Technoeconomic analysis of a fungal pretreatment-based cellulosic ethanol production

Cellulosic biomass shows great potential as feedstock for bioethanol production. Despite clear benefits in terms of greenhouse gas mitigation and bioproduct potential, the commercial production of cellulosic ethanol remains economically challenging at the current state of technology. This paper pres...

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Main Authors: Onu Onu Olughu, Lope G. Tabil, Tim Dumonceaux, Edmund Mupondwa, Duncan Cree, Xue Li
Format: Article
Language:English
Published: Elsevier 2023-09-01
Series:Results in Engineering
Subjects:
Online Access:http://www.sciencedirect.com/science/article/pii/S2590123023003869
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author Onu Onu Olughu
Lope G. Tabil
Tim Dumonceaux
Edmund Mupondwa
Duncan Cree
Xue Li
author_facet Onu Onu Olughu
Lope G. Tabil
Tim Dumonceaux
Edmund Mupondwa
Duncan Cree
Xue Li
author_sort Onu Onu Olughu
collection DOAJ
description Cellulosic biomass shows great potential as feedstock for bioethanol production. Despite clear benefits in terms of greenhouse gas mitigation and bioproduct potential, the commercial production of cellulosic ethanol remains economically challenging at the current state of technology. This paper presents a technoeconomic analysis of a fungal pretreatment-based cellulosic ethanol plant with a processing capacity of 2000 tonnes of switchgrass per day. The production process model was designed and simulated using SuperPro Designer. The plant's ethanol yield, capital investment per unit capacity, and unit ethanol production cost were estimated to be 211.90 L/t of switchgrass, $ 3.60/L, and $ 1.44/L of ethanol, respectively. Fungal pretreatment was the major contributor (72%) to the total capital investment, mainly due to the large quantity of equipment required in the process. A positive net present value (NPV) was generated for the baseline model at ethanol selling price of $ 1.50/L, which increased by 5-fold for 80% glucose yield. Glucose yield was the most sensitive to NPV for all the process parameters evaluated.
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spelling doaj.art-dc5bc682bb6447fcac680fadaa2c14662023-09-18T04:30:33ZengElsevierResults in Engineering2590-12302023-09-0119101259Technoeconomic analysis of a fungal pretreatment-based cellulosic ethanol productionOnu Onu Olughu0Lope G. Tabil1Tim Dumonceaux2Edmund Mupondwa3Duncan Cree4Xue Li5Department of Chemical and Biological Engineering, University of Saskatchewan, 57 Campus Drive, Saskatoon, SK, S7N 5A9, Canada; Corresponding author.Department of Chemical and Biological Engineering, University of Saskatchewan, 57 Campus Drive, Saskatoon, SK, S7N 5A9, Canada; Corresponding author.Agriculture and Agri-Food Canada, Saskatoon Research Centre, 107 Science Place, Saskatoon, SK, S7N 0X2, CanadaDepartment of Chemical and Biological Engineering, University of Saskatchewan, 57 Campus Drive, Saskatoon, SK, S7N 5A9, Canada; Agriculture and Agri-Food Canada, Saskatoon Research Centre, 107 Science Place, Saskatoon, SK, S7N 0X2, CanadaDepartment of Mechanical Engineering, University of Saskatchewan, 57 Campus Drive, Saskatoon, SK, S7N 5A9, CanadaAgriculture and Agri-Food Canada, Saskatoon Research Centre, 107 Science Place, Saskatoon, SK, S7N 0X2, CanadaCellulosic biomass shows great potential as feedstock for bioethanol production. Despite clear benefits in terms of greenhouse gas mitigation and bioproduct potential, the commercial production of cellulosic ethanol remains economically challenging at the current state of technology. This paper presents a technoeconomic analysis of a fungal pretreatment-based cellulosic ethanol plant with a processing capacity of 2000 tonnes of switchgrass per day. The production process model was designed and simulated using SuperPro Designer. The plant's ethanol yield, capital investment per unit capacity, and unit ethanol production cost were estimated to be 211.90 L/t of switchgrass, $ 3.60/L, and $ 1.44/L of ethanol, respectively. Fungal pretreatment was the major contributor (72%) to the total capital investment, mainly due to the large quantity of equipment required in the process. A positive net present value (NPV) was generated for the baseline model at ethanol selling price of $ 1.50/L, which increased by 5-fold for 80% glucose yield. Glucose yield was the most sensitive to NPV for all the process parameters evaluated.http://www.sciencedirect.com/science/article/pii/S2590123023003869Cellulosic ethanolFungal pretreatmentSwitchgrassTechnoeconomic analysisNet present value
spellingShingle Onu Onu Olughu
Lope G. Tabil
Tim Dumonceaux
Edmund Mupondwa
Duncan Cree
Xue Li
Technoeconomic analysis of a fungal pretreatment-based cellulosic ethanol production
Results in Engineering
Cellulosic ethanol
Fungal pretreatment
Switchgrass
Technoeconomic analysis
Net present value
title Technoeconomic analysis of a fungal pretreatment-based cellulosic ethanol production
title_full Technoeconomic analysis of a fungal pretreatment-based cellulosic ethanol production
title_fullStr Technoeconomic analysis of a fungal pretreatment-based cellulosic ethanol production
title_full_unstemmed Technoeconomic analysis of a fungal pretreatment-based cellulosic ethanol production
title_short Technoeconomic analysis of a fungal pretreatment-based cellulosic ethanol production
title_sort technoeconomic analysis of a fungal pretreatment based cellulosic ethanol production
topic Cellulosic ethanol
Fungal pretreatment
Switchgrass
Technoeconomic analysis
Net present value
url http://www.sciencedirect.com/science/article/pii/S2590123023003869
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AT timdumonceaux technoeconomicanalysisofafungalpretreatmentbasedcellulosicethanolproduction
AT edmundmupondwa technoeconomicanalysisofafungalpretreatmentbasedcellulosicethanolproduction
AT duncancree technoeconomicanalysisofafungalpretreatmentbasedcellulosicethanolproduction
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