Dual catalyst-sorbent role of dolomite in the steam reforming of raw bio-oil for producing H2-rich syngas

2020 ◽  
Vol 200 ◽  
pp. 106316 ◽  
Author(s):  
Beatriz Valle ◽  
Naiara García-Gómez ◽  
Aingeru Remiro ◽  
Javier Bilbao ◽  
Ana G. Gayubo
Keyword(s):  
2017 ◽  
Vol 19 (18) ◽  
pp. 4315-4333 ◽  
Author(s):  
Aitor Ochoa ◽  
Borja Aramburu ◽  
Beatriz Valle ◽  
Daniel E. Resasco ◽  
Javier Bilbao ◽  
...  

This work investigates the correlation of the reaction conditions and the reaction medium composition with the deactivation behavior of a Ni/La2O3-αAl2O3 catalyst used in the steam reforming of bio-oil.


Author(s):  
Mira Abou Rjeily ◽  
Cédric Gennequin ◽  
Hervé Pron ◽  
Edmond Abi-Aad ◽  
Jaona Harifidy Randrianalisoa

2010 ◽  
Vol 2010 ◽  
pp. 1-15 ◽  
Author(s):  
Abdul-Majeed Azad ◽  
Desikan Sundararajan

Clean power source utilizing vast logistic fuel reserves (jet fuels, diesel, and coal) would be the main driver in the 21st century for high efficiency. Fuel processors are required to convert these fuels into hydrogen-rich reformate for extended periods in the presence of sulfur, and deliver hydrogen with little or no sulfur to the fuel cell stack. However, the jet and other logistic fuels are invariably sulfur-laden. Sulfur poisons and deactivates the reforming catalyst and therefore, to facilitate continuous uninterrupted operation of logistic fuel processors, robust sulfur-tolerant catalysts ought to be developed. New noble metal-supported ceria-based sulfur-tolerant nanocatalysts were developed and thoroughly characterized. In this paper, the performance of single metal-supported catalysts in the steam-reforming of kerosene, with 260 ppm sulfur is highlighted. It was found that ruthenium-based formulation provided an excellent balance between hydrogen production and stability towards sulfur, while palladium-based catalyst exhibited rapid and steady deactivation due to the highest propensity to sulfur poisoning. The rhodium supported system was found to be most attractive in terms of high hydrogen yield and long-term stability. A mechanistic correlation between the role of the nature of the precious metal and the support for generating clean desulfurized -rich reformate is discussed.


2011 ◽  
Vol 25 (7) ◽  
pp. 3289-3297 ◽  
Author(s):  
Pedro J. Ortiz-Toral ◽  
Justinus Satrio ◽  
Robert C. Brown ◽  
Brent H. Shanks

2017 ◽  
Vol 209 ◽  
pp. 346-357 ◽  
Author(s):  
F. Bimbela ◽  
J. Ábrego ◽  
R. Puerta ◽  
L. García ◽  
J. Arauzo

RSC Advances ◽  
2014 ◽  
Vol 4 (36) ◽  
pp. 18924-18929 ◽  
Author(s):  
Xun Hu ◽  
Lijun Zhang ◽  
Dehua Dong ◽  
Gongxuan Lu

A reactor with constant-temperature and stepwise decreasing-temperature zones is developed, which can catalyze steam reforming of bio-oil derived organics and methane to produce hydrogen-rich gas with only trace CO in a wide temperature region.


2010 ◽  
Vol 33 (12) ◽  
pp. 2021-2028 ◽  
Author(s):  
P. Lan ◽  
Q. Xu ◽  
M. Zhou ◽  
L. Lan ◽  
S. Zhang ◽  
...  

Author(s):  
Piyush Pratap Singh ◽  
Neelkanth Nirmalkar ◽  
Tarak Mondal

Catalytic steam reforming (SR) of agricultural waste derived bio-oil for hydrogen production is a unique technology, offering twin benefits of waste management as well as sustainable energy production. In the...


2019 ◽  
Vol 49 (4) ◽  
pp. 297-302
Author(s):  
Yanina P. Maidana ◽  
Eduardo Izurieta ◽  
Andres I. Casoni ◽  
Maria A. Volpe ◽  
Eduardo Lopez ◽  
...  

This work focuses on the study of hydrogen production process departing from waste lignocellulosic biomass. The bio-oil was first obtained by non-catalytic fast pyrolysis of sunflower seed hulls. Subsequently, it was upgraded to reduce the concentration of higher molecular weight compounds by water addition and mixing. A 1/1 bio-oil:water ratio was selected here. Later, a thermodynamic analysis based on free energy minimization was profited to study the steam reforming process of the upgraded bio-oil sample. The influence of the operation temperature on the reforming was analyzed. The highest hydrogen yields were obtained at ~740°C. A comparison with acetic acid used as model compound of the bio-oil is included. Results show that acetic acid is not a good approximation of a real aqueous phase of upgraded bio oil fraction. The study concludes with an analysis on the energetic efficiency, showing that its maximum is presented at lower temperatures than the maximum yield, due to the thermal requirements of preheating.


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