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STEAM GENERATION
Type of steam Enthalpy of steam Volume of steam v(m 3 / kg)
h kJ / kg
Vwet xvg @ pressure( initial volume),
Wet steam hwet m(hf xhfg hw ) volume entering superheater, volume
leaving evaporator)
Dry saturated hdry m(hfg hw ) Vdry Vg @ pressure
n 1 hsup 1941
Superheated hsup mhg Cp s t ss t s hw Vsup
n
(final volume,
P
volume leaving superheated steam)
Other formulas under steam generations:
Enthalpy of the: Formula
1. Sensible heat H sensible mhf @ pressure hf @ t w
2. Latent heat H latent mhfg @ pressure
3. Superheat H sup erheat mCp s (t ss t s )
POSSIBLE QUESTIONS:
1. Steam which contains 3, 5% moisture enters a super heater at a pressure
of 3 MPa. The steam is then superheated to a temperature of 350 C at
constant pressure.
Calculate the following with the aid of steam table:
1.1. The enthalpy transferred in the superheater in kJ/kg
1.2. The volume of steam entering the superheater
1.3. The volume of superheated steam leaving the superheater
2. 10 kg of water, at a pressure of 920 kPa and a temperature of 60 C is
heated at the boiling point, then to dry saturated steam and then to
superheat, with a temperature of 210 C . The specific heat capacity of
superheated steam is 2, 1 kJ/kg. C and that of water is 4, 187 kJ/kg.K
Calculate the following with the aid of steam table:
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N5 Power Machines STEAM GENETATION
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2.1. The enthalpy of the sensible heat
2.2. The enthalpy of the latent heat
2.3. The enthalpy of the superheat
2.4. The enthalpy of the total heat required for superheating the water in
MJ
2.5. The saturated temperature
3. 1 kg of supply water at 0 C is changed to wet steam with a dryness fraction
of 0, 82 and at a pressure of 1, 4 MPa. The wet steam is then heated at
the same pressure to form superheated steam which has a volume of
0, 1568 m 3 . The specific heat capacity of superheated steam is 2, 15 kJ/kg.
C
Calculate the following with the aid of steam tables:
3.1. The enthalpy of the superheated steam
3.2. The temperature of the superheated steam
3.3. The initial volume entering the superheater
3.4. The change in specific volume
4. 11, 5 kg of water at a pressure of 880 kPa and a temperature of 48 C is
heated to boiling point, then dry saturated steam and then to superheat,
with a temperature of 210 C . The specific capacity of superheated steam
is 2, 1 kJ/kg. C and that of water is 4, 187 kJ/kg.K
Calculate the following with the aid of steam table:
4.1. The enthalpy of the sensible heat
4.2. The enthalpy of the latent heat
4.3. The enthalpy of the superheat
4.4. The enthalpy of the total heat required for superheating the water in
MJ
4.5. The saturated temperature
5. Steam which contains 4, 2% moisture enters a superheater at a pressure
of 4 MPa. The steam is then superheated to a temperature of 400 C at
constant pressure.
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Calculate the following with the aid of steam tables:
5.1. The heat transferred in the superheater in kJ/kg
5.2. The volume of steam entering the superheater
5.3. The volume of superheated steam leaving the superheater
6. Water which has a mass of 8, 5 kg and a temperature of 40, 3 C is used to
form steam at a pressure of 980 kPa. The steam is then superheated to a
temperature of 214 C . The specific heat capacity of superheated steam is
2, 1 kJ/kg.K
Calculate with the aid of steam tables:
6.1. The sensible heat
6.2. The latent heat
6.3. The superheat
6.4. The total heat required to superheat the steam
6.5. The saturated temperature
7. With the aid of steam table, calculate the following:
7.1. The enthalpy found in 2 kg of steam which has a pressure of 480
kPa and is 7, 3%
7.2. The enthalpy of a kilogram of steam which has a pressure of 1, 5
MPa, a temperature of 396c and the specific heat capacity of steam
is 2, 1 kJ/kg. C
7.3. The dryness fraction of wet steam which has an enthalpy of 2 650
kJ/kg at a pressure of 1, 3 MPa
7.4. The heat required to change 2, 3 kg of water from a temperature of
31 C to dry saturated steam at a pressure of 1 000 kPa
8. Supply water enters a boiler at a pressure of 60, 1 C and the pressure in
the boiler is 4 MPa. The steam formed is superheated to 310 C and the
superheated steam is 2, 1 kJ/kg. C .
Calculate the specific volume of the steam per kilogram
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9. Calculate the total heat and specific volume required to form 8 kg of steam
in each of the following conditions of steam if the temperature of the boiling
water is 40, 3 C and the pressure of the boiler is 1 000 kPa.
9.1. The dryness fraction of steam is 0, 82
9.2. The steam dry sat1urated
9.3. The steam is superheated with a temperature of 110 C and the
specific heat capacity is 2, 4 kJ/kg. C
The internal energy of the vapour (study examples in page 114)
Steam before expansion (it can either be wet, dry or superheated) = steam
after expansion (it can either be wet, dry saturated or superheated)
U 1 int ernalenergy of the vapour h1 P1V1
if the steam at the inlet is wet steam which means h1 hwet and V1 Vwet
U 2 int ernal energy after exp ansio2n h2 P2V2
same thing applies here if the steam is sup erheated steamh1 hsup and V2 Vsup
U mU 2 U 1
3, 5 kg of steam is expanded from 2 000 kPa and 300 C to a pressure of
280 kPa. The specific heat capacity of superheated steam is 2, 1 kJ/kg.K.
The steam is 10% at the latter pressure.
Calculate the total change of the internal energy
Other activities page 116 activity 8. 2 No: 1-3
10. 4 673, 5 kJ of heat is dissipated from 1, 75 kg of wet steam which is
at a pressure of 2 000 kPa. The supply water which is used to form the
steam entering the evaporator is 26, 6 C . The wet steam is then
superheated to 350 C . The specific heat capacity of water is 4, 187
kJ/kg.K
Calculate the following:
10.1. The dryness fraction of the wet steam
10.2. The change in enthalpy from wet steam to superheated steam for 1
kg of steam
10.3. The increase in specific volume of the steam for 1 kg of steam
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