№ files_lp_4_process_2_43444
Peer-reviewed chemical engineering research article analyzing a simulated integrated plant design for the production of isopropanol and acetone from propylene, including process modelling, energy integration, and economic sensitivity evaluation.
Year: 2025
Journal: Chemical Engineering Transactions
Volume: xxx
Publisher: AIDIC Servizi S.r.l.
Organization: Italian Association of Chemical Engineering (AIDIC)
ISBN: 979-12-81206-17-5
ISSN: 2283-9216
Authors: Marco Vaccari; Federico Baglioni; Leonardo Zandó; Leonardo Tognotti
Affiliation: University of Pisa, Department of Civil and Industrial Engineering
Country of affiliation: Italy
Corresponding author: Marco Vaccari
Contact email: [email protected]
Academic field: Chemical Engineering
Research topic: Process simulation and integrated production of isopropanol and acetone
Software used: UniSim Design© R491
Feedstocks analyzed: Propylene; Water
Proposed plant location: Near Paradip refinery, India
Planned production capacity: 71.5 kton/year of isopropanol; 104.4 kton/year of acetone
Operating schedule: 335 days per year; 24 hours per day
Plant lifespan considered: 10 years
Key processes: Direct hydration of propylene; Extractive distillation of IPA–water azeotrope; Dehydrogenation of isopropanol to acetone
Economic analysis elements: Sensitivity analysis of feedstock prices, product prices, utility costs, and inflation rates
Price: 8 / 10 USD
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