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A radioactive isotope decays at a rate proportional to its concentration. If the concentration of an isotope is \(C(\mathrm{mg} / \mathrm{L}),\) then its rate of decay may be expressed as $$r_{\mathrm{d}}[\mathrm{mg} /(\mathrm{L} \cdot \mathrm{s})]=k C$$ where \(k\) is a constant. (a) A volume \(V(\mathrm{L})\) of a solution of a radioisotope whose concentration is \(C_{0}(\mathrm{mg} / \mathrm{L})\) is placed in a closed vessel. Write a balance on the isotope in the vessel and integrate it to prove that the half-life \(t_{1 / 2}\) of the isotope \(-\) by definition, the time required for the isotope concentration to decrease to half of its initial value- equals ( \(\ln 2\) )/ \(k\). (b) The half-life of \(^{56} \mathrm{Mn}\) is \(2.6 \mathrm{h}\). A batch of this isotope that was used in a radiotracing experiment has been collected in a holding tank. The radiation safety officer declares that the activity (which is proportional to the isotope concentration) must decay to \(1 \%\) of its present value before the solution can be discarded. How long will this take?

Short Answer

Expert verified
The time necessary for a radioactive isotope to decay to 1% of its original concentration is calculated by solving the decay equation. For ^56 Mn, this time is found to be approximately 54.4 hours.

Step by step solution

01

Derive the Half-life Formula

The rate of decay \(r_d\) is given by the relation \( r_d=kC\), or \(\frac{dC}{dt}=-kC\). This is a first order differential equation. On separating the variables and integrating, we get \(\int_{C_0}^{C}\frac{dC'}{C'}=-k\int_{0}^{t}dt'\). Solving the integrals we have \( \ln{C} - \ln{C_0} = -kt\). Dividing through by -1, \(\ln\left(\frac{C_0}{C}\right) = kt\). For half-life \(C = \frac{C_0}{2}\), therefore, \(\ln2 = kt_{1/2}\). Hence, \(t_{1/2} = \frac{ln2}{k}\).
02

Calculate the Time Required

The given half-life is \(2.6h\). We know that \(t_{1/2} = \frac{\ln2}{k}\), from which we get \(k = \frac{\ln2}{2.6h}\). Now we need to find the time \(t\) when the isotope decays to 1% of its current concentration. Substituting \(C=\frac{C_0}{100}\) in the equation \(\ln\left(\frac{C_0}{C}\right) = kt\), we get \(t = \frac{\ln100}{k}\). Substituting \(k\) from the previous step, \(t = \frac{\ln100}{\ln2 / 2.6h}\), we get the time required.

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Key Concepts

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

Half-life
Understanding half-life is crucial in the study of radioactive decay. It refers to the time required for half of a radioactive isotope's quantity to decay. This measure is important because it helps predict how long a substance will remain active and hazardous.
In our context, the half-life is calculated using the formula:\[t_{1/2} = \frac{\ln 2}{k}\]Here, \(k\) is the decay constant, a value that indicates the likelihood of decay per unit time. The formula shows that the half-life is inversely proportional to \(k\), meaning the faster the decay (larger \(k\)), the shorter the half-life.
Understanding half-life allows scientists to gauge how long radioactive substances will remain dangerous and helps in planning safe handling and disposal. It also has a big role in radiotracing, archaeological dating, and nuclear medicine.
Differential Equations
Differential equations often describe how quantities change over time, and they play a vital role in modeling the decay process of radioactive isotopes. The decay rate given by:\[\frac{dC}{dt} = -kC\]This is a first-order differential equation, indicating that the rate of change of the concentration depends directly on the concentration itself. "Separating variables," we can integrate both sides to solve for the concentration function over time.
The general solution to this differential equation gives:\[\ln \frac{C_0}{C} = kt\]This equation allows calculation of the concentration of isotopes at any given time \(t\). Understanding and solving differential equations provide insights into the behavior and prediction of isotopic concentration over time, a crucial step for applications like radiotracing and determining safe levels of exposure.
Isotope Concentration
Isotope concentration levels indicate the amount of a radioactive substance present in a solution. It's crucial to manage due to the potential hazards of radioactivity. The concentration \(C\) decreases over time as the isotope decays, and this decrease follows a logarithmic pattern as described by the equation:\[\frac{dC}{dt} = -kC\]Understanding concentration is important for numerous reasons:
  • Ensuring safety in handling radioactive materials, as exposure must be minimized.
  • Accurate measurement helps in scientific research, including radiotracing techniques in medicine and environmental studies.
  • Managing waste and disposal, as the concentration needs to be reduced to safe levels prior to disposal.
Therefore, being aware of how concentration levels change over time can greatly aid in effective and safe management of radioactive substances. Calculating when the isotope concentration reduces to a safe level such as 1% of its original amount is vital in various industrial and research settings.

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Most popular questions from this chapter

A 10.0 -ft compressed-air tank is being filled. Before the filling begins, the tank is open to the atmosphere. The reading on a Bourdon gauge mounted on the tank increases linearly from an initial value of 0.0 to 100 psi after 15 seconds. The temperature is constant at \(72^{\circ} \mathrm{F}\), and atmospheric pressure is 1 atm. (a) Calculate the rate \(\dot{n}\) (lb-mole/s) at which air is being added to the tank, assuming ideal-gas behavior. (Suggestion: Start by calculating how much is in the tank at \(t=0 .)\) (b) Let \(N(t)\) equal the number of Ib-moles of air in the tank at any time. Write a differential balance on the air in the tank in terms of \(N\) and provide an initial condition. (c) Integrate the balance to obtain an expression for \(N(t)\). Check your solution two ways. (d) Estimate the Ib-moles of oxygen in the tank after two minutes. List reasons your answer might be inaccurate, assuming there are no mistakes in your calculation.

A steam coil is immersed in a stirred tank. Saturated steam at 7.50 bar condenses within the coil, and the condensate emerges at its saturation temperature. A solvent with a heat capacity of \(2.30 \mathrm{kJ} /\left(\mathrm{kg} \cdot^{\cdot} \mathrm{C}\right)\) is fed to the tank at a steady rate of \(12.0 \mathrm{kg} / \mathrm{min}\) and a temperature of \(25^{\circ} \mathrm{C},\) and the heated solvent is discharged at the same flow rate. The tank is initially filled with \(760 \mathrm{kg}\) of solvent at \(25^{\circ} \mathrm{C},\) at which point the flows of both steam and solvent are commenced. The rate at which heat is transferred from the steam coil to the solvent is given by the expression $$\dot{Q}=U A\left(T_{\mathrm{steam}}-T\right)$$ where \(U A\) (the product of a heat transfer coefficient and the coil surface area through which the heat is transferred) equals \(11.5 \mathrm{kJ} /\left(\min \cdot^{\circ} \mathrm{C}\right) .\) The tank is well stirred, so that the temperature of the contents is spatially uniform and equals the outlet temperature. (a) Prove that an energy balance on the tank contents reduces to the equation given below and supply an initial condition. \frac{d T}{d t}=1.50^{\circ} \mathrm{C} / \mathrm{min}-0.0224 T (b) Without integrating the equation, calculate the steady-state value of \(T\) and sketch the expected plot of \(T\) versus \(t,\) labeling the values of \(T_{\mathrm{b}}\) at \(t=0\) and \(t \rightarrow \infty\) (c) Integrate the balance equation to obtain an expression for \(T(t)\) and calculate the solvent temperature after 40 minutes. (d) The tank is shut down for routine maintenance, and a technician notices that a thin mineral scale has formed on the outside of the steam coil. The coil is treated with a mild acid that removes the scale and reinstalled in the tank. The process described above is run again with the same steam conditions, solvent flow rate, and mass of solvent charged to the tank, and the temperature after 40 minutes is \(55^{\circ} \mathrm{C}\) instead of the value calculated in Part (c). One of the system variables listed in the problem statement must have changed as a result of the change in the stirrer. Which variable would you guess it to be, and by what percentage of its initial value did it change?

A gas leak has led to the presence of 1.00 mole \(\%\) carbon monoxide in a \(350-\mathrm{m}^{3}\) laboratory. \(^{4}\) The leak was discovered and sealed, and the laboratory is to be purged with clean air to a point at which the air contains less than the OSHA (Occupational Safety and Health Administration) specified Permissible Exposure Level (PEL) of 35 ppm (molar basis). Assume that the clean air and the air in the laboratory are atthe same temperature and pressure and that the laboratory air is perfectly mixed throughout the purging process. (a) Let \(t_{\mathrm{r}}(\mathrm{h})\) be the time required for the specified reduction in the carbon monoxide concentration. Write a differential CO mole balance, letting \(N\) equal the total moles of gas in the room (assume constant), the mole fraction of CO in the room air, and \(\dot{V}_{\mathrm{p}}\left(\mathrm{m}^{3} / \mathrm{h}\right)\) the flow rate of purge air entering the room (and also the flow rate of laboratory air leaving the room). Convert the balance into an equation for \(d x / d t\) and provide an initial condition. Sketch a plot of \(x\) versus \(t,\) labeling the value of \(x\) at \(t=0\) and the asymptotic value at \(t \rightarrow \infty\) (b) Integrate the balance to derive an equation for \(t_{r}\) in terms of \(\dot{V}_{\mathrm{p}}\) (c) If the volumetric flow rate is \(700 \mathrm{m}^{3} / \mathrm{h}\) (representing a tumover of two room volumes per hour), how long will the purge take? What would the volumetric flow rate have to be to cut the purge time in half? (d) Give several reasons why it might not be safe to resume work in the laboratory after the calculated purge time has elapsed. What precautionary steps would you advise taking at this point?

Water is added at varying rates to a 300 -liter holding tank. When a valve in a discharge line is opened, water flows out at a rate proportional to the height and hence to the volume \(V\) of water in the tank. The flow of water into the tank is slowly increased and the level rises in consequence, until at a steady input rate of \(60.0 \mathrm{L} / \mathrm{min}\) the level just reaches the top but does not spill over. The input rate is then abruptly decreased to \(40.0 \mathrm{L} / \mathrm{min}\). (a) Write the equation that relates the discharge rate, \(\dot{V}_{\text {out }}(\mathrm{L} / \mathrm{min}),\) to the volume of water in the tank, \(V(\mathrm{L}),\) and use it to calculate the steady-state volume when the input rate is \(40 \mathrm{L} / \mathrm{min}\). (b) Write a differential balance on the water in the tank for the period from the moment the input rate is decreased \((t=0)\) to the attainment of steady state \((t \rightarrow \infty),\) expressing it in the form \(d V / d t=\cdots \cdot\) Provide an initial condition. (c) Without integrating the equation, use it to confirm the steady-state value of \(V\) calculated in Part (a) and then to predict the shape you would anticipate for a plot of \(V\) versus \(t\). Explain your reasoning. (d) Separate variables and integrate the balance equation to derive an expression for \(V(t)\). Calculate the time in minutes required for the volume to decrease to within \(1 \%\) of its steady-state value.

The demand for biopharmaceutical products in the form of complex proteins is growing. These proteins are most often produced by cells genetically engineered to produce the protein of interest, known as a recombinant protein. The cells are grown in a liquid culture, and the protein is harvested and purified to generate the final product. Sf9 cells obtained from the fall armyworm can be used to produce protein therapeutics. Consider the growth of Sf9 cells in a bench-top bioreactor operating at \(22^{\circ} \mathrm{C}\), with a liquid volume of 4.0 liters that may be assumed constant. Oxygen required for cell growth and protein production is supplied in air fed at \(22^{\circ} \mathrm{C}\) and 1.1 atm. During the process, the gas leaving the bioreactor at \(22^{\circ} \mathrm{C}\) and 1 atm is analyzed continuously. The data can be used to calculate the rate at which oxygen is taken up in the culture, which in turn can be used to determine the Sf9 cell growth rate (a quantity difficult to measure directly) and consistency of the operation from batch to batch. (a) Analysis of the exhaust gas at a time 25 hours after the process is started shows a composition of \(15.5 \mathrm{mol} \% \mathrm{O}_{2}, 78.7 \% \mathrm{N}_{2},\) and the balance \(\mathrm{CO}_{2}\) and small amounts of other gases. Determine the value of the oxygen use rate (OUR) in mmol \(\mathrm{O}_{2}\) consumed \((\mathrm{L} \cdot \mathrm{h})\) at that point in time. Assume that nitrogen is not absorbed by the culture. (b) OUR is related to cell concentration, \(X(\mathrm{g} \text { cells } / \mathrm{L}),\) by \(\mathrm{OUR}=q_{0_{2}} X,\) where \(q_{0_{2}}\) is the specific rate of oxygen consumption. Analysis of a sample of the culture taken at \(t=25 \mathrm{h}\) finds that the concentration of cells is \(5.0 \mathrm{g}\) cells/L. What is the value of \(q_{\mathrm{O}_{2}} ?\) (Do not forget to include its units.) (c) Six hours after this measurement, the exhaust gas contains 14.5 mol\% \(\mathrm{O}_{2}\) and the percentage of \(\mathrm{N}_{2}\) is unchanged. What is the concentration of cells, \(X,\) at that point? Assume that the specific rate of oxygen consumption does not change as long as the process temperature is constant. (d) The growth rate of cells can be expressed as: $$\frac{d X}{d t}=\mu_{\mathrm{g}} X$$ where \(\mu_{g}\) is the specific growth rate, with units of \(\mathrm{h}^{-1}\). Beginning with this equation and treating \(\mu_{\mathrm{g}}\) as a constant, derive an expression for \(t(X) .\) Use the data from the previous parts of the problem to determine \(\mu_{\mathrm{g}}\) (include units). Then calculate the cell-doubling time \(\left(t_{\mathrm{d}}\right),\) defined as the time for the cell concentration to double.

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