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Temp Vapor (°C) | Pressure vf Specific Volume |(m³/kg) Enthalpy (kJ/kg) hf Entropy (kJ/kg-K) sf y (kPa) V hv h % % Vv SV 82 80 52.5 67 2200 2500 14 4 180 145 33 6 2320 6.72 7 123 15 8 130 5.75 9 700.5 2500 10 115 1.005

Temp Vapor (°C) | Pressure vf Specific Volume |(m³/kg) Enthalpy (kJ/kg) hf Entropy (kJ/kg-K) sf y (kPa) V hv h % % Vv SV 82 80 52.5 67 2200 2500 14 4 180 145 33 6 2320 6.72 7 123 15 8 130 5.75 9 700.5 2500 10 115 1.005

Introduction to Chemical Engineering Thermodynamics
Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Chapter1: Introduction
Section: Chapter Questions
Problem 1.1P
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Can you please help me, Can u please answer from 1-10  or just the hard one to solve from 1-10

here is the sample solution for item no.1

 Please used this STEAM TABLE: https://drive.google.com/file/d/1hU6YI7iEsHYQqrnIHy8lLsEgqkpIRjqZ/view?usp=sharing

Specific Volume (m³/kg) vf Temp| Vapor Entropy 2123 s0 11684 Enthalpy (kJ/kg) h X y (kJ/kg-K) sf (°C) Pressure % % 20 80 (kPa) hf hø 82 51.9 22 0.0010 36 3.162 0-4332 43.090269. 03. c1 1 1og80 7.585o 2 52.5 67 3 14 2200 1602.34 145 e2 4 |0.7646 2500 86.27 B.73 33 40 2320 6.72 7 123 15 5.75 of 26 Q 2 BI D D Page view A ad D Addtet V Daw Q Erase 8 130 P kPa m3/kg m3/kg m3/kg kJkg Kkg kJ/kg kJ/kg K kJ/kg K KJkg K 9 700.5 2500 kJ/kg 2223.21 54 14.999 0.001014 10.02 10.02 225.848 2599.36 2373.51 225.833 2449.04 0.7543 8.0091 7.2547 7.1959 10 115 1.005 56 16507 0.001015 9.159 9.158 234.202 2602.85 2368.65 234.185 2451.66 2217.48 0.7798 7.9757 58 18.143 0.001016 8.381 8.380 242.558 2606.34 2363. 242.540 2454.27 2211.73 0.8051 7.9428 7.1377 11 225 120 60 19.916 0.001017 7.679 7.678 250.918 2609.80 2358.89 250.898 2456 87 2205.97 0.8302 7.9104 7.0802 12 200 3200 62 21.834 0.001018 7.044 7.043 259.281 2613.26 2353.98 259.259 2459.46 2200.20 0.8552 7.8786 7.0234 23.906 26.144 6.470 267.647 2616.70 2349.05 2462.04 0.8801 7.8472 6.9671 6.9115 64 0.001019 6.469 267.623 2194.41 13 3420 8.75 0.001020 5.949 5.948 276.016 2620.13 275.990 2464.61 2188.62 0.9048 66 2344.11 7.8163 12 3 68 28.557 0.001021 5.475 284.389 2623.54 2339.15 284.360 2467.16 2182.80 0.9294 7.7859 6.8564 3.476 14 70 1.1859 70 31.156 0.001023 0.001024 5.047 5.046 292.765 2626.94 2334.18 292.733 2176.97 0.9539 7.7559 6.8020 S.046 4.655 5,047 292.135 2469.71 15 22 72 33.952 4.656 4.050 301.144 2630.32 2329.18 301.109 2472.24 2171.13 0.9782 7.7263 6.7481 2165.27 2159.40 74 36.957 0.001025 4.300 4.299 309.527 2633.69 2324.16 309.489 2474.76 2477.27 4.500 309 489 1.0024 1.0024 76972 7.6972 6.048 6.6948 76 40.184 0.001026 3.976 3.975 317.913 2637.04 2319.13 317.872 1.0265 7.6686 6.6421 h: 326.303 LOSOS 7.6403 Solue 78 43.645 0.001028 3.680 3.679 2640.37 2314.07 326.258 2479.76 2153.51 1.0505 65899 for Solution 47.353 2308.99 334.648 2482.25 2147.60 2484.72 80 0.001029 3.409 3.408 334.696 2643.69 1.0743 7.6125 6.5382 Solve for x: (82 S1322 0.001030 3.162 3.161 343.093 2303.90 7.5850 2646.99 2650.27 343.040 2141.68 1.0980 6.4870 x= h-hf/hg-hf Example only for #1 84 55.567 0.001032 2.935 2.934 351.494 2298.78 351.437 2487.17 2135.74 L1216 7.5579 64364 hf : 343.093 86 60.102 0.001033 2.727 2.726 359.899 2653.53 2293.64 359.837 2489.62 2129.78 1.1450 7.5313 6.3862 64.942 0.001034 2.537 2.536 368.308 2656.78 228847 368.240 2492.04 2123.80 7.5050 63366 88 1.1684 2.361 70.104 75.603 2.360 2.199 2494.46 2496.86 376.720 2660.01 2663.21 2283.29 376.648 385.059 2117.81 L.1916 6.2874 7.4790 6 7.4534 90 0.001036 hg: 2646.99 92 0.001037 2.200 385.137 2278.08 2111.80 12147 803.872 Plkg solve for S: Solve for v/h/s Sf= 1.0930 7.5850 o O61030 t 0.2(3.162-0.0030) = 6.6332 2. SA54 KJ
Transcribed Image Text:Specific Volume (m³/kg) vf Temp| Vapor Entropy 2123 s0 11684 Enthalpy (kJ/kg) h X y (kJ/kg-K) sf (°C) Pressure % % 20 80 (kPa) hf hø 82 51.9 22 0.0010 36 3.162 0-4332 43.090269. 03. c1 1 1og80 7.585o 2 52.5 67 3 14 2200 1602.34 145 e2 4 |0.7646 2500 86.27 B.73 33 40 2320 6.72 7 123 15 5.75 of 26 Q 2 BI D D Page view A ad D Addtet V Daw Q Erase 8 130 P kPa m3/kg m3/kg m3/kg kJkg Kkg kJ/kg kJ/kg K kJ/kg K KJkg K 9 700.5 2500 kJ/kg 2223.21 54 14.999 0.001014 10.02 10.02 225.848 2599.36 2373.51 225.833 2449.04 0.7543 8.0091 7.2547 7.1959 10 115 1.005 56 16507 0.001015 9.159 9.158 234.202 2602.85 2368.65 234.185 2451.66 2217.48 0.7798 7.9757 58 18.143 0.001016 8.381 8.380 242.558 2606.34 2363. 242.540 2454.27 2211.73 0.8051 7.9428 7.1377 11 225 120 60 19.916 0.001017 7.679 7.678 250.918 2609.80 2358.89 250.898 2456 87 2205.97 0.8302 7.9104 7.0802 12 200 3200 62 21.834 0.001018 7.044 7.043 259.281 2613.26 2353.98 259.259 2459.46 2200.20 0.8552 7.8786 7.0234 23.906 26.144 6.470 267.647 2616.70 2349.05 2462.04 0.8801 7.8472 6.9671 6.9115 64 0.001019 6.469 267.623 2194.41 13 3420 8.75 0.001020 5.949 5.948 276.016 2620.13 275.990 2464.61 2188.62 0.9048 66 2344.11 7.8163 12 3 68 28.557 0.001021 5.475 284.389 2623.54 2339.15 284.360 2467.16 2182.80 0.9294 7.7859 6.8564 3.476 14 70 1.1859 70 31.156 0.001023 0.001024 5.047 5.046 292.765 2626.94 2334.18 292.733 2176.97 0.9539 7.7559 6.8020 S.046 4.655 5,047 292.135 2469.71 15 22 72 33.952 4.656 4.050 301.144 2630.32 2329.18 301.109 2472.24 2171.13 0.9782 7.7263 6.7481 2165.27 2159.40 74 36.957 0.001025 4.300 4.299 309.527 2633.69 2324.16 309.489 2474.76 2477.27 4.500 309 489 1.0024 1.0024 76972 7.6972 6.048 6.6948 76 40.184 0.001026 3.976 3.975 317.913 2637.04 2319.13 317.872 1.0265 7.6686 6.6421 h: 326.303 LOSOS 7.6403 Solue 78 43.645 0.001028 3.680 3.679 2640.37 2314.07 326.258 2479.76 2153.51 1.0505 65899 for Solution 47.353 2308.99 334.648 2482.25 2147.60 2484.72 80 0.001029 3.409 3.408 334.696 2643.69 1.0743 7.6125 6.5382 Solve for x: (82 S1322 0.001030 3.162 3.161 343.093 2303.90 7.5850 2646.99 2650.27 343.040 2141.68 1.0980 6.4870 x= h-hf/hg-hf Example only for #1 84 55.567 0.001032 2.935 2.934 351.494 2298.78 351.437 2487.17 2135.74 L1216 7.5579 64364 hf : 343.093 86 60.102 0.001033 2.727 2.726 359.899 2653.53 2293.64 359.837 2489.62 2129.78 1.1450 7.5313 6.3862 64.942 0.001034 2.537 2.536 368.308 2656.78 228847 368.240 2492.04 2123.80 7.5050 63366 88 1.1684 2.361 70.104 75.603 2.360 2.199 2494.46 2496.86 376.720 2660.01 2663.21 2283.29 376.648 385.059 2117.81 L.1916 6.2874 7.4790 6 7.4534 90 0.001036 hg: 2646.99 92 0.001037 2.200 385.137 2278.08 2111.80 12147 803.872 Plkg solve for S: Solve for v/h/s Sf= 1.0930 7.5850 o O61030 t 0.2(3.162-0.0030) = 6.6332 2. SA54 KJ
Specific Volume (m³/kg) V Temp Vapor (°C) Pressure vf Enthalpy (kJ/kg) Entropy (kJ/kg-K) sf y (КРa) hf hv h % % SV 82 80 52.5 67 3 14 2200 2500 4 180 5 145 33 6. 2320 6.72 7 123 15 8 130 5.75 9 700.5 2500 10 115 1.005 11 225 120 200 3200 3420 8.75 14 70 12 15 22 35 16 112 95 17 55.5 40 18 133 100 2320 19 73 20 255 250 21 180 200 2345 Or0 9
Transcribed Image Text:Specific Volume (m³/kg) V Temp Vapor (°C) Pressure vf Enthalpy (kJ/kg) Entropy (kJ/kg-K) sf y (КРa) hf hv h % % SV 82 80 52.5 67 3 14 2200 2500 4 180 5 145 33 6. 2320 6.72 7 123 15 8 130 5.75 9 700.5 2500 10 115 1.005 11 225 120 200 3200 3420 8.75 14 70 12 15 22 35 16 112 95 17 55.5 40 18 133 100 2320 19 73 20 255 250 21 180 200 2345 Or0 9
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