| Home > Publications database > Re-evaluating 2-heptanol as solvent for the extraction of 2,3-butanediol from water > print |
| 001 | 1052061 | ||
| 005 | 20260120203626.0 | ||
| 024 | 7 | _ | |a 10.1016/j.cep.2025.110591 |2 doi |
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| 100 | 1 | _ | |a Graf von Westarp, William |0 0000-0002-6137-8942 |b 0 |
| 245 | _ | _ | |a Re-evaluating 2-heptanol as solvent for the extraction of 2,3-butanediol from water |
| 260 | _ | _ | |a Amsterdam [u.a.] |c 2026 |b Elsevier |
| 336 | 7 | _ | |a article |2 DRIVER |
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| 520 | _ | _ | |a The performance of an extraction-distillation process for separating 2,3-butanediol from H2O was evaluated in a recent study, finding high efficeincy when using 2-heptanol as solvent for extraction. Since the study was based on liquid-liquid equilibrium (LLE) data mainly derived from molecular simulations, the aim of this communication was to consolidate the database by providing experimental phase equilibrium data and to re-evaluate 2-heptanol as solvent. Based on LLE experiments, a solvent-to-feed ratio (S/F) of 3.175 was required to recover 95 % of 2,3-BDO in a counter-current extraction column. This S/F is 21.9 times higher than the estimation derived from the data based on molecular simulations. The high S/F results in a strong dilution of 2,3-BDO in the extract. Experimental investigation of the boiling point data of the 2,3-BDO – 2-heptanol system for subsequent distillation revealed the presence of a temperature minimum azeotrope at low 2,3-BDO concentrations, which limits the feasibility of the overall process. Since the use of 2-heptanol as solvent is oftentimes referred to in the community of diol separation, the results presented in the work at hand are relevant to a broad readership. |
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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.cep.2025.110591 |g Vol. 219, p. 110591 - |0 PERI:(DE-600)2013149-5 |p 110591 - |t Chemical engineering and processing |v 219 |y 2026 |x 0255-2701 |
| 856 | 4 | _ | |u https://juser.fz-juelich.de/record/1052061/files/1-s2.0-S0255270125004374-main.pdf |y OpenAccess |
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