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Techno‐economic analysis of a production‐scale torrefaction system for cellulosic biomass upgrading
Author(s) -
Shah Ajay,
Darr Matthew J.,
Medic Dorde,
Anex Robert P.,
Khanal Sami,
Maski Dev
Publication year - 2011
Publication title -
biofuels, bioproducts and biorefining
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.931
H-Index - 83
eISSN - 1932-1031
pISSN - 1932-104X
DOI - 10.1002/bbb.336
Subject(s) - torrefaction , raw material , biomass (ecology) , environmental science , cellulosic ethanol , water content , pulp and paper industry , capital cost , waste management , moisture , process engineering , materials science , engineering , chemistry , agronomy , pyrolysis , cellulose , geotechnical engineering , electrical engineering , organic chemistry , chemical engineering , composite material , biology
Torrefaction of biomass early in the supply chain is one method of enhancing or preservin biomass quality during storage; reducing storage and transportation costs; attaining uniformity among different feedstock types; and meeting biorefineries' quality and quantity demands for feedstock in a cost effective and sustainable manner. The main objectives of this study were to analyze the mass and energy balance, to assess the techno‐economic feasibility of a production‐scale torrefaction system, and to quantify the sensitivity of energy and cost results to changes in initial feedstock moisture content, torrefaction process temperature, plant operating window, and initial capital investment. The output from this analysis provides clear guidance on the opportunities and costs associated with production‐scale torrefaction of biomass as a feedstock intermediate. Analysis of energy results indicated that the net external energy required for the torrefaction process increased and energy efficiency of the torrefaction system decreased with increasing moisture contents. However, both of these energy metrics exhibited a decreasing trend with increasing process temperatures. In addition to the energy results, unit torrefaction process cost exhibited a decreasing trend with decreasing initial moisture contents of feedstock and decreasing torrefaction process temperatures. For the typical moisture content of 30% wb , process temperature of 240°C, plant operating window of 6 mo.yr ‐1 and initial capital investment of $7.5 million for the system with rated capacity of 25 Tton.hr ‐1 , unit torrefaction process cost was estimated to be 17.5 $‐Tton ‐1 . Additional system improvements through capital cost reduction and wider operating windows can yield a torrefaction product cost of ∼12 $‐Tton ‐1 . © 2011 Society of Chemical Industry and John Wiley & Sons, Ltd

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