Teledyne 9060Z APPENDIX1,CONSTITUENTVALUESFORVARIOUSFUELS,

Model9060ZManual
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57
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APPENDIX1,CONSTITUENTVALUESFORVARIOUSFUELS
Ifthetransmitterissetuptohavereadoutoroutputofcombustibles,oxygendeficiency,maximum
carbondioxideorcombustionefficiency,thenthefuelconstituentsmustbeentered.Anyorallofthe
variablescanbemodifiedandenteredinCOMMISSIONINGmenufunctions#50to56.(Seechapter
7.2.23).Yourfuelsupplierorchemistshouldbeabletogiveyouallthesevalues.
A istheheatofcombustionofthefuelpergramatomofcontainedcarbon.
H istheH/Catomratiointhefuel.
O istheO/Catomratiointhefuel.
N istheN/Catomratiointhefuel.
S istheS/Catomratiointhefuel.
M istheratioofH2OmoleculestoCatomsinthefuel
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FUEL A H O N S M
BlastFurnaceGas 50.55 0.08 1.3 3.08 b a
CokeOvenGas 256.88 5.6 0.25 0.23 b a
ProducerGas 101.98 1.18 1.02 2.9 b a
NaturalGas 209.9 3.86 00.1 00
Propane,Natural 176.4 2.69 0 0 00
Butane,Refinery 166.1 2.34 0 0 00
Methanol 172.59 3.97 1‐ ‐ ‐
Gasoline,Motor 157.58 2.01 0 0 00
No1DistillateOil 149.65 1.83 0‐ 0‐
No2DistillateOil 145.18 1.71 ‐ ‐ 0‐
No4FuelOil 145.54 1.6 ‐ ‐ 0.010
No5ResidualOil 142.25 1.44 ‐ 0 00
No6ResidualOil 136.52 1.25 0.01 0 00
Wood,Non‐Resinous 110.91 2.26 1.07 0 0c
Coal,Bituminous 116.88 0.74 0.05 0 00.03
Coal,Anthracite 104.98 0.35 0.05 00.010.04
Coke 99.63 0.11 0.01 0.01 00.01
a. Themoisturelevelvariesdependingontheprocessdetails.Thecalculatedvalues
assumeM=O.
b. Thesulfurlevelvariesdependingontheprocessdetails.Thecalculatedvalues
assumeS=O.
c. Variable.
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ValuescalculatedfromtheNorthAmericanCombustionHandbook,Tables2.1aand2.1b.
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