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∆H 0 298

∆H T. ∆H 0 298. Reactants. Products. (T). (T). ∆H products = Σ C p (298-T) =- Σ C p (T-298). ∆H reactant = Σ C p (T-298). Reactants. Products. fuel, 상온. [products + H 2 O (g) ]. [products + H 2 O (l) ]. dq. dq = Higher Heating Value = │-∆H L │. Cooling. O 2.

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∆H 0 298

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  1. ∆HT • ∆H0298 Reactants Products (T) (T) ∆Hproducts=ΣCp(298-T) =-ΣCp(T-298) ∆Hreactant=ΣCp(T-298) Reactants Products

  2. fuel, 상온 [products + H2O(g)] [products + H2O(l)] dq dq = Higher Heating Value = │-∆HL│ Cooling O2 dq = Lower Heating Value = │-∆Hg│ 미국 우리나라, 중동 HHV = LHV + [latent heat, heat of vaporization] * Latent heat = 44,000J/mole = 9712 Kcal/Kgmole → table 2-3 p.17

  3. *Cp(°K기준):

  4. ex 2-7) Energy Balance • 성분; C6H6 : 70% Excess air : 10% • C : 8.2% Preheating air : 300°C • Ash : 9.3% Heat loss : 5% • H2O : 12.5% Burning rate : 1100Kg/hr Air(300°C) 5% Heat loss 5% Heat loss Combustion Chamber Combustion Chamber Waste (1100Kg/hr) Water 100°C Steam (15.8atm) 180°C Ash 100 Kg of Waste 를 기준, C6H6 : 70% → 70Kg/78 = 0.897Kgmole, C : 8.2% → 0.683 Kgmole Ash : 9.3%, H2O : 12.5% → 0.694 Kgmole 0.897C6H6 + 0.683C + (1.1)x(O2 + 3.76N2) → 6.065CO2 + 2.691H2O + 0.1xO2 + (1.1x)(3.76)N2 For O2, 1.1xO2 = 6.065 + 1.345 +0.1x, x = 7.41 0.897C6H6 + 0.683C + (1.1)(7.14)(O2 + 3.76N2) → 6.065CO2 + 2.691H2O + 0.714O2 + (8.151)(3.76)N2

  5. * 총 수분배출 mole수 : (2.691 + 0.694) Kgmoles/100Kg of waste • * Dry gas moles : 6.065 + 0.741 + (8.151)(3.76) • = 37.5Kgmole/100Kg of waste • *시간당 배출되는 dry gas : (37.5Kgmole/100Kg of waste)(1100Kg/hr) • = 41.25 Kgmole/hr

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