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Analysis of the Effect of in situ Product Removal on the Stability and Performance of a Continuous Bioreactor with Cell Separator for Ethanol Production

Kaushik Ghosh
K.B. Ramachandran


Puni tekst: engleski pdf 366 Kb

str. 285-296

preuzimanja: 395

citiraj


Sažetak

In this study, the behaviour of a continuous membrane bioreactor with in situ removal of product ethanol by pervaporation and cell recycle has been investigated. The kinetic model used is an unstructured growth model taking into account product as well
as substrate inhibition and the product formation rate is represented by the Leudeking-Piret model. The effect of pervaporation on the performance of the system with cell separator is evaluated in terms of ethanol productivity and its stability. The stability analysis carried out using elementary principles of bifurcation theory shows that
the reactor is characterized by the presence of steady-state multiplicity and hysteresis.
The simulation results also demonstrate that the in situ removal of ethanol by pervaporation increases productivity as the ethanol inhibition barrier is overcome. Introduction of both pervaporation and cell recycling increases the region of instability in the
system but the instability region moves to higher values of dilution rate. This allows stable operation of a fermentor at higher dilution rates to achieve increased productivity.

Ključne riječi

Cell recycling; ethanol fermentation; pervaporation; stability; productivity

Hrčak ID:

16391

URI

https://hrcak.srce.hr/16391

Datum izdavanja:

1.10.2007.

Posjeta: 916 *