Cost model · BeamStack® in-situ cross-stack vs zirconia probe

Fuel saved by trimming excess oxygen

Lower excess oxygen means less heat carried out of the stack by air you did not need to heat. This model prices that saving on your plant. It is the only one of our cost models where the argument is fuel rather than instrument cost, and where the saving can be far larger than either instrument.

Plant

Rated capacity is not fuel consumption. The model converts one to the other using your load factor and boiler efficiency, so enter the nameplate rating here rather than an estimate of what you actually burn.

MW
hours, max 8760
percent of rated capacity
percent, fuel to useful heat
EUR per MWh

Combustion

The efficiency figure below is a rule of thumb, not a constant. The gain per percentage point of oxygen removed rises with flue gas temperature and with the starting oxygen level, so a plant with a hot stack recovers more than one with a cold stack. Use your own figure if you have one from a combustion survey.

percent in flue gas
percent in flue gas
percent, from your commissioning
percent of fuel

Zirconia probe

EUR
EUR
EUR per year

BeamStack® cross-stack analyzer

EUR
EUR
EUR per year
The instrument difference is small against the fuel bill. What decides this case is whether the measurement lets your combustion control hold a lower oxygen setpoint safely, which depends on the burner, the turndown range and the control loop as much as on the analyzer.
Shared assumptions and financing
count, applied to both
years
percent per year
display only, no conversion

Enter your figures above

The model runs as soon as the fields are filled.

Annual fuel bill

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-

Annual fuel saved

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-

Extra capital over zirconia

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including installation

Net position over horizon

-

present value

Cumulative net position, present value

Net position, BeamStack against zirconia Break-even line Payback

Present value over the horizon
Line Zirconia BeamStack Difference
Talk to us about your combustion control Send us the stack conditions, the fuel and your current oxygen setpoint and we will tell you whether the trim your control system can actually hold matches what this model assumes.

Method. Fuel input in MWh is rated capacity multiplied by operating hours and load factor, divided by boiler efficiency. The fuel bill is that figure multiplied by your fuel cost. The saving is the fuel bill multiplied by the oxygen reduction and the efficiency gain per percentage point. Capital and installation fall in month zero, fuel savings and service costs accrue evenly across the year, and everything is discounted to present value at the rate you set.

The chart is drawn to scale. The saving is a small percentage of a large number, and it looks like a small percentage of a large number, because a chart that exaggerated it to make it visible would not be worth showing you.

What this model does not decide. Whether your plant can hold a lower oxygen setpoint is a question about the burner, the turndown range, the control loop and the fuel, and it is answered by a combustion survey rather than by an analyzer datasheet. This model prices the saving if the trim is achievable. It does not establish that it is, and it is not a substitute for burner commissioning. The starting values are illustrative placeholders, not published prices for any product and not a quotation for any competing instrument.