AIChE Journal · 2008 · 167 citations · 13 references
Process IntegrationEngineeringBioenergyEnergy EfficiencyEnergy ConversionEnergy Systems EngineeringOptimal System DesignEnergy AnalysisHeat IntegrationEnergy OptimizationPlant DesignSystems EngineeringLinear OptimizationBiomass UtilizationEnergy ProductionEthanol ProductionEnergyEnergy CropEnergy ManagementHeat Integration Study
Capital cost, energy usage, and yields all contribute to production cost, influencing the viability of corn‑based ethanol as a sustainable fuel. The study aims to reduce operating costs of corn‑based ethanol plants through heat integration and mathematical programming. A mixed‑integer nonlinear programming model with short‑cut mass and energy balances and two nonlinear subproblems determines network connections and flows, followed by heat integration of multieffect distillation columns to further reduce energy consumption. The optimized design cuts steam consumption by more than 40 % compared to the initial basic design. © 2008 American Institute of Chemical Engineers AIChE J, 2008.
Abstract In this work, we address the problem of optimizing corn‐based bioethanol plants through the use of heat integration and mathematical programming techniques. The goal is to reduce the operating costs of the plant. Capital cost, energy usage, and yields—all contribute to production cost. Yield and energy usage also influence the viability of corn‐based ethanol as a sustainable fuel. We first propose a limited superstructure of alternative designs including the various process units and utility streams involved in ethanol production. Our objective is to determine the connections in the network and the flow in each stream in the network such that we minimize the energy requirement of the overall plant. This is accomplished through the formulation of a mixed‐integer nonlinear programming problem involving short‐cut models for mass and energy balances for all the units in the system, where the model is solved through two nonlinear programming subproblems. We then perform a heat integration study on the resulting flowsheet; the modified flowsheet includes multieffect distillation columns that further reduces energy consumption. The results indicate that it is possible to reduce the current steam consumption required in the transformation of corn into fuel grade ethanol by more than 40% compared to initial basic design. © 2008 American Institute of Chemical Engineers AIChE J, 2008
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