Warning: foreach() argument must be of type array|object, bool given in /var/www/html/web/app/themes/studypress-core-theme/template-parts/header/mobile-offcanvas.php on line 20

How can you convert the general mole balance equation for a given species, Equation \((1-4),\) to a general mass balance equation for that species?

Short Answer

Expert verified
To convert the general mole balance equation to a general mass balance equation for a given species, first understand the relationship between moles and mass using the molar mass (\(M_A\)). Then, replace the moles and molar flow rates in the mole balance equation with their corresponding mass and mass flow rate expressions. The resulting general mass balance equation for species A will be: \(\frac{d(m_A)}{dt} = q_{A0} - q_A + V\dot{R_A}\)

Step by step solution

01

Recall the general mole balance equation

The general mole balance equation for a given species is given by: Equation (1-4): \(\frac{d(N_A)}{dt} = F_{A0} - F_A + V\dot{r_A}\) where: - \(N_A\) represents the number of moles of species A - \(F_{A0}\) represents the molar flow rate at which species A enters the system - \(F_A\) represents the molar flow rate at which species A leaves the system - \(V\) represents the volume of the system - \(\dot{r_A}\) represents the rate of generation of species A in the system (moles per unit volume and time)
02

Understand the relationship between moles and mass

The relationship between moles and mass is given by the molar mass (\(M_A\)) of species A. The molar mass of a substance is the mass of one mole of that substance, measured in grams per mole. Knowing this relationship, we can write the following expressions for species A: 1. Mass of species A = \(m_A = N_A * M_A\) 2. Mass flow rate at which species A enters the system = \(q_{A0} = F_{A0} * M_A\) 3. Mass flow rate at which species A leaves the system = \(q_A = F_A * M_A\) 4. Rate of generation of species A in terms of mass = \(\dot{R_A} = \dot{r_A} * M_A\)
03

Substitute the expressions for moles to mass in the mole balance equation

Now let's substitute the expressions from Step 2 into the mole balance equation: First, differentiate the mass of species A with respect to time: \(\frac{d(m_A)}{dt} = \frac{d(N_A * M_A)}{dt}\) Using the chain rule of differentiation, we get: \(\frac{d(m_A)}{dt} = M_A * \frac{d(N_A)}{dt}\) Now, substitute the expressions for mass flow rates and the rate of generation: \(M_A * \frac{d(N_A)}{dt} = M_A * (F_{A0} - F_A + V\dot{r_A})\) Divide the entire equation by \(M_A\): \(\frac{d(m_A)}{dt} = q_{A0} - q_A + V\dot{R_A}\) This is the general mass balance equation for species A.

Unlock Step-by-Step Solutions & Ace Your Exams!

  • Full Textbook Solutions

    Get detailed explanations and key concepts

  • Unlimited Al creation

    Al flashcards, explanations, exams and more...

  • Ads-free access

    To over 500 millions flashcards

  • Money-back guarantee

    We refund you if you fail your exam.

Over 30 million students worldwide already upgrade their learning with Vaia!

Key Concepts

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

Mole Balance Equation
Understanding the mole balance equation is central to analyzing chemical reactions and processes. This fundamental equation serves as a basis for determining how species react and change over time within a system.

At its core, the mole balance equation tells us how the number of moles of a substance, represented by \( N_A \), changes during a chemical process. Think of it as keeping track of molecules as they enter, are generated or consumed, and leave a reactor or system. For species A, this is described mathematically as:
\[\frac{d(N_A)}{dt} = F_{A0} - F_A + V\dot{r_A}\]
The equation accounts for the moles entering the system \( F_{A0} \) and leaving \( F_A \) as well as the moles generated \( V\dot{r_A} \) inside the system. Often, understanding and applying this equation requires a clear grasp of concepts like molar flow rates and the rate of generation of a species. By using it, we can analyze and optimize chemical reactors for a wide range of industrial applications, such as the synthesis of pharmaceuticals or the creation of biofuels.
Molar Mass
The molar mass \( M_A \) is a bridge between the microscopic world of atoms and molecules to the macroscopic world we can measure and observe. It represents the weight of a mole of a substance, usually expressed in grams per mole (g/mol).

This concept becomes incredibly useful when converting between moles and grams, which is essential for practical applications like scaling up reactions from the laboratory bench to industrial production. To calculate the mass \( m_A \) of a species A, we can use:
\[m_A = N_A \times M_A\]
Molar mass thus allows us to translate the abstract idea of 'moles' into tangible quantities of mass that are useful in real-world scenarios.
Rate of Generation
The rate of generation, denoted as \( \dot{r_A} \), is a pivotal concept in the study of chemical kinetics and reactor design. It describes the speed at which species A is produced (or consumed) in a reaction per unit volume, typically measured in moles per unit volume per time.

For a given reaction, this rate can either be positive (indicating generation) or negative (indicating consumption). When we consider a reaction happening throughout the entire volume of a system, we obtain the total rate of generation or consumption by multiplying this rate by the system's volume (\( V \)).

In terms of mass, the rate of generation translates to \( \dot{R_A} = \dot{r_A} \times M_A \), reflecting how this parameter is essential for determining the mass change of a species over time within our system.
Mass Flow Rate
The mass flow rate is a key term in understanding how substances move through a system. For a specific species A, it is the mass of A that flows per unit time, denoted as \( q_A \). This rate gives us the power to quantify the actual amount of substance moving in and out of a chemical reactor or process.

In the context of our exercise, the mass flow rate allowing species A to enter the system is \( q_{A0} = F_{A0} \times M_A \), and the corresponding rate at which it leaves is \( q_A = F_A \times M_A \). By determining these rates, we can manage and design processes to ensure that desired reactants are supplied and products removed at the appropriate speeds to maintain efficient operation.

One App. One Place for Learning.

All the tools & learning materials you need for study success - in one app.

Get started for free

Most popular questions from this chapter

(a) There are initially 500 rabbits \((x)\) and 200 foxes \((y)\) on Farmer Oat's property. Use Polymath or MATLAB to plot the concentration of foxes and rabbits as a function of time for a period of up to 500 days. The predator- prey relationships are given by the following set of coupled ordinary differential equations: $$\frac{d x}{d t}=k_{1} x-k_{2} x \cdot y$$ $$\frac{d y}{d t}=k_{3} x \cdot y-k_{4} y$$ Constant for growth of rabbits \(k_{1}=0.02\) day \(^{-1}\) Constant for death of rabbits \(k_{2}=0.00004 /\) (day \(\times\) no. of foxes) Constant for growth of foxes after eating rabbits \(k_{3}=0.0004 /\) (day \(\times\) no. of rabbits) Constant for death of foxes \(k_{4}=0.04\) day \(^{-1}\) What do your results look like for the case of \(k_{3}=0.00004 /\) (day \(\times\) no. of rabbits) and \(t_{\text {final }}=800\) days? Also plot the number of foxes versus the number of rabbits. Explain why the curves look the way they do. Vary the parameters \(k_{1}, k_{2}, k_{3},\) and \(\overline{k_{4}} .\) Discuss which parameters can or cannot be larger than others. Write a paragraph describing what you find. (b) Use Polymath or MATLAB to solve the following set of nonlinear algebraic equations: $$\begin{array}{r} x^{3} y-4 y^{2}+3 x=1 \\ 6 y^{2}-9 x y=5 \end{array}$$ with initial guesses of \(x=2, y=2 .\) Try to become familiar with the edit keys in Polymath MATLAB. See the CD-ROM for instructions.

What assumptions were made in the derivation of the design equation for: (a) the batch reactor? (b) the CSTR? (c) the plug-flow reactor (PFR)? (d) the packed-bed reactor (PBR)? (e) State in words the meanings of \(-r_{A} .-r_{A}^{\prime} .\) and \(r_{A}^{\prime} .\) Is the reaction rate \(-r_{A}\) an extensive quantity? Explain.

Enrico Fermi was an Italian physicist who received the Nobel Prize for his work on nuclear processes. Fermi was famous for his "Back of the Envelope Order of Magnitude Calculation" to obtain an estimate of the answer through logic and making reasonable assumptions. He used a process to set bounds on the answer by saying it is probably larger than one number and smaller than another and arrived at an answer that was within a factor of 10 . Enrico Fermi Problem (EFP) \(=1\) How many piano tuners are there in the city of Chicago? Show the steps in your reasoning. 1\. Population of Chicago________ 2\. Number of people per household________ 3\. Number of households________ 4\. Households with pianos________ 5\. Average number of tunes per year________ 6\. Etc.________ An answer is given on the web under Summary Notes for Chapter 1.

Calculate the time to reduce the number of moles of \(\mathrm{A}\) to \(1 \%\) of its initial value in a constant-volume batch reactor for the reaction and data in Example \(1-1\).

We are going to consider the cell as a reactor. The nutrient corn steep liquor enters the cell of the microorganism Penicillium chrysogenum and is decomposed to form such products as amino acids. RNA, and DNA. Write an unsteady mass balance on (a) the corn steep liquor, (b) RNA, and (c) pencillin. Assume the cell is well mixed and that RNA remains inside the cell.

See all solutions

Recommended explanations on Chemistry Textbooks

View all explanations

What do you think about this solution?

We value your feedback to improve our textbook solutions.

Study anywhere. Anytime. Across all devices.

Sign-up for free