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THMRL:rI CAL. FUEL aJh'SUMmm vs- PPf V OF six <br /> slsl90 <br /> The following calculations are based Oil 1 Lbs. of M% lmvIng 17,000 SIV, <br /> arra one (1 ) Therm of natural gas (100,000 MV) costing $0.50 <br /> process stream � Nat GALS MMETU Nat Gas <br /> B= N1C�31U Catalyt1c 5/lir <br /> P,"v $ LEL Lbs./fir 7bermal $/llr <br /> IVAC 25 <br /> 100 SCFF4 @ 100°F <br /> 500 3.5 0.56 0.22 1.10 0.07 0.35 <br /> 5,000 35.7 5.64 0.'13 0.65 0.07 0-35 <br /> 101000 71 .4 11.27 0.04 0.20 <br /> 15,000 107.1 16.9 0.01 0.05 <br /> 200 S :,I @ 1000F <br /> I 500 3.5 1.12 0.49 Z.ZO 0.14 0.70 <br /> 5,000 35.7 11 .28 0.27 1.35 0.14 0.70 <br /> 10,000 71 .4 22.54 0.08 0.40 <br /> 15,000 107.1 33.8 0.01 0.05 <br /> I250 SCF11 @ 100°F <br /> 500 3.b 1.4 0.55 2.75 0.19 0.95 <br /> 5,000 35.7 14.1 0.34 1.70 0.09 Q.45 <br /> 10,000 71 .4 28.2 0.10 0.50 <br /> 15,000 107.1 42.3 0.01 0.05 <br />