Annual blowdown fuel cost versus cycles of concentration. Currently $11,672 per year at 20 cycles. The target is $7,647 per year at 30 cycles. Boiler alkalinity crosses the 700 ppm ABMA ceiling past 13 cycles.
Fuel cost per year$58,766$29,383$0
102030405060
Cycles of concentration
Reference
How the boiler model works
A steam plant is a circuit: feedwater in, steam out to the process, condensate back, and blowdown discharged to hold dissolved solids at the target cycles. Every pound of blowdown also carries heat that was paid for at the burner, so the water balance and the fuel bill are the same calculation seen from two sides.
The instrument above runs that circuit live. The governing relationships are written out below.
The feedwater pump must supply the steam that leaves as product plus the blowdown that leaves with the concentrated water. As cycles rise, the blowdown share shrinks and the feedwater approaches the steam load.
Steam
Steam load delivered (lb/hr)
Cycles
Cycles of concentration (boiler water vs feedwater)
Assumes
Cycles are greater than 1.
Blowdown
Blowdown=Cycles−1Steam
Blowdown is concentrated boiler water discharged to hold dissolved solids at the target cycles. It drops off sharply as cycles rise, then flattens, the same diminishing return the cooling tower shows.
Steam
Steam load delivered (lb/hr)
Cycles
Cycles of concentration
Assumes
Cycles are greater than 1.
Makeup
Makeup=500Feedwater−Steam×Condensate Return
Makeup is the fresh water bought to cover the feedwater the returned condensate does not. Converted from a mass rate at 500 lb/hr per gpm. More condensate return means less makeup at the same blowdown.
Alkalinity enters with the makeup, is diluted by the makeup fraction of the feedwater, then concentrated by cycles in the boiler. The 700 ppm ABMA guideline (boilers under 300 psi) is the ceiling to watch.
Makeup Alkalinity
Makeup M alkalinity as CaCO3 (ppm)
Makeup Fraction
Makeup as a fraction of feedwater
Cycles
Cycles of concentration
Assumes
ABMA boiler-water alkalinity ceiling 700 ppm for boilers under 300 psi.
Worked example
Take the room's default case: 20,000 lb/hr of steam, 50 percent condensate return, 20 cycles, 80 percent fuel to steam efficiency, 100 ppm makeup alkalinity, and 125 psi operating pressure.
Feedwater
21,053 lb/hr
Blowdown
1,053 lb/hr
Makeup
22.1 gpm
Boiler water alkalinity
1,050 ppm
Heat lost with blowdown
138,947 BTU/hr
Annual fuel cost of that heat
$11,672 per year
Move the condensate return slider and watch makeup, alkalinity, and the fuel line answer together. Returned condensate is water already purchased, treated, and hot.
Common questions
How is boiler blowdown calculated?
Blowdown holds dissolved solids at the target cycles. The feedwater pump supplies the steam that leaves as product plus the blowdown, and blowdown drops off sharply as cycles rise before flattening, the same diminishing return the cooling tower shows.
Why does condensate return matter so much?
Returned condensate is water already purchased, treated, and hot, and it carries no alkalinity back with it. Every point of return displaces makeup, and with it the alkalinity load and the fuel spent heating cold water.
What alkalinity ceiling does the model watch?
The ABMA guideline of 700 ppm boiler water alkalinity for boilers under 300 psi. Alkalinity enters with the makeup and is concentrated by cycles, so the ceiling is what finally caps how high cycles can go.