95-102 Flashcards
(158 cards)
Sulfuric acid is pumped at 3 kg/s through a 60-m length of smooth 25 mm pipe. If the pressure drop falls by one-half, what will be the new
flow rate (kg/s)? Assume the following properties of sulfuric acid: SG=1.84, viscosity=25 cP.
A. 3 B. 2 C. 0.2 D. 0.124
B. 2
Property of fluid that converts kinetic energy to heat energy.
A. viscosity B. fluidity C. shear D. resistance
B. fluidity
Which of the following is an extensive property?
A. temperature B. velocity C. pressure D. mass
D. mass
If the temperature of a confined gas is constant, the pressure is inversely proportional to the volume. This is known as:
A. Charles law B. Archimedes principle
C. Boyle’s law D. Dalton’s law
C. Boyle’s law
Which of the following is the most efficient?
A. Carnot B. Brayton C. Otto D. Diesel
A. Carnot
The achievement of a temperature below that of the immediate surroundings is
A. air conditioning B. drying
C. refrigeration D. evaporation
C. refrigeration
Work is a
A. property of the system
B. state function
C. path function
D. state description of a system
C. path function
Throttling process is
A. a reversible and isothermal process
B. a reversible and constant entropy process
C. an irreversible and constant entropy
D. constant enthalpy
D. constant enthalpy
In the reversible isothermal expansion of an ideal gas at 300 K from 1 to 10 liters, where the gas has an initial pressure of 20 atm, calculate the change in entropy of the gas in cal/°K.
A. 3.20 B.3.46 C. 3.72 D. 3.86
C. 3.72
To have an efficiency of 40 percent, a heat engine that exhausts heat at 350°K must absorb heat at no less than
A. 210 K B. 875 K
C. 583 K D. 1038 K
B. 875 K
If a Carnot engine absorbs 10kJ of heat per cycle when it operates between 500 and 400 K, the work it does per cycle is
A. 2 kJ B. 8 kJ C. 2.5 kJ D. 10kJ
A. 2 kJ
Calculate the entropy change in cal/°K if 350 grams of water at 5°C is mixed with 500 grams of water at 70°C.
A. 4.485 B. 4.580
C. 4.652 D. 4.789
A. 4.485
A rigid tank contains hot fluid that is cooled while being stirred by a paddle wheel. The internal energy of fluid is 800 kJ and loses 500 kJ ofnheat during cooling process with the paddle work of 100 kJ applied on the fluid. Neglecting the energy stored in the paddle wheel, determine the final internal energy of the fluid.
A. 430 kJ B. 340 kJ
C. 400 kJ D. 500 kJ
C. 400 kJ
How many cubic feet per minute of entering air is needed to evaporate 10 lb of water per hour from a rayon, if the air enters at 80°F and 25% humidity and leaves at 170°F and 55% relative humidity. The operating pressure is 14.3 psia.
A. 12.7 cfm B. 145.8 cfm
C. 255.1 cfm D. 322.5 cfm
A. 12.7 cfm
A nitrogen-hydrogen chloride mixture (10 vol% hydrogen chloride) is to be scrubbed with water to remove the hydrogen chloride. To satisfy
environmental concerns, 99% of the inlet HCl must be removed. Assuming that the gas leaving the scrubber will be at 125°F and 1 atm saturated with water, what will be the volume of the gas leaving if we must process 200 lbmol/hr of dry entering gas.
A. 88630 ft3/hr B. 71000 ft3/hr
C. 61210 ft3/hr D. 57441 ft3/hr
A. 88630 ft3/hr
From the data in problem #2, calculate the percentage hydrogen chloride of the gas leaving.
A. 2% B. 0.1%
C. 0.0001% D. 0.02%
B. 0.1%
0.6 m3/s (measured at STP) of gas is to be dried from a dew point of 294 K to a dew point of 277.5 K. how much water must be removed?
Vapour pressure of water at 294 K is 2.5 kN/m2. Vapour pressure of water at 277.5 K is 0.85 kN/m2
A. 2.1 kg/s B. 0.75 kg/s
C. 0.0071 kg/s D. 0.00009 kg/s
C. 0.0071 kg/s
From the data in problem #4, what will be the volume of the gas after drying measured at STP?
A. 0.59 m3/s B. 2.18 m3/s
C. 4.52 m3/s D. 6.78 m3/s
A. 0.59 m3/s
Wet material, containing 70% moisture on a wet basis, is to be dried at a rate of 0.15 kg/s in a counter-current dryer to give a product containing 5% moisture (both on a wet basis). The drying medium consists of air heated to 373 K and containing water vapour with a partial pressure of 1.0 kN/m2. The air leaves the dryer at 313 K and 70% saturated. Calculate how much air will be required to remove the moisture. The vapour pressure of water at 313 K may be taken as 7.4 kN/m2.
A. 0.54 kg/s B. 3.78 kg/s
C. 12.1 kg/s D. 45.1 kg/s
B. 3.78 kg/s
30,000 m3 of cool gas (measured at 289 K and 101.3kN/m2
saturated with water vapour) is compressed to 340 kN/m2
pressure, cooled to
289 K and the condensed water is drained off. Subsequently the pressure is reduced to 170 kN/m3 and the gas is distributed at this pressure and 289 K. What is the percentage absolute humidity after this treatment? The vapour pressure of water at 289 K is 1.8 kN/m2.
A. 30% B. 40% C. 50% D. 60%
C. 50%
When a porous solid was dried under constant-drying conditions, 5 hours were required to reduce the moisture from 30 to 12 lb H2O/lb dry
solid. Critical moisture content is 18 lb H2O/lb dry solid and the equilibrium moisture is 5 lb H2O/lb dry solid. If the drying rate during the falling-rate period is a straight line through the origin, determine the time needed to dry the solid from 30 to 8 lb H2O/lb dry solid.
A. 3.44 hr B. 7.74 hr
C. 1.25 hr D. 2.88 hr
B. 7.74 hr
For acetone at 20°C and 1 bar, volume expansivity (β) =1.478 E-3/°C, isothermal compressibility (κ) =62 E-6/bar and specific volume (V) =1.287 cm3/g. The value of (∂P/∂T)V is
A. 24 bar/°C B. 42 bar/°C
C. 10 bar/°C D. 33 bar/°C
A. 24 bar/°C
For acetone at 20°C and 1 bar, volume expansivity (β) =1.478 E-3/°C, isothermal compressibility (κ) =62 E-6/bar and specific volume (V)=1.287 cm3
/g. The pressure generated when acetone is heated at constant volume from 20°C and 1 bar to 30°C is
A. 241 bar B. 110 bar
C. 177 bar D. 220 bar
A. 241 bar
For acetone at 20°C and 1 bar, volume expansivity (β) =1.478 E-3/°C, isothermal compressibility (κ) =62 E-6/bar and specific volume (V)=1.287 cm3/g. The volume change in (cm3/g) when acetone is changed from 20°C and 1 bar to 0°C and 10 bar.
A. 0.038 B. -0.038
C. 0.144 D. -0.144
B. -0.038