International Journal of Greenhouse Gas Control 8 (2012) 180–195
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International Journal of Greenhouse Gas Control
j our na l ho me p age: www.elsevier.com/locate/ijggc
Optimizing post-combustion CO
2
capture in response to volatile electricity prices
Stuart M. Cohen
a,∗
, Gary T. Rochelle
b
, Michael E. Webber
a
a
Department of Mechanical Engineering, The University of Texas at Austin, 1 University Station C2200, Austin, TX 78712, USA
b
Department of Chemical Engineering, The University of Texas at Austin, 1 University Station C0400, Austin, TX 78712, USA
a r t i c l e i n f o
Article history:
Received 11 August 2011
Received in revised form 15 February 2012
Accepted 17 February 2012
Available online 17 March 2012
Keywords:
CO2 capture
Flexibility
Economics
Electricity markets
Optimization
Amine scrubbing
a b s t r a c t
Flexibly operating CO
2
capture at power plants allows a temporary increase in electrical output, which
could help maintain grid reliability, meet peak demand, or improve profitability when electricity prices
are high. This article presents a versatile optimization model that maximizes profits at a fossil-based
power plant with CO
2
capture by operating in response to volatile electricity prices. The model is demon-
strated for a 500 MW coal-fired unit using 7 molal monoethanolamine for post-combustion CO
2
capture.
The importance of modeling electricity price volatility when valuing flexible capture is demonstrated by
comparing model results to those from a first-order electricity dispatch model that does not incorporate
price volatility. CO
2
emissions and plant economics are then compared for operation under three 20-
year CO
2
price paths and four facility configurations: no CO
2
capture, inflexible CO
2
capture, flexible CO
2
capture that vents CO
2
at partial load, and flexible capture that uses solvent storage to mitigate venting
at partial load. Flexible capture improves investment value over inflexible capture while maintaining
substantial CO
2
emissions reductions, but economic benefits are greatest at low CO
2
prices where CO
2
capture investment might still be unjustifiable. Flexibility provides the greatest economic advantage if
CO
2
prices are $40–50 per metric ton of CO
2
for a substantial portion of plant economic life. Solvent
storage permits greater operating profits and lower CO
2
emissions than a venting-only flexible capture
facility, but benefits can be offset by increased capital costs.
© 2012 Elsevier Ltd. All rights reserved.
1. Introduction
1.1. Introduction to flexible CO
2
capture
Carbon dioxide capture and sequestration (CCS) enables con-
tinued fossil fuel use for electricity production and industrial
processes with substantial reductions in emissions of carbon
dioxide (CO
2
), the greenhouse gas primarily contributing to anthro-
pogenic climate change (Metz et al., 2005). The largest application
for CO
2
capture is electricity production, but while leading CO
2
capture technologies can remove 90% or more CO
2
from power
plant flue gas, the energy requirements for leading CO
2
capture
and compression technologies can reduce net electrical output by
20–30% (7–11% efficiency points) below that of facilities without
CO
2
capture (Chalmers et al., 2010; Rochelle et al., 2011). Most
studies assume that CO
2
capture and compression systems oper-
ate continuously whenever the base plant operates, so any energy
required for CO
2
capture and compression permanently reduces
output and increases electricity production costs (Davison, 2007;
Rubin et al., 2007). However, there is a growing attention to the
∗
Corresponding author. Tel.: +1 512 232 2754; fax: +1 512 471 1045.
E-mail addresses: stuart.cohen@utexas.edu (S.M. Cohen),
gtr@che.utexas.edu (G.T. Rochelle), webber@mail.utexas.edu (M.E. Webber).
value of operating some or all CO
2
capture systems at partial or
zero load and utilizing this flexibility to operate CO
2
capture in
response to variable electricity market conditions (Chalmers et al.,
2009, 2010; Husebye et al., 2010; Ludig et al., 2010).
If the base plant must ever operate variably, some degree of
CO
2
capture flexibility is needed to ensure stable operation across
the base plant power output range (Davison, 2010). However, this
work defines flexible CO
2
capture as operating CO
2
capture sys-
tems at a different, typically lower, fractional load than the base
power plant. With sufficient turbine-generator capacity and a cap-
ture system conducive to flexible operation, reduced load on energy
intensive CO
2
capture systems during full-load base plant opera-
tion could allow net power output to approach non-capture levels.
Alternately, operating the base plant at minimum load while all
flue gas is treated by CO
2
capture reduces the net minimum power
output, which could be desirable if electricity prices fall below oper-
ating costs for too short a time to justify the costs of base plant
shutdown and startup (Chalmers et al., 2009).
Using flexible CO
2
capture to temporarily increase power output
is valuable during periods of peak electricity demand. In a retrofit
application, doing so eliminates the need to invest in new gen-
erating capacity to replace the output lost to CO
2
capture energy
requirements, and peak demand infrequency prevents any signifi-
cant CO
2
emissions increase (Cohen et al., 2010b; Wiley et al., 2010).
In electricity systems with deregulated markets, partial or zero load
1750-5836/$ – see front matter © 2012 Elsevier Ltd. All rights reserved.
doi:10.1016/j.ijggc.2012.02.011