(174c) Kinetics of Cellulose Fragmentation By Pulse-Heated Analysis of Solid Reactions (PHASR)
Pulse-Heated Analysis of Solid Reactions (PHASR)
Saurabh Maduskar, Paul J. Dauenhauer
Department of Chemical Engineering and Materials Science, University of Minnesota, 421 Washington Ave. SE, 484 Amundson Hall, Minneapolis, MN 55455, USA.
Cellulose is a major constituent of biomass and the most abundant biopolymer in the world. During high temperature pyrolysis, it transforms into a liquid intermediate before depolymerizing and volatilizing into condensable bio-oil products for upgrading into fuels and chemicals. The underlying pyrolysis chemistry has been studied for decades, and numerous conflicting mechanisms and kinetics models have been proposed. Lack of the experimental verification of such kinetic models is primarily due to the complexity of the analytical problem. Limitations of conventional analytical systems to measure kinetics of cellulose pyrolysis were identified in terms of five experimental criteria, such as sample length scale, temperature ramp during heating and cooling, sweeping gas flowrate, temperature measurement and control, and product quantification.
To overcome these challenges, Pulse-Heated Analysis of Solid Reactions (PHASR), an experimental microreactor system was developed. The PHASR reactor rapidly heats and cools (~1060C/min) thin film solid samples (10-50 µm thick) at millisecond time scales to control reaction progression, allowing for quantification of vapor, gas, and intermediate products as a function of reaction time.
PHASR reactor system was used to measure millisecond-resolved evolution of cellulose and its volatile fragmentation products over a wide range of temperature (400-525 0C). The results obtained clearly demonstrates the effect of experimental conditions such as sample length scale on product distribution. Energetics of glycosidic bond cleavage was measured by analyzing cyclodextrin, a demonstrated surrogate of cellulose for pyrolysis reactions. Combining the rates of glycosidic bond cleavage with that of product formations, apparent kinetics of product formation was evaluated. The method developed can be used to extract apparent kinetics of product formation from complex biomass samples.
Anhydro-oligosaccharides are known to be present in liquid intermediate during cellulose fragmentation. Using anhydrosugars with varying levoglucosan end group to glucose monomer ratio, it was shown that glucose monomer in anhydrosugars can be used as a surrogate for that of cellulose intermediate to elucidate mechanisms of product formation.
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