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Transport of Small Molecules in Polymers: Overview of Research Activities. Benny D. Freeman Department of Chemical Engineering University of Texas at Austin, Office: CPE 3.404 and CEER 1.308B Tel.: (512)232-2803, e-mail: freeman@che.utexas.edu
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Transport of Small Molecules in Polymers: Overview of Research Activities Benny D. Freeman Department of Chemical Engineering University of Texas at Austin, Office: CPE 3.404 and CEER 1.308B Tel.: (512)232-2803, e-mail: freeman@che.utexas.edu http://www.che.utexas.edu/graduate_research/freeman.htm http://membrane.ces.utexas.edu 1
Freeman Research Group Focus Develop fundamental structure/function rules to guide the preparation of high performance polymers or polymer-based materials for gas and liquid separations as well as barrier packaging applications.
Freeman Research Group Profile • 15 Ph.D. students: • Gas Separations: Qiang Liu, Kevin Stevens, Grant Offord, Tom Murphy, Katrina Czenkusch, David Sanders, Zach Smith* • Liquid Separations: Wei Xie, Dan Miller*, Joe Cook, Geoff Geise, Michelle Oh, Albert Lee, Peach Kasemset* • Barrier Materials: Kevin Tung • 2 Postdocs: Dr. Claudio Ribeiro*, Dr. Chaoyi Ba • Sponsors: • NSF - 5 projects • DOE – 2 projects • Office of Naval Research - 1 project • Industrial sponsors: PSTC, Air Liquide, Kuraray, Kraton Polymers, ConocoPhillips, Statkraft, Dow Water Solutions * = group members who have won major fellowships to support their work from either the US govt. (NSF, DOE) or their home govt.
Current Projects - 1 • Gas Separations • Thermally-Rearranged Polymers for Gas Separation • CO2/CH4 Separation for Natural Gas Purification • Physical Aging in Glassy Polymers • Physical Aging in Microlayered Polymers • CO2/O2 Separation for Food Packaging Applications • Melt Processing Strategies to Prepare Thin Membranes for Gas Separations • Bioethanol Purification (Ethanol/Water Separation)
Current Projects - 2 • Liquid Separations • Chlorine-Tolerant Desalination Membranes • Desalination Membranes Based on Novel Block Copolymers • Fundamental Studies of Ion and Water Transport in Polymers • Melt Processing Strategies to Prepare Desalination Membranes • Bio-inspired Surface Modification of Water Purification Membranes to Improve Fouling Resistance
Current Projects - 3 • Others • Fundamental Studies of Oxygen Scavenging Polymers for High Oxygen Barrier Packaging • Hydrocarbon/Hydrocarbon Pervaporation for Refinery Separations
Fouling: A Major Limitation in Liquid Filtration Membranes Feed flow External fouling 2000x decrease Internal fouling Membrane
Mimicking Mussel Adhesion (“Bio-Glue”) H. Lee, S.M. Dellatore, W.M. Miller, and P.B. Messersmith., Mussel-Inspired Surface Chemistry for Multifunctional Coatings. Science, 318, 426-430 (2007).
Polydopamine: Novel Fouling Resistant Membrane Coating Polydopamine
Polydopamine as Surface “Primer” to Graft PEG to Membrane Surfaces Proposed Polydopamine Structure: PEG ad-layer Michael Addition/ Schiff Base Reaction Polydopamine
Oily Water Filtration Using Pegylated Polydopamine Treated Teflon Microfiltration Membranes Modification: 60 min PDOPA deposition time followed by 60 min 5KDa PEG-NH2 (1mg/mL, 60 °C) Conditions: DP=0.3 atm, crossflow=120 L/h (Re=2500)1500 ppm soybean oil/DC193-water emulsion (non-ionic)
Field Validation - Visual • Two identical UF PAN membranes that are highly hydrophilic • One coated and one non-coated, both processed high fouling water stream from a bio-reactor with a lot of sludge. • 10 minute filtration followed by 1 min backwash cycle for 48+ hours. • Both membranes were taken out and flushed with a hose / water • Modified membrane washes clean • Non-modified retains sludge film • Membrane housings (hydrophobic) also showed significantly better anti-stick, fouling resistant surface
Field Validataion: Ultrafiltration of Bioreactor Effluent Unmodified Modified 2X More Water Processed Between Cleanings 40% Lower Energy • Pressure increases during single filtration/back-flush cycle due to fouling • Almost twice the volume of water could be processed for same end-point pressures • Unmodified shows pressure increase at a rate of 1.55 psi/hr vs. 1.1 psi/hr for modified membrane
Natural Gas Processing • 100 trillion scf of natural gas used worldwide per year • All requires pretreatment • Amine absorption is the leading technology • Membranes have < 5% market share R.W. Baker, K. Lokhandwala, Natural gas processing with membranes: An overview, Industrial & Engineering Chemistry Research. 47 (2008) 2109-2121.
CO2/CH4 Separation Performance 1: PIOFG-1 2: TR-1-350 3: TR-1-400 4: TR-1-450 5-19: OTHER TR POLYMERS H.B. Park, C.H. Jung, Y.M. Lee, A.J. Hill, S.J. Pas, S.T. Mudie, E. van Wagner, B.D. Freeman, & D.J. Cookson, Polymers with Cavities Tuned for Fast, Selective Transport of Small Molecules and Ions, Science, 318, 254-258 (2007).
Cavity Size Distribution from Positron Annihilation Lifetime Spectroscopy (a) PIOFG-1 (b) TR-1-350 (c) TR-1-400 (d) TR-1-450
Beating the Permeability-Selectivity Tradeoff for H2 Purification Lin et al., Science, 311, pp. 639-642 (2006).