Glycerol is a valuablefeedstock, produced in biorefineries asa byproduct of biodiesel production. Esterification of glycerol withacetic acid yields a mixture of mono-, di-, and triacetins. The acetinsare commercially important value-added products with a wide rangeof industrial applications as fuel additives and fine chemicals. Esterificationof glycerol to acetins substantially increases the environmental sustainabilityand economic viability of the biorefinery concept. Among the acetins,diacetin (DA) and triacetin (TA) are considered high-energy-densityfuel additives. Herein, we have studied the economic feasibility ofa facility producing DA and TA by a two-stage process using 100,000tons of glycerol per year using Aspen Plus. The capital costs wereestimated by Aspen Process Economic Analyzer software. The analysisindicates that the capital costs are 71 M$, while the operating costsare 303 M$/year. The gross profit is 60.5 M$/year, while the NPV ofthe project is 235 M$ with a payback period of 1.7 years. Sensitivityanalysis has indicated that the product price has the most impacton the NPV.

Techno-Economic Assessment and Sensitivity Analysis of Glycerol Valorization to Biofuel Additives via Esterification

Pandit K.;Artioli N.;
2023-01-01

Abstract

Glycerol is a valuablefeedstock, produced in biorefineries asa byproduct of biodiesel production. Esterification of glycerol withacetic acid yields a mixture of mono-, di-, and triacetins. The acetinsare commercially important value-added products with a wide rangeof industrial applications as fuel additives and fine chemicals. Esterificationof glycerol to acetins substantially increases the environmental sustainabilityand economic viability of the biorefinery concept. Among the acetins,diacetin (DA) and triacetin (TA) are considered high-energy-densityfuel additives. Herein, we have studied the economic feasibility ofa facility producing DA and TA by a two-stage process using 100,000tons of glycerol per year using Aspen Plus. The capital costs wereestimated by Aspen Process Economic Analyzer software. The analysisindicates that the capital costs are 71 M$, while the operating costsare 303 M$/year. The gross profit is 60.5 M$/year, while the NPV ofthe project is 235 M$ with a payback period of 1.7 years. Sensitivityanalysis has indicated that the product price has the most impacton the NPV.
2023
PE7_3 Simulation engineering and modelling
PE8_15 Industrial biofuel production
PE8_2 Chemical engineering, technical chemistry
Inglese
Internazionale
62
23
9201
9210
10
Glycerol Valorization, Aspen Plus, biodiesel production, Techno-Economic Assessment
https://pubs.acs.org/doi/10.1021/acs.iecr.3c00964?ref=pdf
Goal 13: Climate action
Goal 7: Affordable and clean energy
Goal 12: Responsible consumption and production
Goal 11: Sustainable cities and communities
6
info:eu-repo/semantics/article
262
Pandit, K.; Jeffrey, C.; Keogh, J.; Tiwari, M. S.; Artioli, N.; Manyar, H.
1 Contributo su Rivista::1.1 Articolo in rivista
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/11379/580945
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