scholarly journals Fabrication and (Photo)Electrochemical Properties of Fe2O3/Na2Ti6O13/FTO Films for Water Splitting Process

2012 ◽  
Vol 11 (2) ◽  
pp. 65-69
Author(s):  
Kang-Seop Yun ◽  
Hye-Kyung Ku ◽  
Woo-Seung Kang ◽  
Sun-Jae Kim
2021 ◽  
Vol 1 (1) ◽  
pp. 26-35
Author(s):  
Chin Wei Lai ◽  
Jenny Hui Foong Chau

Hydrogen (H2) has proved itself as a viable future energy carrier and alternative for fossil fuel in terms of ensuring a clean and sustainable energy supply. However, H2 must be made available at a lower cost so that everyone can benefit from it and prevent causing a worldwide ecological imbalance. The usage of photoelectrochemical water splitting (PEC) technology by using TiO2 photocatalyst can produce H2 using renewable solar energy. The essential milestones, as well as the mechanism in PEC H2 generation, are discussed in this article.


2019 ◽  
Vol 102 (5) ◽  
pp. e1900065 ◽  
Author(s):  
Beatrice Adelizzi ◽  
Andreas T. Rösch ◽  
Daan J. van Rijen ◽  
R. Simone Martire ◽  
Serkan Esiner ◽  
...  

2020 ◽  
Vol 145 ◽  
pp. 109544
Author(s):  
S. Swathi ◽  
B. Jansi Rani ◽  
G. Ravi ◽  
R. Yuvakkumar ◽  
S.I. Hong ◽  
...  

Nano Energy ◽  
2019 ◽  
Vol 57 ◽  
pp. 660-669 ◽  
Author(s):  
Truong Thi Hien ◽  
Nguyen Duc Quang ◽  
Chunjoong Kim ◽  
Dojin Kim

2019 ◽  
Vol 3 (2) ◽  
pp. 50 ◽  
Author(s):  
Giampaolo Caputo ◽  
Irena Balog ◽  
Alberto Giaconia ◽  
Salvatore Sau ◽  
Alfonso Pozio

The efficiency of HI concentration/separation from a HIx solution, (mixture of HI/H2O/I2) represents a crucial factor in the sulfur-iodine thermochemical water splitting process for hydrogen production. In this paper, an experimental study on HI cathodic concentration in HIx solution using stacked electro-electrodialysis (EED) cells was carried out under the conditions of 1 atm and at three different temperature (25, 55 and 85 °C) and using a current density of 0.10 A/cm2. Results showed that an increase in HI concentration can be obtained under certain conditions. The apparent transport number (t+) in all the experiments was very close to 1, and the electro-osmosis coefficient (β) changed in a range of 1.08–1.16. The tests showed a detectable, though slow, increase in both the anodic iodine and cathodic hydriodic acid concentrations.


2002 ◽  
Vol 357 (1426) ◽  
pp. 1419-1420 ◽  

This general discussion was chaired by A. W. Rutherford ( Service de Bioénergétique, Saclay, France ) and revolved around two major topics: (i) the implications of X–ray crystallography on the relationships between structure and function; (ii) the molecular mechanisms of the water–splitting process.


2010 ◽  
Vol 35 (14) ◽  
pp. 7357-7368 ◽  
Author(s):  
Gülşah Özişik ◽  
Nesrin Demir ◽  
Mustafa Übeyli ◽  
Hüseyin Yapici

Author(s):  
Y. Tamaura ◽  
H. Kaneko ◽  
Y. Naganuma ◽  
S. Taku ◽  
K. Ouchi ◽  
...  

The rotary-type solar reactor has been developed for solar hydrogen production with the two-step water splitting process using the reactive ceramic (Ni, Mn-ferrite). The rotary-type reactor has the rotating tubular cylinder covered on a reactive ceramic and dual reaction cells for O2-releasing and H2-generation reactions. The successive evolutions of O2 and H2 gases were observed in the O2 releasing and H2 generation reaction cells, respectively, with the prototype (small) reactor (diameter of cylinder ; 4cm). There is an upper limit for the rate of H2 gas evolution in the case of the prototype reactor because of the slow rotation rate in a small irradiation area. To confirm the practical operation of the rotary-type solar reactor with the two-step water splitting process for the simultaneous production of H2 and O2 gases, a scaled-up rotary-type solar reactor with 400cm2 of the irradiation area was fabricated (diameter; 50cm). The scaled-up reactor made of inner and outer short tubular cylinders (stainless steel) has a quartz glass window for the irradiation of reactive ceramic coated on the inner tubular cylinder (cylindrical rotor) and reaction cells were aligned in the sharing spaces between the inner and outer short tubular cylinders with gas sealing mechanisms. In the reactor, reactive ceramic coated on the inner tubular cylinder was heated up to 1800K by using the infrared imaging lamps (solar simulator) with thermal flux = 600kW/m2. The solid solution between YSZ and Ni-ferrite was used as reactive ceramic for the scaled-up reactor in order to prevent from sintering at a high temperature in the O2-releasing reaction, since the sintering of reactive ceramic resulted in lowering the yield of H2 gas evolution in the H2-generation reaction. The amounts of H2 and O2 gases evolved at the rotation rate of 0.3rpm were evaluated to 64cm3 and 30cm3 for 10min with the scaled-up rotary-type solar reactor, respectively, which were much larger than those with the prototype reactor. The simultaneous evolutions of H2 and O2 gases in the two-step water splitting process were repeated by employing the scaled-up reactor with the solid solution between YSZ and Ni-ferrite.


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