Hydrogen‐rich syngas production from chemical looping steam reforming of bio‐oil model compound: Effect of bimetal on LaNi 0.8 M 0.2 O 3 (M = Fe, Co, Cu, and Mn)

2019 ◽  
Vol 43 (9) ◽  
pp. 4534-4545 ◽  
Author(s):  
Chen long Liu ◽  
Dong Chen ◽  
Wenju Wang
Keyword(s):  
Steam Reforming ◽  
Model Compound ◽  
Chemical Looping ◽  
Syngas Production ◽  
Bio Oil ◽  
Compound Effect

Synthesis gas production from bio-oil: steam reforming of ethanol as a model compound

RSC Advances ◽  
2014 ◽  
Vol 4 (72) ◽  
pp. 37964-37972 ◽  
Author(s):  
S. Pavlova ◽  
P. Yaseneva ◽  
V. Sadykov ◽  
V. Rogov ◽  
S. Tikhov ◽  
...  
Keyword(s):  
Synthesis Gas ◽  
Steam Reforming ◽  
Model Compound ◽  
Gas Production ◽  
Ethanol Steam Reforming ◽  
Syngas Production ◽  
Monolithic Catalysts ◽  
Steam Reforming Of Ethanol ◽  
Bio Oil ◽  
Ethanol Steam

Syngas production via ethanol steam reforming has been studied over solid Ru/Ce0.5Zr0.5O2 and alumina supported Ru/Ce0.4Zr0.4Sm0.2O2 as granulated and monolithic catalysts.

Chemical looping steam reforming of bio-oil for hydrogen-rich syngas production: Effect of doping on LaNi0.8Fe0.2O3 perovskite

2020 ◽  
Vol 45 (41) ◽  
pp. 21123-21137 ◽  
Author(s):  
Chenlong Liu ◽  
Dong Chen ◽  
Jangam Ashok ◽  
Plaifa Hongmanorom ◽  
Wenju Wang ◽  
...  
Keyword(s):  
Steam Reforming ◽  
Chemical Looping ◽  
Syngas Production ◽  
Production Effect ◽  
Bio Oil ◽  
Effect Of Doping

Sorbent assisted catalyst of Ni-CaO-La 2 O 3 for sorption enhanced steam reforming of bio-oil with acetic acid as the model compound

2017 ◽  
Vol 119 ◽  
pp. 106-112 ◽  
Author(s):  
Xiao-yong Zhao ◽  
Ya-ping Xue ◽  
Chang-feng Yan ◽  
Zhi-da Wang ◽  
Chang-qing Guo ◽  
...  
Keyword(s):  
Acetic Acid ◽  
Steam Reforming ◽  
Model Compound ◽  
Bio Oil

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.

Catalytic steam reforming of acetic acid as a model compound of bio-oil

2014 ◽  
Vol 160-161 ◽  
pp. 188-199 ◽  
Author(s):  
Francisco Guilherme E. Nogueira ◽  
Paulo G.M. Assaf ◽  
Hudson W.P. Carvalho ◽  
Elisabete M. Assaf
Keyword(s):  
Acetic Acid ◽  
Steam Reforming ◽  
Model Compound ◽  
Bio Oil ◽  
Catalytic Steam Reforming
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