Using the Steam Table, at initial pressure of 0.046 bar and final pressure of 0.107 bar, find the following: Δhfg Table 3: Properties of Saturated Steam-Pressure baseSpecific EntropyKJ/kg KEvapo- Sat.ration VapourPres- Temp. Specific Volume°CSpecific EnthalpykJ/kgsuream'/kgSat. Evapo-Liquid Vapour Liquid ration Vapour Liquidbar:Sat.Sat.Sat.Sat.29.34 2485.0 | 2514.454.71 2470.773.46- 2460.2 2533.688.45 2451.7 2540.2101.00 2444.6 2545.6111.85 2438.5 2550.4121.41 2433.1129.99 2428.2137.77 2423.8144.91 2419.8151.50 2416.0 2567.58.87078.97678.82880.1060.0.1957 8.63310.26070.31190.010 6.9828 .0010001 129.210.015 13.036 .0010006 67.9820.020 17.513 .0010012 67.0060.025 21.096 .0010020 54.256'0.030 24.100 .00100270.035 26.694 .0010033 39.479*0.040 28.963 .0010040 34.8020.045 31.035.0010046 31.1410.050 32.898 .0010052 28.1940.055 34.605 .0010058 25.7710.060 36.183 .0010064 23.7410.065 37.651.0010069 22.016 157.64 2412.5 2570.20.070 39.025 .0010074 20.5310.075 40.316 .00100790.080 41.534.0010084 18.105 173.86 2403.2 2577.10.085 42.689 .00100890.090 43.787 .0010094 16.2040.095 44.333 .00100980.100 45.833 .0010102 14.6750.110 47.7100010111 13.4160.12 49.446 |.0010119 12.3622525.58.4639 8.7246.8.3321 8.64408.57858.22418.1325 8.52328.0530 847558.433545.6670.35442554.52558.22561.62564.70.39070.42250.45070.47630.49957.98287.9197 8.39607.8626 8.36210.52097.81038.33127.7622 1.8.30297.7176 8.27678.25238.22968.20828.18818.1691163.38 2409.2 2572.6168.77 2406.2 2574.90.54070.55910.576319.2397.67600.59250.60790.62240.63610.64937.63717.60037.56577.53307.50187.4439178.69 2400.5183.28 2397.9187.65 2395.3191.83 2392.9199.68 2388.4206.94 2484.311.466 213.70 2380.3 2594.0220.02 2376.7 2596.7225.97 2373.2 | 2599.22579.22581.12583.017.10015.4002584.82583.1E.15110.67388.1177-8.08728.05922591.20.69637.39097.34207.29677.25447.21480.1351.062 .00101260.71720.73670.75498.03348.00937.986952.574 .00101330.15 53.997.0010140 10.0230.16 55.341 .00101470.17 56.615.00101540.18 57.826 .00101600.19 58.982 00101660.1410.6949.4331 231.59 2370.08.9110 236.92 2366.98.4452 241.99 2363.90272 2405 235842601.62603.82605.92361.1 2607.92609.92611.70.77210.78830.80367.1775 7.96587.1424 7.94607.90947.0472 | 7.89250.21 61.145 .00101787.3073 255.88 2355.80.22 62.162 00101830.84536.9951 260.14 2353.36.7093 264.23 2350.9 2615.26.4467 268.18 2348.6 2616.86.2045 271.99 2346.45.9803 275.67 2344.25.7724 279.24 2342.12613.50,85817.01837.87646.9909 7.86116.9644 7,84646.9391 7.83236.9147 7.81886.8912 | 7.805863.139 .00101890.87020.88200.230.24 64.082 .00101940.25 64.99200101990.26 65.871 .00102040.27 66.722 00102092618.32619.92621.30.89320.90410.9146Pbar- 10' Pa - 100 kPa -0.1 Mpa, Pa IN/m2, h kJ/kg, ub- Pv, kJ/kg P in kPa, s- k/kgK, vm/kg, t- °C

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Answered: Using the Steam Table, at initial…

Engineering

Mechanical Engineering

Using the Steam Table, at initial pressure of 0.046 bar and final pressure of 0.107 bar, find the following: Δhfg

Refrigeration and Air Conditioning Technology (MindTap Course List)

8th Edition

ISBN:9781305578296

Author:John Tomczyk, Eugene Silberstein, Bill Whitman, Bill Johnson

Publisher:John Tomczyk, Eugene Silberstein, Bill Whitman, Bill Johnson

Chapter46: Room Air Conditioners

Section: Chapter Questions

Problem 15RQ

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