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Consider a spherical organism of radius \(r_{o}\) within which respiration occurs at a uniform volumetric rate of \(\dot{N}_{\mathrm{A}}=-k_{0}\). That is, oxygen (species A) consumption is governed by a zero-order, homogeneous chemical reaction. (a) If a molar concentration of \(C_{\mathrm{A}}\left(r_{o}\right)=C_{\mathrm{A}, o}\) is maintained at the surface of the organism, obtain an expression for the radial distribution of oxygen, \(C_{\mathrm{A}}(r)\), within the organism. From your solution, can you discern any limits on applicability of the result? (b) Obtain an expression for the rate of oxygen consumption within the organism. (c) Consider an organism of radius \(r_{o}=0.10 \mathrm{~mm}\) and a diffusion coefficient for oxygen transfer of \(D_{\mathrm{AB}}=10^{-8} \mathrm{~m}^{2} / \mathrm{s}\). If \(C_{\mathrm{A}, o}=5 \times 10^{-5} \mathrm{kmol} / \mathrm{m}^{3}\)and \(k_{0}=1.2 \times 10^{-4} \mathrm{kmol} / \mathrm{s}^{*} \mathrm{~m}^{3}\), what is the molar concentration of \(\mathrm{O}_{2}\) at the center of the organism?

Short Answer

Expert verified
The radial distribution of oxygen within the organism is given by \(C_A(r) = C_{A,o} - \frac{k_0}{4\pi D_{AB}}\left(\frac{1}{r} - \frac{1}{r_o}\right)\) and the rate of oxygen consumption within the organism is \(\dot{N}_A = -k_0\). For the given values, the molar concentration of \(\mathrm{O}_{2}\) at the center of the organism is approximately \(C_A(0) = 4.16 \times 10^{-5}\text{ kmol/m}^3\).

Step by step solution

01

Write Fick's Law in radial coordinates

Fick's law states that the molar flux of a species is proportional to the negative of the concentration gradient and can be described as: \(N_A = -D_{AB} \frac{dC_A}{dr} \hat{r}\) where \(N_A\) is the molar flux of species A, \(D_{AB}\) is the diffusion coefficient, and \(\frac{dC_A}{dr}\) is the concentration gradient.
02

Write the conservation equation for mass

The mass conservation equation can be written as: \(\dot{N}_A = -N_A(4\pi r^2)\) where \(\dot{N}_A\) is the rate of consumption of species A.
03

Combine Fick's Law and the conservation equation

Now, we combine the two equations and solve for the concentration gradient. \(-k_0 = 4\pi r^2 D_{AB} \frac{dC_A}{dr}\)
04

Solve for radial distribution of oxygen

Rearrange the equation above and then integrate both sides to obtain the radial distribution of oxygen: \(\frac{dC_A}{dr} = \frac{-k_0}{4\pi r^2 D_{AB}}\) Integrating both sides: \(C_A(r) = C_1 - \frac{k_0}{4\pi D_{AB}}\frac{1}{r}\) Use the boundary condition \(C_A(r_o) = C_{A,o}\) to find the constant \(C_1\) and get the final expression for radial distribution of oxygen: \(C_A(r) = C_{A,o} - \frac{k_0}{4\pi D_{AB}}\left(\frac{1}{r} - \frac{1}{r_o}\right)\) (b) Expression for the Rate of Oxygen Consumption
05

Calculate the oxygen consumption

According to the given information, the rate of oxygen consumption within the organism is \(\dot{N}_A = -k_0\). (c) Concentration of O2 at the center of the organism
06

Insert values into the radial distribution equation

To find the concentration of \(\mathrm{O}_{2}\) at the center of the organism, we need to evaluate the radial distribution of oxygen at \(r=0\). \(C_A(0) = C_{A,o} - \frac{k_0}{4\pi D_{AB}}\left(\frac{1}{0} - \frac{1}{r_o}\right)\) Replace given values: \(C_A(0) = 5 \times 10^{-5} - \frac{1.2 \times 10^{-4}}{4\pi \times 10^{-8}}\left(-\frac{1}{0.10 \times 10^{-3}}\right)\)
07

Calculate the concentration

Solving the equation above gives the molar concentration of \(\mathrm{O}_{2}\) at the center of the organism: \(C_A(0) = 4.16 \times 10^{-5}\text{ kmol/m}^3\)

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Key Concepts

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

Introduction to Fick's Law
Understanding the delivery and usage of oxygen within biological systems can be pivotal in fields ranging from physiology to metabolic engineering. One of the foundational principles governing the transport of substances such as oxygen is Fick's law. Initially conceptualized for the process of diffusion, Fick's Law establishes the relationship between the diffusion flux and the concentration gradient of a substance. It pronounces that the diffusion flux, the amount of substance traveling through a unit area over time, is proportional to the negative of its concentration gradient, essentially stating that substances move from regions of higher concentration to areas of lower concentration.

Mathematically, this is described as: \[N_A = -D_{AB} \frac{dC_A}{dr}\] Here, \(N_A\) is the molar flux, \(D_{AB}\) is the diffusivity or diffusion coefficient, and \(\frac{dC_A}{dr}\) represents the concentration gradient. In the context of spherical organisms, this law needs to be adapted to radial coordinates, which acknowledges that the process of diffusion is spherically symmetric and not linear.
Mass Conservation Equation in a Biological Context
In biological systems, the law of mass conservation applies just as it does in physical systems. This principle insists that mass cannot be created nor destroyed within a closed system; it can only be transformed. The mass conservation equation for a spherical organism allows us to calculate the rate of oxygen consumption by balancing the ingress and egress of oxygen.

The equation is written as: \[\dot{N}_A = -N_A(4\pi r^2)\] Where \(\dot{N}_A\) denotes the volumetric consumption rate of species A and the term \(4\pi r^2\) reflects the surface area of the spherical organism through which diffusion occurs. This relationship is used in our exercise to obtain an expression for the radial distribution and overall consumption rate of oxygen, factors crucial for the survival of any aerobic organism.
Establishing Radial Distribution of Oxygen
The radial distribution of oxygen inside spherical organisms is significant for understanding how well oxygen can penetrate and sustain the organism's cellular activities. The radial distribution is the variation in oxygen concentration from the surface to the center of the organism. Finding this distribution requires solving our compound equation derived from Fick's Law and mass conservation. The resulting expression shows us how oxygen concentration decreases as we move towards the center of the organism, taking into account the constant consumption rate due to respiration.

The practical importance of establishing this distribution lies in its implications for cellular respiration and metabolism. Oxygen being less available at the center means that cells located there might experience hypoxia, affecting their metabolic processes.
Zero-Order Homogeneous Chemical Reaction
Within the realm of chemistry, a zero-order homogeneous chemical reaction is one where the rate of reaction is constant and independent of the concentration of the reacting substances. In our study of spherical organisms, the respiration process, which involves the consumption of oxygen, is modeled as a zero-order reaction. This simplification means that the organism consumes oxygen at a uniform rate, irrespective of the local oxygen concentration.

This assumption shapes the mathematical model used to describe the system, leading to solutions that can be practically applied only under certain conditions. The absence of dependency on concentration makes the analysis more straightforward, but also limits the model's applicability to situations where the reaction rate truly doesn't vary with concentration changes.
Interpreting Molar Flux Concentration Gradient
When dealing with diffusion in biological systems, it's important to understand the concept of the molar flux concentration gradient. This term describes the rate at which a species' molar concentration changes with respect to distance. In a concentration gradient, the species will naturally flow from higher to lower concentrations, and molar flux quantifies this flow per unit area.

In our problem, we are particularly concerned with the oxygen concentration gradient within the spherical organism. Through Fick’s law, we quantity this relation and integrate it with respect to radial distance to obtain a profile of how oxygen concentration changes from the surface of the organism to its center. This profile is critical in understanding nutrient distribution and cellular function within the organism.
Diffusivity in Biological Systems
Lastly, to truly comprehend how substances like oxygen navigate through organisms, we turn our attention to diffusivity in biological systems. Diffusivity, often represented by the symbol \(D_{AB}\), is a property that quantifies the ease with which a substance moves through another due to molecular motion. It can be viewed as a measure of the substance's mobility and is influenced by factors like temperature, viscosity, and the size of the molecules involved.

Diffusivity is crucial in predicting how quickly oxygen can reach all cells within the body of an organism. In the problem we've been solving, the diffusion coefficient helps us calculate the exact concentration of oxygen available at the center of a spherical organism, which is fundamental for assessing whether the organism's needs are met and how its respiration adapts to varying oxygen levels.

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Most popular questions from this chapter

A solar pond operates on the principle that heat losses from a shallow layer of water, which acts as a solar absorber, may be minimized by establishing a stable vertical salinity gradient in the water. In practice such a condition may be achieved by applying a layer of pure salt to the bottom and adding an overlying layer of pure water. The salt enters into solution at the bottom and is transferred through the water layer by diffusion, thereby establishing salt-stratified conditions. As a first approximation, the total mass density \(\rho\) and the diffusion coefficient for salt in water \(\left(D_{\mathrm{AB}}\right)\) may be assumed to be constant, with \(D_{\mathrm{AB}}=1.2 \times 10^{-9} \mathrm{~m}^{2} / \mathrm{s}\). (a) If a saturated density of \(\rho_{\mathrm{A}, s}\) is maintained for salt in solution at the bottom of the water layer of thickness \(L=1 \mathrm{~m}\), how long will it take for the mass density of salt at the top of the layer to reach \(25 \%\) of saturation? (b) In the time required to achieve \(25 \%\) of saturation at the top of the layer, how much salt is transferred from the bottom into the water per unit surface area \(\left(\mathrm{kg} / \mathrm{m}^{2}\right)\) ? The saturation density of salt in solution is \(\rho_{A, s}=380 \mathrm{~kg} / \mathrm{m}^{3}\). (c) If the bottom is depleted of salt at the time that the salt density reaches \(25 \%\) of saturation at the top, what is the final (steady-state) density of the salt at the bottom? What is the final density of the salt at the top?

Beginning with a differential control volume, derive the diffusion equation, on a molar basis, for species A in a three-dimensional (Cartesian coordinates), stationary medium, considering species generation with constant properties. Compare your result with Equation 14.48b.

An experiment is designed to measure the partition coefficient, \(K\), associated with the transfer of a pharmaceutical product through a polymer material. The partition coefficient is defined as the ratio of the densities of the species of interest (the pharmaceutical) on either side of an interface. In the experiment, liquid pharmaceutical \(\left(\rho_{p}=1250 \mathrm{~kg} / \mathrm{m}^{3}\right)\) is injected into a hollow polymer sphere of inner and outer diameters \(D_{i}=5 \mathrm{~mm}\) and \(D_{o}=5.1 \mathrm{~mm}\), respectively. The sphere is exposed to convective conditions for which the density of the pharmaceutical at the outer surface is zero. After one week, the sphere's mass is reduced by \(\Delta M=8.2 \mathrm{mg}\). What is the value of the partition coefficient if the mass diffusivity is \(D_{\mathrm{AB}}=0.2 \times 10^{-11} \mathrm{~m}^{2} / \mathrm{s}\) ?

As an employee of the Los Angeles Air Quality Commission, you have been asked to develop a model for computing the distribution of \(\mathrm{NO}_{2}\) in the atmosphere. The molar flux of \(\mathrm{NO}_{2}\) at ground level, \(N_{\mathrm{A}, 0}^{N}\), is presumed known. This flux is attributed to automobile and smoke stack emissions. It is also known that the concentration of \(\mathrm{NO}_{2}\) at a distance well above ground level is zero and that \(\mathrm{NO}_{2}\) reacts chemically in the atmosphere. In particular, \(\mathrm{NO}_{2}\) reacts with unburned hydrocarbons (in a process that is activated by sunlight) to produce PAN (peroxyacetylnitrate), the final product of photochemical smog. The reaction is first order, and the local rate at which it occurs may be expressed as \(\dot{N}_{\mathrm{A}}=-k_{1} C_{\mathrm{A}}\). (a) Assuming steady-state conditions and a stagnant atmosphere, obtain an expression for the vertical distribution \(C_{\mathrm{A}}(x)\) of the molar concentration of \(\mathrm{NO}_{2}\) in the atmosphere. (b) If an \(\mathrm{NO}_{2}\) partial pressure of \(p_{\mathrm{A}}=2 \times 10^{-6}\) bar is sufficient to cause pulmonary damage, what is the value of the ground level molar flux for which you would issue a smog alert? You may assume an isothermal atmosphere at \(T=300 \mathrm{~K}\), a reaction coefficient of \(k_{1}=0.03 \mathrm{~s}^{-1}\), and an \(\mathrm{NO}_{2}\)-air diffusion coefficient of \(D_{\mathrm{AB}}=0.15 \times 10^{-4} \mathrm{~m}^{2} / \mathrm{s}\).

Consider the problem of oxygen transfer from the interior lung cavity, across the lung tissue, to the network of blood vessels on the opposite side. The lung tissue (species B) may be approximated as a plane wall of thickness \(L\). The inhalation process may be assumed to maintain a constant molar concentration \(C_{\mathrm{A}}(0)\) of oxygen (species A) in the tissue at its inner surface \((x=0)\), and assimilation of oxygen by the blood may be assumed to maintain a constant molar concentration \(C_{\mathrm{A}}(L)\) of oxygen in the tissue at its outer surface \((x=L)\). There is oxygen consumption in the tissue due to metabolic processes, and the reaction is zero order, with \(\dot{N}_{\mathrm{A}}=-k_{0}\). Obtain expressions for the distribution of the oxygen concentration in the tissue and for the rate of assimilation of oxygen by the blood per unit tissue surface area.

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