A liquid mixture containing 40.0 wt% n-octane and the balance n-decane flows into a tank mounted on a balance. The mass in kg indicated by the scale is plotted against time. The data fall on a straight line that passes through the points (t = 3 min, m = 150 kg) and (t= 10 min, m = 250 kg).
(a) Estimate the volumetric flow rate of the liquid mixture.
(b) What does the empty tank weigh?
.
(a)
Interpretation:
Volumetric flow rate of the mixture is to be calculated.
Concept introduction:
Volumetric flow rate of a fluid is the volume of a fluid that passes per unit time. It is mathematically represented as follows:
Volumetric flow rate =
Here,
Answer to Problem 5.1P
19.85 m3/min
Explanation of Solution
Given Information: Density of n-Octane =
Average density of the mixture = avg
Given graph is a straight line with slope as follows:
=
Putting the values, =
=19.85 m3/min
(b)
Interpretation:
Weight of empty tank is to be calculated.
Concept introduction:
A straight line equation is y = mx + c, where,
y = y-axis coordinate
x = x- axis coordinate
m = slope of line
c = intercept of straight line
Weight of a substance = Mass of substance
Answer to Problem 5.1P
1050.16 N
Explanation of Solution
The equation is a straight line with equation
m = at + c
where,
m = mass
a = slope of line
t = time
c = intercept
Mass of empty tank is mass at t = 0
i.e.
m = 0 + c
Mass of empty tank = intercept of the straight line
a =
a = 14.28 kg/min
At t = 3 min, m =150 kg
So,
150 = (14.28) (3) + c
c = 107.16
Therefore, mass of empty tank = 107.16 kg
Now, weight can be calculated using the following formula:
Here, g is acceleration due to gravity.
Putting the values,
W = 107.16
Want to see more full solutions like this?
Chapter 5 Solutions
ELEM.PRIN.OF CHEM.PROCESS-ACCESS
Additional Engineering Textbook Solutions
Introduction To Programming Using Visual Basic (11th Edition)
Java How to Program, Early Objects (11th Edition) (Deitel: How to Program)
Modern Database Management
Elementary Surveying: An Introduction To Geomatics (15th Edition)
Electric Circuits. (11th Edition)
- (11.35. For a binary gas mixture described by Eqs. (3.37) and (11.58), prove that: 4812 Pу132 ✓ GE = 812 Py1 y2. ✓ SE dT HE-12 T L = = (812 - 7 1/8/123) d² 812 Pylyz C=-T Pylyz dT dT² See also Eq. (11.84), and note that 812 = 2B12 B11 - B22. perimental values of HE for binary liquid mixtures ofarrow_forwardplease provide me the solution with more details. because the previous solution is not cleararrow_forwardplease, provide me the solution with details.arrow_forward
- please, provide me the solution with detailsarrow_forwardPlease, provide me the solution with details and plot.arrow_forwardQ2/ An adsorption study is set up in laboratory by adding a known amount of activated carbon to six which contain 200 mL of an industrial waste. An additional flask containing 200 mL of waste but no c is run as a blank. Plot the Langmuir isotherm and determine the values of the constants. Flask No. Mass of C (mg) Volume in Final COD Flask (mL) (mg C/L) 1 804 200 4.7 2 668 200 7.0 3 512 200 9.31 4 393 200 16.6 C 5 313 200 32.5 6 238 200 62.8 7 0 200 250arrow_forward
- مشر on ۲/۱ Two rods (fins) having same dimensions, one made of brass(k=85 m K) and the other of copper (k = 375 W/m K), having one of their ends inserted into a furnace. At a section 10.5 cm a way from the furnace, the temperature brass rod 120°C. Find the distance at which the same temperature would be reached in the copper rod ? both ends are exposed to the same environment. 22.05 ofthearrow_forward4.59 Using the unilateral z-transform, solve the following difference equations with the given initial conditions. (a) y[n]-3y[n-1] = x[n], with x[n] = 4u[n], y[− 1] = 1 (b) y[n]-5y[n-1]+6y[n-2]= x[n], with x[n] = u[n], y[-1] = 3, y[-2]= 2 Ans. (a) y[n] = -2+9(3)", n ≥ -1 (b) y[n]=+8(2)" - (3)", n ≥ -2arrow_forward(30) 6. In a process design, the following process streams must be cooled or heated: Stream No mCp Temperature In Temperature Out °C °C kW/°C 1 5 350 270 2 9 270 120 3 3 100 320 4 5 120 288 Use the MUMNE algorithm for heat exchanger networks with a minimum approach temperature of 20°C. (5) a. Determine the temperature interval diagram. (3) (2) (10) (10) b. Determine the cascade diagram, the pinch temperatures, and the minimum hot and cold utilities. c. Determine the minimum number of heat exchangers above and below the pinch. d. Determine a valid heat exchange network above the pinch. e. Determine a valid heat exchange network below the pinch.arrow_forward
- 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