Sulfur Doped FeOx Nanosheet Arrays Supported on Nickel Foam for Efficient Alkaline Seawater Splitting

2021 ◽  
Author(s):  
Weiju Hao ◽  
Jinli Fan ◽  
Xia Xu ◽  
Yiran Zhang ◽  
Haiyang Lv ◽  
...  

Developing economical, efficient and stable bifunctional catalysts for hydrogen production from seawater is of great significance to hydrogen utilization. Herein, sulfur doped iron oxide nanosheet arrays supported on nickel foam...

ACS Catalysis ◽  
2021 ◽  
pp. 10228-10238
Author(s):  
Iwei Wang ◽  
Yunfei Gao ◽  
Xijun Wang ◽  
Runxia Cai ◽  
Chingchang Chung ◽  
...  

2021 ◽  
Author(s):  
Guojuan Hai ◽  
Jianfeng Huang ◽  
Liyun Cao ◽  
Koji Kajiyoshi ◽  
Long Wang ◽  
...  

Designing cost-effective bifunctional catalysts with high-performance and durability is of great significance for the renewable energy systems. Herein, a typical Fe, Ni-codoped W18O49/NF was prepared via a simple solvothermal method....


Nano Research ◽  
2018 ◽  
Vol 11 (3) ◽  
pp. 1415-1425 ◽  
Author(s):  
Weidong He ◽  
Zhifu Liang ◽  
Keyu Ji ◽  
Qingfeng Sun ◽  
Tianyou Zhai ◽  
...  

RSC Advances ◽  
2015 ◽  
Vol 5 (4) ◽  
pp. 2543-2549 ◽  
Author(s):  
Bo-Jun Li ◽  
Peng-Fei Yin ◽  
Yu-Zhu Zhou ◽  
Zhi-Ming Gao ◽  
Tao Ling ◽  
...  

We present a scalable route for the preparation of single crystalline Cu2ZnSnS4 nanosheet arrays on conductive glass substrate, and demonstrate this architecture as an effective photocathode for solar hydrogen production.


Author(s):  
A. Singh ◽  
F. Al-Raqom ◽  
J. Klausner ◽  
J. Petrasch

The iron/iron-oxide looping cycle has the potential to produce high purity hydrogen from coal or natural gas without the need for gas phase separation: Hydrogen is produced from steam oxidation of iron or Wustite yielding primarily Magnetite; Magnetite is then reduced back to iron/Wustite using syngas (CO+H2). A system model has been developed to identify favorable operation conditions and process configurations. Process configurations for three distinct temperature ranges, (i) 500–950 K, (ii) 950–1100 K, and (iii) 1100–1200 K have been developed. The energy content of high temperature syngas from conventional coal gasifiers is sufficient to drive the looping process throughout the temperature range considered. Temperatures around 1000 K are advantageous for both the hydrogen production step and the iron oxide reduction step. Simulations of a large number of subsequent cycles indicate that quasi-steady operation is reached after approximately 5 cycles. Comparison of simulations and experiments indicate that the process is currently limited by chemical kinetics at lower temperatures. Therefore, product recirculation should be used for a scaled-up process to increase reactant residence times while maintaining sufficient fluidization velocity.


2018 ◽  
Vol 57 (32) ◽  
pp. 10893-10904 ◽  
Author(s):  
Yu Cheng ◽  
Meisong Guo ◽  
Yanan Yu ◽  
Miaomiao Zhai ◽  
Rui Guo ◽  
...  

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