AbstractPost combustion CO2 capture via absorption into aqueous alkanolamine systems is considered to be the most mature and potential technique for CO2 removal from the power plants’ exhaust gases. Modeling and simulation of such plants have achieved an interesting place in research, and several steady state models already exist. Though steady state models are capable of giving an understanding of the process, dynamic models are most useful for controlling and optimizing the plants. A dynamic model for the absorption column in a CO2 removal plant is been developed. Usability of simple thermodynamics for modeling is checked with the development of this model, instead of using complex thermodynamic models which are very popular in recent res...
MEA (monoethanolamine) process is the most extended chemical absorption solvent for CO2 capture in p...
Post-combustion capture by chemical absorption using MEA solvent remains the only commercial techno...
AbstractA rigorous rate-based model for the aqueous ammonia (NH3) based CO2 absorption in a packed c...
AbstractPost combustion CO2 capture via absorption into aqueous alkanolamine systems is considered t...
Power generation from fossil fuel-fired power plants is the largest single source of CO 2 emissions....
Use of complex rate-based models for absorbers in a post-combustion CO2 capture process may lead to ...
This paper discusses the limitations and prospects of using equilibrium-based column models for the ...
AbstractWith an increasing demand on load flexibility in power supply networks, advanced control sys...
Power generation from fossil fuel-fired power plants is the largest single source of CO2 emissions. ...
Recently global warming has become a topic of great interest, involving social, economic and industr...
In this article, pilot plant data for CO2 post-combustion capture are discussed and compared with mo...
Mathematical modelling of CO2 capture from industrial flue gas by absorption into amine solutions su...
CO2 emissions are recognized as a large contributing factor to global warming and climate change. Po...
AbstractA dynamic rate-based amine absorption process model has been developed to predict the dynami...
This paper focuses on modeling and simulation of a post-combustion carbon dioxide capture in a coal-...
MEA (monoethanolamine) process is the most extended chemical absorption solvent for CO2 capture in p...
Post-combustion capture by chemical absorption using MEA solvent remains the only commercial techno...
AbstractA rigorous rate-based model for the aqueous ammonia (NH3) based CO2 absorption in a packed c...
AbstractPost combustion CO2 capture via absorption into aqueous alkanolamine systems is considered t...
Power generation from fossil fuel-fired power plants is the largest single source of CO 2 emissions....
Use of complex rate-based models for absorbers in a post-combustion CO2 capture process may lead to ...
This paper discusses the limitations and prospects of using equilibrium-based column models for the ...
AbstractWith an increasing demand on load flexibility in power supply networks, advanced control sys...
Power generation from fossil fuel-fired power plants is the largest single source of CO2 emissions. ...
Recently global warming has become a topic of great interest, involving social, economic and industr...
In this article, pilot plant data for CO2 post-combustion capture are discussed and compared with mo...
Mathematical modelling of CO2 capture from industrial flue gas by absorption into amine solutions su...
CO2 emissions are recognized as a large contributing factor to global warming and climate change. Po...
AbstractA dynamic rate-based amine absorption process model has been developed to predict the dynami...
This paper focuses on modeling and simulation of a post-combustion carbon dioxide capture in a coal-...
MEA (monoethanolamine) process is the most extended chemical absorption solvent for CO2 capture in p...
Post-combustion capture by chemical absorption using MEA solvent remains the only commercial techno...
AbstractA rigorous rate-based model for the aqueous ammonia (NH3) based CO2 absorption in a packed c...