A Technoeconomic Platform for Early-Stage Process Design and Cost Estimation of Joint Fermentative‒Catalytic Bioprocessing

dc.contributor.author Viswanathan, Mothi
dc.contributor.author Shanks, Brent
dc.contributor.author Raman, D. Raj
dc.contributor.author Rosentrater, Kurt
dc.contributor.department NSF Engineering Research Center for Biorenewable Chemicals
dc.contributor.department Department of Food Science and Human Nutrition (CALS)
dc.contributor.department Center for Crops Utilization Research
dc.contributor.department Department of Chemical and Biological Engineering
dc.contributor.department Department of Agricultural and Biosystems Engineering (ENG)
dc.contributor.department Biorenewable Resources and Technology
dc.contributor.department Environmental Science
dc.contributor.department Sustainable Agriculture
dc.contributor.department Center for Bioplastics and Biocomposites
dc.contributor.department Center for Biorenewable Chemicals
dc.date 2020-02-25T18:35:12.000
dc.date.accessioned 2020-06-30T01:10:23Z
dc.date.available 2020-06-30T01:10:23Z
dc.date.copyright Wed Jan 01 00:00:00 UTC 2020
dc.date.issued 2020-02-16
dc.description.abstract <p>Technoeconomic analyses using established tools such as SuperPro Designer<sup>®</sup> require a level of detail that is typically unavailable at the early stage of process evaluation. To facilitate this, members of our group previously created a spreadsheet-based process modeling and technoeconomic platform explicitly aimed at joint fermentative‒catalytic biorefinery processes. In this work, we detail the reorganization and expansion of this model—ESTEA2 (Early State Technoeconomic Analysis, version 2), including detailed design and cost calculations for new unit operations. Furthermore, we describe ESTEA2 validation using ethanol and sorbic acid process. The results were compared with estimates from the literature, SuperPro Designer<sup>®</sup> (Version 8.5, Intelligen Inc., Scotch Plains, NJ, 2013), and other third-party process models. ESTEA2 can perform a technoeconomic analysis for a joint fermentative‒catalytic process with just 12 user-supplied inputs, which, when modeled in SuperPro Designer<sup>®</sup>, required approximately eight additional inputs such as equipment design configurations. With a reduced amount of user information, ESTEA2 provides results similar to those in the literature, and more sophisticated models (ca. 7%–11% different).</p>
dc.description.comments <p>This article is published as Viswanathan, Mothi Bharath, D. Raj Raman, Kurt A. Rosentrater, and Brent H. Shanks. "A Technoeconomic Platform for Early-Stage Process Design and Cost Estimation of Joint Fermentative‒Catalytic Bioprocessing." <em>Processes</em> 8, no. 2 (2020): 229. DOI: <a href="http://dx.doi.org/10.3390/pr8020229" target="_blank">10.3390/pr8020229</a>. Posted with permission.</p>
dc.format.mimetype application/pdf
dc.identifier archive/lib.dr.iastate.edu/cbe_pubs/414/
dc.identifier.articleid 1415
dc.identifier.contextkey 16646660
dc.identifier.s3bucket isulib-bepress-aws-west
dc.identifier.submissionpath cbe_pubs/414
dc.identifier.uri https://dr.lib.iastate.edu/handle/20.500.12876/13519
dc.language.iso en
dc.source.bitstream archive/lib.dr.iastate.edu/cbe_pubs/414/2020_ShanksBrent_TechnoeconomicPlatform.pdf|||Sat Jan 15 00:10:54 UTC 2022
dc.source.uri 10.3390/pr8020229
dc.subject.disciplines Bioresource and Agricultural Engineering
dc.subject.disciplines Catalysis and Reaction Engineering
dc.subject.keywords SuperPro
dc.subject.keywords early-stage
dc.subject.keywords process modeling
dc.subject.keywords cost analysis
dc.subject.keywords ethanol
dc.subject.keywords sorbic acid
dc.title A Technoeconomic Platform for Early-Stage Process Design and Cost Estimation of Joint Fermentative‒Catalytic Bioprocessing
dc.type article
dc.type.genre article
dspace.entity.type Publication
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