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Optimization Study of Syngas Production from Catalytic Air Gasification of Rice Husk

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@article{IJASEIT9906,
   author = {Adrian Chun Minh Loy and Suzana Yusup and Bing Shen How and Yi Herng Chan and Bridgid Lai Fui Chin and Azry Borhan and Huei Yeong Lim},
   title = {Optimization Study of Syngas Production from Catalytic Air Gasification of Rice Husk},
   journal = {International Journal on Advanced Science, Engineering and Information Technology},
   volume = {10},
   number = {5},
   year = {2020},
   pages = {1784--1791},
   keywords = {catalytic air gasification; optimization; syngas production.},
   abstract = {Catalytic air gasification of rice husk was investigated in this study to optimize the hydrogen and syngas composition using a thermogravimetric analyzer coupled with a mass spectrometer. Then, a fixed bed reactor is used as a pilot plant to evaluate the practicality of the optimum parameters obtained from thermogravimetric analyzer test for upscaling. The catalyst used is coal bottom ash selected based on a previous study and obtained from a local power plant. The results from thermogravimetric analyzer test had shown that the optimum input parameters for syngas composition were at a reaction temperature of 900 ˚C, rice husk particle size of 250 µm, amounts of catalyst of 10 wt%, and air to biomass ratio of 1.25 to obtain product gas with 73.8 vol% of syngas composition. From a fixed bed reactor, 76.2 vol% of syngas composition is obtained, 3.25% higher than the previous test. Furthermore, 84.1 wt% of gaseous product yield, included syngas and CH4, was obtained in the catalytic air gasification using a coal bottom ash catalyst. This showed the potential of coal bottom ash as the substitute for commercial catalysts in catalytic gasification. Lastly, principle component analysis was applied to evaluate the effect of temperature, particle size, air to biomass ratio, and coal bottom ash loading on H2 and syngas production. H2 production appears to be highly sensitive to the reaction temperature. Meanwhile, particle size, air to biomass ratio and catalyst loading were having a positive correlation with CO2 and CH4 but negative correlation with H2.},
   issn = {2088-5334},
   publisher = {INSIGHT - Indonesian Society for Knowledge and Human Development},
   url = {http://ijaseit.insightsociety.org/index.php?option=com_content&view=article&id=9&Itemid=1&article_id=9906},
   doi = {10.18517/ijaseit.10.5.9906}
}

EndNote

%A Chun Minh Loy, Adrian
%A Yusup, Suzana
%A Shen How, Bing
%A Herng Chan, Yi
%A Lai Fui Chin, Bridgid
%A Borhan, Azry
%A Yeong Lim, Huei
%D 2020
%T Optimization Study of Syngas Production from Catalytic Air Gasification of Rice Husk
%B 2020
%9 catalytic air gasification; optimization; syngas production.
%! Optimization Study of Syngas Production from Catalytic Air Gasification of Rice Husk
%K catalytic air gasification; optimization; syngas production.
%X Catalytic air gasification of rice husk was investigated in this study to optimize the hydrogen and syngas composition using a thermogravimetric analyzer coupled with a mass spectrometer. Then, a fixed bed reactor is used as a pilot plant to evaluate the practicality of the optimum parameters obtained from thermogravimetric analyzer test for upscaling. The catalyst used is coal bottom ash selected based on a previous study and obtained from a local power plant. The results from thermogravimetric analyzer test had shown that the optimum input parameters for syngas composition were at a reaction temperature of 900 ˚C, rice husk particle size of 250 µm, amounts of catalyst of 10 wt%, and air to biomass ratio of 1.25 to obtain product gas with 73.8 vol% of syngas composition. From a fixed bed reactor, 76.2 vol% of syngas composition is obtained, 3.25% higher than the previous test. Furthermore, 84.1 wt% of gaseous product yield, included syngas and CH4, was obtained in the catalytic air gasification using a coal bottom ash catalyst. This showed the potential of coal bottom ash as the substitute for commercial catalysts in catalytic gasification. Lastly, principle component analysis was applied to evaluate the effect of temperature, particle size, air to biomass ratio, and coal bottom ash loading on H2 and syngas production. H2 production appears to be highly sensitive to the reaction temperature. Meanwhile, particle size, air to biomass ratio and catalyst loading were having a positive correlation with CO2 and CH4 but negative correlation with H2.
%U http://ijaseit.insightsociety.org/index.php?option=com_content&view=article&id=9&Itemid=1&article_id=9906
%R doi:10.18517/ijaseit.10.5.9906
%J International Journal on Advanced Science, Engineering and Information Technology
%V 10
%N 5
%@ 2088-5334

IEEE

Adrian Chun Minh Loy,Suzana Yusup,Bing Shen How,Yi Herng Chan,Bridgid Lai Fui Chin,Azry Borhan and Huei Yeong Lim,"Optimization Study of Syngas Production from Catalytic Air Gasification of Rice Husk," International Journal on Advanced Science, Engineering and Information Technology, vol. 10, no. 5, pp. 1784-1791, 2020. [Online]. Available: http://dx.doi.org/10.18517/ijaseit.10.5.9906.

RefMan/ProCite (RIS)

TY  - JOUR
AU  - Chun Minh Loy, Adrian
AU  - Yusup, Suzana
AU  - Shen How, Bing
AU  - Herng Chan, Yi
AU  - Lai Fui Chin, Bridgid
AU  - Borhan, Azry
AU  - Yeong Lim, Huei
PY  - 2020
TI  - Optimization Study of Syngas Production from Catalytic Air Gasification of Rice Husk
JF  - International Journal on Advanced Science, Engineering and Information Technology; Vol. 10 (2020) No. 5
Y2  - 2020
SP  - 1784
EP  - 1791
SN  - 2088-5334
PB  - INSIGHT - Indonesian Society for Knowledge and Human Development
KW  - catalytic air gasification; optimization; syngas production.
N2  - Catalytic air gasification of rice husk was investigated in this study to optimize the hydrogen and syngas composition using a thermogravimetric analyzer coupled with a mass spectrometer. Then, a fixed bed reactor is used as a pilot plant to evaluate the practicality of the optimum parameters obtained from thermogravimetric analyzer test for upscaling. The catalyst used is coal bottom ash selected based on a previous study and obtained from a local power plant. The results from thermogravimetric analyzer test had shown that the optimum input parameters for syngas composition were at a reaction temperature of 900 ˚C, rice husk particle size of 250 µm, amounts of catalyst of 10 wt%, and air to biomass ratio of 1.25 to obtain product gas with 73.8 vol% of syngas composition. From a fixed bed reactor, 76.2 vol% of syngas composition is obtained, 3.25% higher than the previous test. Furthermore, 84.1 wt% of gaseous product yield, included syngas and CH4, was obtained in the catalytic air gasification using a coal bottom ash catalyst. This showed the potential of coal bottom ash as the substitute for commercial catalysts in catalytic gasification. Lastly, principle component analysis was applied to evaluate the effect of temperature, particle size, air to biomass ratio, and coal bottom ash loading on H2 and syngas production. H2 production appears to be highly sensitive to the reaction temperature. Meanwhile, particle size, air to biomass ratio and catalyst loading were having a positive correlation with CO2 and CH4 but negative correlation with H2.
UR  - http://ijaseit.insightsociety.org/index.php?option=com_content&view=article&id=9&Itemid=1&article_id=9906
DO  - 10.18517/ijaseit.10.5.9906

RefWorks

RT Journal Article
ID 9906
A1 Chun Minh Loy, Adrian
A1 Yusup, Suzana
A1 Shen How, Bing
A1 Herng Chan, Yi
A1 Lai Fui Chin, Bridgid
A1 Borhan, Azry
A1 Yeong Lim, Huei
T1 Optimization Study of Syngas Production from Catalytic Air Gasification of Rice Husk
JF International Journal on Advanced Science, Engineering and Information Technology
VO 10
IS 5
YR 2020
SP 1784
OP 1791
SN 2088-5334
PB INSIGHT - Indonesian Society for Knowledge and Human Development
K1 catalytic air gasification; optimization; syngas production.
AB Catalytic air gasification of rice husk was investigated in this study to optimize the hydrogen and syngas composition using a thermogravimetric analyzer coupled with a mass spectrometer. Then, a fixed bed reactor is used as a pilot plant to evaluate the practicality of the optimum parameters obtained from thermogravimetric analyzer test for upscaling. The catalyst used is coal bottom ash selected based on a previous study and obtained from a local power plant. The results from thermogravimetric analyzer test had shown that the optimum input parameters for syngas composition were at a reaction temperature of 900 ˚C, rice husk particle size of 250 µm, amounts of catalyst of 10 wt%, and air to biomass ratio of 1.25 to obtain product gas with 73.8 vol% of syngas composition. From a fixed bed reactor, 76.2 vol% of syngas composition is obtained, 3.25% higher than the previous test. Furthermore, 84.1 wt% of gaseous product yield, included syngas and CH4, was obtained in the catalytic air gasification using a coal bottom ash catalyst. This showed the potential of coal bottom ash as the substitute for commercial catalysts in catalytic gasification. Lastly, principle component analysis was applied to evaluate the effect of temperature, particle size, air to biomass ratio, and coal bottom ash loading on H2 and syngas production. H2 production appears to be highly sensitive to the reaction temperature. Meanwhile, particle size, air to biomass ratio and catalyst loading were having a positive correlation with CO2 and CH4 but negative correlation with H2.
LK http://ijaseit.insightsociety.org/index.php?option=com_content&view=article&id=9&Itemid=1&article_id=9906
DO  - 10.18517/ijaseit.10.5.9906