Thermodynamic analysis of hydrogen production via steam reforming of selected components of aqueous bio-oil fraction

2007 ◽  
Vol 32 (2) ◽  
pp. 212-223 ◽  
Author(s):  
E VAGIA ◽  
A LEMONIDOU
Keyword(s):  
Hydrogen Production ◽  
Thermodynamic Analysis ◽  
Steam Reforming ◽  
Oil Fraction ◽  
Bio Oil

Thermodynamic analysis of hydrogen production from model compounds of bio-oil through steam reforming

2013 ◽  
Vol 33 (3) ◽  
pp. 1008-1016 ◽  
Author(s):  
Huaqing Xie ◽  
Qingbo Yu ◽  
Kun Wang ◽  
Xiaobo Shi ◽  
Xinhui Li
Keyword(s):  
Hydrogen Production ◽  
Thermodynamic Analysis ◽  
Steam Reforming ◽  
Model Compounds ◽  
Bio Oil

scholarly journals Thermodynamic Analysis of Hydrogen Production from the Adsorption-enhanced Steam Reforming of Biogas

2014 ◽  
Vol 61 ◽  
pp. 2254-2257 ◽  
Author(s):  
Dang Saebea ◽  
Suthida Authayanun ◽  
Yaneeporn Patcharavorachot ◽  
Amornchai Arpornwichanop
Keyword(s):  
Hydrogen Production ◽  
Thermodynamic Analysis ◽  
Steam Reforming

Catalytic steam reforming of simulated bio-oil for green hydrogen production using highly active LaNixCo1-xO3 perovskite catalyst

2022 ◽  
Author(s):  
Piyush Pratap Singh ◽  
Neelkanth Nirmalkar ◽  
Tarak Mondal
Keyword(s):  
Hydrogen Production ◽  
Waste Management ◽  
Steam Reforming ◽  
Energy Production ◽  
Sustainable Energy ◽  
Agricultural Waste ◽  
Perovskite Catalyst ◽  
Highly Active ◽  
Bio Oil ◽  
Catalytic Steam Reforming

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...

scholarly journals STEAM REFORMING OF UPGRADED BIO-OIL AQUEOUS PHASE FRACTION FROM SUNFLOWER SEED HULLS: THERMODYNAMIC ANALYSIS

2019 ◽  
Vol 49 (4) ◽  
pp. 297-302
Author(s):  
Yanina P. Maidana ◽  
Eduardo Izurieta ◽  
Andres I. Casoni ◽  
Maria A. Volpe ◽  
Eduardo Lopez ◽  
...  
Keyword(s):  
Acetic Acid ◽  
Aqueous Phase ◽  
Thermodynamic Analysis ◽  
Steam Reforming ◽  
Sunflower Seed ◽  
Maximum Yield ◽  
Energetic Efficiency ◽  
Water Addition ◽  
Thermal Requirements ◽  
Bio Oil

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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