02: 720 Ib, /min of Freon HFC 134a undergoing a change in state from (400 Psia and 60 F) to 10 Psia and 60 F. estimate the change in S,H and V?
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Compare the water quality of the natural water sample and tap water analyzed. Which quality parameters of natural water are significantly different from tap water? What quality parameters you measured in this lab are regulated by the National Primary Drinking Water Standards? Is the quality of the tap water in compliance with these standards? 3. (5107 only, bonus for 4107) Compare the results of sulfate measu
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This is for a safety engineering class and the textbook used is Industrial Safety and Health Management by Asfahl & Rieske (7th Edition) but I use the 6th edition and it's the same.
What type of hazard analysis techniques are used for the following project stages? Give two examples for each.
1.) Research and Development
2.) Design
3.) Operation
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Steam enters a turbine at a velocity of 200 m/s. The inlet conditions of the steam are at 4000 kPA and 500°C. The diameter of the inlet pipe is 50 mm. The outlet conditions of the steam are 80 kPa and a quality of 1.0. The diameter of the outlet pipe is 250 mm. Determine the turbine power output in kJ/s assuming the kinetic energy change and potential energy change are both negligible. Calculate the change in kinetic energy to show it is indeed negligible.
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Explain the main components of a battery and how electricity is produced
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Toluene vapors at 1.013 bar, 150°C, are cooled under constant pressure to a final temperature of 22°C. (a) Determine the amount of heat that must be removed (5) (b) How much heat must be removed if the final state is a vapor-liquid mixture that contains 60% vapor by mass. (5) Assume that Cp for vapor phase is a function of temperature, and for liquid toluene Cp is constant (= 155.96 J/(mol K)). The boiling temperature of toluene at 1.013 bar is 110.6°C, and standard heat of vaporization for toluene 38060 J/mol.
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Calculate (using equation) and estimate (using figure) the following: a. Dc in FCC Fe at 912C b. Dc in BCC Fe at 912C c. DNi in FCC Fe at 912C Compare the two values for each case (one from equation and other from figure) and comment on any difference.
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What is the process of acquiring white cast Fe, Gray cast Fe, ductile cast Fe and malleable cast Fe, as well as their carefully sketch microstructures?
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For 1 kg of liquid water, determine the entropy change of the universe when the water is: Initially at 0 C, is heated to 50 C by contact with a thermal reservoir at 50 C and then to 100 C with a thermal reservoir at 100 C Assume Cp = 4.2 kJ/kg-K
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|
Size if aperture (mm) |
Mass retained % |
|
6 |
0 |
|
4 |
26 |
|
2 |
18 |
|
0.75 |
23 |
|
0.50 |
8 |
|
0.25 |
17 |
|
0.125 |
3 |
|
pan |
5 |
Calculate the:
|
Tyler Screen Mesh |
Weight fraction retained |
|
14 |
0.02 |
|
20 |
0.17 |
|
28 |
0.34 |
|
35 |
0.22 |
|
48 |
0.14 |
|
65 |
0.06 |
|
100 |
0.03 |
|
pan |
0.02 |
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Consider the gas phase reversible reaction 2A ↔ B that occurs at atmospheric pressure.
a) If the equilibrium constant Ka = 0.1, what are the equilibrium mole fractions of A and B?
b) Assuming the reaction is elementary, write the rate law using kA and k-A as the forward and reverse rate constants, respectively. What is the equilibrium constant Kc in terms of kA and k-A? Assuming an ideal gas system, write an expression for Ka in terms of kA and k-A. If the temperature is 25oC, what is the value of KC?
c) Assuming the reaction is elementary, and that the forward reaction rate constant kA is 2.4 L/(mol·min), determine the time for the reaction to reach 80% of equilibrium in a constant volume batch reactor. Use the value for KC you obtained in part d to solve the problem.
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Two major functions of the Battery Management System (BMS) are
Contactors Control and Cell Protection.
a. What are the information (data) needed to perform cell
protection in battery pack?
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