Affiliations 

  • 1 College of Engineering at Wadi Addawaser, Prince Sattam Bin Abdulaziz University, Saudi Arabia; Electrical Engineering Department, Faculty of Engineering, Minia University, Egypt. Electronic address: hegazy.hussien@mu.edu.eg
  • 2 College of Engineering at Wadi Addawaser, Prince Sattam Bin Abdulaziz University, Saudi Arabia; Computers and Automatic Control Engineering Department, Faculty of Engineering, Tanta University, Egypt
  • 3 Department of Sustainable and Renewable Energy Engineering, University of Sharjah, Sharjah, United Arab Emirates
  • 4 Chemical Engineering Department, Faculty of Engineering, Minia University, Egypt; Center for Advanced Materials Research, University of Sharjah, PO Box 27272, Sharjah, United Arab Emirates
  • 5 Department of Chemical Engineering, Universiti Teknologi PETRONAS, Bander Seri Iskander, Malaysia; Department of Chemical Engineering, University of Gujrat, Gujrat, Pakistan
  • 6 Department of Sustainable and Renewable Energy Engineering, University of Sharjah, Sharjah, United Arab Emirates; Mechanical Engineering and Design, Aston University, School of Engineering and Applied Science, Aston Triangle, Birmingham, B4 7ET, United Kingdom. Electronic address: aolabi@sharjah.ac.ae
Sci Total Environ, 2019 Mar 25;658:1150-1160.
PMID: 30677979 DOI: 10.1016/j.scitotenv.2018.12.284

Abstract

Fossil fuel depletion and the environmental concerns have been under discussion for energy production for many years and finding new and renewable energy sources became a must. Biomass is considered as a net zero CO2 energy source. Gasification of biomass for H2 and syngas production is an attractive process. The main target of this research is to improve the production of hydrogen and syngas from palm kernel shell (PKS) steam gasification through defining the optimal operating parameters' using a modern optimization algorithm. To predict the gaseous outputs, two PKS models were built using fuzzy logic based on the experimental data sets. A radial movement optimizer (RMO) was applied to determine the system's optimal operating parameters. During the optimization process, the decision variables were represented by four different operating parameters. These parameters include; temperature, particle size, CaO/biomass ratio and coal bottom ash (CBA) with their operating ranges of (650-750 °C), (0.5-1 mm), (0.5-2) and wt% (0.02-0.10), respectively. The individual and interactive effects of different combinations were investigated on the production of H2 and syngas yield. The optimized results were compared with experimental data and results obtained from Response Surface Methodology (RSM) reported in literature. The obtained optimal values of the operating parameters through RMO were found 722 °C, 0.92 mm, 1.72 and 0.06 wt% for the temperature, particle size, CaO/biomass ratio and coal bottom ash, respectively. The results showed that syngas production was significantly improved as it reached 65.44 vol% which was better than that obtained in earlier studies.

* Title and MeSH Headings from MEDLINE®/PubMed®, a database of the U.S. National Library of Medicine.