2019
DOI: 10.1007/s00449-019-02102-z
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Application of process system engineering tools to the fed-batch production of poly(3-hydroxybutyrate-co-3-hydroxyvalerate) from a vinasses–molasses Mixture

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Cited by 17 publications
(20 citation statements)
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“…The differences obtained in the calculated feeding profiles influence the polymer obtained, not only in terms of polymer concentration but also in terms of thermo-mechanical properties. 31 The substrate control law applied, for most of the time, the highest feed flow rate in order to keep the substrate concentration at 23 g/L. On the other hand, the combined-oriented optimization applied a high feed flow rate during the first process stage (where X t (t) < X trh ), but then, during the second stage, the feeding policy changed and the feed flow rate was kept at low values.…”
Section: Resultsmentioning
confidence: 99%
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“…The differences obtained in the calculated feeding profiles influence the polymer obtained, not only in terms of polymer concentration but also in terms of thermo-mechanical properties. 31 The substrate control law applied, for most of the time, the highest feed flow rate in order to keep the substrate concentration at 23 g/L. On the other hand, the combined-oriented optimization applied a high feed flow rate during the first process stage (where X t (t) < X trh ), but then, during the second stage, the feeding policy changed and the feed flow rate was kept at low values.…”
Section: Resultsmentioning
confidence: 99%
“…Although the attained productivity (0.364 g/L h) is low, it is around 35% higher than previously reported values for PHA production from a similar vinasses-molasses mixture at 5 L-scale. 31 Furthermore, in a complete review, Blunt et al 44 mentioned that the highest volumetric PHA productivity reported in the open literature (using sucrose as substrate at 6.6 L scale) is 5.1 g/L h (reported by Wang and Lee 45 Since then, similar results have not been reported on a scale of more than 100 L. According to the authors in their review, it was found that more recently, fed-batch and cyclic (batch and fedbatch) bioreactor operation strategies have reported productivities of 1 g/L h to 2 g/ L h under more realistic conditions for pilot or industrial-scale production (i.e. including the utilization of lower-cost waste carbon substrates and atmospheric air as aeration medium).…”
Section: Resultsmentioning
confidence: 99%
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