WorksheetsThermal Engg II (Unit I - Quiz 2)
Total questions: 10
Worksheet time: 5mins
Nozzle efficiency is given by
h1−h3h1−h3s
h1−h3sh1−h3
h1s−h3h1−h3
h1−h3h1s−h3
In the figure shown,
Frictional loss in divergent portion
Frictional loss in convergent portion
No frictional loss
Frictional loss in both in convergent and divergent portion
During expansion of steam in a nozzle as shown in figure, the condition of steam at throat i.e. at state 2 is
Wet
Saturated
Supersaturated
Superheated
V2mv2 With respect to the nozzle shown, this equation gives ____________ (Note m - mass flow rate)
Area of nozzle at throat
Area of nozzle at exit
Area of nozzle at inlet
None of the above
When inlet velocity is considered in a nozzle, the following equation can be used to calculate the velocity at throat
44.72 h1−h2
44.72h01−h2
44.72h2−h1
44.72h2−h01
During expansion of steam through a nozzle as shown in figure, the condition of steam at throat is
Superheated
Wet
Saturated
Supersaturated
During expansion in a convergent - divergent nozzle, the enthalpy of steam under isentropic conditions:
at inlet section 1-1 is 3100 kJ/kg;
at throat section 2-2, 2900 kJ/kg and
at exit section 3-3, 2700 kJ/kg
If there is a frictional loss of 15 % of overall enthalpy drop in divergent portion, What would be the enthalpy at exit.
2770 kJ/kg
2640 kJ/kg
2760 kJ/kg
2670 kJ/kg
During expansion in a convergent - divergent nozzle, the enthalpy of steam under isentropic conditions:
at inlet section 1-1 is 3100 kJ/kg;
at throat section 2-2, 2900 kJ/kg and
at exit section 3-3, 2700 kJ/kg
If there is a frictional loss of 50 kJ in divergent portion, What would be the enthalpy at exit.
2650 kJ/kg
2750 kJ/kg
2950 kJ/kg
2850 kJ/kg
In the figure, superheated steam at state 1, after reaching state a, expands under supersaturated condition. The temperature of steam at state b is
Equal to Tsat at p2
Greater than Tsat at p2
Less than Tsat at p2
None of the above
The degree of supersaturation is
pbsatpb
pbpbsat
pbp2
p2pb
