Production of synthesis gas by partial oxidation and steam reforming of biomass pyrolysis oils

被引:75
|
作者
Rennard, David [1 ]
French, Rick [2 ]
Czernik, Stefan [2 ]
Josephson, Tyler [1 ]
Schmidt, Lanny [1 ]
机构
[1] Univ Minnesota, Dept Chem Engn & Mat Sci, Minneapolis, MN 55455 USA
[2] Natl Renewable Energy Lab, Golden, CO 80401 USA
关键词
Pyrolysis oil; Bio-oil; Syngas; Catalytic partial oxidation; Steam reforming; Rhodium; CATALYTIC PARTIAL OXIDATION; NOBLE-METAL CATALYSTS; BIO-OIL; HYDROGEN-PRODUCTION; AQUEOUS-PHASE; SEQUENTIAL CRACKING; MODEL COMPOUNDS; BED REACTOR; FUEL; FRACTION;
D O I
10.1016/j.ijhydene.2010.01.143
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
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. H(2) and CO can be produced autothermally over Rh-Cc catalysts with millisecond contact times. Co-processing of bio-oil with methane or methanol improved the reactor operation stability. (C) 2010 Professor T. Nejat Veziroglu. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:4048 / 4059
页数:12
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