"#########   !      %   !" q'qqq,'ANALYSIS OF COMBUSTION OF GASEOUS FUEL5'FUEL: Oklahoma natural gas, Sample 5, Table 3-4'COMPONENT ' xi ' MWi'MASS i / ' mf|i 'CARBON'MASS C /' OXYGEN 'MASS O2/ 'OF FUEL'MOLE FUEL 'FACTOR'MASS FUEL ' FACTOR'MASS FUEL 'CH4)i K@m? ? @V'|0?m@ 'C2H48 ضm۶m?08ضm۶m@8 'C2H6i<p= ף@a? ?0<xB0>?@e@<0x88s?'H2  'CO  8       ضm۶m?8    $I$I? 8    'N2   8 I +@   U?           'CO2   X MbX9?   `n;E?   .袋?X y ?       'O2  @               ?? P 'MW FUEL= X(\@? P ?? P 1!2?? P ,f@? P'THEORETICAL A/F=P`#V@  'THEORETICAL MOLE A/F= xǮY@ %$'ORSAT ANALYSIS'MASS j / 'CARBON  'MASS C/'COMPONENT ' xj ' MW|j'MOLE dfg ' mf|j 'FACTOR'MASS dfg 'CO2'Xp= ףp@hԴ.?.袋?X ?'O2g@(\?0f?'CO8`(\?L1?ضm۶m?88f?'N2??P8@F<-???P' MW dfg=xGz@?P??PX D??P#'DRY FLUE GAS N2/C MASS RATIO=>@E'A/F = [(FLUE GAS N2/C)(C IN FUEL)-N2 IN FUEL]{28.9/[(.79)(28)]} ' = 0Aby@  [ A?'PER CENT EXCESS AIR =%4@G!'MASS OF REACTANTS PER MASS OF FUEL = MASS OF PRODUCTS PER MASS OF"'FUEL = A/F +1 ="Aby@