Trab 3 Sist Térmicos 2

C7H16\n12.12.261 = 70 kg/mol\np = 750 kPa\n\u03c1 = 900 kg/m3\nX = 0.329\nC12H26 + 0.0853 C6H12 + NO2 (O2 + 7.36 L/h) -> aC2Q2 + bH2O + dN2\na = 13.6207\nb = 19.5354\nNO2 = 2/3 13.6207 + 19.5354 - 0.0853\nNO2 = 20.8031\nMolar mass = 29.023\nṁ = 1.170 + 0.0853(29.296)\nṁf/ṁar = 99.023/28.97\n\nV_m = Ẇ / (10.735)\nẆ = 738.833 W\nC1 = 1\nẆ = 1.651111\nẆ_in = ṁPen\nẆ_in = ṁPen \u2022 X\n\nṁ_ent = P/D\nT = P \u2022 \u0394V\nT = 3.0 x 10^8 (6.823.90.4.T1.4)\nT = 1481.3 J\n\nb) T3-T2 = 276.92C\n0.1, 1.27\n0.687 - 1 = 1 / (16.5)(0.1)(0.913)(1) (0.33)\n0.333 1\n0.7766\nb = 1\n\nb^ - 1\n1.0 = 1.010126B - 1.0126 b\n1.305 ab b^1.305 = 1.305 (B - 1)\n\nb^1.305\nb = 1.0\n\nmiṡ = 3.96x10^8\nṁf = 23.02 kg/h\nṁar = 14.7\n\nmar = ṁf (17.47 mi53)\n= 33.96 kg/h\n\nD) Ẇ_in = 798.83 kW\nẆ_out = 185.11 kW\nẆ_out = 1798.833 - (178.735)\nẆ = 13.88 kW T3 - T2 = 276.92C\n0.1, 1.27\n\n0.687 - 1 = 1 / (8.465)(8^1) (8^1)/(B-1) \n1/ (3.305)(0.333) = 1/ (0.7766)(b^ 1.305)\n\nb = 1\n\nb^ - 1 = 1.010126B - 1.0126 => beta = 1\n\nb^ - 1 = 1.0\n\nṁs = 3.36x10^8 ṁf = 23.02 kg/h\n\nṁar = ṁf /14.7 = 33.96 kg/h\n\nẆ_in = 798.83 kW\nẆ_out = 185.11 kW\nẆ_out - 1798.833 = (178.735)\n\nẆ = 13.88 kW