Frank Seibert
University of Texas at Austin
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Computer-aided chemical engineering | 2012
Chechet Biliyok; Adekola Lawal; Meihong Wang; Frank Seibert
Abstract Dynamic modelling for post-combustion CO 2 capture using monoethanolamine (MEA) solvent has been validated at steady state in the past. This paper presents a dynamic validation. The absorber and regenerator were modelled using the two-film theory in gPROMS®. Electrolyte NRTL model in Aspen Properties® is used to describe the chemical equilibrium and vapour-liquid equilibrium. The CO 2 capture process was simulated. The temperature profile of the absorber, the capture level and the regenerator duty were compared with pilot plant data logs. It is observed that the model satisfactorily predicts the behaviour of the pilot plant due to a number of process inputs and disturbances, producing trends in close agreement with the data logs.
Greenhouse Gas Control Technologies 7#R##N#Proceedings of the 7th International Conference on Greenhouse Gas Control Technologies 5– September 2004, Vancouver, Canada | 2005
Frank Seibert; Ian Wilson; Christopher Lewis; Gary T. Rochelle
Publisher Summary A typical application of low-pressure absorption using packing columns is carbon dioxide (CO2) capture. CO2 absorption by aqueous solutions occurs by mass transfer with chemical reaction in the liquid boundary layer. In carbon dioxide absorption, the rate of mass transfer primarily depends on the gas/liquid contact area, not on mass transfer rates within the phases. This chapter presents a study that aims to describe a method for measuring directly the interfacial area using a well-known chemical absorption system, air/ CO2/caustic. In this study, an experimental technique has been developed that allows direct measurement of the contact area for gas/liquid contacting. To minimize the effect of gas phase mass transfer resistance and associated errors in the measured contact areas, a dilute caustic (0.1 N NaOH) solution is utilized. Effective gas/liquid contact areas for a variety of commercially significant random and structured packings, obtained from a 42-cm diameter scrubber, have been provided. The effects of liquid and gas rates and their influence on liquid spreading and rivulet formation have also been discussed.
International Journal of Greenhouse Gas Control | 2012
Chechet Biliyok; Adekola Lawal; Meihong Wang; Frank Seibert
Energy Procedia | 2011
Frank Seibert; Eric Chen; Micah Perry; S. Briggs; R. Montgomery; Gary T. Rochelle
Energy Procedia | 2013
Chao Wang; Micah Perry; Frank Seibert; Gary T. Rochelle
Energy Procedia | 2014
Chao Wang; Micah Perry; Frank Seibert; Gary T. Rochelle
Archive | 2014
Frank Seibert; Stephen William Briggs; Stacy S. Truscott; Peter B. Kipp
Industrial & Engineering Chemistry Research | 2016
Chao Wang; Di Song; Frank Seibert; Gary T. Rochelle
CO2 Capture 2013 - Topical Conference at the 2013 AIChE Annual Meeting: Global Challenges for Engineering a Sustainable Future | 2013
Chao Wang; Micah Perry; Frank Seibert; Gary T. Rochelle
2013 AIChE Spring Meeting and 9th Global Congress on Process Safety, AIChE 2013 | 2013
Chao Wang; Micah Perry; Gary T. Rochelle; Frank Seibert