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STEAM CONDENSORS
The function of steam condenser is to:
I. Create a region of low pressure into which the turbine or engine could exhaust
II. Supply pure feed water to the hot well at a temperature nearly equal to that of
exhaust steam
Two types of steam condensers:
I. The jet condenser
II. The surface condenser
M water Mass Of cooling water; M steam Mass of exhaust steam; hc hf @ t c (enthalpy of
the condensate); t rise in temperature of water ; x dryness fractionof exhauststeam ;
t1 inlet temperature of cooling water and t 2 outlet temperture of cooling water
P
101,325
B r M r the pressure of the condenser
760
M steam hf xhfg hc M water cp water t water while cp of cooling is 4,187 kJ / kg.K
1 2
temperature log difference 1 t c t w(inlet ) 2 t c t w( outlet )
1
ln
2
If the steam is dry saturated which means the dryness fraction is 1 x 1
AIR PUMPS
Function of air pumps: are being used to remove air from the condenser to maintain a
vacuum in the condenser
Two types of air pumps:
I. The Edwards air pumps
II. The rotary air pumps
Air leakage R Tair
capacity of the air pump volume of air pump
Pair
where Pa is called partial pressure of air pumps
Possible questions:
1. Every hour a surface condenser processes 6 500 kg exhaust steam, which has a
dryness fraction of 0, 83. Air leakage into the condenser is at a rate of 1, 2
kg/1000 kg of steam. The air pump suction and the condensate have a
temperature of 31 C each. The barometer and vacuum gauge reading is 760
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mmHg and 662 mmHg respectively. The temperature of cooling water is
increased by 21 C after it passes through the condenser. The specific heat
capacity of water is 4 187 J/kg.K and gas constant for air is 0, 288 kJ/kg.K
Calculate the following:
1.1. The mass of cooling water required by the condenser every minute
1.2. The capacity of air pump in m 3 / min
2. A steam turbine supplies a surface condenser with 6 800 kg of steam per hour,
which is 25% wet. The barometer reading is 750 mm Hg and the manometer
reading is 667 mm Hg. The condensate and the air pump suction has a
temperature of 37, 7 C . The cooling water enters the condenser at 22 C and
leaves at 42 C . The air leakage is 0, 8kg for every 1000 kg of outlet steam and
the gas constant for air is 0,287 kJ/kg.K
Calculate the following:
2.1. The mass of cooling water required by the condenser every minute
2.2. The capacity of air pump in m 3 / min
3. The condenser in Question 2 is fitted with an air-cooling section which lowers the
temperature from 37, 7 C to 21,1 C .
Calculate the following:
3.1. The new capacity of air pump in m 3 / min
3.2. The percentage of saving in pump volume
4. A surface condenser has a vacuum-meter reading of 689, 3 mm mercury and a
barometer reading of 757 mm mercury. Wet steam with a dryness fraction of 0,93
is supplied to this condenser at a rate of 3 450 kg/hour. The cooling water enters
the condenser at 20,5 C and leaves at 32,4 C and the condensate has a
temperature 31 C . The specific heat capacity of the cooling water is 4,187
kJ/kg.K
Calculate the following:
4.1. The pressure in the condenser
4.2. The mass of cooling water required by the condenser every minute
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5. A surface condenser handles 4 520 kg of wet steam, with a dryness fraction of 0,
81 every hour. The barometer and vacuum meter readings are 760 mm Hg and
662 mm Hg respectively. The temperature of the condensate and the air pump
suction is 39 C . Cooling water enters the condenser at 20 C and leaves at 35,5
C . The gas constant for air is 0, 288 kJ/kg.K and the S.H.C of water is 4, 187
kJ/kg.K
Calculate the following;
5.1. The quantity of cooling water required in kg/min
5.2. The capacity of air pump required in m 3 / min
5.3. The capacity of the new air pump in m 3 / min if the air was cooled to 36, 2
C before being pumped from the condenser
6. Exhaust steam with a dryness fraction of 0, 89 enters a surface condenser, which
has a vacuum of 699, 5 mm mercy and is condensed to water at a temperature
of 34, 6 C . The barometer reading is 760 mm Hg. The suction temperature of
the air pump is 34, 6 C and R for is 0, 287 kJ/kg.K
Calculate the following:
6.1. The combined pressure of the steam and air in the condenser
6.2. The partial pressure of the air
6.3. The mass of air extracted for every kilogram of steam whilst considering
that air and steam occupy the same volume
7. 2 450 kg of the exhaust steam is condensed per hour in a surface condenser,
whilst air leaks into the condenser at a rate of 2,3 kg/h. 50 kg water is used to
condense one kg of steam with a dryness fraction of 0,83. The condensate and
air pump suction have a temperature of 36, 2 C . The barometer reading is 760
mmHg and vacuum gauge reading is 685 mmHg. The air pump has volumetric
efficiency of 87% and R for air is 0, 288 kJ/kg.K and S.H.C for superheated
steam is 2,1 kJ/kg C
Calculate the following:
7.1. The combined pressure of the steam and air pump in the condenser
7.2. The partial pressure of the air
7.3. The air pump capacity in m 3 / hour
7.4. The rise in temperature of the cooling water
FOR MORE EXERCISES TURN TO PAGE 148 [ACTIVITY 11.2] V.A.A HAAGNER
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