4.5 Article

Integration of poly-3-(hydroxybutyrate-co-hydroxyvalerate) production by Haloferax mediterranei through utilization of stillage from rice-based ethanol manufacture in India and its techno-economic analysis

Journal

WORLD JOURNAL OF MICROBIOLOGY & BIOTECHNOLOGY
Volume 31, Issue 5, Pages 717-727

Publisher

SPRINGER
DOI: 10.1007/s11274-015-1823-4

Keywords

Poly-3-(hydroxybutyrate-cohydroxyvalerate); Haloferax mediterranei; Stillage; Desalination; Techno-economic

Funding

  1. Department of Biotechnology (West Bengal)
  2. Department of Science and Technology-Promotion of University Research and Scientific Excellence (Phase II)
  3. Department of Science and Technology-Innovation in Science Pursuit for Inspired Research schemes [IF 110461]

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Haloferax mediterranei has potential for economical industrial-scale production of polyhydroxyalkanoate (PHA) as it can utilize cheap carbon sources, has capacity for nonsterile cultivation and allows simple product recovery. Molasses-based Indian distilleries are converting themselves to cereal-based distilleries. Waste stillage (14 l) of rice-based ethanol industry was used for the production of PHA by H. mediterranei in the simple plug-flow reactor configuration of the activated sludge process. Cells utilized stillage and accumulated 63 +/- A 3 % PHA of dry cell weight and produced 13.12 +/- A 0.05 g PHA/l. The product yield coefficient was 0.27 while 0.14 g/l h volumetric productivity was reached. Simultaneous lowering of 5-day biochemical oxygen demand and chemical oxygen demand values of stillage by 82 % was attained. The biopolymer was characterized as poly-3-(hydroxybutyrate-co-17.9 mol%-hydroxyvalerate) (PHBV). Directional properties of decanoic acid jointly with temperature-dependent water solubility in decanoic acid were employed for two-step desalination of the spent stillage medium in a cylindrical baffled-tank with an immersed heater and a stirrer holding axial and radial impellers. 99.3 % of the medium salts were recovered and re-used for PHA production. The cost of PHBV was estimated as US$2.05/kg when the annual production was simulated as 1890 tons. Desalination contributed maximally to the overall cost. Technology and cost-analysis demonstrate that PHA production integrated with ethanol manufacture is feasible in India. This study could be the basis for construction of a pilot plant.

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