2011
DOI: 10.1021/ie200534n
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Estimating Specific Chemical Exergy of Biomass from Basic Analysis Data

Abstract: Estimation of chemical exergy of biomass is one of the basic steps in performance analysis and optimization of biomass conversion systems. A practical method for estimating specific chemical exergy of biomass on dry basis (db) from basic analysis data was developed on Szargut's reference environment model. The method is based on exergy and entropy equations of reaction, Gibbs free energy relations, a modified estimation of the standard entropy of organic matter in biomass and an assumption about original state… Show more

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Cited by 119 publications
(42 citation statements)
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“…The specific chemical exergy, ex ch depends on the chemical composition of a substance in its particular state, and if it is in equilibrium with the reference environment [28]. For solid fuels, the specific chemical exergy can be estimated based on the elemental compositions of the fuel [29][30][31][32][33][34][35][36][37].…”
Section: Exergy Analysismentioning
confidence: 99%
“…The specific chemical exergy, ex ch depends on the chemical composition of a substance in its particular state, and if it is in equilibrium with the reference environment [28]. For solid fuels, the specific chemical exergy can be estimated based on the elemental compositions of the fuel [29][30][31][32][33][34][35][36][37].…”
Section: Exergy Analysismentioning
confidence: 99%
“…According to the results suggested by Song et al [56], exergy flow related to the biomass used by the boiler is:…”
Section: Biomass Heatermentioning
confidence: 99%
“…The exergy received, Ex b , and delivered, Exu b , by the biomass boiler are determined from, (7) (8) where e CH is the chemical exergy of dry biomass; estimates for a variety of feedstocks are given in [31].…”
Section: 1mentioning
confidence: 99%
“…(29) where A r is the receiver's absorber area and C p is the specific heat capacity of the HTF. The useful heat gain, Q u , is determined from: (30) where, (31) and T in and T a are the receiver inlet temperature and ambient temperature. The fluid temperature rise, ∆T, for a given mass flow rate is calculated from: (32) The receiver sections which act as a pre-heater, evaporator and boiler have to be treated individually.…”
Section: 2mentioning
confidence: 99%