| Literature DB >> 34241997 |
David Danaci1, Mai Bui2,3, Camille Petit1, Niall Mac Dowell2,3.
Abstract
As more countries commit to a net-zero GHG emission target, we need a whole energy and industrial system approach to decarbonization rather than focus on individual emitters. This paper presents a techno-economic analysis of monoethanolamine-based post-combustion capture to explore opportunities over a diverse range of power and industrial applications. The following ranges were investigated: feed gas flow rate between 1-1000 kg ·s-1, gas CO2 concentrations of 2-42%mol, capture rates of 70-99%, and interest rates of 2-20%. The economies of scale are evident when the flue gas flow rate is <20 kg ·s-1 and gas concentration is below 20%mol CO2. In most cases, increasing the capture rate from 90 to 95% has a negligible impact on capture cost, thereby reducing CO2 emissions at virtually no additional cost. The majority of the investigated space has an operating cost fraction above 50%. In these instances, reducing the cost of capital (i.e., interest rate) has a minor impact on the capture cost. Instead, it would be more beneficial to reduce steam requirements. We also provide a surrogate model which can evaluate capture cost from inputs of the gas flow rate, CO2 composition, capture rate, interest rate, steam cost, and electricity cost.Entities:
Keywords: BECCS; CO2 capture; capture cost; capture rate; decarbonization; industrial CCS; post-combustion capture; techno-economic analysis
Year: 2021 PMID: 34241997 DOI: 10.1021/acs.est.0c07261
Source DB: PubMed Journal: Environ Sci Technol ISSN: 0013-936X Impact factor: 9.028