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A depletion MOSFET is given to have large VA, VP = 2.8 V, IDSS = 4.3 mA, vDS = 4.5 V, and vGS = 1.2 V.
(a) Is the MOSFET operating in the active region?
(b) Find iD.
(c) Comment on whether the device is operating in the depletion mode or in the enhancement mode.
The left side of of the mechanical energy equation has three terms: P/p, (1/2)av^2 and gz. show that each of these terms has the dimension of energy per mass of fluid by....a) converting each term to units of Btu/lbm beginning with pressure in psi, d..
Discuss the consequent effects on the real and reactive power losses, and on the voltage drop across the series impedance of the transmission system.
Determine the number of theoretical plates required to reduce to hydrocarbon content of 0.05 mole % assuming the oil is non-volatile.
100 moles of Benzene (A) and Toluene mixture containing 50% (mole) of Benzene is subjected to a differential distillation at atmospheric pressure till the composition of benzene in the residue is 33%. Calculate the total moles of the mixture disti..
find the current from the supply source. Sketch the phasor diagram showing all quantities involved.
Write down a balanced chemical equation for the polymerization and Name the polymer formed by this polymerization.
What is the drawdown at the perimeter of the well pumping 225 gpm when both wells are operating?
Describe how you would find the critical temperature for thermal damage. Do you expect that to be lower or higher than a constant temperature case of the same exposure duration?
In Problem 12.4.1 neglect the saturation of the core, leakage, and fringing. Neglect also the reluctance of the ferromagnetic circuit. Assuming that the cross-sectional area of the center leg is twice the area of the outer legs, obtain expressions..
determine the induced voltage at (a) full load, and (b) one-half full load. Neglect brush-contact drop.
Estimate the number-average molecular weight that is required to give a tensile strength of195MPa.
Calculate the equilibrium conversion and the CSTR and PFR volumes necessary to achieve 98% of the equilibrium conversion and calculate the time to reach 90% conversion if the reactor is a batch reactor filled to the brim.
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