ELEMENTS OF CHEM. REACTION ENGR
5th Edition
ISBN: 9780135486498
Author: Fogler
Publisher: INTER PEAR
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Chapter 14, Problem 14.7P
Interpretation Introduction
Interpretation:
The percentage of chlorine that would be removed under the given proposed scheme has to be determined.
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67%
D
三
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Determine the relative amounts (in terms of volume fractions) for a 67.0 wt% Pb-33.0 wt% Mg alloy at 425°C. The densities of lead
and magnesium at 425°C are given as follows:
PPb 10.96 g/cm³
=
PMg 1.68 g/cm³
You may also want to use Animated Figure 9.20.
Va
=
0.4558
0.5442
VMg2Pb
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Thesis/Dissertation, Research, Or Independent Study In Mechanical Engineering
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A
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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
Chapter 14 Solutions
ELEMENTS OF CHEM. REACTION ENGR
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- 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.arrow_forwardplease, provide me with right resultsarrow_forwardEx. HW. A vertical glass tube, 2cm ID & 5m long in heated uniformly over its length. The water enter at (200-204 C) & 68.9 bar calculated the pressure drop if the flowrate 0.15 Kg/s & the power applied as a heat to the fluid is 100KW using the homogeneous model. Given that enthalpy at inlet temp.=0.87MJ/Kg, enthalpy saturation temp (285C)=1.26 MJ/Kg and μl=0.972*10-4 Ns/m2, μG=2.89*10-5 Ns/m2, UG=2.515*10-2m3/Kg and the change in UG over range of pressure=-4.45*10-4m3/Kg/bar.arrow_forward
- 4. An experimental test rig is used to examine two-phase flow regimes in horizontal pipelines. A particular experiment involved uses air and water at a temperature of 25°C, which flow through a horizontal glass tube with an internal diameter of 25.4 mm and a length of 40 m. Water is admitted at a controlled rate of 0.026 kgs at one end and air at a rate of 5 x 104 kgs in the same direction. The density of water is 1000 kgm³, and the density of air is 1.2 kgm. Determine the mass flow rate, the mean density, gas void fraction, and the superficial velocities of the air and water. Answer: 0.02605 kgs 1, 61.1 kgm³, 0.94, 0.822 ms-1, 0.051 ms-1arrow_forwardand the viscosity of the water is 1.24 × 104 Nsm 2. Answer: Slug flow 1. Determine the range of mean density of a mixture of air in a 50:50 oil-water liquid phase across a range of gas void fractions. The den- sity of oil is 900 kgm³, water is 1000 kgm³, and gas is 10 kgm³.arrow_forwardA chemical reaction takes place in a container of cross-sectional area 50.0 cm2. As a result of the reaction, a piston is pushed out through 15 cm against an external pressure of 121 kPa. Calculate the work done (in J) by the system.arrow_forward
- Example 7.2 Steam is generated in a high pressure boiler containing tubes 2.5 m long and 12.5 mm internal diameter. The wall roughness is 0.005 mm. Water enters the tubes at a pressure of 55.05 bar and a temperature of 270°C, and the water flow rate through each tube is 500 kg/h. Each tube is heated uniformly at a rate of 50 kW. Calle (a) Estimate the pressure drop across each tube (neglecting end effects) using (i) the homogeneous flow model and (ii) the Martinelli-Nelson correlation. (b) How should the calculation be modified if the inlet temperature were 230°C at the same pressure?arrow_forwardPlease solve this question by simulation in aspen hysysarrow_forward(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_forward
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