Energy from renewable source is expected to complement the energy derived from fossil fuel resources. Gasification is a versatile thermochemical process for solid waste fuel conversion. In the current paper, syngas production from palm kernel shell (PKS) and polyethylene waste blend in a catalytic steam gasification process is studied. In order to acquire the optimum condition of syngas production, the effect of main variables such as reaction temperature, steam/feedstock (S/F) ratio, polyethylene waste/biomass (P/B) ratio on syngas production was investigated and optimized via Taguchi design of experiment approach. Under the optimized condition of 800 C, P/B ratio: 0.3 w/w and S/F ratio: 1 w/w, the total syngas yield and hydrogen yield achieved are 422.40 g syngas/kg feedstock and 135.27 g H2/kg feedstock, respectively

Syngas production from palm kernel shell and polyethylene waste blend in fluidized bed catalytic steam co-gasification process / ALIPOUR MOGHADAM ESFAHANI, Reza; Suzana, Yusup; Yoshimitsu, Uemura; Bridgid Lai Fui, Chin; Hon Loong, Lam; Ahmed Al, Shoaibi. - In: ENERGY. - ISSN 0360-5442. - STAMPA. - 75:(2014), pp. 40-44. [10.1016/j.energy.2014.04.062]

Syngas production from palm kernel shell and polyethylene waste blend in fluidized bed catalytic steam co-gasification process

ALIPOUR MOGHADAM ESFAHANI, REZA;
2014

Abstract

Energy from renewable source is expected to complement the energy derived from fossil fuel resources. Gasification is a versatile thermochemical process for solid waste fuel conversion. In the current paper, syngas production from palm kernel shell (PKS) and polyethylene waste blend in a catalytic steam gasification process is studied. In order to acquire the optimum condition of syngas production, the effect of main variables such as reaction temperature, steam/feedstock (S/F) ratio, polyethylene waste/biomass (P/B) ratio on syngas production was investigated and optimized via Taguchi design of experiment approach. Under the optimized condition of 800 C, P/B ratio: 0.3 w/w and S/F ratio: 1 w/w, the total syngas yield and hydrogen yield achieved are 422.40 g syngas/kg feedstock and 135.27 g H2/kg feedstock, respectively
2014
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/11583/2565141
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