Crossflow microfiltration of fungal fermentation broths to obtain natural extracts

Autores/as

  • Azahara Linares Pérez BioflowSur S.L. Polígono Industrial el Florío, C/Industria nº 9, 18015. Granada
  • Abdelmounim Badih Akhrif BioflowSur S.L. Polígono Industrial el Florío, C/Industria nº 9, 18015. Granada
  • Mª Begoña Herrera Rodríguez Área de Fisiología Vegetal. Dpto. de Fisiología, Anatomía y Biología Celular. Universidad Pablo de Olavide Olavide, Carretera Utrera, km. 1, 41013. Sevilla
  • Juan J. Camacho Cristóbal Área de Fisiología Vegetal. Dpto. de Fisiología, Anatomía y Biología Celular. Universidad Pablo de Olavide Olavide, Carretera Utrera, km. 1, 41013. Sevilla

Palabras clave:

Crossflow filtration, ceramic membrane, fouling

Resumen

Motivation: One of the main milestones after developing a laboratory scale product is to transform the acquired knowledge into an economic production structure. The production of natural extracts in BioflowSur is carried out by using a fermentation process; then, natural extracts are separated from the fungus by vacuum filtration. However, this type of filtration is not feasible with large volumes so that the use of tangential microfiltration with membrane technology was studied.
Methods: The fungal fermentation broth was filtrated using a bench-scale crossflow filtration unit (Prozesstechnik GmbH) equipped with a ceramic membrane either of 0,2 μm pore diameter (with active layer) or 5-8 μm pore diameter (without active layer). Two modes of operation were used: concentration and diafiltration. In the first mode the product concentrates in small volumes and in the second mode water is added to facilitate the filtration [1].
Results: The diafiltration was discarded as mode of operation after the first test due to the generation of large volumes that complicate the subsequent extraction of the active principle. In addition, results reveal that the optimal temperature is 30ºC because higher temperatures facilitate the passage of residues to the permeate.
The concentration tests performed with the membrane of 0.2 μm showed that there was active principle in the concentrate and in the permeate, while the membrane of 5-8 μm allowed fungus to pass to the permeate after several rounds of filtration. In addition, the high pressures generated due to the fouling drastically reduced the flow and, hence, increased the time of the process [2].

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Publicado

2017-03-01

Cómo citar

(1)
Linares Pérez, A.; Badih Akhrif, A.; Herrera Rodríguez, M. B.; Camacho Cristóbal, J. J. Crossflow Microfiltration of Fungal Fermentation Broths to Obtain Natural Extracts. Bs 2017, 1.

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