@article{scholars4158,
           title = {Syngas production from palm kernel shell and polyethylene waste blend in fluidized bed catalytic steam co-gasification process},
          volume = {75},
            note = {cited By 105},
             doi = {10.1016/j.energy.2014.04.062},
       publisher = {Elsevier Ltd},
         journal = {Energy},
           pages = {40--44},
            year = {2014},
            issn = {03605442},
          author = {Moghadam, R. A. and Yusup, S. and Uemura, Y. and Chin, B. L. F. and Lam, H. L. and Al Shoaibi, A.},
        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{\^A}oC, P/B ratio: 0.3 w/w and S/F ratio: 1 w/w, the total syngas yield and hydrogen yield achieved are 422.40g syngas/kg feedstock and 135.27g H2/kg feedstock, respectively. {\^A}{\copyright} 2014 Elsevier Ltd.},
        keywords = {Biomass; Design of experiments; Feedstocks; Fluidization; Fluidized bed process; Fluidized beds; Fossil fuel deposits; Gasification; Hydrogen; Hydrogen production; Polyethylenes, Catalytic steam gasifications; Energy; Energy from renewable sources; Fossil fuel resources; Optimized conditions; Syn-gas; Taguchi design of experiment; Thermo chemical process, Synthesis gas, catalysis; energy efficiency; gas production; optimization; reaction kinetics; temperature effect; thermochemistry; waste management},
             url = {https://www.scopus.com/inward/record.uri?eid=2-s2.0-84908059815&doi=10.1016\%2fj.energy.2014.04.062&partnerID=40&md5=1db86a7ebcf0db8bc1e3dd8c8bafc432}
}