Modeling of Combustion Systems A Practical Approach 2 pptx
Modeling of Combustion Systems A Practical Approach 2 pptx
... 8. 329 54.5 3.94 2. 258 2. 180 13.40 23 .59 35.4 8 .21 3.00 20 … … 0 .25 0 8. 125 51.8 6.58 2. 258 2. 127 22 .36 22 .48 57.7 13.39 2. 9 62 30 … … 0 .27 7 8.071 51 .2 7 .26 2. 258 2. 113 24 .70 22 .18 63.4 14.69 2. 953 40 ... (in.) Area (ft) © 20 06 by Taylor & Francis Group, LLC 564 Modeling of Combustion Systems: A Practical Approach 521 .40.495493.680005. 7...
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Modeling of Combustion Systems A Practical Approach 1 pot
... (Dry) Waste Gases Natural Gas LPG Cracked Gas Coking Gas Reforming Gas FCC Gas Refinery Gas Sample 1 Refinery Gas Sample 2 PSA Gas Flexicoking Gas Tulsa Alaska Netherlands Algeria Propane Butane CH 4 93.4% ... LLC Fuel and Combustion Properties 543 TABLE A. 4 © 20 06 by Taylor & Francis Group, LLC 534 Modeling of Combustion Systems: A Practical Approach TABLE A. 1 Physic...
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Modeling of Combustion Systems A Practical Approach 3 docx
... kinetic lbm ft 2 /sec 2 kg m 2 /sec 2 1 2 2 Energy, potential lbm ft 2 /sec 2 kg m 2 /sec 2 1 2 2 Enthalpy, molar Btu/lbmol W/kgmol –1 1 2 2 Enthalpy, specific Btu/lbm W/kg 2 2 Enthalpy, volumetric ... molar Btu/lbmol W/kgmol –1 1 2 2 Gas constant, universal psia ft 3 /lbmol °R m 3 kPa/kgmol K –1 1 2 2 –1 Heat Btu/h W 1 2 –3 Heat capacity, molar Btu/l...
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Modeling of Combustion Systems A Practical Approach 4 doc
... -4 +2 +4 49 In 114.818 -18-18-3 +3 86 Rn (22 2) - 32- 18-8 0 85 At (21 0) - 32- 18-7 84 Po (20 9) - 32- 18-6 +2 +4 83 Bi 20 8.98038 - 32- 18-5 +3 +5 82 Pb 20 7 .2 - 32- 18-4 +2 +4 81 Tl 20 4.3833 - 32- 18-3 +1 +3 1 H 1.00794 1 +1 -1 1 Group IA 30 Zn 65.409 -8-18 -2 +2 29 Cu 63.546 -8-18-1 +1 +2 28 Ni 58.6934 -8-16 -2 +2 +3 27 Co 58.93 320 0 -8-15 -2 26 Fe 55.845 -8-14...
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Modeling of Combustion Systems A Practical Approach 5 docx
... 3 .20 3.09 3.01 2. 95 2. 90 2. 85 2. 72 2.65 2. 60 2. 57 2. 51 2. 46 2. 40 90% 3 .23 2. 86 2. 66 2. 54 2. 45 2. 39 2. 34 2. 30 2. 27 2. 25 2. 17 2. 12 2.10 2. 08 2. 04 2. 01 1.97 12 99% 9.33 6.93 5.95 5.41 5.06 4. 82 ... 3.37 3 .28 3 .21 3.08 2. 98 2. 87 95% 4.54 3.68 3 .29 3.06 2. 90 2. 79 2. 71 2. 64 2. 59 2. 54 2. 40 2. 33 2. 28 2. 25 2. 18 2. 12...
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Modeling of Combustion Systems A Practical Approach 6 pdf
... easier. TABLE F.3 Positional Number Representation in Base 2 (e.g., 1110.11 2 = 14.75) Exponent … 321 0. –1 2 –3… Exponential notation … 2 3 2 2 2 1 2 0 .2 –1 2 2 2 –3 … Decimal notation … 8 421 . 1 /21 /41/8… Binary ... E 16 32 1110 15 F 17 33 1111 16 10 20 100 10000 © 20 06 by Taylor & Francis Group, LLC 610 Modeling of Combustion Systems: A Practical A...
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Modeling of Combustion Systems A Practical Approach 7 pot
... 614 Modeling of Combustion Systems: A Practical Approach Usually, one defines a reaction coordinate known as the conversion (x k ), having the property that for species k the reaction starts at ... is a constant and N k is a variable. We may also write (G.6) For constant density, we have , where [k] is the concentration of species k, and [k 0 ] is the starting concentra-...
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Modeling of Combustion Systems A Practical Approach 8 doc
... reactant, the double-headed arrow (↔) means that both the forward and reverse reactions occur (typically at different rates), k is an index from 1 to n products, p k is the number of moles of ... If we wish to express K eq in terms of mole fraction rather than concentration for gases, then, using the ideal gas law, we obtain (H.3) rr pp 11 22 11 22 RR PP++↔++$$ rp jj j m kk k n R =...
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Modeling of Combustion Systems A Practical Approach 9 pdf
... 2 =− 3 321 123 3 321 331 122 322 13 () −− () +− () aaa aa aaa aa aaa aaa aaa a aa aa 11 12 13 21 22 23 31 32 33 11 22 23 32 33 = −− +a aa aa a aa aa 21 12 13 32 33 31 12 13 22 23 aaaa aaaa aaaa aaa 11 12 13 14 21 22 23 24 31 ... 32 33 34 41 42 443 44 11 22 23 24 32 33 34 42 43 44 21 1 a a aaa aaa aaa a a =− 22 1314 32 33 34 42 43 44 31...
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Modeling of Combustion Systems A Practical Approach 10 ppsx
... 18% 20 % 22 % 24 % y y y wet dry H2O O O =−1 2 2 , , © 20 06 by Taylor & Francis Group, LLC 138 Modeling of Combustion Systems: A Practical Approach (2. 1 6a) (2. 16b) TWP is the volumetric flue-gas-to-fuel ... + 1 /2 O 2 → CO + ψ /2 H 2 (2. 1) © 20 06 by Taylor & Francis Group, LLC ever, smaller rectangular slots may have manufacturing advantages. In prac-...
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