4.4 Article

Harvesting of Microalgae Biomass Using Ceramic Microfiltration at High Cross-Flow Velocity

Journal

APPLIED BIOCHEMISTRY AND BIOTECHNOLOGY
Volume 193, Issue 4, Pages 1147-1169

Publisher

SPRINGER
DOI: 10.1007/s12010-020-03455-y

Keywords

Microalgae harvesting; Chlorella vulgaris; Cross-flow microfiltration; Alumina membrane; Tangential velocity; Fouling mechanisms

Funding

  1. French Embassy in Cote d'Ivoire
  2. Centre International de Recherche Agronomique pour le Developpement (CIRAD)

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This study investigated the use of ceramic membrane microfiltration for harvesting microalgae at relatively high cross-flow velocity, showing it to be a suitable option for certain microalgae such as Chlorella vulgaris. Different algal suspensions were tested to understand the impact of feedstock characteristics on permeation flux and resistance mechanisms. The results suggest that the process can achieve high permeation fluxes with varying contributions from cake resistance and pore adsorption/blocking, depending on the algal species.
This study aimed to investigate the harvesting of microalgae by microfiltration (MF) on a ceramic membrane at relatively high cross-flow velocity (CFV) of interest for commercial processes. Pilot-scale harvesting was conducted with algal suspensions (Chlorella vulgaris and Tisochrysis lutea (T-Iso)) and algal supernatants (Porphyridium cruentum) to assess the effect of feedstock characteristics and understand flux decline mechanisms. In total recycle mode (C. vulgaris, 1 g/L), high steady-state permeation flux around 200 L/m(2)/h was achieved. Total filtration resistance was mainly due to cake resistance (R-c, 57%) and pore adsorption and blocking (R-a, 40%). The process hydrodynamic conditions seemed to have relatively little effect on Chlorella cell integrity. In concentration mode, average permeate flux decreased from 441 to 73 L/m(2)/h with increasing feed concentration (C. vulgaris, 0.25-1 g/L); the contribution of R-c decreased (82 to 57%), while that of R-a rose (7 to 40%). With T-Iso suspensions and P. cruentum supernatants at 1 g/L, average permeate flux was 59 and 49 L/m(2)/h, respectively, with predominance of R-c and R-a, respectively. Distinct fouling mechanisms were inferred to explain the superior filterability of C. vulgaris. The results show that ceramic membrane MF at relatively high CFV could be a suitable option for harvesting certain microalgae including C. vulgaris.

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