Recover Heat from Boiler Blowdown PDF Print E-mail
Written by USDOE Office of Industrial Technologies   
Thursday, 01 July 2010 11:11

Recover Heat from Boiler Blowdown

Heat can be recovered from boiler blowdown by using a heat exchanger to preheat boiler makeup water. Any boiler with continuous blowdown exceeding 5% of the steam rate is a good candidate for the introduction of blowdown waste heat recovery. Larger energy savings occur with high-pressure boilers. The following table shows the potential for heat recovery from boiler blowdown.

Recoverable Heat from Boiler Blowdown
Blowdown Rate, % Boiler
Feedwater
Heat Recovered, Million Btu per hour (MMBtu/hr)
Steam Pressure, psig
50 100 150 250 300
2
0.45
0.5
0.55 0.65 0.65
4
0.9
1.0
1.1 1.3 1.3
6
1.3
1.5
1.7 1.9 2.0
8
1.7
2.0
2.2 2.6 2.7
10 2.2
2.5 2.8 3.2 3.3
20 4.4 5.0 5.6 6.4 6.6

Based on a steam production rate of 100,000 pounds per hour, 60°F makeup water, and 90% heat recovery.

Example
In a plant where the fuel cost is $8.00 per million Btu ($8.00/MMBtu), a continuous blowdown rate of 3,200 pounds per hour (lb/hr) is maintained to avoid the buildup of high concentrations of dissolved solids. What are the annual savings if a makeup water heat exchanger is installed that recovers 90% of the blowdown energy losses? The 80% efficient boiler produces 50,000 pounds per hour (lb/hr) of 150-pounds- per-square-inch-gauge (psig) steam. It operates for 8,000 hours per year. The blowdown ratio is:

Blowdown Ratio =         3,200           = 6.0%
    3,200 + 50,000

From the table, the heat recoverable corresponding to a 6% blowdown ratio with a 150-psig boiler operating pressure is 1.7 MMBtu/hr. Since the table is based on a steam production rate of 100,000 lb/hr, the annual savings for this plant are:

Annual Energy Savings = [1.7MMBtu/hrx(50,000lb/hr/100,000lb/hr)x8,000hr/yr]/0.80
= 8,500 MMBtu

 

Annual Cost Savings = 8,500 MMBtu/yr x $8.00/MMBtu
= $68,000

Blowdown Energy Recovery
Blowdown waste heat can be recovered with a heat exchanger, a flash tank, or flash tank in combination with a heat exchanger. Lowering the pressure in a flash tank allows a portion of the blowdown to be converted into low-pressure steam. This low-pressure steam is most typically used in deaerators. Drain water from the flash tank is then routed through a heat exchanger. Cooling the blowdown has the additional advantage of helping to comply with local codes limiting the discharge of high-temperature liquids into the sewer system.

Adapted from an Energy TIPS fact sheet that was originally published by the Industrial Energy Extension Service of Georgia Tech.

FOR ADDITIONAL INFORMATION, PLEASE CONTACT:
EERE Information Center
1-877-EERE-INF (1-877-337-3463)

Industrial Technologies Program
Energy Efficiency and Renewable Energy
U.S. Department of Energy
Washington, DC 20585-0121
 

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