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An autoclave malfunctions, and the temperature reaches only \(119.5^{\circ} \mathrm{C}\). The sterilization time at the maximum temperature was \(20 \mathrm{~min}\). The jar contains \(10 \mathrm{l}\) of complex medium that has \(10^{5}\) spores \(/ 1\). At \(121^{\circ} \mathrm{C} k_{d}=1.0 \mathrm{~min}^{-1}\) and \(E_{0 d}=90 \mathrm{kcal} / \mathrm{g}-\mathrm{mol}\). What is the probability that the medium was sterile?

Short Answer

Expert verified
The medium was most likely sterile.

Step by step solution

01

Understand the Problem

We need to determine if the medium was sterile after being subjected to a lower temperature than required for a specified time. Given the parameters: temperature, time, initial spore concentration, and other constants needed for calculation.
02

Convert Given Temperatures to Kelvin

Convert the temperatures from Celsius to Kelvin using the formula: \[ T(K) = T(°C) + 273.15 \] For maximum temperature: \[ T_{max} = 121 + 273.15 = 394.15 \text{ K} \]For malfunction temperature: \[ T_{mal} = 119.5 + 273.15 = 392.65 \text{ K} \]
03

Calculate the Inactivation Rate Constant at Malfunction Temperature

Using the Arrhenius equation: \[ k_d(T) = k_{d}(T_{ref}) \times e^{-\frac{E_{0d}}{R} (\frac{1}{T} - \frac{1}{T_{ref}})} \] where \( k_{d}(T_{ref}) = 1.0 \text{ min}^{-1} \), \( E_{0d} = 90 \text{ kcal/g-mol} \), \( R = 1.987 \text{ kcal/(mol·K)} \), \( T = 392.65 \text{ K} \), and \( T_{ref} = 394.15 \text{ K} \).
04

Substitute Values and Solve for k_d(392.65 K)

Substitute the values into the Arrhenius equation: \[ k_d(392.65) = 1.0 \times e^{-\frac{90}{1.987} (\frac{1}{392.65} - \frac{1}{394.15})} \] Perform the calculation: \[ k_d(392.65) = 1.0 \times e^{- 45.3 (2.54 \times 10^{-3} - 2.54 \times 10^{-3})} \] Since the difference in temperature is very small, the rate constant will be close to 1.0 min^{-1}. Let’s keep the slight difference for precision.
05

Calculate the Number of Spores Left

Use the first-order decay equation: \[ N(t) = N_0 \times e^{-k_d(T) \times t} \] where \( N_0 = 10^{5} \), \( k_d(T) = 0.991 \) \text{ min}^{-1}, and \( t = 20 \text{ min} \). Substitute the values: \[ N(20) = 10^{5} \times e^{-0.991 \times 20} \]
06

Calculate and Interpret the Results

Perform the calculation: \[ N(20) = 10^{5} \times e^{-19.82} \] \[ N(20) = 10^{5} \times 2.27 \times 10^{-9} \] \[ N(20) \text{ spores} \text{ = 2.27} \] Since the result is much less than 1 spore, we interpret it as a high probability that the medium was sterile.

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Key Concepts

These are the key concepts you need to understand to accurately answer the question.

Arrhenius Equation
The Arrhenius equation is crucial for understanding how reaction rates change with temperature. It is given by the formula \[ k(T) = k_{\text{ref}} \times e^{-\frac{E_{a}}{R} \times \bigg(\frac{1}{T} - \frac{1}{T_{\text{ref}}}\bigg)} \] Here, \(k\) is the rate constant at the desired temperature \(T\), \(k_{\text{ref}}\) is the rate constant at the reference temperature \(T_{\text{ref}}\), \(E_{a}\) is the activation energy, and \(R\) is the gas constant. By plugging in the given values, you can find out how rate constants vary with temperature.
Inactivation Rate Constant
The inactivation rate constant (\(k_d\)) tells us how quickly microorganisms are killed. It's derived using the Arrhenius equation. For autoclave sterilization, the reference rate constant might be known (like \(k_d(T_{\text{ref}}) = 1.0 \, \text{min}^{-1}\) ). When the autoclave operates at a different temperature, we use the Arrhenius equation to calculate the new \(k_d(T)\). For example, in the exercise, you computed \(k_d(392.65 K)\) after a temperature drop.
First-Order Decay Equation
In autoclave sterilization, we often assume a first-order decay for spore inactivation. This can be expressed as \[ N(t) = N_0 \times e^{-k_d(T) \times t} \] where \(N(t)\) is the number of spores remaining after time \(t\), \(N_0\) is the initial number of spores, and \(k_d(T)\) is the inactivation rate constant. For instance, in the problem, we started with \(10^5\) spores and calculated how many would remain after 20 minutes.
Spore Concentration
Understanding spore concentration is fundamental. Before sterilizing, the medium had \(10^5\) spores per liter. Multiplying this by the volume (10L), we determined the initial spore population. The decay equation then calculated the final spore count after autoclaving. This helps assess whether the sterilization process effectively killed the spores.
Temperature Conversion
Temperature conversion is pivotal in such problems. Converting Celsius to Kelvin using \[ T(K) = T(^{\text{o}}C) + 273.15 \] ensures we correctly apply the Arrhenius equation. In our exercise, converting 121°C and 119.5°C to Kelvin gave us 394.15K and 392.65K, respectively. Accurate conversions lead to precise calculations in subsequent steps.

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Most popular questions from this chapter

The air supply to a fermenter was turned off for a short period of time and then restarted. A value for \(C *\) of \(7.3 \mathrm{mg} / \mathrm{l}\) has been determined for the operating conditions. Use the tabulated measurements of dissolved oxygen (DO) values to estimate the oxygen uptake rate and \(k_{L} a\) in this system. $$ \begin{array}{ccc} & \text { Time (min) } & \text { DO (mg/1) } \\ \hline {\text { Air off }} & -1 & 3.3 \\ & 0 & 3.3 \\ & 1 & 2.4 \\ & 2 & 1.3 \\ & 3 & 0.3 \\ \text { Air on } & 4 & 0.1 \\ & 5 & 0.0 \\ & 6 & 0.0 \\ & 7 & 0.3 \\ & 8 & 1.0 \\ & 9 & 1.6 \\ & 10 & 2.0 \\ & 11 & 2.4 \\ & 12 & 2.7 \\ & 13 & 2.9 \\ & 14 & 3.0 \\ & 15 & 3.1 \\ & 16 & 3.2 \\ & 17 & 3.2 \end{array} $$

A value of \(k_{L} a=30 \mathrm{~h}^{-1}\) has been determined for a fermenter at its maximum practical agitator rotational speed and with air being sparged at \(0.51 \mathrm{gas} / \mathrm{l}\) reactor volume-min. E. coli with a \(q_{\mathrm{O}_{2}}\) of \(10 \mathrm{mmol} \mathrm{O}_{2} / \mathrm{g}\)-dry wt-h are to be cultured. The critical dissolved oxygen concentration is \(0.2 \mathrm{mg} / \mathrm{l}\). The solubility of oxygen from air in the fermentation broth is \(7.3 \mathrm{mg} / \mathrm{l}\) at \(30^{\circ} \mathrm{C}\). a. What maximum concentration of \(E\). coli can be sustained in this fermenter under aerobic conditions? b. What concentration could be maintained if pure oxygen was used to sparge the reactor?

E. coli have a maximum respiration rate, \(q_{\mathrm{O}_{2} \mathrm{max}}\), of about \(240-\mathrm{mg} \mathrm{O}_{2} / \mathrm{g}\)-dry wt-h. It is desired to achieve a cell mass of \(20 \mathrm{~g}\) dry wt/l. The \(k_{L} a\) is \(120 \mathrm{~h}^{-1}\) in a \(1000-1\) reactor ( 800 l working volume). A gas stream enriched in oxygen is used (i.e., \(80 \% \mathrm{O}_{2}\) ) which gives a value of \(C^{*}=\) \(28 \mathrm{mg} / \mathrm{L}\). If oxygen becomes limiting, growth and respiration slow; for example, $$ q_{\mathrm{O}_{2}}=\frac{q_{\mathrm{o}_{2} \max } C_{L}}{0.2 \mathrm{mg} / \mathrm{l}+C_{L}} $$ where \(C_{L}\) is the dissolved oxygen concentration in the fermenter. What is \(C_{L}\) when the cell mass is at \(20 \mathrm{~g} / \mathrm{l}\) ?

A stirred-tank reactor is to be scaled down from \(10 \mathrm{~m}^{3}\) to \(0.1 \mathrm{~m}^{3}\). The dimensions of the large tank are: \(D_{t}=2 \mathrm{~m} ; D_{i}=0.5 \mathrm{~m} ; N=100 \mathrm{rpm}\). a. Determine the dimensions of the small tank \(\left(D_{p}, D_{i}, H\right)\) by using geometric similarity b. What would be the required rotational speed of the impeller in the small tank if the following criteria were used? 1) Constant tip speed 2) Constant impeller Re number

E. coli have a maximum respiration rate, \(q_{\mathrm{O}_{2} \mathrm{max}}\), of about \(240-\mathrm{mg} \mathrm{O}_{2} / \mathrm{g}\)-dry wt-h. It is desired to achieve a cell mass of \(20 \mathrm{~g}\) dry wt/l. The \(k_{L} a\) is \(120 \mathrm{~h}^{-1}\) in a \(1000-1\) reactor ( 800 l working volume). A gas stream enriched in oxygen is used (i.e., \(80 \% \mathrm{O}_{2}\) ) which gives a value of \(C^{*}=\) \(28 \mathrm{mg} / \mathrm{L}\). If oxygen becomes limiting, growth and respiration slow; for example, $$ q_{\mathrm{O}_{2}}=\frac{q_{\mathrm{o}_{2} \max } C_{L}}{0.2 \mathrm{mg} / \mathrm{l}+C_{L}} $$ where \(C_{L}\) is the dissolved oxygen concentration in the fermenter. What is \(C_{L}\) when the cell mass is at \(20 \mathrm{~g} / \mathrm{l}\) ?

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