A boiler generates 50,000 lb/hr of saturated steam at 300
psia, out of which 10,000 lb/hr is taken for process and is returned to the deaerator
as condensate at 180 degree F, the remainder is consumed. Makeup water enters
the DA tank at 70 degree F and steam is available at 300 psia for deaeration.
The DA tank operates at 25 psia. The blow down has TDS of 1,500 ppm by weight
and make up has a TDS of 100 ppm. Evaluate the blow down and deaeration steam
quantities.
Solution:
If boiler concentration is 0.5 ppm solid and water hardness
concentration is 2,500 ppm: then the percent moisture in steam = Steam Purity,
ppm / Boiler water concentration, ppm or
percent moisture in steam = (0.5 / 2,500) * 100 = 0.02 so
the steam quality = 100 – 0.02 = 99.98 %
DA Energy balance:
The mass balance around two control volumes gives us:
If M is the make up
water to DA, D is the steam for deaeration to DA, F the BFW and B is the
Blowdown
For the boiler 50,000 + B = F and for DA: 10,000 + M + D = F
Eq (1)
by equating this two we will have: 50,000 + B = 10,000 + M +
D
10,000 * 148 + 1,202.8 * D + M * 38 = 209 * F = 209 *
(50,000 + B) Eq (2)
Balance of the solids in the makeup and blowdown gives 100 *
M = 1,500 B Eq (3)