@article{
 title = {Production of synthesis gas by partial oxidation and steam reforming of biomass pyrolysis oils},
 type = {article},
 year = {2010},
 identifiers = {[object Object]},
 keywords = {Bio-oil,Catalytic partial oxidation,Pyrolysis oil,Rhodium,Steam reforming,Syngas},
 pages = {4048-4059},
 volume = {35},
 websites = {http://doi.org/10.1016/j.ijhydene.2010.01.143},
 id = {a5452c0a-5d00-3c53-81b6-b7140430e500},
 created = {2015-05-27T20:16:20.000Z},
 file_attached = {false},
 profile_id = {2ec95624-dda0-36b1-af4c-dcf557e1476e},
 last_modified = {2018-09-08T03:21:22.041Z},
 read = {false},
 starred = {false},
 authored = {true},
 confirmed = {true},
 hidden = {false},
 citation_key = {Rennard2010},
 private_publication = {false},
 abstract = {As the lowest cost biomass-derived liquids, pyrolysis oils (also called bio-oils) represent a promising vector for biomass to fuels conversion. However, bio-oils require upgrading to interface with existing infrastructure. A potential pathway for producing fuels from pyrolysis oils proceeds through gasification, the conversion to synthesis gas. In this work, the conversion of bio-oils to syngas via catalytic partial oxidation over Rh-Ce is evaluated using two reactor configurations. In one instance, pyrolysis oils are oxidized in excess steam in a freeboard and passed over the catalyst in a second zone. In the second instance, bio-oils are introduced directly to the catalyst. Coke formation is avoided in both configurations due to rapid oxidation. H2 and CO can be produced autothermally over Rh-Ce catalysts with millisecond contact times. Co-processing of bio-oil with methane or methanol improved the reactor operation stability. ?? 2010 Professor T. Nejat Veziroglu.},
 bibtype = {article},
 author = {Rennard, David and French, Rick and Czernik, Stefan and Josephson, Tyler and Schmidt, Lanny},
 journal = {International Journal of Hydrogen Energy},
 number = {9}
}

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