
Fundamentals of Chemical Engineering Thermodynamics (MindTap Course List)
1st Edition
ISBN: 9781111580704
Author: Kevin D. Dahm, Donald P. Visco
Publisher: Cengage Learning
expand_more
expand_more
format_list_bulleted
Question
Chapter 3.9, Problem 8P
Interpretation Introduction
Interpretation:
The time taken to filling the pool.
Concept Introduction:
The mass balance equation for the material entering from three sources: hose, barrel, and rain.
Here, mass flow rate of hose, barrel, and rain is
Expert Solution & Answer

Trending nowThis is a popular solution!

Students have asked these similar questions
Water at 20°C flows at a steady average velocity of 5.25 m/s
through a smooth pipe of diameter 5.08 cm. The flow is fully
developed through the entire section of pipe. The total pipe
length is 10.56 m, and there are two 90' elbows. Determine the
friction coefficient and the head loss due to friction per meter
length of the pipe.
Control
volume
Prepared by Engr. Kirsten Ga
Problem 2. For an irreversible liquid phase reaction A -> B, the reaction rate is of the first
order with respect to the reactant concentration C_A. this reaction is performed in a
cascade of two identical CSTRs at 100 degrees Celsius. (same reactor size and
isothermal). The inlet concentration of A of the first CSTR is 2mol/L. The outlet
concentration of A of the 2nd CSTR is 0.5 mol/L. the inlet flow rate of the 1st reactor is 100
L/h. and the feed temperature is 20 degrees Celsius. The average heat capacity of the
reactant/product/solvent mixture is a constant: 2J/g*K, the density of the mixture is a
constant: 1 kg/L. The heat of reaction is 50 kJ/mol (exothermic). The reaction rate constant
at 100 degrees Celsius is 0.5/h.
(a) Determine the outlet concentration of A of the first CSTR
(b) What is the heat transfer requirement for the first CSTR?
(c) if this reaction is performed in a plug-flow reactor, what is the size of plug-flow
reactor required for achieving the same conversion…
The energy release (Q_g) and energy loss (Q_r) curves of an irreversible oxidation reaction
are shown below. Q_r curves can be shifted by adjusting the feed temperature.
Q,& QE
E
Qg
(a) Are these points of intersection
between energy release and energy
loss curves stable operating
conditions?
Point of
Intersection
A
Stable or Unstable
B
A
D
T
(b) Which point represents the ignition condition?
B
с
D
E
F
G
Chapter 3 Solutions
Fundamentals of Chemical Engineering Thermodynamics (MindTap Course List)
Ch. 3.8 - 10 m3 of saturated steam at T = 150C is mixed with...Ch. 3.8 - Prob. 2ECh. 3.8 - Prob. 3ECh. 3.8 - Prob. 4ECh. 3.8 - Prob. 5ECh. 3.8 - Prob. 6ECh. 3.8 - Prob. 7ECh. 3.9 - Prob. 8PCh. 3.9 - Prob. 9PCh. 3.9 - Prob. 10P
Ch. 3.9 - Prob. 11PCh. 3.9 - Prob. 12PCh. 3.9 - Prob. 13PCh. 3.9 - Prob. 14PCh. 3.9 - Prob. 15PCh. 3.9 - Prob. 16PCh. 3.9 - Prob. 17PCh. 3.9 - Prob. 18PCh. 3.9 - Prob. 19PCh. 3.9 - Prob. 20PCh. 3.9 - Prob. 21PCh. 3.9 - Prob. 22PCh. 3.9 - Prob. 23PCh. 3.9 - Prob. 24PCh. 3.9 - Prob. 25PCh. 3.9 - Prob. 26PCh. 3.9 - 20 lb-mol/min of the compound enters a...Ch. 3.9 - Prob. 28PCh. 3.9 - Prob. 29PCh. 3.9 - Prob. 30PCh. 3.9 - Prob. 31P
Knowledge Booster
Similar questions
- Problem 1. For an irreversible liquid phase reaction 2A -> B, the reaction rate is of the 2nd order with respect to the reactant concentration CA. The concentration-dependent reaction rate is plotted below. This reaction is performed in a cascade of two identical CSTRS (same reactor size and temperature). The inlet concentration of A of the 1st CSTR is 2 mol/L. The outlet concentration of A of the 2nd CSTR is 1 mol/L. The inlet flow rate of the 1st reactor is 100 L/h. Please use the graphical method to determine the outlet concentration of A of the first CSTR and the size of each CSTR. Please briefly show the procedure for reactor size calculation. (-4-7) 15225050 45 40 35 30 0 0.5 11.761.5 C₂ Q C (mol.L¹) Co 20 2.5arrow_forward15.15 A 0.20-m-thick brick wall (k = 1.3 W/m K) separates the combustion zone of a furnace from its surroundings at 25°C. For an outside wall surface temperature of 100°C, with a convective heat-transfer coefficient of 18 W/m² K, what will be the inside wall surface temperature at steady-state conditions? .arrow_forwardAn MF membrane has pore-size distribution as follows: d(pore)0.33 fraction¼ 1.5 mm, d(pore)0.33 fraction¼ 1.0 mm, and d(pore)0.33 fraction¼ 0.5 mm. Required (a) Determine the distribution of flux density for each pore size. (b) Show by a plot the distribution of pore sizes and the distribution of flux density. solvearrow_forward
- A gas pipeline, NPS 20 with 0.500 in. wall thickness, transports natural gas (specific gravity = 0.6) at a flow rate of 250 MMSCFD at an inlet temperature of 60°F. Assuming isothermal flow, calculate the velocity of gas at the inlet and outlet of the pipe if the inlet pressure is 1000 psig and the outlet pressure is 850 psig. The base pressure and base temperature are 14.7 psia and 60°F, respectively. Assume compressibility factor Z = 1.00. What is the erosional velocity for this pipeline based on the above data and a compressibility factor Z = 0.90?arrow_forwardH.W.1 : The elementary liquid phase reaction A + BR + S is conducted in a setup consisting of a mixed reactor, into which two reactant solutions are introduced, followed by a plug flow reactor. The component B is used in a large excess so that the reaction is first order with respect to A. Various ways to increase the production rate are suggested, one of which is to reverse the order of these units. How would this change/affect conversion?arrow_forwardH.W.2 : The kinetics of the liquid phase decomposition of A is studied in two mixed flow reactors in series, the second unit having twice the volume of the first one. At steady state with a feed with CA, = 1 mol/l and mean residence time of 96 s in the first reactor, the concentration of A in the first unit (reactor) is 0.5 mol/l and in the second is 0.25 mol/l. Find the rate equation for the decomposition of A.arrow_forward
- A natural gas consists of the following molar composition: C1 = 0.871, C2 0.084, C3 = 0.023, CO2 = 0.016 and H2S = 0.006. Calculate the gas gravity to airarrow_forward8 9:07 D Asiacell من تدوير العجلة. إستمر في إستخدام تطبیق آسياسيل للحصول على المزيد من العروض المميزة! الأحد، ١٦ مارس إنتهت صلاحية الإنترنت التي تلقيتها من تدوير العجلة. إستمر في إستخدام تطبیق آسياسيل للحصول على المزيد من العروض المميزة! الاثنين، ۱۷ مارس 1000 د ارسلت من ر رصيدك الى 7707268140 في 2025/03/17. 350 د تم إستقطاعها من رصيدك لهذه العملية 8000 د ارسلت من رصيدك الى 7707268140 في 2025/03/17. 350 د تم إستقطاعها من رصيدك لهذه العملية Vol) Voi) ٨:٥٤ ص ٢:١٤ ص ٩:٥٢ م 29:07 III =arrow_forwardPGE508 Assignment 2 A mixture with 4% n-pentane, 40% n-hexane, 50% n-heptane, and 6% n-octane is to be distilled at 14.7 lb/in² (1 atm.) with 98% of the hexane and 1% of the heptane recovered in the distillate. If the liquid feed is a saturated liquid (i.e., q= 1). Calculate i.) The product compositions, ii.) The top and bottom temperature iii.) Minimum reflux ratio (Rm), iv.) Minimum theoretical plates and v.) Actual plates when the reflux ratio is 2Rm. Table 1: Component boiling point and molar mass Component Boiling point n-C5 97°F n-C 156.2°F n-C 209.1°F n-C8 258.1°F Molar mass 72.2 86.2 100.2 114.2 Hint: Since 1% of heptane is specified to be recovered in the distillate, 99% of heptane is to be recovered in the bottom.arrow_forward
arrow_back_ios
SEE MORE QUESTIONS
arrow_forward_ios
Recommended textbooks for you
- Introduction to Chemical Engineering Thermodynami...Chemical EngineeringISBN:9781259696527Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark SwihartPublisher:McGraw-Hill EducationElementary Principles of Chemical Processes, Bind...Chemical EngineeringISBN:9781118431221Author:Richard M. Felder, Ronald W. Rousseau, Lisa G. BullardPublisher:WILEYElements of Chemical Reaction Engineering (5th Ed...Chemical EngineeringISBN:9780133887518Author:H. Scott FoglerPublisher:Prentice Hall
- Industrial Plastics: Theory and ApplicationsChemical EngineeringISBN:9781285061238Author:Lokensgard, ErikPublisher:Delmar Cengage LearningUnit Operations of Chemical EngineeringChemical EngineeringISBN:9780072848236Author:Warren McCabe, Julian C. Smith, Peter HarriottPublisher:McGraw-Hill Companies, The

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

Elementary Principles of Chemical Processes, Bind...
Chemical Engineering
ISBN:9781118431221
Author:Richard M. Felder, Ronald W. Rousseau, Lisa G. Bullard
Publisher:WILEY

Elements of Chemical Reaction Engineering (5th Ed...
Chemical Engineering
ISBN:9780133887518
Author:H. Scott Fogler
Publisher:Prentice Hall


Industrial Plastics: Theory and Applications
Chemical Engineering
ISBN:9781285061238
Author:Lokensgard, Erik
Publisher:Delmar Cengage Learning

Unit Operations of Chemical Engineering
Chemical Engineering
ISBN:9780072848236
Author:Warren McCabe, Julian C. Smith, Peter Harriott
Publisher:McGraw-Hill Companies, The