Miss : SALSABEEL H. AL JOUJOU

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Miss : SALSABEEL H. AL JOUJOU Fermenter Miss : SALSABEEL H. AL JOUJOU

A fermenter also called bioreactor is a vessel in which a particular microbial is grown under controlled condition to produce a desired byproduct or biomass. The aim of fermentation is to provide stabilized condition for growth of cells and better production of a desired byproduct. In an ideal fermentation important parameters of fermentation ( PH, temperature , gas transfer , heat transfer , agitation and foaming) are tightly regulated .

In the laboratory , the fermentation is carried out in conical flask as the volume of fermentation media is small i.e. up to 500- 1000 ml . These flasks are made up of glass or plastic material. The flasks are kept in an incubator-shaker in which the temperature and aeration can be regulate .

There are many types of fermenters , but a conventional fermenter has a following feature a fermenter is made up of non-corrosive cylindrical steel vessel which can easily withstand a temperature of 150-190C and a pressure. The vessel has many inlets for addition gases , media component , acids- alkalies as well as outlets for escape of gases and sample collection for various tests to be performed during incubation.

The vessel also has provision for ports for various sensors like PH , temperature and dissolved oxygen (DO) . The fermentation vessel has a provision for cooling the fermentation broth ,if the incubation temperature rises above the requisite temperature. The latter phenomenon is observed in exothermic fermentations like ethanol fermentation.

The fermenter is cooled down by passing cold water in the jacket surrounding the vessel or in the coils present inside the vessel. The fermenters are fitted with an agitator for uniform mixing of the media .

for production of a desired microbial product , it is of almost importance to optimize physical (PH , temp. , aeration etc. ) and chemical ( carbon , nitrogen , mineral sources etc.) composition of the fermentation medium . To maintain these stringent condition , microbes are grown in containers called as fermenters or bioreactors . The capacity of bioreactors may vary from 10 liters to 100,000 liters depending on the byproduct .

In general , fermentation process is divide into two parts:- 1. Up Stream Processing ( USP ). 2. Down Stream Processing ( DSP). USP is basically involved in the :- a) preparation of a seed culture ( i.e. inoculums preparation) preparation of fermentation medium and its sterilization c) the fermentation process for optimal production of a metabolite .

DSP is concerned with the recovery of product , its concentration and purification and disposal of biowaste generated out of the fermentation process.

Types of bioreactors : (Based on the design of bioreactors) , they can be classified as : a) Stirred tank bioreactor . b)Bubble column bioreactor . c) Airlift bioreactor . d) Fluidized bed bioreactor e) Packed bed bioreactor .

a) Stirred tank bioreactor : It is also called stirred tank reactor (STR). It is fitted with impellors ( agitators ) which are connected to motor drivin shaft located centrally in the reactor .

b) Bubble column bioreactor : This type of bioreactor lacks impellers . The air is pumped into the fermenter through a plate located at the base of the bioreactor . This plate has many openings through which air or gas is passed in the form of bubbles into the liquid medium contained in the bioreactor . The introduction of air/gas in this manner results in uniform mixing of the fermentation broth.

c)Airlift bioreactor : In this the inside of the bioreactor is divide into two zones (riser zone and downcorner zone) with the help of a baffle or a draft tube . The air enters the vessel through the bottom part of the rise zone resulting in upward movement of the medium. The upper portion of medium then enters the downcorner zone and flows down to the base of the bioreactor

d) Fluidized bed bioreactor : In this type of bioreactor the immobilized cells or enzymes , present in the form of beads , are suspended in the lower cylindrical portion of bioreactor . The air is pumped in the vessel from the bottom of the bioreactor . The upper portion of the bioreactor comprises of cell free broth containing the bioproducts of fermentation .

This upper portion is collected in a separate tanks the new medium is pumped in the lower vessel .

e) Packed bed bioreactor : In this type of reactor , the vessel is loosely packed with matrix to which a biocatalyst ( cells or enzymes ) has been immobilized . The substrate is poured onto the matrix from the top of reactor and the bioproducts are collected from the bottom of reactor .