Nickel catalysts applied in steam reforming of glycerol for hydrogen production

2009 ◽  
Vol 10 (13) ◽  
pp. 1656-1660 ◽  
Author(s):  
Ivana N. Buffoni ◽  
Francisco Pompeo ◽  
Gerardo F. Santori ◽  
Nora N. Nichio
Keyword(s):  
Hydrogen Production ◽  
Steam Reforming ◽  
Nickel Catalysts

Hydrogen production from catalytic steam reforming of glycerol over various supported nickel catalysts

2017 ◽  
Vol 42 (14) ◽  
pp. 9087-9098 ◽  
Author(s):  
Nurul Huda Zamzuri ◽  
Ramli Mat ◽  
Nor Aishah Saidina Amin ◽  
Amin Talebian-Kiakalaieh
Keyword(s):  
Hydrogen Production ◽  
Steam Reforming ◽  
Nickel Catalysts ◽  
Supported Nickel Catalysts ◽  
Catalytic Steam Reforming

Hydrogen Production by Steam Reforming of Ethanol Using Cobalt and Nickel Catalysts Supported on Strontium Titanate

2005 ◽  
Vol 34 (5) ◽  
pp. 668-669 ◽  
Author(s):  
Kohei Urasaki ◽  
Kazuhisa Tokunaga ◽  
Yasushi Sekine ◽  
Eiichi Kikuchi ◽  
Masahiko Matsukata
Keyword(s):  
Hydrogen Production ◽  
Strontium Titanate ◽  
Steam Reforming ◽  
Nickel Catalysts ◽  
Steam Reforming Of Ethanol ◽  
Cobalt And Nickel

scholarly journals Synthesis and Characterization of Co/Ni/CoNi-ZSM-5 Catalyst for Hydrogen Production

2018 ◽  
Vol 156 ◽  
pp. 06013
Author(s):  
Widayat Widayat ◽  
Arianti Nuur Annisa ◽  
Hantoro Satriadi ◽  
Syaiful Syaiful
Keyword(s):  
Hydrogen Production ◽  
Steam Reforming ◽  
Hydrothermal Process ◽  
Coke Formation ◽  
Nickel Catalysts ◽  
Catalyst Synthesis ◽  
Cobalt Nickel ◽  
Crystalline Product ◽  
Production Of Hydrogen

Nickel is commonly used as a catalyst in hydrogen production. However, the use of nickel catalysts in the steam reforming process has the disadvantage of coke formation and high cost. Therefore, in this research, Ni/ZSM-5 catalyst synthesis was used to reduce production cost and an addition of cobalt (Co) metal to avoid coke formation. The method consists of a synthesis of ZSM-5 catalyst using hydrothermal process. Furthermore, the crystalline product was impregnated with the metal cobalt, nickel and combination of cobalt-nickel as much as 2% by weight metal/weight of the catalyst. Then the XRD and EDX characterization of Co/ZSM-5, Ni/ZSM-5, and CoNi/ZSM-5 was done followed by catalytic testing in the production of hydrogen from glycerol using steam reforming process. From XRD characterization results showed that Co/ZSM-5 catalyst has a crystallinity of 78.69%, Ni/ZSM-5 catalyst has 70.04% crystallinity and CoNi/ZSM-5 catalyst has 76.99% crystallinity. Catalytic testing on hydrogen production showed that CoNi/ZSM-5 catalyst produced the highest hydrogen concentration of 1,756.33 ppm while Ni/ZSM-5 catalyst produces 1,240 ppm and Co/ZSM-5 catalyst produces 491 ppm.

Hydrogen production from glycerin by steam reforming over nickel catalysts

2008 ◽  
Vol 33 (5) ◽  
pp. 1097-1100 ◽  
Author(s):  
Sushil Adhikari ◽  
Sandun D. Fernando ◽  
Agus Haryanto
Keyword(s):  
Hydrogen Production ◽  
Steam Reforming ◽  
Nickel Catalysts

Hydrogen production via steam reforming of ethylene glycol over Attapulgite supported nickel catalysts

2018 ◽  
Vol 43 (45) ◽  
pp. 20438-20450 ◽  
Author(s):  
Yishuang Wang ◽  
Mingqiang Chen ◽  
Xiaojing Li ◽  
Zhonglian Yang ◽  
Tian Liang ◽  
...  
Keyword(s):  
Hydrogen Production ◽  
Ethylene Glycol ◽  
Steam Reforming ◽  
Nickel Catalysts ◽  
Supported Nickel Catalysts
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