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Junior MRDS, Costa EC, Ferreira CC, Bernar LP, da Silva MP, de Andrade Mâncio A, Santos MC, da Mota SAP, de Castro DAR, Junior SD, Borges LEP, Araújo ME, Machado NT. Simulation of Organic Liquid Product Deoxygenation through Multistage Countercurrent Absorber/Stripping Using CO2 as Solvent with Aspen-HYSYS: Process Modeling and Simulation. Molecules 2022; 27:molecules27072211. [PMID: 35408610 PMCID: PMC9000492 DOI: 10.3390/molecules27072211] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [MESH Headings] [Track Full Text] [Download PDF] [Figures] [Journal Information] [Subscribe] [Scholar Register] [Received: 12/30/2021] [Revised: 03/04/2022] [Accepted: 03/23/2022] [Indexed: 11/29/2022] Open
Abstract
In this work, the deoxygenation of organic liquid products (OLP) obtained through the thermal catalytic cracking of palm oil at 450 °C, 1.0 atmosphere, with 10% (wt.) Na2CO3 as a catalyst, in multistage countercurrent absorber columns using supercritical carbon dioxide (SC-CO2) as a solvent, with an Aspen-HYSYS process simulator, was systematically investigated. In a previous study, the thermodynamic data basis and EOS modeling necessary to simulate the deoxygenation of OLP was presented. This work addresses a new flowsheet, consisting of 03 absorber columns, 10 expansions valves, 10 flash drums, 08 heat exchanges, 01 pressure pump, and 02 make-ups of CO2, aiming to improve the deacidification of OLP. The simulation was performed at 333 K, 140 bar, and (S/F) = 17; 350 K, 140 bar, and (S/F) = 38; 333 K, 140 bar, and (S/F) = 25. The simulation shows that 81.49% of OLP could be recovered and that the concentrations of hydrocarbons in the extracts of absorber-01 and absorber-02 were 96.95 and 92.78% (wt.) on a solvent-free basis, while the bottom stream of absorber-03 was enriched in oxygenated compounds with concentrations of up to 32.66% (wt.) on a solvent-free basis, showing that the organic liquid products (OLP) were deacidified and SC-CO2 was able to deacidify the OLP and obtain fractions with lower olefin contents. The best deacidifying condition was obtained at 333 K, 140 bar, and (S/F) = 17.
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Affiliation(s)
- Manoel Raimundo Dos Santos Junior
- Graduate Program of Natural Resources Engineering of Amazon, Campus Profissional-UFPA, Rua Augusto Corrêa N° 1, Belém 66075-110, Brazil
| | - Elinéia Castro Costa
- Graduate Program of Natural Resources Engineering of Amazon, Campus Profissional-UFPA, Rua Augusto Corrêa N° 1, Belém 66075-110, Brazil
| | - Caio Campos Ferreira
- Graduate Program of Natural Resources Engineering of Amazon, Campus Profissional-UFPA, Rua Augusto Corrêa N° 1, Belém 66075-110, Brazil
| | - Lucas Pinto Bernar
- Graduate Program of Natural Resources Engineering of Amazon, Campus Profissional-UFPA, Rua Augusto Corrêa N° 1, Belém 66075-110, Brazil
| | - Marcilene Paiva da Silva
- Graduate Program of Chemical Engineering, Campus Profissional-UFPA, Rua Augusto Corrêa N° 1, Belém 66075-900, Brazil
| | - Andréia de Andrade Mâncio
- Graduate Program of Natural Resources Engineering of Amazon, Campus Profissional-UFPA, Rua Augusto Corrêa N° 1, Belém 66075-110, Brazil
| | - Marcelo Costa Santos
- Graduate Program of Chemical Engineering, Campus Profissional-UFPA, Rua Augusto Corrêa N° 1, Belém 66075-900, Brazil
| | - Sílvio Alex Pereira da Mota
- Graduate Program of Natural Resources Engineering of Amazon, Campus Profissional-UFPA, Rua Augusto Corrêa N° 1, Belém 66075-110, Brazil
| | - Douglas Alberto Rocha de Castro
- Graduate Program of Natural Resources Engineering of Amazon, Campus Profissional-UFPA, Rua Augusto Corrêa N° 1, Belém 66075-110, Brazil
| | - Sergio Duvoisin Junior
- Faculty of Chemical Engineering, Universidade do Estado do Amazonas-UEA, Avenida Darcy Vargas N° 1200, Manaus 69050-020, Brazil
| | - Luiz Eduardo Pizarro Borges
- Laboratory of Catalyst Preparation and Catalytic Cracking, Section of Chemical Engineering, Instituto Militar de Engenharia-IME, Praça General Tibúrcio N° 80, Rio de Janeiro 22290-270, Brazil
| | - Marilena Emmi Araújo
- Graduate Program of Chemical Engineering, Campus Profissional-UFPA, Rua Augusto Corrêa N° 1, Belém 66075-900, Brazil
| | - Nélio Teixeira Machado
- Graduate Program of Natural Resources Engineering of Amazon, Campus Profissional-UFPA, Rua Augusto Corrêa N° 1, Belém 66075-110, Brazil
- Faculty of Sanitary and Environmental Engineering, Campus Profissional-UFPA, Rua Augusto Corrêa N° 1, Belém 66075-110, Brazil
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Carvalho VS, Dias ALB, Rodrigues KP, Hatami T, Mei LHI, Martínez J, Viganó J. Supercritical fluid adsorption of natural extracts: Technical, practical, and theoretical aspects. J CO2 UTIL 2022. [DOI: 10.1016/j.jcou.2021.101865] [Citation(s) in RCA: 2] [Impact Index Per Article: 1.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 02/07/2023]
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Ueno Y, Hoshino Y, Ota M, Sato Y, Inomata H. Experiments and Simulation of Counter-Current Extraction (Subcritical Fluid Separation) by Supercritical CO 2 with Hops-Extract Ethanol Solution. KAGAKU KOGAKU RONBUN 2021. [DOI: 10.1252/kakoronbunshu.47.23] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/11/2022]
Affiliation(s)
- Yusuke Ueno
- Department of Chemical Engineering, Graduate school of Engineering, Tohoku University
| | - Yuki Hoshino
- Department of Chemical Engineering, Graduate school of Engineering, Tohoku University
| | - Masaki Ota
- Department of Chemical Engineering, Graduate school of Engineering, Tohoku University
- Department of Frontier Science for Advanced Environment, Graduate school of Environmental Studies, Tohoku University
| | - Yoshiyuki Sato
- Department of Chemical Engineering, Graduate school of Engineering, Tohoku University
- Department of Applied Chemistry and Environment, Tohoku Institute of Technology
| | - Hiroshi Inomata
- Department of Chemical Engineering, Graduate school of Engineering, Tohoku University
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Hoshino Y, Ueno Y, Ota M, Sato Y, Inomata H. Measurement and Correlation of Vapor–Liquid Distribution Coefficients of Compounds Contained in Hops-Extract Ethanol Solution with Supercritical CO 2. KAGAKU KOGAKU RONBUN 2021. [DOI: 10.1252/kakoronbunshu.47.17] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/11/2022]
Affiliation(s)
- Yuki Hoshino
- Department of Chemical Engineering, Graduate School of Engineering, Tohoku University
| | - Yusuke Ueno
- Department of Chemical Engineering, Graduate School of Engineering, Tohoku University
| | - Masaki Ota
- Department of Chemical Engineering, Graduate School of Engineering, Tohoku University
- Department of Frontier Science for Advanced Environment, Graduate School of Environmental Studies, Tohoku University
| | - Yoshiyuki Sato
- Department of Chemical Engineering, Graduate School of Engineering, Tohoku University
- Department of Applied Chemistry and Environment, Tohoku Institute of Technology
| | - Hiroshi Inomata
- Department of Chemical Engineering, Graduate School of Engineering, Tohoku University
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Zema DA, Calabrò PS, Folino A, Tamburino V, Zappia G, Zimbone SM. Valorisation of citrus processing waste: A review. WASTE MANAGEMENT (NEW YORK, N.Y.) 2018; 80:252-273. [PMID: 30455006 DOI: 10.1016/j.wasman.2018.09.024] [Citation(s) in RCA: 148] [Impact Index Per Article: 24.7] [Reference Citation Analysis] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 05/17/2018] [Revised: 07/28/2018] [Accepted: 09/12/2018] [Indexed: 06/09/2023]
Abstract
This study analyses the quantitative and qualitative characteristics of citrus peel waste and discusses the systems for its valorisation. Citrus peel waste (CPW) is the main residue of the citrus processing industries and is characterised by a seasonal production (which often requires biomass storage) as well as high water content and concentration of essential oils. The disposal of CPW has considerable constraints due to both economic and environmental factors. Currently this residue is mainly used as food for animals, thanks to its nutritional capacity. If enough agricultural land is available close to the processing industries, the use of CPW as organic soil conditioner or as substrate for compost production is also possible, thus improving the organic matter content of the soil. Recently, the possibility of its valorisation for biomethane or bioethanol production has been evaluated by several studies, but currently more research is needed to overcome the toxic effects of the essential oils on the microbial community. Considering the high added value of the compounds that can be recovered from CPW, it has promising potential uses: in the food industry (for production of pectin, dietary fibres, etc.), and in the cosmetic and pharmaceutic industries (extraction of flavonoids, flavouring agents and citric acid). However, in many cases, these uses are still not economically sustainable.
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Affiliation(s)
- D A Zema
- Department AGRARIA, Università Mediterranea di Reggio Calabria, loc. Feo di Vito, 89122 Reggio Calabria, Italy
| | - P S Calabrò
- Department of Civil, Energy, Environmental and Materials Engineering, Università Mediterranea di Reggio Calabria, via Graziella, loc. Feo di Vito, 89122 Reggio Calabria, Italy.
| | - A Folino
- Department AGRARIA, Università Mediterranea di Reggio Calabria, loc. Feo di Vito, 89122 Reggio Calabria, Italy
| | - V Tamburino
- Department AGRARIA, Università Mediterranea di Reggio Calabria, loc. Feo di Vito, 89122 Reggio Calabria, Italy
| | - G Zappia
- Department AGRARIA, Università Mediterranea di Reggio Calabria, loc. Feo di Vito, 89122 Reggio Calabria, Italy
| | - S M Zimbone
- Department AGRARIA, Università Mediterranea di Reggio Calabria, loc. Feo di Vito, 89122 Reggio Calabria, Italy
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Negro V, Mancini G, Ruggeri B, Fino D. Citrus waste as feedstock for bio-based products recovery: Review on limonene case study and energy valorization. BIORESOURCE TECHNOLOGY 2016; 214:806-815. [PMID: 27237574 DOI: 10.1016/j.biortech.2016.05.006] [Citation(s) in RCA: 67] [Impact Index Per Article: 8.4] [Reference Citation Analysis] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 02/06/2016] [Revised: 04/16/2016] [Accepted: 05/04/2016] [Indexed: 05/27/2023]
Abstract
The citrus peels and residue of fruit juices production are rich in d-limonene, a cyclic terpene characterized by antimicrobial activity, which could hamper energy valorization bioprocess. Considering that limonene is used in nutritional, pharmaceutical and cosmetic fields, citrus by-products processing appear to be a suitable feedstock either for high value product recovery or energy bio-processes. This waste stream, more than 10MTon at 2013 in European Union (AIJN, 2014), can be considered appealing, from the view point of conducting a key study on limonene recovery, as its content of about 1%w/w of high value-added molecule. Different processes are currently being studied to recover or remove limonene from citrus peel to both prevent pollution and energy resources recovery. The present review is aimed to highlight pros and contras of different approaches suggesting an energy sustainability criterion to select the most effective one for materials and energy valorization.
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Affiliation(s)
- Viviana Negro
- Department of Applied Science and Technology, Politecnico di Torino, Corso Duca degli Abruzzi 24, Torino 10129, Italy
| | - Giuseppe Mancini
- Department of Industrial Engineering, University of Catania, Viale A. Doria 6, Catania 95125, Italy
| | - Bernardo Ruggeri
- Department of Applied Science and Technology, Politecnico di Torino, Corso Duca degli Abruzzi 24, Torino 10129, Italy
| | - Debora Fino
- Department of Applied Science and Technology, Politecnico di Torino, Corso Duca degli Abruzzi 24, Torino 10129, Italy.
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