Strictly don't use chatgpt Only handwritten (Quick) 3. Steam enters a diffuser operating at steady state with a pressure of 3 bar, a temperature of 200 °C, and a velocity of 100 m/s. Steam exits the diffuser as a saturated vapor, with a velocity of 10 m/s. Heat transfer occurs from the steam to its surroundings at a rate of 200 kJ/kg of steam flowing. Neglecting potential energy effects, determine the exit pressure, in bar. (Note: 1 kJ/kg-1000 m²/s²) (1) (2) TABLE A-3 Pressure Conversions: Properties of Saturated Water (Liquid-Vapor): Pressure Table 1 bar 0.1 MPa = 10 kPa Specific Volume m/kg Internal Energy kj/kg Enthalpy kj/kg Entropy kj/kg K Sat. Press. bar Temp. Liquid Sat. Vapor Sat. Liquid Sat. Vapor Sat. "C By x 10' Liquid Evap. hy Sat. Vapor he Sat. Liquid Sat. Vapor Press. 51 bar 0.04 28.96 1.0040 34.800 0.06 36.16 1.0064 23.739 0.08 41.51 1.0084 18.103 0.10 45.81 1.0102 0.20 60.06 1.0172 14.674 7.649 0.30 69.10 1.0223 5.229 0.40 75.87 0.50 0.60 85.94 0.70 89.95 1.0265 3.993 81.33 1.0300 3.240 1.0331 1.0360 2.732 2.365 121.45 2415.2 151.53 2425.0 173.87 2432.2 191.82 2437.9 251.38 2456.7 289.20 2468.4 317.53 2477.0 340.44 2483.9 359.79 2489.6 376.63 2494.5 251.40 2358.3 121.46 2432.9 2554.4 151.53 2415.9 2567.4 0.5210 8.3304 173.88 2403.1 2577.0 0.5926 191.83 2392.8 2584.7 0.6493 8.1502 2609.7 0.8320 7.9085 0.4226 8.4746 0.04 0.06 8.2287 0.08 0.10 0.20 289.23 2336.1 2625.3 0.9439 7.7686 317.58 2319.2 2636.8 1.0259 340.49 2305.4 2645.9 1.0910 0.30 7.6700 0.40 7.5939 0.50 359.86 2293.6 2653.5 1.1453 7.5320 376.70 2283.3 2660.0 1.1919 7.4797 0.60 0.70 0.80 0.90 96.71 93.50 1.0380 2.087 1.0410 1.00 99.63 1.0432 1.50 111.4 1.0528 2.00 120.2 1.0605 1.869 1.694 1.159 0.8857 391.58 2498.8 405.06 2502.6 417.36 2506.1 466.94 2519.7 504.49 2529.5 391.66 2274.1 2665.8 1.2329 7.4346 405.15 2265.7 2670.9 1.2695 7.3949 417.46 2258.0 2675.5 1.3026 7.3594 467.11 2226.5 2693.6 1.4336 7.2233 504.70 2201.9 2706.7 1.5301 7.1271 0.80 0.90 1.00 1.50 2.00 2.50 127.4 1.0672 0.7187 3.00 133.6 1.0732 0.6058 535.10 2537.2 561.15 2543.6 3.50 138.9 1.0786 0.5243 4.00 143.6 1.0836 4.50 147.9 1.0882 0.4625 0.4140 583.95 2546.9 604.31 622.25 535.37 2181.5 2716.9 1.6072 7.0527 561.47 2163.8 2725.3 584.33 2148.1 2732.4 1.7275 2553.6 604.74 2133.8 2738.6 1.7766 6.8959 2557.6 623.25 2120.7 2743.9 1.8207 6.8565 2.50 1.6718 6.9919. 3.00 6.9405 3.50 4.00 4.50 TABLE A-4 Properties of Superheated Water Vapor T °C m³/kg kJ/kg kJ/kg kJ/kg. K m³/kg kJ/kg kJ/kg kJ/kg. K p = 1.5 bar =0.15 MPa (Tsat = 111.37°C) Sat. 1.159 2519.7 2693.6 120 1.188 2533.3 2711.4 160 1.317 2595.2 2792.8 p = 3.0 bar =0.30 MPa (Tsat=133.55°C) 7.2233 0.606 2543.6 2725.3 6.9919 7.2693 7.4665 0.651 240 200 1.444 2656.2 2872.9 1.570 2717.2 2952.7 7.6433 7.8052 280 1.695 2778.6 3032.8 7.9555 2587.1 2782.3 7.1276 0.716 2650.7 2865.5 7.3115 0.781 2713.1 2947.3 7.4774 0.844 2775.4 3028.6 7.6299 320 1.819 2840.6 3113.5 8.0964 360 1.943 2903.5 3195.0 8.2293 400 2.067 2967.3 3277.4 8.3555 0.907 2838.1 3110.1 7.7722 0.969 2901.4 3192.2 7.9061 1.032 2965.6 3275.0 8.0330 440 2.191 3032.1 3360.7 500 2.376 3131.2 3487.6 8.6466 600 2.685 3301.7 3704.3 8.9101 8.4757 1.341 1.094 3030.6 3358.7 8.1538 1.187 3130.0 3486.0 8.3251 3300.8 3703.2 8.5892