Page 131 - Boiler_Operators_Handbook,_Second_Edition
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116                                                                               Boiler Operator’s Handbook

               that combustion air as an input. However, simple input  the steam in the steam tables in the appendix, subtract
               output efficiency calculations only include the heating  the enthalpy of the water supplied to the plant and mul-
               value of the fuel. They’re used to avoid measuring the  tiply by the number of pounds of steam produced to get
               energy added by fan motors and pump motors along  an output in Btu. Divide by 100,000 to convert to therms
               with that hotter combustion air. Combustion efficiency  and one million for decatherms or million Btu.
               calculations will show a negative loss because the tem-     If you’re getting condensate back, you’ll have to
               perature of the hotter air is subtracted from the tempera-  meter it or subtract makeup and blowdown from steam
               ture of the flue gas.                                output to determine the quantity of it. Use the enthalpy
                    For reasons I don’t understand everyone concen-  in the steam tables for water at the condensate tempera-
               trates on boiler efficiency when it doesn’t change very  ture. Multiply by pounds of condensate returned to get
               much and has little to do with the overall “plant effi-  Btu. Adjust that result to match your output units and
               ciency” which the boiler operator should be attending  subtract from the steam output to get plant output.
               to. This is a bigger problem when there is so much con-     Maybe you’re generating electricity too, use the
               fusion over what boiler efficiency really is. Two identical  conversion and add that to your output.
               boilers in different plants can have the same boiler ef-     For hot water plants determine the water flow rate.
               ficiency and combustion efficiency but one will produce  Hopefully it is constant. Convert gallons per minute to
               less usable energy than the other because it has a higher  pounds per hour then multiply by the number of hours
               blowdown rate. The energy absorbed by the water and  in the day, week, or month you’re evaluating. One gpm
               steam in the boiler (ASME definition) includes the heat  is approximately 500 pounds per hour so multiplying
               added to the blowdown water. Two plants with identi-  gpm by 500 is close enough. The time period is deter-
               cal boilers and loads can have different plant efficiencies  mined by how you measure your fuel usage. If you’re
               simply because one plant doesn’t have water softeners  relying on the gas billing it’s usually the month and
               so it must blow down more. Maybe they both have  you’ll use 720 or 744 hours depending on the month (ex-
               softeners but one has very little condensate return; it  cept February which will be 672 or 696). Once you have
               must heat the makeup water to replace that condensate  the number of pounds you were pumping around you
               and blow down more. Those and other variations can  multiply it by the temperature difference of the water.
               produce plants with boilers having an 80% efficiency  After all, the definition of a Btu is the amount of heat
               operating with a plant efficiency as low as 40%. Take a  required to raise the temperature of water one degree.
               plant with a mismatch between equipment and load and     You’ll have to use an average temperature for re-
               that plant efficiency can be as low as 20%.          turn water (or supply water if you control on the return
                    So what’s “Plant Efficiency?” It’s the amount of  temperature) to calculate the output. Since the loads
               heat you deliver to the facility, the usable heat you gen-  swing, a Btu meter, which constantly performs that cal-
               erate, divided by the energy used in the plant. What you  culation, should be an integral part of your plant so you
               deliver to the facility is your output. I like to use energy  can measure your output.
               in steam or hot water going down the pipe to the plant     That’s it, plant efficiency is your output divided
               less the energy in the condensate or return water. That  by input. You can calculate it regularly or use some of
               way my output is what the facility is using. The energy  the rate measurements we’re about to cover. So, what
               used in the plant includes electric power in addition to  do you do with it? You compare it! By measuring your
               fuel.                                                plant efficiency you’re developing a measure that will
                    A kilowatt-hour is 3,413 Btu. Multiply the kWh  allow you to determine, first and foremost, if the plant
               on your electric bill by that number to know how many  performance is consistent, increasing, or decreasing. You
               Btus were added by electricity. If you’re firing gas and  want to produce the highest efficiency or highest rate of
               want to deal in therms then multiply the kWh in your  output per unit of input that you can. It’s called burning
               electric bill by 34.13 to convert the electricity use to  less fuel and using less electricity while still satisfying
               therms. If you’re larger and use decatherms or millions  the load.
               of Btu multiply it by 3.413. With identical units you can     So, you measure it to determine where you are.
               add your electrical and fuel energy inputs to the plant to  You’ll discover that running one boiler instead of two
               get the total energy used.                           makes a big difference. You’ll find out when you shut
                    If you deliver steam to the facility and get nothing  down the continuous blowdown heat recovery system
               back you’re a 100% makeup plant and the energy you’re  that it costs a lot more to operate without it. However,
               delivering is all in the steam. Look for the enthalpy of  continuous blowdown saves more money in water than
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