Chapter 5 Ft Edited

May 3, 2019 | Author: Puvenez Tamalantan | Category: Sterilization (Microbiology), Growth Medium, Temperature, Bacteria, Steam
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CHAPTER 5 STERILIZATION

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Introduction A fermentation product is produced by the culture of a certain organism, or organisms, in a nutrient medium. If the fermentation is invaded by a foreign microorganism then the following consequences may occur: i) The medi medium um would would have have to to suppor supportt the grow growth th of both both the the produ producti ction on organism & the contaminant, resulting in a loss of productivity. ii) If the ferm fermentati entation on is a contin continuous uous one one then then the contami contaminant nant may‘outgrow’ the production organism & displace it from the fermentation.

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v) The contaminant may degrade the desired product; this is common in bacterial contamination of antibiotic fermentations where the contaminant would have to be resistant to the normal inhibitory effect of  the antibiotic & degradation of the antibiotic is a common resistance mechanism, e.g. the degradation of  -lactam antibiotics by - lactamaseproducing bacteria. vi) Contamination of a bacterial fermentation with phage could result in the lysis of the culture.

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• Avoidance of contamination may be achieved by:

i) Usi Using ng a pur pure e inocu inoculum lum to start start the fer ferment mentati ation. on. ii) Steril Sterilizing izing the medium to be employ employed. ed. iii) Steril Sterilizing izing the fermenter fermenter vessel. iv) Sterilizing all materials to be added to the fermentation during the process. v) Maint Maintainin aining g aseptic aseptic condition condition during during the the fermentation. fermentation.

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Medium Sterilization • The first step in the sterilization of any medium is the selection of an appropriate vessel in which to carry out the sterilization process. • This is obviously volume dependent and can range from something as simple as a screw cap bottle, through shake flasks for inoculum development, to the complexicity of the bioreactor itself. • Sterilization is normally carried out by heat or filtration. Although other methods exists, such as irradiation, chemical

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• Before the techniques which are used for the steam sterilization for the culture medium are discussed, it is necessary to discuss the kinetics of sterilization. • The destruction of microorganisms by steam (moist heat) may be described as a first-order chemical reaction, & may be represented by the following equation:

-dN/dt = kN Where; N is the number of viable organism present

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On integration of equation, give kt Nt/No = e  – kt

Where, No is the number of viable organisms present at the start of the sterilization treatment Nt is the number of viable organism present after a treatment period, t

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-

The relationship between T and the reaction rate constant is:

d ln k/dT = E/RT2 E is the activation energy R is the gas constant T is the absolute temperatur temperature e

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Deindoerfer and Humphrey (1959) used the term ln No/Nt as a design criterion for sterilization which has been variously called the DEL FACTOR, Nabla factor & sterilization criterion represented by the term . The Del factor is a measure of the fractional reduction in viable organism org anism count produced by a certain heat and time regime.

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A risk factor of one batch in a thousand being contaminated is frequently used in the fermentation industry. Two basic types reaction contribute to the loss of nutrient quality during sterilization: i) Inte Interac raction tion betw between een nutr nutrient ient com compone ponents nts of of the med medium. ium.

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ii) Degradation of heat labile (heat sensitive) components such as vitamins & amino acids. • Reaction of this type may be minimized by using a suitable time-temperature sterilization regime.

The thermal destruction of essential media components

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• in the consideration of Del factor it was evident that the same

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Advantages of continuous sterilization over batch

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Advantages of batch sterilization over continuous

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THE DESIGN OF BATCH STERILIZATION PROCESS

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The destruction of a nutrient may be considered a first-order reaction & its rate will be affected by T xt/xo = e  –kt Where k is the reaction rate constant Or

xo/xt = ekt

Thus, taking natural logarithms,

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STERILIZATION OF THE FERMENTER - If the the med mediu ium m is ste steri rili lize zed d in a sep separa arate te batc batch h cook cooker, er, or or is continuously sterilized, then the fermenter has to be sterilized separately before the sterile medium is added to it. - This This is norm normall ally y achie achieved ved by heat heating ing the jac jacket ket or ccoil oilss of the fermenter with steam & sparging steam into the vessel through all entries. - Ste Steam am pr pres essu sure re is is hel held d 15 ps psii in in the the vess vessel el fo forr 20 mi min n

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STERILIZATION OF AIR

- Filt Filters ers fo forr the the rem remov oval al of of micr microo oorga rgani nism sm fro from m environment may be divided into two larger group

an an

i) Those Those which which the the pores pores in in the fil filter ter are are small smaller er than than the the particles which are to be removed. ii) Those which which the pores pores are larger larger than than the particles particles which which are to be removed.

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Filter made from fibrous material such as - Cotton - Glass - Steel wool

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