Solvent Recovery System for a CO2-MEA Reactive Absorption-Stripping Plant

Claudio Madeddu, Massimiliano Errico*, Davide Porcu, Roberto Baratti

*Kontaktforfatter for dette arbejde

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Resumé

The solvent recovery section from the exhaust gas represents an important auxiliary part for an industrial CO2 post-combustion capture plant by the reactive absorption-stripping process. In this work, a partial condenser and a water-wash section configuration were designed to reach 1 ppm of solvent in the exhaust gas, and compared using the Total Annual Cost (TAC) as economic index. Both the configurations ensured the required recovery performance. The results highlighted that the partial condenser alternative is more convenient in terms of capital annualized costs and water make-up, but at the same time it is strongly penalized by the high operating costs for the cooling water. Therefore, the configuration in which the absorber is equipped with the water-wash section resulted the option with the minimum TAC.
OriginalsprogEngelsk
BogserieChemical engineering transactions
Vol/bind74
Sider (fra-til)805-810
ISSN1974-9791
DOI
StatusUdgivet - 2019
Begivenhed14th International Conference on Chemical and Process Engineering - RoyalCarlton Hotel, Via Montebello 8, Bologna, Italien
Varighed: 26. maj 201929. maj 2019
Konferencens nummer: 14
http://www.aidic.it/icheap14/

Konference

Konference14th International Conference on Chemical and Process Engineering
Nummer14
LokationRoyalCarlton Hotel, Via Montebello 8
LandItalien
ByBologna
Periode26/05/201929/05/2019
Internetadresse

Fingeraftryk

Exhaust gases
Recovery
Water
Costs
Cooling water
Operating costs
Economics

Citer dette

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title = "Solvent Recovery System for a CO2-MEA Reactive Absorption-Stripping Plant",
abstract = "The solvent recovery section from the exhaust gas represents an important auxiliary part for an industrial CO2 post-combustion capture plant by the reactive absorption-stripping process. In this work, a partial condenser and a water-wash section configuration were designed to reach 1 ppm of solvent in the exhaust gas, and compared using the Total Annual Cost (TAC) as economic index. Both the configurations ensured the required recovery performance. The results highlighted that the partial condenser alternative is more convenient in terms of capital annualized costs and water make-up, but at the same time it is strongly penalized by the high operating costs for the cooling water. Therefore, the configuration in which the absorber is equipped with the water-wash section resulted the option with the minimum TAC.",
author = "Claudio Madeddu and Massimiliano Errico and Davide Porcu and Roberto Baratti",
year = "2019",
doi = "10.3303/CET1974135",
language = "English",
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pages = "805--810",
journal = "Chemical engineering transactions",
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}

Solvent Recovery System for a CO2-MEA Reactive Absorption-Stripping Plant. / Madeddu, Claudio; Errico, Massimiliano; Porcu, Davide; Baratti, Roberto.

I: Chemical engineering transactions, Bind 74, 2019, s. 805-810.

Publikation: Bidrag til tidsskriftKonferenceartikelForskningpeer review

TY - GEN

T1 - Solvent Recovery System for a CO2-MEA Reactive Absorption-Stripping Plant

AU - Madeddu, Claudio

AU - Errico, Massimiliano

AU - Porcu, Davide

AU - Baratti, Roberto

PY - 2019

Y1 - 2019

N2 - The solvent recovery section from the exhaust gas represents an important auxiliary part for an industrial CO2 post-combustion capture plant by the reactive absorption-stripping process. In this work, a partial condenser and a water-wash section configuration were designed to reach 1 ppm of solvent in the exhaust gas, and compared using the Total Annual Cost (TAC) as economic index. Both the configurations ensured the required recovery performance. The results highlighted that the partial condenser alternative is more convenient in terms of capital annualized costs and water make-up, but at the same time it is strongly penalized by the high operating costs for the cooling water. Therefore, the configuration in which the absorber is equipped with the water-wash section resulted the option with the minimum TAC.

AB - The solvent recovery section from the exhaust gas represents an important auxiliary part for an industrial CO2 post-combustion capture plant by the reactive absorption-stripping process. In this work, a partial condenser and a water-wash section configuration were designed to reach 1 ppm of solvent in the exhaust gas, and compared using the Total Annual Cost (TAC) as economic index. Both the configurations ensured the required recovery performance. The results highlighted that the partial condenser alternative is more convenient in terms of capital annualized costs and water make-up, but at the same time it is strongly penalized by the high operating costs for the cooling water. Therefore, the configuration in which the absorber is equipped with the water-wash section resulted the option with the minimum TAC.

U2 - 10.3303/CET1974135

DO - 10.3303/CET1974135

M3 - Conference article

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