scholarly journals Microwave-driven hydrogen production (MDHP) from water and activated carbons (ACs). Application to wastewaters and seawater

RSC Advances ◽  
2021 ◽  
Vol 11 (50) ◽  
pp. 31590-31600
Author(s):  
Satoshi Horikoshi ◽  
Leo Takahashi ◽  
Kirara Sueishi ◽  
Honoka Tanizawa ◽  
Nick Serpone

We report on the low-temperature steam reforming and water–gas shift processes to generate H2 efficiently from water passed through MW-heated activated carbon (AC) particles, contrary to the inefficient conventional steam reforming at T ≈ 600 °C.

2015 ◽  
Vol 4 (5) ◽  
Author(s):  
Prem Kumar Seelam ◽  
Anne-Riikka Rautio ◽  
Mika Huuhtanen ◽  
Krisztian Kordas ◽  
Riitta L. Keiski

AbstractSteam reforming of biofuels such as bioethanol offers a clean and sustainable route to improve hydrogen production capacity for the hydrogen economy. In this work, the influence of the carbon support type (carbon nanotube [CNT], activated carbon [AC] and graphitic carbon black [GCB]) and the addition of Pt (1 wt.%, 1.5 wt.% and 2 wt.%) and ZnO (10 wt.%) to Ni


Author(s):  
Leteng Lin ◽  
Li Sun ◽  
Xiaodong Zhang ◽  
Xiaolu Yi ◽  
Min Xu

Hydrogen is currently being widely regarded as a futural energy carrier to reduce carbon emissions and other NOx and SOx pollutants. Many researchers have proved that hydrogen can be efficiently used in solid oxide fuel cells -gas turbine system (SOFC-GT) and molten carbonate fuel cells-gas turbine system (MCFC-GT). Hydrogen production from biomass resources offers the advantage of providing a renewable energy carrier for extensive reduction of the CO2 emission. A secondary steam reforming process which consists of steam reforming of methane and water gas shift was proposed to further convert CH4, CO and other hydrocarbons in biomass pyrolysis gas for promoting hydrogen yield. According to respective reaction mechanism, simulating calculations were carried out in two reforming processes separately. With the favor of PRO/II, the effects of reaction temperature and steam to carbon ratio on hydrogen yield were discussed in details in the steam reforming of methane. A reasonable calculation method was established for simulating the water gas shift process in which the effects of temperature and steam to CO ratio was investigated. The simulation made good results in optimizing reaction conditions for two reformers and predicting the volume rate of all gas components. It is proved by simulation that hydrogen-rich gas with >68 mol% H2 could be produced, and the hydrogen yield could reach 48.18 mol H2/(Kg Biomass) and 45.85 mol/(Kg Biomass) respectively when using corn straw and rice husk as feedstock. The experiment data from a related reference was adopted to prove the reasonability of the simulation results which could show the feasibility of secondary steam reforming process, as well as provide good references for practical process operation.


2011 ◽  
Vol 4 (2) ◽  
pp. 122-145
Author(s):  
Kyriaki Polychronopoulou ◽  
Christos M. Kalamaras ◽  
Angelos M. Efstathiou

2007 ◽  
Vol 122 (1-2) ◽  
pp. 9-19 ◽  
Author(s):  
Harold N. Evin ◽  
Gary Jacobs ◽  
Javier Ruiz-Martinez ◽  
Uschi M. Graham ◽  
Alan Dozier ◽  
...  

2016 ◽  
Vol 0 (0) ◽  
Author(s):  
Yi-Jiang Wu ◽  
Ping Li ◽  
Jian-Guo Yu ◽  
Adelino F. Cunha ◽  
Alirio E. Rodrigues

AbstractConcerns about the environment and fossil fuel depletion led to the concept of “hydrogen economy”, where hydrogen is used as an energy carrier. Nowadays, hydrogen is mostly produced from fossil fuel resources by natural gas reforming, coal gasification, as well as the water-gas-shift (WGS) reaction involved in these processes. Alternatively, bioethanol, glucose, glycerol, bio-oil, and other renewable biomass-derived feedstocks can also be employed for hydrogen production via steam reforming process. The combination of steam reforming and/or WGS reaction with


2020 ◽  
Vol 3 (6) ◽  
pp. 881-917 ◽  
Author(s):  
Parisa Ebrahimi ◽  
Anand Kumar ◽  
Majeda Khraisheh

AbstractThe water-gas shift reaction (WGSR) is an intermediate reaction in hydrocarbon reforming processes, considered one of the most important reactions for hydrogen production. Here, water and carbon monoxide molecules react to generate hydrogen and carbon dioxide. From the thermodynamics aspect, pressure does not have an impact, whereas low-temperature conditions are suitable for high hydrogen selectivity because of the exothermic nature of the WGSR reaction. The performance of this reaction can be greatly enhanced in the presence of suitable catalysts. The WGSR has been widely studied due do the industrial significance resulting in a good volume of open literature on reactor design and catalyst development. A number of review articles are also available on the fundamental aspects of the reaction, including thermodynamic analysis, reaction condition optimization, catalyst design, and deactivation studies. Over the past few decades, there has been an exceptional development of the catalyst characterization techniques such as near-ambient x-ray photoelectron spectroscopy (NA-XPS) and in situ transmission electron microscopy (in situ TEM), providing atomic level information in presence of gases at elevated temperatures. These tools have been crucial in providing nanoscale structural details and the dynamic changes during reaction conditions, which were not available before. The present review is an attempt to gather the recent progress, particularly in the past decade, on the catalysts for low-temperature WGSR and their structural properties, leading to new insights that can be used in the future for effective catalyst design. For the ease of reading, the article is divided into subsections based on metals (noble and transition metal), oxide supports, and carbon-based supports. It also aims at providing a brief overview of the reaction conditions by including a table of catalysts with synthesis methods, reaction conditions, and key observations for a quick reference. Based on our study of literature on noble metal catalysts, atomic Pt substituted Mn3O4 shows almost full CO conversion at 260 °C itself with zero methane formation. In the case of transition metals group, the inclusion of Cu in catalytic system seems to influence the CO conversion significantly, and in some cases, with CO conversion improvement by 65% at 280 °C. Moreover, mesoporous ceria as a catalyst support shows great potential with reports of full CO conversion at a low temperature of 175 °C.


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