• Title of article

    Comparison of combustion and pyrolysis for energy generation in a sugarcane mill

  • Author/Authors

    Nsaful، نويسنده , , F. and Gِrgens، نويسنده , , J.F. and Knoetze، نويسنده , , J.H.، نويسنده ,

  • Issue Information
    روزنامه با شماره پیاپی سال 2013
  • Pages
    11
  • From page
    524
  • To page
    534
  • Abstract
    The study focusses on the comparison of biomass to energy conversion process (BMECP) models to convert sugar mill biomass (bagasse) into energy products via combustion and pyrolysis as thermochemical pathways. Bagasse was converted to steam and electricity via combustion using 40 bar, 63 bar and 82 bar Condensing Extraction Steam Turbines (CEST) systems and a 30 bar back pressure steam turbine (BPST) system. Two BMECPs, namely partial fast pyrolysis and pure fast pyrolysis systems, were modeled for the pyrolysis pathway. In the Pure Fast Pyrolysis BMECP all the input bagasse stream was converted to pyrolysis products, with subsequent combustion of some of these products to generate steam and electricity for sugar mill operations. In the partial fast pyrolysis BMECP, a fraction of the bagasse is combusted directly to supply steam and electricity to the sugar mill, while the remaining fraction is pyrolyzed to generate pyrolysis products. All process models were simulated in AspenPlus® and were assessed on their ability to supply the energy requirement of to two sugar mill scenarios: More efficient mill and less efficient mill. The economic viability of BMECPs was determined using Aspen Process Economic Analyzer. Both combustion based and pyrolysis based BMECPs were capable of meeting the energy requirement of the sugar mill, although the pyrolysis based BMECP had limited steam and electricity production rates due to the accumulation of energy in pyrolysis products. High energy valued pyrolysis products resulted in higher overall process efficiencies of 85.09% and 87.65% for partial fast pyrolysis and Pure Fast Pyrolysis BMECPs respectively compared to 77.48% for the most efficient combustion BMECP (82 bar CEST). CO2 savings were higher for the pyrolysis based BMECPs due to the sequestration of carbon in pyrolysis products. The 63 bar CEST combustion system was the most economic viable option, while the Pure Fast Pyrolysis BMECP was the least viable. The increased energy efficiency and environmental benefits of pyrolysis-based processes are therefore off-set by increases in production costs.
  • Keywords
    COMBUSTION , Pyrolysis , process modeling , economic modeling , BIOMASS
  • Journal title
    Energy Conversion and Management
  • Serial Year
    2013
  • Journal title
    Energy Conversion and Management
  • Record number

    2337005