R C/Cnet<br />

�<br />

mol<br />

m2 �<br />

s<br />

Ratio of carbon processed by a component to net carbon captured by the total system []<br />

R H2O/<strong>CO2</strong> Ratio of water lost by evaporation to <strong>CO2</strong> absorbed by NaOH solution, molar basis []<br />

RH Relative humidity of <strong>air</strong><br />

S Average surface area of spray per unit bulk volume in the contactor<br />

�<br />

m2 surface<br />

m2 �<br />

contactor<br />

t time since a drop leaves the nozzle or since a parcel of <strong>air</strong> entered the contactor [s]<br />

T Temperature of <strong>air</strong><br />

V Volume of the contactor [m 3 ]<br />

Vd Volume of a drop<br />

ΔCH2O Difference between inlet and outlet water vapor concentration in the contactor<br />

ΔG Change in free energy<br />

67

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