A mathematical approach for the estimation of biomass production rate in solid state fermentation
โ Scribed by J. A. Rodriguez Leon; L. Sastre; J. Echevarria; G. Delgado; W. Bechstedt
- Publisher
- John Wiley and Sons
- Year
- 1988
- Tongue
- English
- Weight
- 221 KB
- Volume
- 8
- Category
- Article
- ISSN
- 0138-4988
No coin nor oath required. For personal study only.
๐ SIMILAR VOLUMES
Zymotis bioreactors for solid-state fermentation (SSF) are packed-bed bioreactors with internal cooling plates. This design has potential to overcome the problem of heat removal, which is one of the main challenges in SSF. In ordinary packed-bed bioreactors, which lack internal plates, large axial t
The development of large-scale solid-state fermentation (SSF) processes is hampered by the lack of simple tools for the design of SSF bioreactors. The use of semifundamental mathematical models to design and operate SSF bioreactors can be complex. In this work, dimensionless design factors are used
The mixing and heat transfer phenomena within rotating drum bioreactors (RDBs) used for solid-state fermentation processes are poorly studied. The potential for the establishment of axial temperature gradients within the substrate bed was explored using a heat transfer model. For growth of Aspergill
The relationships between 13 C NMR chemical shifts of aromatic carbons and the inter-ring torsion angles (ร) of two phenyl rings in biphenyl and its substituted derivatives were systematically examined. The chemical shifts of C1, C2 and C6 carbons (ฯ C1 , ฯ C2 and ฯ C6 ) of the biphenyl group in the
Production of conidia of the biocontrol fungus Coniothyrium minitans by solid-state cultivation in a packed-bed reactor on an industrial scale is feasible. Spore yield and oxygen consumption rate of C. minitans during cultivation on oats and three inert solids (hemp, perlite, and bagasse) saturated