"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."

Doesn't this directly contradict the APS analysis, which gives numbers
closer to $1000/t?
(with no sequestration)

Gregory Benford

On Wed, Jul 25, 2012 at 3:31 AM, Andrew Lockley <[email protected]>wrote:

> 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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