An immobilized cell reactor with simultaneous product separation. I. Reactor design and analysis

Publisher Website
Google Scholar
Abstract
A four‐phase reactor–separator (gas, liquid, solid, and immobilized catalyst) is proposed for fermentations characterized by a volatile product and nonvolatile substrate.In this reactor, the biological catalyst is immobilized onto a solid column packing and contacted by the liquid containing the substrate.A gas phase is also moved through the column to strip the volatile product into the gas phase. The Immobilized Cell Reactor–Separator (ICRS) consists of two basic gas–liquid flow sections: a cocurrent “enricher” followed by a countercurrent–“stripper”.In this article, an equilibrium stage model of the reactor is developed to determine the feasibility and important operational variables of such a reactor–separator. The ICRS concept is applied to the ethanol from whey lactose fermentation using some preliminary immobilized cell reactor performance data. A mathematical model for a steady‐state population based on an adsorbed monolayer of cells is also developed for the reactor. The ICRS model demonstrated that the ICRS should give a significant increase in reactor productivity as compared to an identically sized Immobilized Cell Reactor (ICR) with no separation. The gas‐phase separation of the product also allows fermentation of high inlet substrate concentrations. The model is used to determine the effects of reactor parameters on ICRS performance including temperature, pressure, gas flow rates, inlet substrate concentration, and degree of microbial product inhibition.