Analysis of Equilibrium-Based TSA Processes for Direct Capture of CO2 from Air

http://pubs.acs.org/doi/abs/10.1021/ie300691c?prevSearch=air%2Bcapture&searchHistoryKey=

DOI: 10.1021/ie300691c

Abstract
Direct capture of CO2 from air is a concept that, if successfully
implemented, could lead to capture of CO2 from disperse sources. We
have developed process models to consider the viability of
adsorption-based air capture technologies. Our models focus on using
an amino-modified silica adsorbent, TRI-PE-MCM-41, and a structured
monolithic contactor unit. We have studied several different
temperature swing adsorption processes using the purity of CO2 and
annual product throughput as metrics for comparing process
performance. This analysis identifies some of the operational
parameters, adsorbent characteristics, and other factors that have a
significant effect on the performance of the process. Using the total
energy requirement of the process and available sources of energy,
such as low pressure steam and electricity, we carry out an economic
analysis to obtain a net operating cost for air capture of CO2. We
identify a process with a daily throughput of 1.1 t CO2 at 88.5%
purity using standard shipping container sized air capture units. The
total energy required (6745 MJ/t CO2) is dominated by the parasitic
losses—sensible heat requirements of the contactor (40%) and the
adsorbent (28%) and not by the mechanical energy associated with air
flow (5%). On the basis of our analysis of factors such as source of
electricity, availability of low pressure steam, and geographic
location, the net operating cost of capture is estimated to be $100/t
CO2. These cost estimates do not include capital expenses necessary to
construct or maintain the air capture units. Potential strategies for
further reducing the energy and monetary cost of these processes are
identified. Our analysis supports continued work to establish the
technological and economic feasibility of adsorption-based air
capture.

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