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Consider a long nuclear fuel rod which is surrounded by an annular layer of aluminum "cladding",as shown below. Within the fuel rod, heat is produced by fission; this heat sources is dependenton position, with a source strength varying approximately asSn = Sn0"1 + brRF2#where Sn0 is the heat per unit volume per unit time produced at r = 0, and r is the distancefrom the axis of the fuel rod. Calculate the maximum temperature in the fuel rod, if the outersurface of the cladding is in contact with a liquid coolant at temperature TL, the heat transfercoefficient of the cladding-coolant interface being hL. The thermal conductivities of fuel rodand cladding are kF and kC.
determine the kVA rating of the autotransformer, the kVA transformed by transformer action, and the kVA conducted.
Calculate the required value of Ta1 if the film temperature falls to 34°C, and the value if it rises to 36°C.
Calculate the energy. Which substance in Table 6.1 has the largest temperature change when 550. g of the substance absorbs 10.7 kJ of energy? Calculate the temperature change.
Preliminary design work has been done on a process to recover a valuable product froman effluent gas stream. The gas will be scrubbed with a solvent in a packed column;the recovered product and solvent separated by distillation; and the solvent co..
what percent of the maximum allowable flow rate is being used
From the magnetic material characteristics shown in Figure 11.1.2, estimate the relative permeability µr at a flux density of 1 T for M-19and AISI 1020 materials..
Find the efficiency of the transformer when it is delivering 7.5 kVA at 230 V and 0.85 power factor lagging.
When the J and K inputs of a JKFF are tied to logic 1, this device is known as a divide-by-2 counter. Complete the timing diagram shown in Figure P6.1.49 for this counter.
The table below gives the enthalpy of benzene(1)-heptane(2) solutions at 20 °C 1 bar as a function of the mol fraction of benzene. Calculate and plot the excess enthalpy at 20 °C, 1 bar.
Assume negligible miscibility between the aqueous and organic liquids in each other, and ignore any change in density on removal or addition of the enzyme to either stream.
A typical product stream is 52.26% ethylene, 5.49% ethanol, 0.16% ether, 36.81% water, and 5.28% inserts. Calculate the selectivity of ethylene for ethanol and for ether.
Nitrobenzene is fed to the reactor as a vapor, with three times the stoichiometric quantity of hydrogen. The conversion of the nitrobenzene, to all products, is 96%, and the selectivity for aniline is 95%.
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