Kinetic modeling of the production of hydrogen from the methanol-steam reforming process over Mn-promoted coprecipitated Cu-Al catalyst

1996 ◽  
Vol 51 (14) ◽  
pp. 3697-3708 ◽  
Author(s):  
Raphael O. Idem ◽  
Narendra N. Bakhshi
RSC Advances ◽  
2016 ◽  
Vol 6 (36) ◽  
pp. 30176-30183 ◽  
Author(s):  
Jiajia Zhou ◽  
Ye Zhang ◽  
Guisheng Wu ◽  
Dongsen Mao ◽  
Guanzhong Lu

A series of binary Cu/ZrO2 catalysts by choosing different composition ratios and different precipitation sequences have been prepared for the production of hydrogen by steam reforming of methanol (SRM).


2018 ◽  
Vol 54 (86) ◽  
pp. 12242-12245 ◽  
Author(s):  
Shaojun Qing ◽  
Xiaoning Hou ◽  
Yajie Liu ◽  
Lindong Li ◽  
Xiang Wang ◽  
...  

Using sustained release catalysis, CuAlO2 catalyst demonstrates excellent catalytic performance for methanol steam reforming and can be completely regenerated.


2006 ◽  
Vol 116 (3) ◽  
pp. 354-360 ◽  
Author(s):  
T. Valdés-Solís ◽  
G. Marbán ◽  
A.B. Fuertes

Energies ◽  
2020 ◽  
Vol 13 (7) ◽  
pp. 1564 ◽  
Author(s):  
Guoqiang Wang ◽  
Feng Wang ◽  
Bohong Chen

Automobile exhaust heat recovery is considered to be an effective means to enhance fuel utilization. The catalytic production of hydrogen by methanol steam reforming is an attractive option for onboard mobile applications, due to its many advantages. However, the reformers of conventional packed bed type suffer from axial temperature gradients and cold spots resulting from severe limitations of mass and heat transfer. These disadvantages limit reformers to a low efficiency of catalyst utilization. A novel rib microreactor was designed for the hydrogen production from methanol steam reforming heated by automobile exhaust, and the effect of inlet exhaust and methanol steam on reactor performance was numerically analyzed in detail, with computational fluid dynamics. The results showed that the best operating parameters were the counter flow, water-to-alcohol (W/A) of 1.3, exhaust inlet velocity of 1.1 m/s, and exhaust inlet temperature of 773 K, when the inlet velocity and inlet temperature of the reactant were 0.1 m/s and 493 K, respectively. At this condition, a methanol conversion of 99.4% and thermal efficiency of 28% were achieved, together with a hydrogen content of 69.6%.


2017 ◽  
Vol 203 ◽  
pp. 400-407 ◽  
Author(s):  
C.S.R. Azenha ◽  
C. Mateos-Pedrero ◽  
S. Queirós ◽  
P. Concepción ◽  
A. Mendes

2019 ◽  
pp. 1-18
Author(s):  
Fazil Qureshi ◽  
Faizan Ahmad ◽  
Mohammad Idrees ◽  
Ali Asif Khan ◽  
Sadaf Zaidi

Nanomaterials ◽  
2021 ◽  
Vol 11 (12) ◽  
pp. 3234
Author(s):  
Luis F. Bobadilla ◽  
Lola Azancot ◽  
Svetlana Ivanova ◽  
Juan J. Delgado ◽  
Francisca Romero-Sarria ◽  
...  

Methanol adsorption over both supported NiSn Nps and analogous NiSn catalyst prepared by impregnation was studied by in situ diffuse reflectance infrared Fourier transform spectroscopy (DRIFTS) to gain insights into the basis of hydrogen production from methanol steam reforming. Different intermediate species such as methoxides with different geometry (bridge and monodentate) and formate species were identified after methanol adsorption and thermal desorption. It is proposed that these species are the most involved in the methanol steam reforming reaction and the major presence of metal-support interface sites in supported NiSn Nps leads to higher production of hydrogen. On the basis of these results, a plausible reaction mechanism was elucidated through the correlation between the thermal stability of these species and the evolution of the effluent gas released. In addition, it was demonstrated that DME is a secondary product generated by condensation of methoxides over the acid sites of alumina support in an acid-catalyzed reaction.


Sign in / Sign up

Export Citation Format

Share Document