ELEM.PRINCIPLES OF CHEMICAL PROCESSES
ELEM.PRINCIPLES OF CHEMICAL PROCESSES
4th Edition
ISBN: 9781119571070
Author: FELDER
Publisher: WILEY
bartleby

Videos

Textbook Question
Book Icon
Chapter 10, Problem 10.12P

. A gas leak has led to the presence of 1.00 mole% carbon monoxide in a 350-m3laboratory.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 at the same temperature and pressure and that the laboratory air is perfectly mixed throughout the purging process,

  1. Let tr(h) be the time required for the specified reduction in the carbon monoxide concentration.

Write a differential CO mole balance, letting A equal the total moles of gas in the room (assume constant), the mole fraction of CO in the room air, and V ˙ P ( m 3 / h ) 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 dx/dt and provide an initial condition. Sketch a plot of x versus Z, labeling the value of x at t = 0 and the asymptotic value at t ? 8.

Integrate the balance to derive an equation for trin terms of V ˙ P .

  1. If the volumetric flow rate is 700 m3/h (representing a turnover 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?
  2. 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?

Blurred answer
Students have asked these similar questions
Advance Statistics and DOL 01 (90%): Use the below experimental regions information and the data given in the below table to run and analyze the Yield of reactor presented below: Factors; Response: Temperature (°C): (150, 250) Pressure (bar): (1.5, 10) Flow Rate (L/min): (10, 30) Yield (%): Hypothetical yield data for each combination of factors. Use 2 factorial, full factorial, Central Composite, and Box-Behnken designs to construct the design tables that are required to run the experiments (real and coded). Then analyze the results using MINITAB software to show the regression model for you think is the Yield and most effective parameters and interaction. Which design do the giving best model fitting based on your results? (Note; use 3 center point). 02 (10%): Use the Hypothetical yield data shown in the below Table to find the variance and standard deviation and the median. Hypothetical Yield Data Run Temperature (°C) Pressure (bar) Flow Rate (L/min) Yield (%) 1 150 1 10 65 2 150 1…
Derive the formula boundary-s layer, thickness 5x Rex
Q2] The reaction AR + S is irreversible and first order. It is conducted in a PFR with 50 tubes, each with 0.5 in diameter and 1.0 m of height. 200 kg/h of reactant A (MW-80 g/gmol) with 30% inert is introduced at a pressure of 50 atm at 500°C. The output conversion is 80%. Calculate the average residence time.

Additional Engineering Textbook Solutions

Find more solutions based on key concepts
Here is the code for the displayValue method, shown earlier in this chapter: public static void displayValue(in...

Starting Out with Java: From Control Structures through Objects (7th Edition) (What's New in Computer Science)

What is the difference between overriding a superclass method and overloading a superclass method?

Starting Out with Java: From Control Structures through Data Structures (4th Edition) (What's New in Computer Science)

Knowledge Booster
Background pattern image
Chemical Engineering
Learn more about
Need a deep-dive on the concept behind this application? Look no further. Learn more about this topic, chemical-engineering and related others by exploring similar questions and additional content below.
Similar questions
SEE MORE QUESTIONS
Recommended textbooks for you
Text book image
Introduction to Chemical Engineering Thermodynami...
Chemical Engineering
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:McGraw-Hill Education
Text book image
Elementary Principles of Chemical Processes, Bind...
Chemical Engineering
ISBN:9781118431221
Author:Richard M. Felder, Ronald W. Rousseau, Lisa G. Bullard
Publisher:WILEY
Text book image
Elements of Chemical Reaction Engineering (5th Ed...
Chemical Engineering
ISBN:9780133887518
Author:H. Scott Fogler
Publisher:Prentice Hall
Text book image
Process Dynamics and Control, 4e
Chemical Engineering
ISBN:9781119285915
Author:Seborg
Publisher:WILEY
Text book image
Industrial Plastics: Theory and Applications
Chemical Engineering
ISBN:9781285061238
Author:Lokensgard, Erik
Publisher:Delmar Cengage Learning
Text book image
Unit Operations of Chemical Engineering
Chemical Engineering
ISBN:9780072848236
Author:Warren McCabe, Julian C. Smith, Peter Harriott
Publisher:McGraw-Hill Companies, The
Mod-01 Lec-23 Degrees of freedom analysis; Author: nptelhrd;https://www.youtube.com/watch?v=c4h85JjrkzQ;License: Standard YouTube License, CC-BY
Introduction to Degrees of Freedom; Author: LearnChemE;https://www.youtube.com/watch?v=tW1ft4y5fQY;License: Standard Youtube License