The evaluation of autothermal methane reforming for hydrogen production over Ni/CeO2 catalysts

2018 ◽  
Vol 43 (49) ◽  
pp. 22340-22346 ◽  
Author(s):  
Soodeh Sepehri ◽  
Mehran Rezaei ◽  
Yuan Wang ◽  
Aryan Younesi ◽  
Hamidreza Arandiyan
2009 ◽  
Vol 1 (6) ◽  
pp. 205-215 ◽  
Author(s):  
C.N. Ávila-Neto ◽  
S.C. Dantas ◽  
F.A. Silva ◽  
T.V. Franco ◽  
L.L. Romanielo ◽  
...  

Energies ◽  
2020 ◽  
Vol 13 (15) ◽  
pp. 3783 ◽  
Author(s):  
Martin Khzouz ◽  
Evangelos Gkanas ◽  
Jia Shao ◽  
Farooq Sher ◽  
Dmytro Beherskyi ◽  
...  

This work investigates life cycle costing analysis as a tool to estimate the cost of hydrogen to be used as fuel for Hydrogen Fuel Cell vehicles (HFCVs). The method of life cycle costing and economic data are considered to estimate the cost of hydrogen for centralised and decentralised production processes. In the current study, two major hydrogen production methods are considered, methane reforming and water electrolysis. The costing frameworks are defined for hydrogen production, transportation and final application. The results show that hydrogen production via centralised methane reforming is financially viable for future transport applications. The ownership cost of HFCVs shows the highest cost among other costs of life cycle analysis.


2015 ◽  
Vol 40 (48) ◽  
pp. 17272-17283 ◽  
Author(s):  
A.L. Martínez-Salazar ◽  
J.A. Melo-Banda ◽  
A.I. Reyes de la Torre ◽  
Y. Salazar-Cerda ◽  
M.A. Coronel-García ◽  
...  

Author(s):  
M. Gambini ◽  
M. Vellini

In this paper two options for H2 production by means of fossil fuels are presented, evaluating their performance when integrated with advanced H2/air cycles. The investigation has been developed with reference to two different schemes, representative both of consolidated technology (combined cycle power plants) and of innovative technology (a new advance mixed cycle, named AMC). The two methods, here considered, to produce H2 are: • coal gasification: it permits transformation of a solid fuel into a gaseous one, by means of partial combustion reactions; • steam-methane reforming: it is the simplest and potentially the most economic method for producing hydrogen in the foreseeable future. These hydrogen production plants require material and energy integrations with the power section, and the best connections must be investigated in order to obtain good overall performance. The main results of the performed investigation are quite variable among the different H2 production options here considered: for example the efficiency value is over 34% for power plants coupled with coal decarbonization system, while it is in a range of 45–48% for power plants coupled with natural gas decarbonization. These differences are similar to those attainable by advanced combined cycle power plants fuelled by natural gas (traditional CC) and coal (IGCC). In other words, the decarbonization of different fossil fuels involves the same efficiency penalty related to the use of different fossil fuel in advanced cycle power plants (from CC to IGCC for example). The CO2 specific emissions depend on the fossil fuel type and the overall efficiency: adopting a removal efficiency of 90% in the CO2 absorption systems, the CO2 emission reduction is 87% and 82% in the coal gasification and in the steam-methane reforming respectively.


2014 ◽  
Vol 136 (3) ◽  
Author(s):  
Jong Tak Jang ◽  
Ki June Yoon ◽  
Gui Young Han

In order to utilize sustainable solar energy, cyclic operations of syngas production by methane reforming (reduction) and subsequent hydrogen production by water splitting (oxidation) were performed by using simulated solar-light irradiation to ZrO2-supported CeO2 particles which were coated on a SiC ceramic foam disk. This redox process is a promising chemical pathway for storage and transportation of solar heat by converting solar energy to chemical energy. By properly adjusting the methane reforming time, carbon deposition due to the undesirable methane decomposition could be avoided. The produced syngas had the H2/CO ratio of 2.0, which is suitable for the Fischer–Tropsch synthesis or methanol synthesis, and the produced pure hydrogen can be used for fuel cells. When the cyclic reactions were repeated several times at two temperatures (800 °C, 900 °C), the conversion of CeO2 and the H2 yield were reasonable and were maintained nearly constant from the second cycle, exhibiting good stability of the redox process.


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