Moving bed temperature swing adsorption for CO2 capture from a natural gas combined cycle power plant

Giorgia Mondino; Carlos A. Grande; Richard Blom; Lars O. Nord

Moving bed temperature swing adsorption for CO₂ capture from a natural gas combined cycle power plant

Giorgia Mondino^*, Carlos A. Grande, Richard Blom, Lars O. Nord

^*Corresponding author for this work

Chemical Engineering

Research output: Contribution to conference › Paper › peer-review

Abstract

The present work considers the employment of a Moving Bed Temperature Swing Adsorption process for CO2 capture as alternative to the most commercial absorption-based technologies, in the context of Natural Gas Combined Cycle power plants. A detailed mathematical model consisting of heat, mass and momentum balance was implemented in gPROMS software, in order to investigate the system behavior under different operating conditions and design parameters. Results show that under the simulated process conditions, the system is suitable for capturing CO2 at high purity and high capture rate. Promising results are obtained also in terms of process energy duty, by performing a preliminary analysis that takes into account the heat required for sorbent regeneration.

Original language	English (US)
State	Published - 2018
Event	14th International Conference on Greenhouse Gas Control Technologies, GHGT 2018 - Melbourne, Australia Duration: Oct 21 2018 → Oct 25 2018

Conference

Conference	14th International Conference on Greenhouse Gas Control Technologies, GHGT 2018
Country/Territory	Australia
City	Melbourne
Period	10/21/18 → 10/25/18

Keywords

CCS
NGCC
post-combustion
Zeolite 13X

ASJC Scopus subject areas

Industrial and Manufacturing Engineering
Management, Monitoring, Policy and Law
Pollution
General Energy

Cite this

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title = "Moving bed temperature swing adsorption for CO2 capture from a natural gas combined cycle power plant",

abstract = "The present work considers the employment of a Moving Bed Temperature Swing Adsorption process for CO2 capture as alternative to the most commercial absorption-based technologies, in the context of Natural Gas Combined Cycle power plants. A detailed mathematical model consisting of heat, mass and momentum balance was implemented in gPROMS software, in order to investigate the system behavior under different operating conditions and design parameters. Results show that under the simulated process conditions, the system is suitable for capturing CO2 at high purity and high capture rate. Promising results are obtained also in terms of process energy duty, by performing a preliminary analysis that takes into account the heat required for sorbent regeneration.",

keywords = "CCS, NGCC, post-combustion, Zeolite 13X",

author = "Giorgia Mondino and Grande, {Carlos A.} and Richard Blom and Nord, {Lars O.}",

note = "Publisher Copyright: {\textcopyright} 2018 GHGT 2018 - 14th International Conference on Greenhouse Gas Control Technologies. All rights reserved.; 14th International Conference on Greenhouse Gas Control Technologies, GHGT 2018 ; Conference date: 21-10-2018 Through 25-10-2018",

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TY - CONF

T1 - Moving bed temperature swing adsorption for CO2 capture from a natural gas combined cycle power plant

AU - Mondino, Giorgia

AU - Grande, Carlos A.

AU - Blom, Richard

AU - Nord, Lars O.

PY - 2018

Y1 - 2018

N2 - The present work considers the employment of a Moving Bed Temperature Swing Adsorption process for CO2 capture as alternative to the most commercial absorption-based technologies, in the context of Natural Gas Combined Cycle power plants. A detailed mathematical model consisting of heat, mass and momentum balance was implemented in gPROMS software, in order to investigate the system behavior under different operating conditions and design parameters. Results show that under the simulated process conditions, the system is suitable for capturing CO2 at high purity and high capture rate. Promising results are obtained also in terms of process energy duty, by performing a preliminary analysis that takes into account the heat required for sorbent regeneration.

AB - The present work considers the employment of a Moving Bed Temperature Swing Adsorption process for CO2 capture as alternative to the most commercial absorption-based technologies, in the context of Natural Gas Combined Cycle power plants. A detailed mathematical model consisting of heat, mass and momentum balance was implemented in gPROMS software, in order to investigate the system behavior under different operating conditions and design parameters. Results show that under the simulated process conditions, the system is suitable for capturing CO2 at high purity and high capture rate. Promising results are obtained also in terms of process energy duty, by performing a preliminary analysis that takes into account the heat required for sorbent regeneration.

KW - CCS

KW - NGCC

KW - post-combustion

KW - Zeolite 13X

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AN - SCOPUS:85181585473

T2 - 14th International Conference on Greenhouse Gas Control Technologies, GHGT 2018

Y2 - 21 October 2018 through 25 October 2018

ER -