@article{
 title = {A semi-analytical method for determining the optimal stripper pressure in CO<inf>2</inf> capture and liquefaction using monoethanolamine (MEA)},
 type = {article},
 year = {2016},
 keywords = {CCS,MEA,Optimal stripper pressure,Optimization,Process design,Process integration},
 volume = {46},
 id = {01acef31-ac20-30cc-b868-7921ef1a783c},
 created = {2019-02-13T12:19:07.939Z},
 file_attached = {false},
 profile_id = {e2d2f261-b93b-3381-802e-ec4f45d345ec},
 last_modified = {2019-02-13T12:19:07.939Z},
 read = {false},
 starred = {false},
 authored = {true},
 confirmed = {false},
 hidden = {false},
 private_publication = {false},
 abstract = {© 2016 Elsevier Ltd. The operation pressure of a distillation column is one of the key variables in optimizing the required energy in a carbon capture and storage (CCS) chain. It affects the steam drag point in power plants, the regeneration energy in capture process and the compression energy in the liquefaction process. A new semi-analytical method for determining optimal stripper pressure for the CCS process using MEA as an absorbent is proposed based on the integrated simulation model. Total required energy is represented as a function of the pressure based on the equivalent work. Two different method - simultaneous and sequential - are applied to solve the optimization problem. The results show that the total energy has a monotonous decreasing function with respect to the stripper pressure and the higher stripper pressure is favorable when a terminal pressure is above 10 bar. When the terminal pressure has a small value near 5 bar, the total energy shows a convex form and the optimal stripper pressure is located between 1 and 2.2 bar.},
 bibtype = {article},
 author = {Park, T. and Lee, S.G. and Kim, S.H. and Lee, U. and Han, C. and Lee, J.M.},
 doi = {10.1016/j.ijggc.2016.01.019},
 journal = {International Journal of Greenhouse Gas Control}
}

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The operation pressure of a distillation column is one of the key variables in optimizing the required energy in a carbon capture and storage (CCS) chain. It affects the steam drag point in power plants, the regeneration energy in capture process and the compression energy in the liquefaction process. A new semi-analytical method for determining optimal stripper pressure for the CCS process using MEA as an absorbent is proposed based on the integrated simulation model. Total required energy is represented as a function of the pressure based on the equivalent work. Two different method - simultaneous and sequential - are applied to solve the optimization problem. The results show that the total energy has a monotonous decreasing function with respect to the stripper pressure and the higher stripper pressure is favorable when a terminal pressure is above 10 bar. When the terminal pressure has a small value near 5 bar, the total energy shows a convex form and the optimal stripper pressure is located between 1 and 2.2 bar.","bibtype":"article","author":"Park, T. and Lee, S.G. and Kim, S.H. and Lee, U. and Han, C. and Lee, J.M.","doi":"10.1016/j.ijggc.2016.01.019","journal":"International Journal of Greenhouse Gas Control","bibtex":"@article{\n title = {A semi-analytical method for determining the optimal stripper pressure in CO<inf>2</inf> capture and liquefaction using monoethanolamine (MEA)},\n type = {article},\n year = {2016},\n keywords = {CCS,MEA,Optimal stripper pressure,Optimization,Process design,Process integration},\n volume = {46},\n id = {01acef31-ac20-30cc-b868-7921ef1a783c},\n created = {2019-02-13T12:19:07.939Z},\n file_attached = {false},\n profile_id = {e2d2f261-b93b-3381-802e-ec4f45d345ec},\n last_modified = {2019-02-13T12:19:07.939Z},\n read = {false},\n starred = {false},\n authored = {true},\n confirmed = {false},\n hidden = {false},\n private_publication = {false},\n abstract = {© 2016 Elsevier Ltd. The operation pressure of a distillation column is one of the key variables in optimizing the required energy in a carbon capture and storage (CCS) chain. It affects the steam drag point in power plants, the regeneration energy in capture process and the compression energy in the liquefaction process. A new semi-analytical method for determining optimal stripper pressure for the CCS process using MEA as an absorbent is proposed based on the integrated simulation model. Total required energy is represented as a function of the pressure based on the equivalent work. Two different method - simultaneous and sequential - are applied to solve the optimization problem. The results show that the total energy has a monotonous decreasing function with respect to the stripper pressure and the higher stripper pressure is favorable when a terminal pressure is above 10 bar. When the terminal pressure has a small value near 5 bar, the total energy shows a convex form and the optimal stripper pressure is located between 1 and 2.2 bar.},\n bibtype = {article},\n author = {Park, T. and Lee, S.G. and Kim, S.H. and Lee, U. and Han, C. and Lee, J.M.},\n doi = {10.1016/j.ijggc.2016.01.019},\n journal = {International Journal of Greenhouse Gas Control}\n}","author_short":["Park, T.","Lee, S.","Kim, S.","Lee, U.","Han, C.","Lee, J."],"biburl":"https://bibbase.org/service/mendeley/e2d2f261-b93b-3381-802e-ec4f45d345ec","bibbaseid":"park-lee-kim-lee-han-lee-asemianalyticalmethodfordeterminingtheoptimalstripperpressureincoinf2infcaptureandliquefactionusingmonoethanolaminemea-2016","role":"author","urls":{},"keyword":["CCS","MEA","Optimal stripper pressure","Optimization","Process design","Process integration"],"metadata":{"authorlinks":{"lee, u":"https://bibbase.org/service/mendeley/e2d2f261-b93b-3381-802e-ec4f45d345ec"}},"downloads":0},"search_terms":["semi","analytical","method","determining","optimal","stripper","pressure","inf","inf","capture","liquefaction","using","monoethanolamine","mea","park","lee","kim","lee","han","lee"],"keywords":["ccs","mea","optimal stripper pressure","optimization","process design","process integration"],"authorIDs":["53Eu6D3PGMBxXrRti","5c9c263cdec2ee1000000059","5uJTfYkz8g7sk4JGG","6LPbpLbgj2WL9rTzb","AFsKowzSGCYXtGgnA","F4ihjugSzaCtFvgvq","F7oWt4p9yWJajZxgS","KPt2RkeANfpK5kHe7","MKLATA3QnWw9tFT4P","P5P9YzrQ4afhAENuh","T3LhxYRHS6uSW3MGr","WCrkCJcD3nYDojs5Q","XSMne33P8tn6zKHwM","YFy9eDRKiXTNAZztq","nxqNTEDeDzQdthSrH","pkLWRR8R3EpxYie5W","qMYFbvSwNNx7dzdta","rPjAGc5MiJuKRrR2w","usCJjqr7DyEHWYEmm","y8HTa5oEmRuqgHAe9"],"dataSources":["Mtx83Ei99HeufLMJ3","ya2CyA73rpZseyrZ8"]}