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| Hauptseite > Publikationsdatenbank > Terpenoids as solvents for the separation of 2,3-butanediol from water: Phase equilibria and process evaluation > print |
| Hauptseite > Publikationsdatenbank > Terpenoids as solvents for the separation of 2,3-butanediol from water: Phase equilibria and process evaluation > print |
| 001 | 1052065 | ||
| 005 | 20260120203626.0 | ||
| 024 | 7 | _ | |a 10.1016/j.fluid.2025.114572 |2 doi |
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| 100 | 1 | _ | |a von Westarp, William Graf |0 0000-0002-6137-8942 |b 0 |
| 245 | _ | _ | |a Terpenoids as solvents for the separation of 2,3-butanediol from water: Phase equilibria and process evaluation |
| 260 | _ | _ | |a New York, NY [u.a.] |c 2026 |b Science Direct |
| 336 | 7 | _ | |a article |2 DRIVER |
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| 520 | _ | _ | |a 2,3-butanediol (2,3-BDO) is a versatile platform chemical that can be produced via fermentation in aqueous solution. The energy intensive recovery of the high boiling 2,3-BDO from water via distillation hinders the economic viability of biotechnological produced 2,3-BDO. Hence, extraction-distillation processes using novel solvents from the class of terpenoids, namely menthol, thymol, and carvacrol, are proposed. To this end, binary and ternary liquid-liquid equilibrium (LLE) data for H2O, 2,3-BDO, and each terpenoid, as well as boiling point data for 2,3-BDO and the respective terpenoid, are measured. The thermodynamic phase equilibria are correlated with the non-random two liquid (NRTL) model and consecutive process design of the extraction-distillation processes is conducted using Aspen Plus. Conventional solvents (isobutanol, 1-butanol, and oleylalcohol), thymol, and carvacrol are assessed in terms of specific exergy demand for the production of 2,3-BDO. The lowest specific exergy demands were found for oleyl alcohol (5.38 kJ g−1) and thymol (5.14 kJ g−1), carvacrol (5.49 kJ g−1). Hence, terpenoids are a competitive class of solvents and should be included in solvent screening approaches. |
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| 700 | 1 | _ | |a Hense, Janik |0 0000-0003-1570-6914 |b 1 |
| 700 | 1 | _ | |a Haas, Moritz |0 0000-0001-8610-1328 |b 2 |
| 700 | 1 | _ | |a Jupke, Andreas |0 P:(DE-Juel1)194474 |b 3 |e Corresponding author |
| 773 | _ | _ | |a 10.1016/j.fluid.2025.114572 |g Vol. 600, p. 114572 - |0 PERI:(DE-600)1483573-3 |p 114572 - |t Fluid phase equilibria |v 600 |y 2026 |x 0378-3812 |
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