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Question

An industrial fermentor containing $10,000 \text{ L}$ of medium needs to be sterilized. The initial spore concentration in the medium is $10^6 \text{ spores mL}^{-1}$. The desired probability of contamination after sterilization is $10^{-3}$. The death rate of spores at $121 \text{ °C}$ is $4 \text{ min}^{-1}$. Assume that there is no cell death during heating and cooling phases. The holding time of the sterilization process is __________ min (rounded off to the nearest integer).

Sterilization Time Calculation

This solution details the calculation for determining the holding time required for sterilizing an industrial fermentor, based on spore death kinetics.

Sterilization Data

  • Initial spore concentration ($N_0$): $10^6 \text{ spores mL}^{-1}$
  • Medium volume ($V$): $10,000 \text{ L}$
  • Target contamination probability ($P_{contam}$): $10^{-3}$
  • Spore death rate constant ($k$) at $121 \text{ °C}$: $4 \text{ min}^{-1}$

Initial Spore Load Calculation

First, calculate the total number of spores initially present in the fermentor.

  1. Convert the medium volume to milliliters: $V = 10,000 \text{ L} \times 1000 \text{ mL/L} = 10^7 \text{ mL}$
  2. Calculate the total initial spore count ($N_{0, \text{total}}$): $N_{0, \text{total}} = N_0 \times V = (10^6 \text{ spores mL}^{-1}) \times (10^7 \text{ mL}) = 10^{13} \text{ spores}$

Sterilization Kinetics Equation

The number of surviving spores after time $t$ is governed by first-order kinetics: $N(t) = N_0 e^{-kt}$. The Sterility Assurance Level (SAL) aims to minimize the probability of contamination. For a large initial population, the probability of contamination ($P_{contam}$) is approximately equal to the expected number of survivors ($E[N_{survivors}]$).

The sterilization requirement is that the expected number of survivors must be less than or equal to the target contamination probability:

$E[N_{survivors}] \le P_{contam}$

Substituting the expression for $E[N_{survivors}] = N_{0, \text{total}} e^{-kt}$:

$N_{0, \text{total}} e^{-kt} \le P_{contam}$ $10^{13} \text{ spores} \times e^{-kt} \le 10^{-3}$

This simplifies to finding the required reduction factor:

$e^{-kt} \le \frac{10^{-3}}{10^{13}} = 10^{-16}$

Holding Time Calculation

Solve for the holding time ($t$) using the death rate constant ($k$).

  1. Take the natural logarithm of both sides of the inequality: $-kt \le \ln(10^{-16})$ $-kt \le -16 \ln(10)$
  2. Rearrange to find $kt$: $kt \ge 16 \ln(10)$
  3. Isolate the holding time $t$: $t \ge \frac{16 \ln(10)}{k}$
  4. Substitute the given values, with $k = 4 \text{ min}^{-1}$: $t \ge \frac{16 \times \ln(10)}{4 \text{ min}^{-1}}$ $t \ge 4 \ln(10) \text{ min}$
  5. Calculate the minimum holding time using $\ln(10) \approx 2.3026$: $t \ge 4 \times 2.3026 \text{ min}$ $t \ge 9.2104 \text{ min}$

Rounded Holding Time

The calculated minimum holding time is approximately $9.2104$ minutes. The question requires this value to be rounded off to the nearest integer.

Rounding $9.2104$ to the nearest integer yields $9$ minutes.

Therefore, the holding time of the sterilization process is 9 min (rounded off to the nearest integer).

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Important Questions from Sterilization of Air and Media

  1. The decimal reduction time of a microbe during sterilization at $120 \text{ °C}$ with a first order thermal death rate constant of $1 \text{ min}^{-1}$ will be _______________  min (rounded off to 1 decimal place).

  2. A pilot sterilization was carried out in a vessel containing $100 \text{ m}^3$ medium with an initial spore concentration of $10^8 \text{ spores/ml}$. The accepted level of contamination after sterilization is 1 spore in the entire vessel. The specific death rate constant for the spore is $2 \text{ min}^{-1}$ at $121 \text{ }^\circ C$. Assuming no death takes place during the heating and cooling cycles, the holding time at $121 \text{ }^\circ C$ (rounded off to nearest integer) is ________________ min.
  3. Decimal reduction time of a bacterial strain is $20$ min. Specific death rate constant in $min^{-1}$ (rounded off to two decimal places) is____.

  4. Moist heat sterilization of spores at $121 \text{ } ^\circ C$ follows first order kinetics as per the expression: 

    $ \frac{dN}{dt} = -k_d N $ 

    where, N is the number of viable spores, t is the time, $k_d$ is the rate constant and $ \frac{dN}{dt} $ is the rate of change of viable spores. 

    If $k_d$ value is $1.0 \text{ min}^{-1}$, the time (in minutes) required to reduce the number of viable spores from an initial value of $10^{10}$ to a final value of 1 is (up to two decimal places)______.

  5. Decimal reduction time of bacterial spores is 23 min at $121 \ °C$ and the death kinetics follow first order. One liter medium containing $10^9$ spores per mL was sterilized for 10 min at $121 \ °C$ in a batch sterilizer. The number of spores in the medium after sterilization (assuming destruction of spores in heating and cooling period is negligible) will be ____________________ $ \times 10^7$.
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