Long Soln Flashcards

1
Q

A single-effect evaporator is concentrating a feed of 9072 kg/h of a 10 wt % solution of NaOH in water to a product of 50% solids. The pressure of the saturated steam used is 42 kPa (gage) and the pressure in the vapor space of the evaporator is 20 kPa (abs). The overall heat-transfer coefficient is 1988 W/m2-K. The feed temperature is 288.8 K. The heating surface required

A

340 m2

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2
Q

The engine cylinder of a motorcycle is constructed of 2024-6 aluminum alloy and is of height H = 0.15 m and outside diameter D = 50 mm. Under typical operating conditions the outer surface of the cylinder is at a temperature of 500 K and is exposed to ambient air at 300 K, with a convection coefficient of 50 W/m? • K. Annular fins are integrally cast with the cylinder to increase heat transfer to the surround ings. Consider five such fins, which are of thickness t = 6 mm, length L = 20 mm, and equally spaced. What is the increase in heat transfer due to use of the fins?

A

454 W

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3
Q

The wall of an industrial furnace is constructed from 0.15-m-thick fireclay brick having a thermal conductivity of 1.7 W/m • K. Measurements made during steady-state operation reveal temperatures of 1400 and 1150 K at the inner and outer sur-faces, respectively. What is the rate of heat loss through a wall that is 0.5 m by 1.2 m on a side?

A

1700 W

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4
Q

An uninsulated steam pipe passes through a room in which the air and walls are at 25°C. The outside diameter of the pipe is 70 mm, and its surface temperature and emissivity are 200°C and 0.8, respectively. What are the surface emissive power and irradiation? If the coefficient associated with free convection heat transfer from the surface to the air is 15 W/m’ • K, what is the rate of heat loss from the surface per unit length of pipe?

A

998 W/m

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5
Q

A spherical, thin-walled metallic container is used to store liquid nitrogen at 77 K. The container has a diameter of 0.5 m and is covered with an evacuated, reflective insulation composed of silica powder. The insulation is 25 mm thick, and its outer surface is exposed to ambient air at 300 K. The convection coefficient isknown to be 20 W/m? - K. The latent heat of vaporization and the density of liquid nitrogen are 2 X 10* J/kg and 804 kg/m’, respectively. What is the rate of heat transfer to the liquid nitrogen?

A

13.06 W

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6
Q

A spherical, thin-walled metallic container is used to store liquid nitrogen at 77 K. The container has a diameter of 0.5 m and is covered with an evacuated, reflective insulation composed of silica powder. The insulation is 25 mm thick, and its outer surface is exposed to ambient air at 300 K. The convection coefficient isknown to be 20 W/m? - K. The latent heat of vaporization and the density of liquid nitrogen are 2 X 10* J/kg and 804 kg/m’, respectively. What is the rate of liquid boil-off?

A

7 L/day

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7
Q

Steam condensing on the outer surface of a thin-walled circular tube of diameter D = 50 mm and length L = 6 m maintains a uniform outer surface temperature of 100°C. Water flows through the tube at a rate of in = 0.25 kg/s, and its inlet and outlet temperatures are Tm = 15°C and Tmo = 57°C. What is the average convection coefficient associated with the water flow?

A

755 W/m2K

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8
Q

A single-effect evaporator is concentrating a feed of 9072 kg/h of a 10 wt % solution of NaOH in water to a product of 50% solids. The pressure of the saturated steam used is 42 kPa (gage) and the pressure in the vapor space of the evaporator is 20 kPa (abs). The overall heat-transfer coefficient is 1988 W/m2-K. The feed temperature is 288.8 K. The steam economy

A

0.81

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9
Q

The model ‘6SE-TCA3 Perkins’ diesel engine have a stroke of 190 mm and a bore of 160 mm. If its clearance volume is 5% of the swept volume, determine the pressure and temperature at the end of compression when the inlet condition is 1 bar, 27o C.

A

P 67.2 bar
T 956 K

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10
Q

A closed rigid container has a volume of 1 m 3 and holds air at 345 kPa and 20°C. Heat is added until the temperature is 327°C. Determine the change in Internal Energy:-

a) Using an average value of the specific heat.

b) Taking into account the variation of specific heat with temperature.

A

a 932 kJ
b 1018.7 kJ

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11
Q

An adiabatic steam turbine expands steam from a pressure of 6 MPa and a temperature of 500°C to a pressure of 10 KPa The isentropic efficiency of the turbine is 0.82 and changes in kinetic and potential energy may be neglected. Determine the state of the steam at exit from the turbine and the specific work transfer.

A

mixture 0.917
849 kJ/kg

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12
Q

A steam turbine receives steam at 2 MPa and 250o C, and exhausts at 0.1 MPa, 0.85 dry.

a) Neglecting heat losses and changes in ke and Pe, estimate the work output per kg steam.

b) If, when allowance is made for friction, radiation, and leakage losses, the actual work obtained is 80% of that estimated in (a), calculate the power output of the turbine when consuming 600 kg of steam per minute.

A

a 539 kJ/kg
b 4.31 MW

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13
Q

A boiler receives feed water at 40o C and delivers steam at 2 MPa and 500o C. If the furnace is oil fired, the calorific value of oil being 42000 kJ/kg and 4000 kg oil are burned while 45000 kg of steam are produced, determine :

a) the heat supplied in the boiler.

b) the efficiency of the boiler.

A

a 1.484 x 10^8 kJ
b 88%

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14
Q

Air, which may be considered a perfect gas, enters an adiabatic nozzle with negligible velocity. The entry pressure is 6 bar and the exit pressure is 1 bar; the entry temperature is 760 K. The flow throughout the nozzle is reversible and the mass flow rate is 2 kg/s. Calculate the exit velocity.

A

782 m/s

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15
Q

Self-ignition would occur in an engine using certain brand of petrol if the temperature due to compression reaches 350o C; when the inlet condition is 1 bar, 27o C.

Calculate the highest compression ratio possible in order to avoif self-ignition, if the compression is according to

a) adiabatic, with index of 1.4; and

b) polytropic, with index of 1.3

A

a 6.2
b 11.4

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16
Q

Self-ignition would occur in the engine using certain brand of petrol if the temperature due to compression reached 350°C. Calculate the highest ratio of compression that may be used to avoid pre-ignition if the law of compression is PV 1.3 = c. Assume inlet condition of 27°C and 1bar.

A

11.36

17
Q

The furnace at the Bataan Refinery is using a fuel gas which contains methane, ethane, and 20% nitrogen. The Orsat analysis of the combustion products showed 7.8% CO2, 7.4% O2, and 84.8%N2. The gas is burned with excess air. The % methane in the fuel gas is

A

57.24

18
Q

The temperature of tempering oil baths maintained at 400°C during
heat treatment of steel is measured by a/an __________
thermocouple.

A

iron constantan

19
Q

Tomato juice having a concentration of 12 wt% solids is being concentrated to 25% solids in a film-type evaporator. The maximum allowable temperature for the tomato juice is 135°F, which will be the temperature of the product. The feed enters at 100°F. Saturated steam at 25 psia is used for heating. The overall heat- transfer coefficient U is 600 BTU/hr-ft2-oF and the area A is 50
ft2. The heat capacity of the feed Cp is estimated as 0.95 BTU/lb- °F. Neglect any boiling-point rise if present. Calculate the feed
rate of tomato juice to the evaporator.

A

5600 lb

20
Q

Tomato juice having a concentration of 12 wt% solids is being concentrated to 25% solids in a film-type evaporator. The maximum allowable temperature for the tomato juice is 135°F, which will be the temperature of the product. The feed enters at 100°F. Saturated steam at 25 psia is used for heating. The overall heat- transfer coefficient U is 600 BTU/hr-ft2-oF and the area A is 50
ft2. The heat capacity of the feed Cp is estimated as 0.95 BTU/lb- °F. Neglect any boiling-point rise if present. Calculate the feed
rate of tomato juice to the evaporator.

A

5600 lb

21
Q

For the liquid phase zero order irreversible reaction A B, the
conversion of A in a CSTR is found to be 0.3 at a space velocity
of 0.1min-1 . What will be the conversion for a PFR with a space
velocity of 0.2 min-1? Assume that all the other operating
conditions are the same for CSTR and PFR.

A

0.60

22
Q

Water, flowing in a steel pipe of diameter 0.02 m, is to be cooled
from 40°C to 30°C. The velocity of water in the steel pipe is 1.5
m/s. The inside surface temperature of the steel pipe is
maintained at 25°C. The physical properties of water at mean bulk
temperature of the fluid area:
Specific heat = 4.174 KJ/kg
Density = 985 kg/m3
Thermal conductivity = 0.623 W/m-K.
Viscosity = 7.65 x 10-4 Pa-s.
Calculate the length of the tube required

A

5.3 m

23
Q

A solution is to be concentrated from 10% to 65% solids in a
vertical long tube evaporator. The solution has a negligible
elevation of boiling point and its specific heat can be taken to
be the same as that of water. Steam is available at 203.6 kPa,
and the condenser operates at 13.33 kPa. The feed enters the
evaporator at 295 K. The total evaporation is to be 25,000 kg/h
of water. The overall heat transfer coefficient is 2800 W/m2-K.
Calculate the heat-transfer surface area of the evaporator.

A

90.7 m2

24
Q

Three material A, B and C of equal thickness and of thermal
conductivity of 20, 40 and 60 kcal/hr-m2-°C respectively are
joined together. The temperature outside of A and C are 30°C and
100°C respectively. The interface between B and C will be at a
temperature of __________ °C.

A

70

25
Q

3 kg/s of steam enters an adiabatic condenser at a pressure of
100kPa with dryness fraction 0.80, and the condensate leaves the
condenser at a temperature of 300C. The condenser is cooled by
water which enters at a temperature of 50C and leaves at a
temperature of 250C. Calculate the mass flow rate of cooling water
required if all changes in kinetic and potential energy may be
neglected.

A

75 kg/s

26
Q

. A simple distillation column separates a binary mixture A and B.
The relative volatility of A with respect to B is 2. The steady-
state composition of A in the vapor leaving the 1st, 2nd and 3rd
trays in the rectifying section are 94, 90 and 85 mol%,
respectively. For ideal trays and constant molal overflow, the
reflux-to-distillate ratio is

A

3.0

27
Q

he interfacial area per unit volume of dispersion, in a gas-
liquid contactor, for fractional hold up of gas = 0.1 and gas
bubble diameter = 0.5 mm is given by (in m2/m3)

A

1200

28
Q

A nuclear reactor generates 3000 MW of heat. The heat is transferred in a heat exchanger of energy transfer efficiency 75% into steam which is expanded in a turbine in order to produce a power output. The steam is condensed in a condenser, releasing 1800 MW of heat, and pumped back through the heat exchanger by a feed pump which requires 3% of the power output from the turbine. Determine:

a) The net power output from the plant.

b) The power output from the turbine.

c) The overall thermal efficiency of the plant.

A

A 463.9 MW
B 450 MW
C 15%