Techno-economic analysis of inulooligosaccharides, protein, and biofuel co-production from Jerusalem artichoke tubers: A biorefinery approach
Oscar K. K. Bedzo
Department of Process Engineering, Stellenbosch University, Stellenbosch, South Africa
Search for more papers by this authorCorresponding Author
Mohsen Mandegari
Department of Process Engineering, Stellenbosch University, Stellenbosch, South Africa
Correspondence to: Mohsen Mandegari, Department of Process Engineering, Stellenbosch University, Private Bag X1,
Stellenbosch 7602, South Africa. E-mail: mandegari@sun.ac.za
Search for more papers by this authorJohann F. Görgens
Department of Process Engineering, Stellenbosch University, Stellenbosch, South Africa
Search for more papers by this authorOscar K. K. Bedzo
Department of Process Engineering, Stellenbosch University, Stellenbosch, South Africa
Search for more papers by this authorCorresponding Author
Mohsen Mandegari
Department of Process Engineering, Stellenbosch University, Stellenbosch, South Africa
Correspondence to: Mohsen Mandegari, Department of Process Engineering, Stellenbosch University, Private Bag X1,
Stellenbosch 7602, South Africa. E-mail: mandegari@sun.ac.za
Search for more papers by this authorJohann F. Görgens
Department of Process Engineering, Stellenbosch University, Stellenbosch, South Africa
Search for more papers by this authorAbstract
Jerusalem artichoke (JA) is a crop with excellent potential for application in biorefineries. It can resist drought, pests, and diseases and can thrive well in marginal lands with little fertilizer application. The JA tubers contain considerable quantities of inulin, which is suitable for the production of inulooligosaccharides (IOS), as a high-value prebiotic, dietary fiber. In this study, five JA tuber biorefinery scenarios were simulated in Aspen Plus® and further evaluated by techno-economic and sensitivity analyses. Production of IOS, proteins and animal feed was studied in scenarios A and C, applying various biorefinery configurations. Scenario B explored the option of producing only IOS and the sale of residues as animal feed. Scenarios D and E investigated the economic potential of biofuel generation from residues after IOS and protein production by generation of biogas and ethanol respectively, from residues. Based on the chosen economic indicators, scenario B resulted in the lowest minimum selling price (MSP) of 3.91 US$ kg−1 (market price 5.0 US$ kg−1) with correspondingly reduced total capital investment (TCI) and total operating cost (TOC) per mass unit produced of IOS of 18.91 and 2.59 US$ kg−1 respectively, compared with other studied scenarios. Considering the set production scale, it is more profitable when the residues are sold as animal feed instead of being converted into biofuel, due to the capital-intensive nature of the biofuel production processes. The coproduction of protein had a negative impact on the economics of the process as the associated capital and operating expenditure outweighed the associated revenue. © 2020 Society of Chemical Industry and John Wiley & Sons, Ltd
Supporting Information
Filename | Description |
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bbb2105-sup-0001-Supinfo.docxWord 2007 document , 139.1 KB |
Table S1: Properties of the user-defined components used in the IOS production process Table S2: Stream table for scenario A Table S3: Stream table for scenario B Table S4: Stream table for scenario C Table S5: Summary of stream table for scenario D Table S6: Stream table for scenario E Table S7: Stream table for scenario E (Contd.) Table S8: IOS production, fermentation and anaerobic digestion reactions Table S9: Operating conditions, Aspen model specifications, sizing and costing of major equipment Table S10: Other, minor equipment unit information Table S11: Costing worksheet for estimation of capital investment |
Please note: The publisher is not responsible for the content or functionality of any supporting information supplied by the authors. Any queries (other than missing content) should be directed to the corresponding author for the article.
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