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uΔh σtstat (B.64) The results of the uncertainty calculations for the enthalpy change for each gas are shown in Table B-2. The uncertainties for the mass fraction of the four gases are all calculated using the same general formula: MF 2 MF 2 MF 2 uMF un n um m um m air air fuel fuel (B.65) (B.66) (B.67) (B.68) (B.69) The partial derivatives for the mass fraction uncertainty of CO2 are: MFCO2 nCO2 MWCO2 44.0095kgkmol1 2,860skmol1 mfuel mair 0.0005067kgs1 0.0149kgs1 MF CO2 CO2 CO2 3.64105 kmols1 44.0095kgkmol1 0.0005067kgs1 0.0149kgs1 2 n MW mair mfuel mair 2 3.64105 kmols1 44.0095kgkmol1 6.75skg1 MF n MW CO2 CO2 CO2 mfuel mfuel mair 2 0.0005067kgs1 0.0149kgs1 2 6.75skg1 The uncertainty for the CO2 molar flow rate is: Table B-2. Uncertainty results for exhaust gas enthalpy calculations. u n u xC m MW 4.716106 kgs1 12 167.311kgkmol1 CO2 3.382107 kmols1 fuel fuel Gas σ t-stat Uncertainty CO2 1.070191 2.4469 2.61866 H2O 0.391521 2.4469 0.95802 N2 0.215784 2.3646 0.51025 O2 0.400227 2.3646 0.94639 208PDF Image | WASTE HEAT RECOVERY FROM A HIGH TEMPERATURE DIESEL ENGINE
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