Improved utilization of biomass-derived carbon by co-processing with hydrogen-rich feedstocks in millisecond reactors

Joshua L. Colby; Paul J Dauenhauer; Brian C. Michael; Aditya Bhan; Lanny D. Schmidt

doi:10.1039/b920387g

Improved utilization of biomass-derived carbon by co-processing with hydrogen-rich feedstocks in millisecond reactors

Joshua L. Colby, Paul J Dauenhauer, Brian C. Michael, Aditya Bhan, Lanny D. Schmidt

Chemical Engineering and Materials Science

Research output: Contribution to journal › Article › peer-review

14 Scopus citations

Abstract

A reactor capable of improving the utilization of biomass-derived carbon during thermochemical conversion to synthesis gas is demonstrated experimentally. By co-processing hydrogen-deficient biomass (H/C∼2) with hydrogen-rich feedstocks (H/C≥4) through catalytic partial oxidation, 100% of the fuel carbon atoms fed to the reactor can be converted to CO.

Original language	English (US)
Pages (from-to)	378-380
Number of pages	3
Journal	Green Chemistry
Volume	12
Issue number	3
DOIs	https://doi.org/10.1039/b920387g
State	Published - Mar 19 2010

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10.1039/b920387g

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abstract = "A reactor capable of improving the utilization of biomass-derived carbon during thermochemical conversion to synthesis gas is demonstrated experimentally. By co-processing hydrogen-deficient biomass (H/C∼2) with hydrogen-rich feedstocks (H/C≥4) through catalytic partial oxidation, 100% of the fuel carbon atoms fed to the reactor can be converted to CO.",

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AU - Dauenhauer, Paul J

AU - Michael, Brian C.

AU - Bhan, Aditya

AU - Schmidt, Lanny D.

PY - 2010/3/19

Y1 - 2010/3/19

N2 - A reactor capable of improving the utilization of biomass-derived carbon during thermochemical conversion to synthesis gas is demonstrated experimentally. By co-processing hydrogen-deficient biomass (H/C∼2) with hydrogen-rich feedstocks (H/C≥4) through catalytic partial oxidation, 100% of the fuel carbon atoms fed to the reactor can be converted to CO.

AB - A reactor capable of improving the utilization of biomass-derived carbon during thermochemical conversion to synthesis gas is demonstrated experimentally. By co-processing hydrogen-deficient biomass (H/C∼2) with hydrogen-rich feedstocks (H/C≥4) through catalytic partial oxidation, 100% of the fuel carbon atoms fed to the reactor can be converted to CO.

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Improved utilization of biomass-derived carbon by co-processing with hydrogen-rich feedstocks in millisecond reactors

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