Process modelling and techno-economic analysis of natural gas combined cycle integrated with calcium looping

Calcium looping (CaL) is promising for large-scale CO2 capture in the power generation and industrial sectors due to the cheap sorbent used and the relatively low energy penalties achieved with this process. Because of the high operating temperatures the heat utilisation is a major advantag...

Full description

Bibliographic Details
Main Authors: Erans María, Hanak Dawid P., Mir Jordi, Anthony Edward J., Manovic Vasilije
Format: Article
Language:English
Published: VINCA Institute of Nuclear Sciences 2016-01-01
Series:Thermal Science
Subjects:
Online Access:http://www.doiserbia.nb.rs/img/doi/0354-9836/2016/0354-98361500209E.pdf
id doaj-08b894cb74ee44fc8ec889e1e420bd74
record_format Article
spelling doaj-08b894cb74ee44fc8ec889e1e420bd742021-01-02T01:11:28ZengVINCA Institute of Nuclear SciencesThermal Science0354-98362334-71632016-01-0120suppl. 1596710.2298/TSCI151001209E0354-98361500209EProcess modelling and techno-economic analysis of natural gas combined cycle integrated with calcium loopingErans María0Hanak Dawid P.1Mir Jordi2Anthony Edward J.3Manovic Vasilije4Cranfield University, Combustion and CCS Centre, Bedford, Bedfordshire, UKCranfield University, Combustion and CCS Centre, Bedford, Bedfordshire, UKCranfield University, Combustion and CCS Centre, Bedford, Bedfordshire, UKCranfield University, Combustion and CCS Centre, Bedford, Bedfordshire, UKCranfield University, Combustion and CCS Centre, Bedford, Bedfordshire, UKCalcium looping (CaL) is promising for large-scale CO2 capture in the power generation and industrial sectors due to the cheap sorbent used and the relatively low energy penalties achieved with this process. Because of the high operating temperatures the heat utilisation is a major advantage of the process, since a significant amount of power can be generated from it. However, this increases its complexity and capital costs. Therefore, not only the energy efficiency performance is important for these cycles, but also the capital costs must be taken into account, i.e. techno-economic analyses are required in order to determine which parameters and configurations are optimal to enhance technology viability in different integration scenarios. In this study the integration scenarios of CaL cycles and natural gas combined cycles (NGCC) are explored. The process models of the NGCC and CaL capture plant are developed to explore the most promising scenarios for NGCC-CaL integration with regards to efficiency penalties. Two scenarios are analysed in detail, and show that the system with heat recovery steam generator (HRSG) before and after the capture plant exhibited better performance of 49.1% efficiency compared with that of 45.7% when only one HRSG is located after the capture plant. However, the techno-economic analyses showed that the more energy efficient case, with two HRSGs, implies relatively higher cost of electricity (COE), 44.1€/MWh, when compared to that of the reference plant system (33.1€/MWh). The predicted cost of CO2 avoided for the case with two HRSGS is 29.3 €/ton CO2.http://www.doiserbia.nb.rs/img/doi/0354-9836/2016/0354-98361500209E.pdfNGCCcalcium loopingefficiency penaltytechno-economic analysis
collection DOAJ
language English
format Article
sources DOAJ
author Erans María
Hanak Dawid P.
Mir Jordi
Anthony Edward J.
Manovic Vasilije
spellingShingle Erans María
Hanak Dawid P.
Mir Jordi
Anthony Edward J.
Manovic Vasilije
Process modelling and techno-economic analysis of natural gas combined cycle integrated with calcium looping
Thermal Science
NGCC
calcium looping
efficiency penalty
techno-economic analysis
author_facet Erans María
Hanak Dawid P.
Mir Jordi
Anthony Edward J.
Manovic Vasilije
author_sort Erans María
title Process modelling and techno-economic analysis of natural gas combined cycle integrated with calcium looping
title_short Process modelling and techno-economic analysis of natural gas combined cycle integrated with calcium looping
title_full Process modelling and techno-economic analysis of natural gas combined cycle integrated with calcium looping
title_fullStr Process modelling and techno-economic analysis of natural gas combined cycle integrated with calcium looping
title_full_unstemmed Process modelling and techno-economic analysis of natural gas combined cycle integrated with calcium looping
title_sort process modelling and techno-economic analysis of natural gas combined cycle integrated with calcium looping
publisher VINCA Institute of Nuclear Sciences
series Thermal Science
issn 0354-9836
2334-7163
publishDate 2016-01-01
description Calcium looping (CaL) is promising for large-scale CO2 capture in the power generation and industrial sectors due to the cheap sorbent used and the relatively low energy penalties achieved with this process. Because of the high operating temperatures the heat utilisation is a major advantage of the process, since a significant amount of power can be generated from it. However, this increases its complexity and capital costs. Therefore, not only the energy efficiency performance is important for these cycles, but also the capital costs must be taken into account, i.e. techno-economic analyses are required in order to determine which parameters and configurations are optimal to enhance technology viability in different integration scenarios. In this study the integration scenarios of CaL cycles and natural gas combined cycles (NGCC) are explored. The process models of the NGCC and CaL capture plant are developed to explore the most promising scenarios for NGCC-CaL integration with regards to efficiency penalties. Two scenarios are analysed in detail, and show that the system with heat recovery steam generator (HRSG) before and after the capture plant exhibited better performance of 49.1% efficiency compared with that of 45.7% when only one HRSG is located after the capture plant. However, the techno-economic analyses showed that the more energy efficient case, with two HRSGs, implies relatively higher cost of electricity (COE), 44.1€/MWh, when compared to that of the reference plant system (33.1€/MWh). The predicted cost of CO2 avoided for the case with two HRSGS is 29.3 €/ton CO2.
topic NGCC
calcium looping
efficiency penalty
techno-economic analysis
url http://www.doiserbia.nb.rs/img/doi/0354-9836/2016/0354-98361500209E.pdf
work_keys_str_mv AT eransmaria processmodellingandtechnoeconomicanalysisofnaturalgascombinedcycleintegratedwithcalciumlooping
AT hanakdawidp processmodellingandtechnoeconomicanalysisofnaturalgascombinedcycleintegratedwithcalciumlooping
AT mirjordi processmodellingandtechnoeconomicanalysisofnaturalgascombinedcycleintegratedwithcalciumlooping
AT anthonyedwardj processmodellingandtechnoeconomicanalysisofnaturalgascombinedcycleintegratedwithcalciumlooping
AT manovicvasilije processmodellingandtechnoeconomicanalysisofnaturalgascombinedcycleintegratedwithcalciumlooping
_version_ 1724363135124504576