Hydrogen production via catalytic reforming of the bio-oil model compounds: Acetic acid, phenol and hydroxyacetone

2014 ◽  
Vol 39 (32) ◽  
pp. 18675-18687 ◽  
Author(s):  
Shurong Wang ◽  
Qinjie Cai ◽  
Fan Zhang ◽  
Xinbao Li ◽  
Li Zhang ◽  
...  
Keyword(s):  
Acetic Acid ◽  
Hydrogen Production ◽  
Model Compounds ◽  
Catalytic Reforming ◽  
Bio Oil

Catalytic reforming of acetic acid as a model compound of bio-oil for hydrogen production over Ni-CeO2-MgO/olivine catalysts

2014 ◽  
Vol 34 (3) ◽  
pp. 915-922 ◽  
Author(s):  
Xingmin Xu ◽  
Changsen Zhang ◽  
Yonggang Liu ◽  
Yunpu Zhai ◽  
Ruiqin Zhang ◽  
...  
Keyword(s):  
Acetic Acid ◽  
Hydrogen Production ◽  
Model Compound ◽  
Catalytic Reforming ◽  
Bio Oil

Effect of mixing bio-oil aqueous phase model compounds on hydrogen production in non-catalytic supercritical reforming

2017 ◽  
Vol 2 (5) ◽  
pp. 679-687 ◽  
Author(s):  
F. J. Gutiérrez Ortiz ◽  
F. J. Campanario ◽  
P. Ollero
Keyword(s):  
Hydrogen Production ◽  
Aqueous Phase ◽  
Mixing Model ◽  
Phase Model ◽  
Hydrogen Yield ◽  
Model Compounds ◽  
Supercritical Conditions ◽  
Bio Oil

The effect of mixing model compounds on the hydrogen yield under supercritical conditions is studied by proposed potential pathways.

Hydrogen Production via Sorption Enhanced Steam Reforming of Acetic Acid: A Thermodynamic Study

2013 ◽  
Vol 724-725 ◽  
pp. 769-772 ◽  
Author(s):  
Peng Fu ◽  
Wei Ming Yi ◽  
Zhi He Li ◽  
Xue Yuan Bai
Keyword(s):  
Acetic Acid ◽  
Hydrogen Production ◽  
Steam Reforming ◽  
Model Compound ◽  
Molar Ratio ◽  
Basic Requirement ◽  
Reaction Thermodynamics ◽  
Bio Oil ◽  
Favorable Temperature ◽  
Thermodynamics Of Sorption

The reaction thermodynamics of sorption enhanced steam reforming (SESR) of acetic acid as a model compound of bio-oil for hydrogen production were investigated and contrasted with acetic acid steam reforming (SR). The most favorable temperature for SR is approximately 650 °C. However, the optimum temperature for SESR is around 550 °C, which is about 100 °C lower than that for SR. The highest hydrogen concentration from SR is only 67%, which is below the basic requirement of hydrogen purity for fuel cells. In SESR, hydrogen purities are over 99% in 500-550 °C with a calcium oxide to acetic acid molar ratio (CAMR) of 4 and a water to acetic acid molar ratio (WAMR) greater than 6. The results show that hydrogen production from sorption enhanced steam reforming of acetic acid should be a promising direction.

scholarly journals Effect of operating conditions on the sorption enhanced steam reforming of blends of acetic acid and acetone as bio-oil model compounds

2016 ◽  
Vol 177 ◽  
pp. 579-590 ◽  
Author(s):  
G. Esteban-Díez ◽  
María V. Gil ◽  
C. Pevida ◽  
D. Chen ◽  
F. Rubiera
Keyword(s):  
Acetic Acid ◽  
Steam Reforming ◽  
Operating Conditions ◽  
Model Compounds ◽  
Bio Oil

Hydrogen Production From Crude Bio-oil and Biomass Char by Electrochemical Catalytic Reforming

2011 ◽  
Vol 24 (4) ◽  
pp. 477-483 ◽  
Author(s):  
Xing-long Li ◽  
Shen Ning ◽  
Li-xia Yuan ◽  
Quan-xin Li
Keyword(s):  
Hydrogen Production ◽  
Catalytic Reforming ◽  
Bio Oil ◽  
Biomass Char

Hydrogen production from bio-oil model compounds dry (CO2) reforming over Ni/Al2O3 catalyst

2016 ◽  
Vol 41 (3) ◽  
pp. 1494-1501 ◽  
Author(s):  
Ming Fu ◽  
Wei Qi ◽  
Qingli Xu ◽  
Suping Zhang ◽  
Yongjie Yan
Keyword(s):  
Hydrogen Production ◽  
Model Compounds ◽  
Co2 Reforming ◽  
Bio Oil ◽  
Al2o3 Catalyst

Hydrogen production from acetic acid decomposition as bio-oil model molecule over supported metal catalysts

2020 ◽  
Vol 45 (53) ◽  
pp. 28732-28751
Author(s):  
Maria H. Brijaldo ◽  
Alexander E. Caytuero ◽  
José J. Martínez ◽  
Hugo Rojas ◽  
Fabio B. Passos
Keyword(s):  
Acetic Acid ◽  
Hydrogen Production ◽  
Metal Catalysts ◽  
Supported Metal Catalysts ◽  
Acid Decomposition ◽  
Model Molecule ◽  
Bio Oil ◽  
Supported Metal
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