/*! This file is auto-generated */ .wp-block-button__link{color:#fff;background-color:#32373c;border-radius:9999px;box-shadow:none;text-decoration:none;padding:calc(.667em + 2px) calc(1.333em + 2px);font-size:1.125em}.wp-block-file__button{background:#32373c;color:#fff;text-decoration:none} Problem 27 An experiment is designed to mea... [FREE SOLUTION] | 91Ó°ÊÓ

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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 \(D_{\mathrm{AB}}=0.2 \times 10^{-11} \mathrm{~m}^{2} / \mathrm{s}\) ?

Short Answer

Expert verified
The partition coefficient, \(K\), for the pharmaceutical product passing through the polymer material is approximately \(4.3\).

Step by step solution

01

Define given variables

First, we need to define all the given variables for better understanding and easy calculation. Here are the given variables: - Density of the pharmaceutical, \(\rho_p = 1250 kg/m^3\) - Inner diameter of the sphere, \(D_i = 5mm\) - Outer diameter of the sphere, \(D_o = 5.1mm\) - Mass reduction after one week, \(\Delta M = 8.2 mg\) - Mass diffusivity, \(D_{AB} = 0.2 \times 10^{-11} m^2/s\)
02

Calculate the radius of the sphere

Calculate the inner and outer radius of the sphere. Inner radius, \(r_i = \frac{D_i}{2} = \frac{5 \times 10^{-3}}{2} = 2.5 \times 10^{-3}m\) Outer radius, \(r_o = \frac{D_o}{2} = \frac{5.1 \times 10^{-3}}{2} = 2.55 \times 10^{-3}m\)
03

Calculate the mass flow rate of the pharmaceutical

Calculate the mass flow rate (molar transport) of the pharmaceutical product through the sphere: \[ m = \frac{\Delta M}{t} \] where t is the time taken for mass reduction in seconds (one week). Convert time from weeks to seconds: \[ t = 1 \ week \times \frac{7 \ day}{1 \ week} \times \frac{24 \ hour}{1 \ day} \times \frac{3600 \ s}{1 \ hour} = 604800 \ s \] Calculate the mass flow rate (in \(kg/s\)): \[ m = \frac{8.2 \times 10^{-6}}{604800} \approx 1.355 \times 10^{-11} \ kg/s \]
04

Utilize Fick's first law of diffusion

According to Fick's first law of diffusion, the molar transport (mass flow rate) is given by: \[ m = - A \rho_p D_{AB} \frac{dC_A}{dx} \] Since the concentration gradient is across the sphere's thickness, we need to rewrite the equation with respect to the radii of the sphere (i.e., from inner surface \(r_i\) to outer surface \(r_o\)): \[ m = - A \rho_p D_{AB} \frac{\Delta C_A}{\Delta r} \] Where \(\Delta C_A\) is the change in concentration across the sphere's thickness \(\Delta r = r_o - r_i\), and A is the surface area at the inner surface. Calculate the surface area at the inner surface: \[ A = 4 \pi r_i^2 = 4 \pi (2.5 \times 10^{-3})^2 \approx 7.854 \times 10^{-5} \ m^2 \]
05

Calculate the partition coefficient

Rearrange the Fick's first law of diffusion equation to solve for the partition coefficient: \[ K = - \frac{dC_A}{dx} = \frac{m}{A \rho_p D_{AB}} \] Substitute the values and compute K: \[ K = \frac{1.355 \times 10^{-11}}{7.854 \times 10^{-5}\times 1250 \times 0.2 \times 10^{-11}} \approx 4.3 \] Result: The partition coefficient, \(K \approx 4.3\).

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Key Concepts

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

Mass Transfer in Polymers
Mass transfer in polymers is a critical concept in materials science and engineering, particularly when discussing the permeation of gases, vapors, or liquids through polymeric materials.

This process is significant in various applications, including packaging, biomedical devices, and controlled drug delivery systems. The rate of mass transfer within a polymer depends on the interaction between the diffusing species and the polymer matrix. Factors such as the size and shape of the diffusing molecules, the polymer's crystallinity, and its temperature can all influence the diffusion process.

The partition coefficient plays a vital role here. It defines the equilibrium concentration of the diffusing substance on both sides of the polymer interface. In pharmaceutical applications, understanding the partition coefficient helps in predicting how a drug will permeate through polymer-based delivery systems, impacting the drug's release and effectiveness.

In the context of the exercise, the polymer in the form of a hollow sphere represents a barrier the pharmaceutical product must diffuse through. The mass transfer within this polymer then determines the rate of drug delivery to the surrounding environment.
Fick's First Law of Diffusion
Fick's first law of diffusion is a principe rooted in the heart of mass transfer phenomena, often employed to explain and quantify the diffusion process.

This law states that the flux of a substance from a region of high concentration to a region of low concentration is proportional to the concentration gradient. Mathematically, this is expressed as \( J = -D \frac{dC}{dx} \), where \( J \) is the diffusion flux, \( D \) is the diffusivity of the substance, and \( \frac{dC}{dx} \) is the concentration gradient.

In our exercise's context, using Fick's law helps calculate the amount of pharmaceutical that has diffused through the spherical polymer, enabling the effective determination of the partition coefficient. Understanding Fick's law is fundamental for students as it underpins the entire field of diffusion-related processes in pharmaceuticals and numerous other industries.
Pharmaceutical Diffusivity
Pharmaceutical diffusivity refers to the ease with which drug molecules migrate within another medium, such as a polymer or a biological tissue.

In practice, it's a measure of how fast a pharmaceutical compound can spread through a substance, and it is a crucial parameter in the design of drug delivery systems. The diffusivity, often denoted by \( D \), affects how quickly a drug is released from its carrier and how it subsequently distributes within the body.

Physicochemical properties of the drug and the medium, temperature, and molecular interactions all influence diffusivity. In our exercise, the known diffusivity value (\( D_{AB} \) for the pharmaceutical product) is critical for calculating the partition coefficient. These calculations help to ensure that the drug is released in a controlled manner to achieve desired therapeutic effects.
Molar Transport
Molar transport, in the domain of physical chemistry and engineering, pertains to the movement of moles of a substance per unit time. It's essentially the molar flow rate and can refer to both the macroscopic and microscopic movement of particles.

In the context of mass transfer operations, molar transport is measured when considering the rate at which a substance moves through a given area. This concept can be applied using Fick's first law of diffusion as seen in the exercise, with the molar transport being equivalent to the mass flow rate of the pharmaceutical through the polymer sphere.

The calculation of molar transport is critical when designing systems where controlled release of a substance is needed, such as in pharmaceutical applications, where the steady and predictable delivery of a drug is necessary for efficacy and safety.

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Most popular questions from this chapter

A He-Xe mixture containing \(0.75\) mole fraction of helium is used for cooling of electronics in an avionics application. At a temperature of \(300 \mathrm{~K}\) and atmospheric pressure, calculate the mass fraction of helium and the mass density, molar concentration, and molecular weight of the mixture. If the cooling system capacity is \(10 \mathrm{~L}\), what is the mass of the coolant?

Hydrogen gas is used in a process to manufacture a sheet material of \(6-\mathrm{mm}\) thickness. At the end of the process, \(\mathrm{H}_{2}\) remains in solution in the material with a uniform concentration of \(320 \mathrm{kmol} / \mathrm{m}^{3}\). To remove \(\mathrm{H}_{2}\) from the material, both surfaces of the sheet are exposed to an airstream at \(500 \mathrm{~K}\) and a total pressure of \(3 \mathrm{~atm}\). Due to contamination, the hydrogen partial pressure is \(0.1 \mathrm{~atm}\) in the airstream, which provides a convection mass transfer coefficient of \(1.5 \mathrm{~m} / \mathrm{h}\). The mass diffusivity and solubility of hydrogen (A) in the sheet material (B) are \(D_{\mathrm{AB}}=2.6 \times 10^{-8} \mathrm{~m}^{2} / \mathrm{s}\) and \(S_{\mathrm{AB}}=160 \mathrm{kmol} / \mathrm{m}^{3} \cdot\) atm, respectively. (a) If the sheet material is left exposed to the airstream for a long time, determine the final content of hydrogen in the material \(\left(\mathrm{kg} / \mathrm{m}^{3}\right)\). (b) Identify and evaluate the parameter that can be used to determine whether the transient mass diffusion process in the sheet can be assumed to be characterized by a uniform concentration at any time during the process. Hint: This situation is analogous to that used to determine the validity of the lumped-capacitance method for a transient heat transfer analysis. (c) Determine the time required to reduce the hydrogen mass density at the center of the sheet to twice the limiting value calculated in part (a).

A 100-mm-long, hollow iron cylinder is exposed to a \(1000^{\circ} \mathrm{C}\) carburizing gas (a mixture of \(\mathrm{CO}\) and \(\mathrm{CO}_{2}\) ) at its inner and outer surfaces of radii \(4.30\) and \(5.70 \mathrm{~mm}\), respectively. Consider steady-state conditions for which carbon diffuses from the inner surface of the iron wall to the outer surface and the total transport amounts to \(3.6 \times 10^{-3} \mathrm{~kg}\) of carbon over \(100 \mathrm{~h}\). The variation of the carbon composition (weight \(\%\) carbon) with radius is tabulated for selected radii. $$ \begin{array}{lllllllll} r(\mathrm{~mm}) & 4.49 & 4.66 & 4.79 & 4.91 & 5.16 & 5.27 & 5.40 & 5.53 \\ \text { Wt.C }(\%) & 1.42 & 1.32 & 1.20 & 1.09 & 0.82 & 0.65 & 0.46 & 0.28 \end{array} $$ (a) Beginning with Fick's law and the assumption of a constant diffusion coefficient, \(D_{\mathrm{C}-\mathrm{Fe}}\), show that \(d \rho_{\mathrm{C}} / d(\ln r)\) is a constant. Sketch the carbon mass density, \(\rho_{\mathrm{C}}(r)\), as a function of \(\ln r\) for such a diffusion process. (b) The foregoing table corresponds to measured distributions of the carbon mass density. Is \(D_{\mathrm{C}-\mathrm{Fe}}\) constant for this diffusion process? If not, does \(D_{\mathrm{C}-\mathrm{Fe}}\) increase or decrease with an increasing carbon concentration? (c) Using the experimental data, calculate and tabulate \(D_{\mathrm{C}-\mathrm{Fe}}\) for selected carbon compositions.

The presence of \(\mathrm{CO}_{2}\) in solution is essential to the growth of aquatic plant life, with \(\mathrm{CO}_{2}\) used as a reactant in the photosynthesis. Consider a stagnant body of water in which the concentration of \(\mathrm{CO}_{2}\left(\rho_{\mathrm{A}}\right)\) is everywhere zero. At time \(t=0\), the water is exposed to a source of \(\mathrm{CO}_{2}\), which maintains the surface \((x=0)\) concentration at a fixed value \(\rho_{\mathrm{A}, 0}\). For time \(t>0, \mathrm{CO}_{2}\) will begin to accumulate in the water, but the accumulation is inhibited by \(\mathrm{CO}_{2}\) consumption due to photosynthesis. The time rate at which this consumption occurs per unit volume is equal to the product of a reaction rate constant \(k_{1}\) and the local \(\mathrm{CO}_{2}\) concentration \(\rho_{\mathrm{A}}(x, t)\). (a) Write (do not derive) a differential equation that could be used to determine \(\rho_{\mathrm{A}}(x, t)\) in the water. What does each term in the equation represent physically? (b) Write appropriate boundary conditions that could be used to obtain a particular solution, assuming a "deep" body of water. What would be the form of this solution for the special case of negligible \(\mathrm{CO}_{2}\) consumption \(\left(k_{1} \approx 0\right)\) ?

An old-fashioned glass apothecary jar contains a patent medicine. The neck is closed with a rubber stopper that is \(20 \mathrm{~mm}\) tall, with a diameter of \(10 \mathrm{~mm}\) at the bottom end, widening to \(20 \mathrm{~mm}\) at the top end. The molar concentration of medicine vapor in the stopper is \(2 \times 10^{-3} \mathrm{kmol} / \mathrm{m}^{3}\) at the bottom surface and is negligible at the top surface. If the mass diffusivity of medicine vapor in rubber is \(0.2 \times 10^{-9} \mathrm{~m}^{2} / \mathrm{s}\), find the rate \((\mathrm{kmol} / \mathrm{s})\) at which vapor exits through the stopper.

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