TY  - JOUR
SN  - 15567036
PB  - Taylor and Francis Inc.
EP  - 663
AV  - none
N1  - cited By 18
TI  - Reforming of glycerol for hydrogen production over Ni based catalysts: Effect of support type
SP  - 657
Y1  - 2017///
UR  - https://www.scopus.com/inward/record.uri?eid=2-s2.0-85015107294&doi=10.1080%2f15567036.2016.1244580&partnerID=40&md5=85010eb47f7f93f8357d853fe701f736
JF  - Energy Sources, Part A: Recovery, Utilization and Environmental Effects
A1  - Mohd Arif, N.N.
A1  - Harun, N.
A1  - Yunus, N.M.
A1  - Vo, D.-V.N.
A1  - Azizan, M.T.
A1  - Zainal Abidin, S.
VL  - 39
N2  - This current work focuses on hydrogen production that is a component in syngas by glycerol dry reforming over 15 nickel (Ni) loading supported on different oxides, namely CaO, ZrO2, and La2O3. The screening process was conducted in a fixed-bed reactor at 700°C under atmospheric pressure. It was found that 15 Ni/CaO showed the best performance in screening studies. The effect of temperature and the carbon to glycerol ratio (CGR) was then analyzed for this catalyst. From the analysis, it was seen that 15 Ni/CaO has its optimum condition at 800°C and CGR = 1, where it gives the highest glycerol conversion (XG = 37.66) and hydrogen yield (YH = 32.45). © 2017 Taylor & Francis Group, LLC.
IS  - 7
KW  - Atmospheric pressure; Catalysts; Chemical reactors; Glycerol; Hydrogen; Nickel; Nickel oxide; Oxides; Zirconia
KW  -  Dry reforming; Effect of supports; Effect of temperature; Fixed bed reactor; Glycerol conversions; Ni-based catalyst; Optimum conditions; Screening process
KW  -  Hydrogen production
ID  - scholars8730
ER  -