@book{
 title = {Integration of Retrofitted Coal-fired Power Plant with CCS: Power De-rate Minimization},
 type = {book},
 year = {2015},
 source = {Computer Aided Chemical Engineering},
 keywords = {CCS,Parametric optimization,Power de-rate,Variable evaluation},
 volume = {37},
 id = {4c8eac08-f9e3-39ad-b42c-8958dc9dd41e},
 created = {2019-02-13T12:19:07.543Z},
 file_attached = {false},
 profile_id = {e2d2f261-b93b-3381-802e-ec4f45d345ec},
 last_modified = {2019-02-13T12:19:07.543Z},
 read = {false},
 starred = {false},
 authored = {true},
 confirmed = {false},
 hidden = {false},
 private_publication = {false},
 abstract = {© 2015 Elsevier B.V. Post-combustion carbon dioxide (CO2) capture using aqueous monoethanolamine (MEA) has been the most widely implicated method utilizing existing coal-fired power plants. However, the heat and energy requirement of the solvent regeneration and CO2 liquefaction results in a 30% decrease in net power output, which is called "power de-rate". In this study, optimum operating conditions of the integrated CCS process are proposed by simulation-based parametric optimization to reduce the power de-rate. Post-combustion CO2 capture with aqueous MEA and CO2 liquefaction integrated with a 550MWe supercritical coal-fired power plant was simulated base on the data of a 0.1MW pilot plant in South Korea. The stripper operating pressure and liquid to gas ratio were chosen as the manipulated variables based on the variable evaluation. The power de-rate was reduced to 17.4% when operating at optimum conditions.},
 bibtype = {book},
 author = {An, J. and Lee, U. and Jung, J. and Han, C.},
 doi = {10.1016/B978-0-444-63578-5.50086-4}
}

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Post-combustion carbon dioxide (CO2) capture using aqueous monoethanolamine (MEA) has been the most widely implicated method utilizing existing coal-fired power plants. However, the heat and energy requirement of the solvent regeneration and CO2 liquefaction results in a 30% decrease in net power output, which is called \"power de-rate\". In this study, optimum operating conditions of the integrated CCS process are proposed by simulation-based parametric optimization to reduce the power de-rate. Post-combustion CO2 capture with aqueous MEA and CO2 liquefaction integrated with a 550MWe supercritical coal-fired power plant was simulated base on the data of a 0.1MW pilot plant in South Korea. The stripper operating pressure and liquid to gas ratio were chosen as the manipulated variables based on the variable evaluation. 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