TY - JOUR
T1 - Investigation of Alternative Strategies for Integrating Post-combustion CO2 Capture to a Natural Gas Combined Cycle Power Plant
AU - Biliyok, Chechet
AU - Canepa, Roberto
AU - Hanak, Dawid P.
N1 - Publisher Copyright:
© 2015 American Chemical Society.
PY - 2015/7/16
Y1 - 2015/7/16
N2 - With increasing urgency for global action toward climate change mitigation, this study is undertaken to evaluate integration options for post-combustion CO2 capture (PCC) on gas-fired power plants. High-fidelity models of a natural gas combined cycle power plant, a PCC plant, and a CO2 compression train are integrated for a 90% CO2 capture level. Three options to provide steam for solvent regeneration are explored: extracting steam from the intermediate-pressure (IP)/low-pressure (LP) crossover, using a gas-fired package boiler, and extracting steam from the LP drum. The effect of pressure losses because of steam extraction, a factor ignored in previous analyses, is also considered. The integrated plant net efficiency is 47.8, 40.4, and 44.9%, respectively, for the aforementioned scenarios. Next, supplementary firing of gas turbine exhaust is employed to generate an ample amount of steam to preserve plant net output under a sliding pressure scenario and meet solvent regeneration requirements. It is observed that the net plant efficiency converges to a value of 43.5% for the options considered.
AB - With increasing urgency for global action toward climate change mitigation, this study is undertaken to evaluate integration options for post-combustion CO2 capture (PCC) on gas-fired power plants. High-fidelity models of a natural gas combined cycle power plant, a PCC plant, and a CO2 compression train are integrated for a 90% CO2 capture level. Three options to provide steam for solvent regeneration are explored: extracting steam from the intermediate-pressure (IP)/low-pressure (LP) crossover, using a gas-fired package boiler, and extracting steam from the LP drum. The effect of pressure losses because of steam extraction, a factor ignored in previous analyses, is also considered. The integrated plant net efficiency is 47.8, 40.4, and 44.9%, respectively, for the aforementioned scenarios. Next, supplementary firing of gas turbine exhaust is employed to generate an ample amount of steam to preserve plant net output under a sliding pressure scenario and meet solvent regeneration requirements. It is observed that the net plant efficiency converges to a value of 43.5% for the options considered.
UR - http://www.scopus.com/inward/record.url?scp=84937123909&partnerID=8YFLogxK
U2 - 10.1021/acs.energyfuels.5b00811
DO - 10.1021/acs.energyfuels.5b00811
M3 - Article
AN - SCOPUS:84937123909
SN - 0887-0624
VL - 29
SP - 4624
EP - 4633
JO - Energy and Fuels
JF - Energy and Fuels
IS - 7
ER -