Determine the transfer function H(s)/Q(s) for the liquid-level
system shown in Fig. Resistances R1
and R2 are linear. The flow rate from tank 3 is maintained constant
at b by means of a pump; i.e.,
the flow rate from tank 3 is independent of head h. The tanks are
noninteracting
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What does natural gas processing include (at the field level)?
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What is the general approach used in Nylon polymerization to get high molecular weights?
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Styrene is almost a unique monomer, in that it can be polymerized by practically all methods of chain polymerization.
A. Free radical
B. Anionic
C. Cationic
D. Co-ordination (i.e., with a catalyst)
Which of these methods would you use to make isotactic polystyrene? why?
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Waste management: What are the main forms of waste produced in the petrochemical industry and how are these maanged using recycling, reusing, incineration, landfills, and composting?
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In the game of craps, people bet on the outcome of the throw of
two, six-sided dice. Specifically, wagers are placed on the sum of
the outcome on the upward facing number on each of the two dice. We
are going to discuss relative likelihoods by counting the number of
ways (the number of microstates) associated with specific sums (the
macrostate).
A. How many microstates are associated with a throw summing to
4?
B. How many microstates are associated with a throw summing to 5?
C. How many microstates are associated with a throw summing to 10?
D. Which is more likely, rolling 2 dice that sum up to 4 or rolling 2 dice that sum up to 5?
E. Which is more likely, rolling 2 dice that sum up to 4 or rolling 2 dice that sum up to 10?
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The following module data are those for the DuPont B-10 permeator
Membrane recovery ratio: 35%
Salt rejection: 99.2%
Maximum applied pressure: 6895 kPa
Minimum brine flow rate: 1.584 m3/d
Maximum brine flow rate: 14.256 m3/d
Permeate flow rate: 2.46 m3/d
Design Data
Feed salinity is 42,000 ppm
Permeate flow rate: 5000 m3/d
Permeate pressure: 101 kPa
Design a single stage system by calculating the number of modules, osmotic pressure, permeation pressure difference, flow rates, and stream salinity.
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In: Other
Problem 1
Rectification. McCabe-Thiele Method. A mixture of benzene-toluene is to be distilled in a fractionating tower at 101.3 kPa. The column is fed 120 kg mol /h of a saturated liquid at the boiling point with 60 mol % benzene and 40 mol % toluene. The content of the distillate is 92 mol % benzene, and of the bottoms 5 mol % benzene. The reflux ratio is 3:1.
(a) Calculate the kg mol/h distillate: D=_______
(b) Calculate the kg mol/h bottoms: W=__________
(c) Attach the plot with the equilibrium line, 45? degree line, q-line, enriching and stripping operating lines, and stepping off the trays. Show with the dashed lines the stepping off assuming the Murphree tray efficiency is 0.5.
(d) Identify the position of the feed (the tray number) and inidicate the relative position of the feed to the tray: feed from bottom, from top, or both from top and from bottom.
Feed on tray ______from__________
(e) Determine graphically the theoretical number of trays:
N= _________plus a reboiler
(f) Determine graphically the actual number of trays for the case of Murphree efficiency
0.5:
N= ______plus a reboiler
(g) Calculate the overall tray efficiency in case of 0.5 Murphree tray efficiency: E0 =
(h) Attach the plot with the equilibrium line, 45? degree line, q-line, and enriching and
stripping operating lines for the case of minimum reflux ratio.
(i) Identify the point of intersection of the enriching operating line and q-line for the case of minimum reflux ratio:
x= _______y=_______
(j) Find minimum reflux ratio:
Rm=________
Estimating random-packed tower height. Consider random-packed tower in which distillation is performed under the same conditions as in Problem 1. Using 2-in Metal Intalox rings, calculate the HETP and the height of the tower.
(a) HETP=____
(b) The tower height par H= ______
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Compare and contrast the key characteristics of anionic polymerization and conventional free-radical polymerization
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What is the difference between HIPS and ABS in terms of chemical compositions? Explain the toughening mechanism associated with those two types of plastics.
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Agricultural irrigation uses a significant amount of water, and in some regions it has overwhelmed other water needs. Suppose water is drawn from a reservoir and delivered into an irrigation ditch. For most of the length of the ditch, the delivery is through a 10-cm ID pipe, and in the last few meters the pipe diameter is 7 cm. The exit from the pipe is 300 m lower than the pipe inlet.
(a) Assume that the pipe is smooth (i.e., ignore friction) and that the delivery rate is 4000 kg/h. Estimate the required pressure difference between pipe inlet and outlet. How far below the surface of the reservoir is the pipe inlet?
(b) How would your answer be different if the pipe were not smooth? Explain.
(c) What are possible environmental impacts of diverting significant quantities of river water for use in irrigation? Cite at least two sources for your response.
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a. Draw a process diagram to produce AlN powders by carbothermic reduction process. Include all possible steps, and briefly explain each step if needed.
b. In this process, what would be the keys to obtain high quality sinterable AlN powders?
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In an air-conditioning system, dry air flows over tubes carrying refrigerant R134a. The air is cooled by transferring heat to the R134a; the air enters with a volume flow rate of 0.75 m3 s–1 at 305 K and 100 kPa, and it exits at 290 K and 95 kPa. The R134a enters at 4 bar in a vapor-liquid coexistence state with a quality of 20%; it exits at 4 bar and 30 °C. Ignoring heat transfer at the outer surface of the air conditioner, neglecting kinetic and potential energy changes, and assuming a steady state, determine a) the mass flow rate of R134a and b) the rate of heat transfer between the air and the R134a. Use the available tables, diagrams, and other reliable sources to obtain required thermodynamic data.
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a.Why the Carnot cycle is not a realistic model for steam power plant? Justify your answer. [3 marks]
b. A steam power plant operates on a simple ideal Rankine cycle between the pressure limits of 9 MPa and 15 kPa. The mass flow rate of the steam through the cycle is 35 kg/s. The moisture content of the steam at the turbine is not to exceed 10 %.
i. Generate the T - s (Temperature – specific entropy) diagram of the cycle. [4 marks]
ii. Determine the minimum turbine inlet temperature in °C. [6 marks]
iii. Calculate the thermal efficiency of the cycle. [4 marks]
iv. Does the performance of the given Rankine cycle improve if the steam leaves the turbine as saturated vapor? Explain your answer. [
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