Modeling and simulation of gas separations with spiral‐wound membranes. Issue 8 (7th June 2020)

• Record Type: Journal Article
• Authors: DeJaco, Robert F.; Loprete, Kenneth; Pennisi, Kenneth; Majumdar, Sudip; Siepmann, J. Ilja; Daoutidis, Prodromos; Murnen, Hannah; Tsapatsis, Michael
• Is Part Of: AIChE journal. Volume 66:Issue 8(2020)
• Page Start: n/a
• Page End: n/a
• Publication Date: 2020-06-07
• Subjects: Membrane separations -- computational fluid dynamics (CFD) -- design (process simulation) -- gas purification -- mathematical modeling; Chemical engineering -- Periodicals; Génie chimique -- Périodiques; 660.28
• DOI: 10.1002/aic.16274
• Languages: English
• ISSNs: 0001-1541

Abstract

Abstract: Models for gas separations with spiral‐wound membranes are developed and found to exhibit good agreement with experiments performed on N2 /O2 mixtures. The two‐dimensional (2D) model can be accurately approximated by a one‐dimensional (1D) surrogate model when the spacer widths are chosen to make the channel pressure drops small. Subsequently, the separation of propane/propylene mixtures from the recycle purge stream of a polypropylene reactor is investigated. Assuming ideal gas is found to lead to significant overestimations in membrane stage cuts (sometimes more than 10%), an extent comparable to that associated with extrapolating constant olefin permeance from a low‐pressure condition. While olefin permeance can change significantly with pressure, using a constant‐permeance formulation can result in a small (< 2.5%) underprediction in stage cut if the value for the permeance is taken from the feed condition. Finally, membrane properties and costs necessary for a viable separation process are discussed.