2021
DOI: 10.1016/j.jaap.2021.105157
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Techno-economic Assessment of Co-gasification of Rice Husk and Plastic Waste as an Off-grid Power Source for Small Scale Rice Milling - an Aspen Plus Model

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Cited by 59 publications
(22 citation statements)
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“…The HCOALGEN method includes different empirical correlations to estimate heat of combustion, enthalpy of formation and specific heat; whereas the DCOALIGT method is based on the empirical correlations from the Institute of Gas Technology (IGT) to estimate density. The most usual physical property methods reported in the literature for modeling gasification processes are PR-BM and RKS-BM [18,19,24,[32][33][34][35], both providing comparable results [36]. The Peng-Robinson cubic equation of state with Boston-Mathias alpha function (PR-BM) was used to estimate all the thermodynamic properties of the conventional components involved in the integrated process.…”
Section: Plant Description and Process Modelingmentioning
confidence: 99%
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“…The HCOALGEN method includes different empirical correlations to estimate heat of combustion, enthalpy of formation and specific heat; whereas the DCOALIGT method is based on the empirical correlations from the Institute of Gas Technology (IGT) to estimate density. The most usual physical property methods reported in the literature for modeling gasification processes are PR-BM and RKS-BM [18,19,24,[32][33][34][35], both providing comparable results [36]. The Peng-Robinson cubic equation of state with Boston-Mathias alpha function (PR-BM) was used to estimate all the thermodynamic properties of the conventional components involved in the integrated process.…”
Section: Plant Description and Process Modelingmentioning
confidence: 99%
“…• The integrated gasification plant is operating under steady-state conditions within a zero-dimensional and time independent approach where hydrodynamic effects are disregarded [14, 17-19, 24, 33-35, 37-39]. • Heat losses to the surrounding environment and pressure drops across all unit operations are neglected [19,24,[32][33][34][35][37][38][39]]. • All chemical reactions reach thermodynamic equilibrium conditions and reaction kinetics are not considered [14, 17-19, 24, 33-35, 37-39].…”
Section: Plant Description and Process Modelingmentioning
confidence: 99%
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