Future technological and economic performance of IGCC and FT production facilities with and without CO2 capture: Combining component based learning curve and bottom-up analysis
Publication date
2013
Authors
Knoope, M.M.J.
Meerman, J.C.
Ramirez, C.A.
Faaij, A.P.C.
Editors
Advisors
Supervisors
Document Type
Article
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(c) UU Universiteit Utrecht, 2013
Abstract
This study aims to investigate the technological and economic prospects of integrated gasification facilities
for power (IGCC) and Fischer–Tropsch (FT) liquid production with and without CCS over time. For
this purpose, a component based experience curve was constructed and applied to identify the potential
performance improvement of integrated gasification facilities. The results of the experience curve were
compared with a bottom-up technology analysis conducted in previous work (Meerman et al., 2012).
Results indicate that substantial cost reductions and performance improvements are possible, especially
for IGCC with CCS. For instance, the costs of electricity production (COE) may decrease from
82
D2008/MWh at present to 50
D2008/MWh in 2050, if solid oxide fuel cells become commercially available
(with a constant coal price of 2.25
D2008/GJ). This cost decrease can only be realized if installed IGCC
capacity increase to over 600 GWe and installed CCS capacity to over 3000 GWe equivalent. Also IGCC
without CCS have considerable learning potential, with COE projected to decrease from the current 60
to 40
D2008/MWh in the long term. Furthermore, the COE of IGCC without CCS could be competitive with
the current market price in the short term. Initial support is, however, needed to realize the first 20 GWe.
Currently, coal-based FT-liquids are already competitive at an oil price of 77
D2008/bbl for FT-liquids
without CCS and of 83
D2008/bbl with CCS, resulting in CO2 capture costs of only 11
D2008/t CO2. By 2050,
production costs of FT-liquids could drop to 9.3
D2008/GJ for FT-liquids without CCS and to 10
D2008/GJ for
FT-liquids with CCS. To realize this cost reduction, an installed capacity of about 430 GWth FT is needed.
The bottom-up and the component based experience curve analyses gave comparable trends regarding
the potential development of efficiency, capital costs and production costs for a scenario with a strong
growth in IGCC, FT and CCS capacity. The main advantage of combining the two approaches is that it
becomes clear how cost reductions can be achieved, what kind of capacity development and the time
frame is required to reach the projected improvements.
Keywords
Gasification, Experience, Learning, CCS, FT-liquids, IGCC