Thermodynamic Model of CO2 Deposition in Cold Climates
- Sandra K. S. Boetcher, Matthew J. Traum, Ted von Hippel
*link.springer.com*/article/10.1007/s10584-019-02587-3
<https://link.springer.com/article/10.1007/s10584-019-02587-3>

A thermodynamic model, borrowing ideas from psychrometric principles, of a
cryogenic direct-air CO2-capture system utilizing a precooler is used to
estimate the optimal CO2 removal fraction to minimize energy input per
tonne of CO2. Energy costs to operate the system scale almost linearly with
the temperature drop between the ingested air and the cryogenic
desublimation temperature of CO2, driving siting to the coldest accessible
locations. System performance in three Arctic/Antarctic regions where the
proposed system can potentially be located is analyzed. Colder ambient
temperatures provide colder system input air temperature yielding lower CO2
removal energy requirements. A case is also presented using direct-sky
radiative cooling to feed colder-than-ambient air into the system. Removing
greater fractions of the ingested CO2 lowers the CO2 desublimation
temperature, thereby demanding greater energy input for air cooling. It
therefore is disadvantageous to remove all CO2 from the processed air, and
the optimal mass fraction of CO2 desublimated under this scheme is found to
be ~0.8-0.9. In addition, a variety of precooler effectiveness (*ε* )
values are evaluated. Increasing effectiveness reduces the required system
power input. However, beyond *ε* = 0.7, at certain higher values of
desublimated CO2 mass fraction, the CO2 begins to solidify inside the
precooler before reaching the cryocooler. This phenomenon fouls the
precooler, negating its effectiveness. Further system efficiencies can be
realized via a precooler designed to capture solidified CO2 and eliminate
fouling.

CO2 desublimation thermodynamics cryogenics Arctic/Antarctica


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