TY - JOUR
T1 - Cu-K/Al2O3 based catalysts for conversion of carbon dioxide to methane and carbon monoxide
AU - Ahmad, Waqar
AU - Al-Matar, Ali
AU - Shawabkeh, Reyad
AU - Aslam, Zaheer
AU - Malik, Izhar A.
AU - Irshad, Hafiz M.
N1 - Funding Information:
The authors would like to acknowledge the support of King Abdul Aziz City for Science and Technology (KACST) through the science and technology unit at King Fahd University of Petroleum & Minerals (KFUPM) for funding this research through project # 13-ENV2361-04. In addition, authors would like to acknowledge the department of chemical engineering in KFUPM.
Publisher Copyright:
© 2019, © 2019 Taylor & Francis Group, LLC.
Copyright:
Copyright 2020 Elsevier B.V., All rights reserved.
PY - 2020/9/3
Y1 - 2020/9/3
N2 - A series of Cu-K/Al2O3 catalysts were synthesized by wet impregnation technique. The reduced catalysts were further used for conversion of carbon dioxide to methane and carbon monoxide. Moreover, the fresh and used catalysts were characterized to investigate the changes in the surface morphology, metal dispersion, surface area, crystalline phases, and functional groups of studied catalysts. The SEM analysis of fresh and spent catalysts showed no remarkable difference in surface morphology with irregular shaped agglomerated particles. Furthermore, TEM micrographs presented the well distribution of metal catalyst over alumina support. The decrease in surface area from 115 to 77 m2/g for Cu1.62-K0.5/Al2O3 after reaction was related to sintering and oxidation of catalyst during reaction. XRD revealed the disappearance of some minor peaks which can be associated with the sintering of spent catalyst. FTIR also presented some new peak for spent catalyst which can be linked with metal oxides. Moreover, various reaction conditions of temperature (230, 400, and 600 °C), pressure (1 and 7 bar), and feed molar ratio of H2/CO2 (2:1 and 4:1) were investigated using different Cu loading (0, 1, 1.25, 1.62, and 4 weight percent). A maximum CO2 conversion of 63% with 39% CH4 selectivity was achieved by using Cu1.62-K0.5/Al2O3 at 600 °C, molar ratio of H2/CO2 4 under 7 bar. The presence of K on the surface of synthesized catalyst increased the CO2 conversion from 48% (Cu1/Al2O3) to 55% (Cu1-K0.5/Al2O3) at above mentioned reaction conditions which suggested the promoter effect of K during conversion of carbon dioxide.
AB - A series of Cu-K/Al2O3 catalysts were synthesized by wet impregnation technique. The reduced catalysts were further used for conversion of carbon dioxide to methane and carbon monoxide. Moreover, the fresh and used catalysts were characterized to investigate the changes in the surface morphology, metal dispersion, surface area, crystalline phases, and functional groups of studied catalysts. The SEM analysis of fresh and spent catalysts showed no remarkable difference in surface morphology with irregular shaped agglomerated particles. Furthermore, TEM micrographs presented the well distribution of metal catalyst over alumina support. The decrease in surface area from 115 to 77 m2/g for Cu1.62-K0.5/Al2O3 after reaction was related to sintering and oxidation of catalyst during reaction. XRD revealed the disappearance of some minor peaks which can be associated with the sintering of spent catalyst. FTIR also presented some new peak for spent catalyst which can be linked with metal oxides. Moreover, various reaction conditions of temperature (230, 400, and 600 °C), pressure (1 and 7 bar), and feed molar ratio of H2/CO2 (2:1 and 4:1) were investigated using different Cu loading (0, 1, 1.25, 1.62, and 4 weight percent). A maximum CO2 conversion of 63% with 39% CH4 selectivity was achieved by using Cu1.62-K0.5/Al2O3 at 600 °C, molar ratio of H2/CO2 4 under 7 bar. The presence of K on the surface of synthesized catalyst increased the CO2 conversion from 48% (Cu1/Al2O3) to 55% (Cu1-K0.5/Al2O3) at above mentioned reaction conditions which suggested the promoter effect of K during conversion of carbon dioxide.
KW - Carbon monoxide
KW - Catalyst synthesis
KW - Catalytic hydrogenation
KW - CO conversion
KW - Methane
KW - Operating conditions effect
UR - http://www.scopus.com/inward/record.url?scp=85071916206&partnerID=8YFLogxK
U2 - 10.1080/00986445.2019.1631815
DO - 10.1080/00986445.2019.1631815
M3 - Article
AN - SCOPUS:85071916206
SN - 0098-6445
VL - 207
SP - 946
EP - 960
JO - Chemical Engineering Communications
JF - Chemical Engineering Communications
IS - 7
ER -