Based on the table A-4 and table A-5, contruct P-v abd T-v diagram for water 915APPENDIX 1TABLE A–4Saturated water-Temperature table (Concluded)Internal energy,Entropy,kJ/kg-KSpecific volume,Enthalpy,m/kgkJ/kgkJ/kgSat.Sat.Sat.Sat.Sat.Sat.Sat.Sat.Sat.Temp.,press.,liquid,vapor,liquid,Evap., vapor,liquid,Evap., vapor,liquid,Evap., vapor,T°CPat kPa vfUigh;hghgSig2051724.30.0011640.11508872.861723.52596.4874.87 1920.02794.82.3776 4.0154 6.39302101907.72797.30.0011730.0011810.10429895.38918.021702.92598.3897.61 1899.72.4245 3.9318 6.35632152105.90.0946801681.92599.9920.50 1878.82799.32.4712 3.8489 6.32000.0860942601.32602.32202319.6 0.001190940.791660.5943.55 1857.42801.02.5176 3.7664 6.28402252549.7 0.001199 0.078405963.70 1638.6966.76 1835.42802.22.5639 3.6844 6.24832302797.10.001209 0.071505986.76 1616.12602.9990.14 1812.82802.92.6100 3.6028 6.21282352403062.6 0.0012190.0653000.0597070.0546561010.01593.22603.21013.71789.52803.22.6560 3.5216 6.17750.0012290.0012403347.01033.41569.82603.11037.5 1765.52803.02.7018 3.4405 6.14242453651.21056.91545.72602.71061.5 1740.82802.22.7476 3.3596 6.10722503976.20.001252 0.0500851080.71521.12601.81085.7 1715.32801.02.7933 3.2788 6.07212554322.91104.70.0459414692.3 0.001276 0.0421750.0012631495.8 2600.51110.11689.02799.12.8390 3.1979 6.03692601128.81469.92598.71134.81661.82796.62.8847 3.1169 6.00172655085.3 0.0012890.0387481153.31443.22596.51159.8 1633.72793.52.9304 3.0358 5.96622705503.00.0013030.0356221177.91415.72593.71185.1 1604.62789.72.9762 2.9542 5.93052755946.40.0013170.0327671202.91387.42590.31210.71574.52785.23.02212.8723 5.89442806416.60.0013330.0301531228.21358.22586.41236.71543.22779.93.0681 2.7898 5.85792856914.60.0013490.0277561253.71328.12581.81263.11510.72773.73.1144 2.7066 5.82102907441.80.0013660.0255541279.71296.92576.51289.81476.92766.73.1608 2.6225 5.78342957999.00.0013840.0235281306.01264.52570.51317.11441.62758.73.2076 2.5374 5.74503008587.9 0.001404 0.0216591332.71230.92563.61344.81404.82749.63.2548 2.4511 5.70593059209.4 0.0014250.0199321360.01195.92555.81373.11366.32739.43.3024 2.3633 5.66573109865.0 0.001447 0.0183331387.71159.32547.11402.01325.92727.93.3506 2.2737 5.62433151121.1 2537.21431.610,55611,28412,0510.001472 0.0168491416.11283.42715.03.3994 2.1821 5.58163203250.001499 0.0154701445.11080.92526.01462.01238.52700.63.44912.0881 5.53720.001528 0.0141831475.01038.52513.41493.41191.02684.33.4998 1.9911 5.49083302499.212,85813,70714,60115,54116,5290.001560 0.0129791505.7993.51525.81140.32666.03.5516 1.8906 5.44223350.001597 0.0118481537.5945.52483.01559.41086.02645.43.6050 1.7857 5.39073403450.001638 0.0107831570.7893.82464.51594.61027.42622.03.6602 1.6756 5.33580.001685 0.0097721605.5837.72443.21631.7963.42595.13.7179 1.5585 5.27653500.001741 0.0088061642.4775.92418.31671.2892.72563.93.7788 1.4326 5.211417,57018,66619,82221,044373.95 22,0640.001808 0.0078721682.21726.21777.2355706.42388.61714.0812.92526.93.8442 1.2942 5.13843600.001895 0.006950625.72351.91761.5720.12481.63.9165 1.1373 5.05373650.002015 0.006009526.42303.61817.2605.52422.74.0004 0.9489 4.94933700.0022170.0049531844.5385.62230.11891.2443.12334.34.1119 0.6890 4.80090.003106 0.0031062015.72015.72084.32084.34.4070 04.4070 cen84959_ch18-ap01.qxd 8/11/06 1:21 PM Page 918918 IThermodynamicsTABLE A-5Saturated water-Pressure tableInternal energy,Specific volume,m/kgEnthalpy,kJ/kgEntropy,kJ/kg · KSt.kJ/kgSat.Sat.SatSat.Sat.Sat.Sat.St.Evap.,Press., temp., liquid,P kPaliquid,liquid,h;vapor,vapor,Evap.,vapor, liquid, Evap., vapor,Tu °C VheS1.06.97 0.001000 129.1929.302 2355.22384.529.303 2484.4 2513.7 0.1059 8.8690 8.974913.02 0.001001 87.96417.50 0.001001 66.9901.554.686 2338.12392.854.688 2470.1 2524.7 0.1956 8.6314 8.82702.073.431 2325.52398.973.433 2459.5 2532.9 0.2606 8.4621 8.72272.521.08 0.001002 54.24288.422 2315.42403.888.424 2451.0 2539.4 0.3118 8.3302 8.64213.024.08 0.001003 45.654100.98 2306.92407.9100.982443.9 2544.8 0.3543 8.2222 8.57654.028.96 0.001004 34.791121.392293.12414.5121.392432.3 2553.7 0.4224 8.0510 8.47345.032.870.001005 28.185137.752282.12419.8137.752423.0 2560.7 0.4762 7.9176 8.39387.540.290.001008 19.233168.742261.12245.42429.8168.752405.3 2574.0 0.5763 7.6738 8.25011045.81 0.00101014.670191.792437.2 191.812392.1 2583.9 0.6492 7.4996 8.14881553.97 0.00101410.020225.932222.12448.0 225.942372.3 2598.3 0.7549 7.2522 8.007160.06 0.00101764.96 0.0010202456.0 251.422462.4 271.96207.6481251.402204.62357.5 2608.9 0.8320 7.0752 7.9073271.93289.24317.58256.20342190.42345.5 2617.5 0.8932 6.9370 7.83023069.09 0.0010225.22872178.52467.7 289.272335.3 2624.6 0.9441 6.8234 7.76754075.86 0.0010263.99332158.82476.3 317.622318.4 2636.1 1.0261 6.6430 7.66915081.32 0.0010303.2403340.492142.72483.2 340.542304.7 2645.2 1.0912 6.5019 7.59317591.76 0.0010372.2172384.362111.82496.1384.442278.0 2662.4 1.2132 6.2426 7.455810099.61 0.0010431.6941417.402088.22505.6417.512257.5 2675.0 1.3028 6.0562 7.3589418.95444.23466.97101.325 99.97 0.0010431.67342087.02506.0 419.062256.5 2675.6 1.3069 6.0476 7.3545105.97 0.001048111.35 0.0010532068.82513.02519.2 467.131251.3750444.362240.6 2684.9 1.3741 5.9100 7.28411501.15942052.32226.0 2693.1 1.4337 5.7894 7.2231175116.04 0.0010571.0037486.822037.72524.5 487.012213.1 2700.2 1.4850 5.6865 7.1716200120.21 0.0010610.88578 504.502024.62529.1504.712201.6 2706.3 1.5302 5.5968 7.1270123.97 0.0010642012.72533.22252500.79329 520.47520.712191.0 2711.7 1.5706 5.5171 7.0877127.41 0.0010670.71873 535.082001.82536.8535.352181.2 2716.5 1.6072 5.4453 7.0525275130.58 0.0010700.65732 548.571991.62540.1548.862172.0 2720.9 1.6408 5.3800 7.0207133.52 0.0010730.60582 561.110.56199 572.840.52422 583.890.49133 594.322543.2 561.43573.193001982.12163.5 2724.9 1.6717 5.3200 6.9917325350136.27 0.0010761973.12545.92155.4 2728.6 1.7005 5.2645 6.9650138.86 0.001079584.262550.9 594.731964.62548.52147.7 2732.0 1.7274 5.2128 6.9402375141.30 0.0010811956.62140.4 2735.1 1.7526 5.1645 6.9171400143.61 0.0010840.46242 604.221948.92553.1 604.662133.4 2738.1 1.7765 5.1191 6.8955450147.90 0.0010880.41392 622.651934.5 2557.1 623.142120.3 2743.4 1.8205 5.0356 6.85610.37483 639.540.34261 655.16500151.830.0010931921.22560.7 640.092108.0 2748.1 1.8604 4.9603 6.8207550155.46 0.0010971908.82563.9 655.772096.6 2752.4 1.8970 4.8916 6.78861897.12566.8 670.382569.4 684.08600158.83 0.0011010.31560 669.722085.8 2756.2 1.9308 4.8285 6.7593650161.98 0.0011040.29260 683.371886.12075.5 2759.6 1.9623 4.7699 6.7322700164.950.0011080.27278 696.231875.62571.8 697.002065.8 2762.8 1.9918 4.7153 6.7071750167.75 0.0011110.25552 708.401865.6 2574.0709.242056.4 2765.7 2.0195 4.6642 6.6837

TABLE A–4 Saturated water-Temperature table (Concluded) Specific volume, m/kg Internal energy, kJ/kg Enthalpy, kJ/kg Sat. Sat. Sat. Sat. Sat. Sat. Sat. Temp., press., liquid, vapor, liquid, Evap., vapor, liquid, Evap., vapor, T°C P. kPa h. h

TABLE A–4 Saturated water-Temperature table (Concluded) Specific volume, m/kg Internal energy, kJ/kg Enthalpy, kJ/kg Sat. Sat. Sat. Sat. Sat. Sat. Sat. Temp., press., liquid, vapor, liquid, Evap., vapor, liquid, Evap., vapor, T°C P. kPa h. h

Elements Of Electromagnetics

7th Edition

ISBN:9780190698614

Author:Sadiku, Matthew N. O.

Publisher:Sadiku, Matthew N. O.

ChapterMA: Math Assessment

Section: Chapter Questions

Problem 1.1MA

See similar textbooks

Related questions

Q: From the figure assume that concentrations C1 and C2 are 2.65 and 0.75 kg of carbon per cubic meter…

A: a) The concentrations are given as C1 = 2.65 kg/m^3 C2 = 0.75 kg/m^3 The diffusion constant is D =…

Q: A closed piston-cylinder system consists of 3.0 moles of monatomic gas, initially at temperature…

Q: 2. The piston is initially just touching the linear spring, and water is a compressed liquid. The…

Q: define the standard-state Gibbs function change?

A: The Gibbs function is equal to the difference of Enthalpy minus product of its absolute temperature…

Q: Saturated Refrigerant-134a vapor Saturated liquid A tank occupied by saturated liquid-vapor mixture…

Q: A piston-cylinder device contains Is free to móve. The initial temperature and pressure of the…

Q: t type of relation or and equation of state exist for a PVT system Discuss

A: Given Data⇒ PVT System

Q: One mole of an ideal gas is taken through a cyclic process as shown in the PV diagram below, i.c.…

Q: Find the missing properties and give the phase of the substance. (a) H2O s = 1.75 Btu/lbm R, P = 4…

Q: kg sample of water at 15.0°C is in a calorimeter. You drop a piece of steel with aporation and…

Q: RT B- Find an expression for Cp - Cv if the equation of state is p =- v-b for an ideal gas 34 - and…

Q: a 3-stroke cycle engine with processes of adiabatic expansion, isochoric heating, isobaric…

Q: An ideal gas follows the relationship pV=10 where V is in m3 and p is in kPaa. Draw the pV diagram…

A: NOTE: Even after applying the correct concept my answer is not coming to be equal to any of the…

Q: 2 adiabatic expansion y-1 (1) ..... ..... 3 heating with fixing volume T3 P3 (2) T2 P2 3. T1_P3 .…

Q: The simplest equation of state for liquid water is the so-called stiffened-gas equation of state in…

A: Given:- γ= 4-7π=4×108Pac=4200kJ/kgK To find: a) Volumetric thermal expansion b) Isothermal…

Q: B- Find an expression for Cp - Cv if the equation of state is p = for an ideal gas. RT v-b and Show…

Q: Give an example of Beattie-Bridgeman and the Benedict-Webb-Rubin equations of state

A: The Beattie-Bridgemann equation of state is based on the five experimentally determined constants.…

Q: 22 kg of CO₂ at 300 K is kept in a vessel of 5m³ capacity. Find the pressure exerted by CO₂ in the…

Q: 90 90 bpB Vapor 80 + 80 70 70 Liquid 60 60 50 100% A 80 20 60 40 40 60 20 80 100% B 0% 0% b. What is…

Q: 5) A stainless steel spherical container, with k=15 W/m.K is used for storing chemicals undergoing…

A: To solve this problem, we need to apply the principles of heat transfer in a spherical shell. We…

Q: Using the two relationships below, aC Pm не =V -T ƏT ÔT ( ƏP ƏP nR +B(T) conforms to, show that the…

Q: An ideal gas follows the relationship pv-10 where V is in m' and p is in kPaa. Draw the pV diagram…

Q: B- Find an expression for Cp - Cv if the equation of state is p = RT for ideal gas. na an - and Show…

Q: For an ideal gas, the value of Joule-Thomson co-efficient is?

Q: RT For a gas with the equation of state V= +(aT2 + b)P the P expression of is:

Q: The water in the vessel consisting of liquid and vapor in equilibrium at 8.547 Mpa. It has found out…

A: Given DataP=8.5MPaU=2138.545kJ/kg

Q: A spherical tank 8.5 m in diameter contains methane (CH4) at 450 kPa and 35oC and 10 kg had been…

Q: The saturation table for refrigerant-134a lists the following at -40°C: P= 51.25 kPa, hfg=225.86…

Q: In the project, the theoretical methods will be used to construct the property tables for ammonia…

A: To construct the property tables for ammonia using the Van der Waals equation of state, several…

Q: Contruct a P-v and T-v diagram for water and refrugerant-134a

A: here, Water and R-134 a both are pure substances. so, P-V and T-V diagram mostly look a like, only…

Q: Is it possible to have water vapor at 5°C? If so, what would be the saturated pressure?

A: The temperature of the water vapor is 5 degree centigrade.

Q: The frictionless piston and the cylinder contain 0.2kg of air at 1.5MPa, 350℃ (state 1). This air is…

Q: where are you looking in the steam tables to get the 103 kj/kg , nd how are you getting 163 , for…

Concept explainers

Properties of Pure Substances

A substance with fixed chemical composition throughout is called a pure substance like water, air, and nitrogen. A pure substance does not have to be a single element or compound. A mixture of two or more phases of a pure substance is also a pure substance as long as the chemical composition is the same for all phases. These substances mainly have a constant/ uniform composition. The substances also have fixed boiling and melting points. A pure substance takes part in a chemical reaction to form predictable products.

Question

Based on the table A-4 and table A-5, contruct P-v abd T-v diagram for water

915
APPENDIX 1
TABLE A–4
Saturated water-Temperature table (Concluded)
Internal energy,
Entropy,
kJ/kg-K
Specific volume,
Enthalpy,
m/kg
kJ/kg
kJ/kg
Sat.
Sat.
Sat.
Sat.
Sat.
Sat.
Sat.
Sat.
Sat.
Temp.,
press.,
liquid,
vapor,
liquid,
Evap., vapor,
liquid,
Evap., vapor,
liquid,
Evap., vapor,
T°C
Pat kPa vf
Uig
h;
hg
hg
Sig
205
1724.3
0.001164
0.11508
872.86
1723.5
2596.4
874.87 1920.0
2794.8
2.3776 4.0154 6.3930
210
1907.7
2797.3
0.001173
0.001181
0.10429
895.38
918.02
1702.9
2598.3
897.61 1899.7
2.4245 3.9318 6.3563
215
2105.9
0.094680
1681.9
2599.9
920.50 1878.8
2799.3
2.4712 3.8489 6.3200
0.086094
2601.3
2602.3
220
2319.6 0.001190
940.79
1660.5
943.55 1857.4
2801.0
2.5176 3.7664 6.2840
225
2549.7 0.001199 0.078405
963.70 1638.6
966.76 1835.4
2802.2
2.5639 3.6844 6.2483
230
2797.1
0.001209 0.071505
986.76 1616.1
2602.9
990.14 1812.8
2802.9
2.6100 3.6028 6.2128
235
240
3062.6 0.001219
0.065300
0.059707
0.054656
1010.0
1593.2
2603.2
1013.7
1789.5
2803.2
2.6560 3.5216 6.1775
0.001229
0.001240
3347.0
1033.4
1569.8
2603.1
1037.5 1765.5
2803.0
2.7018 3.4405 6.1424
245
3651.2
1056.9
1545.7
2602.7
1061.5 1740.8
2802.2
2.7476 3.3596 6.1072
250
3976.2
0.001252 0.050085
1080.7
1521.1
2601.8
1085.7 1715.3
2801.0
2.7933 3.2788 6.0721
255
4322.9
1104.7
0.045941
4692.3 0.001276 0.042175
0.001263
1495.8 2600.5
1110.1
1689.0
2799.1
2.8390 3.1979 6.0369
260
1128.8
1469.9
2598.7
1134.8
1661.8
2796.6
2.8847 3.1169 6.0017
265
5085.3 0.001289
0.038748
1153.3
1443.2
2596.5
1159.8 1633.7
2793.5
2.9304 3.0358 5.9662
270
5503.0
0.001303
0.035622
1177.9
1415.7
2593.7
1185.1 1604.6
2789.7
2.9762 2.9542 5.9305
275
5946.4
0.001317
0.032767
1202.9
1387.4
2590.3
1210.7
1574.5
2785.2
3.0221
2.8723 5.8944
280
6416.6
0.001333
0.030153
1228.2
1358.2
2586.4
1236.7
1543.2
2779.9
3.0681 2.7898 5.8579
285
6914.6
0.001349
0.027756
1253.7
1328.1
2581.8
1263.1
1510.7
2773.7
3.1144 2.7066 5.8210
290
7441.8
0.001366
0.025554
1279.7
1296.9
2576.5
1289.8
1476.9
2766.7
3.1608 2.6225 5.7834
295
7999.0
0.001384
0.023528
1306.0
1264.5
2570.5
1317.1
1441.6
2758.7
3.2076 2.5374 5.7450
300
8587.9 0.001404 0.021659
1332.7
1230.9
2563.6
1344.8
1404.8
2749.6
3.2548 2.4511 5.7059
305
9209.4 0.001425
0.019932
1360.0
1195.9
2555.8
1373.1
1366.3
2739.4
3.3024 2.3633 5.6657
310
9865.0 0.001447 0.018333
1387.7
1159.3
2547.1
1402.0
1325.9
2727.9
3.3506 2.2737 5.6243
315
1121.1 2537.2
1431.6
10,556
11,284
12,051
0.001472 0.016849
1416.1
1283.4
2715.0
3.3994 2.1821 5.5816
320
325
0.001499 0.015470
1445.1
1080.9
2526.0
1462.0
1238.5
2700.6
3.4491
2.0881 5.5372
0.001528 0.014183
1475.0
1038.5
2513.4
1493.4
1191.0
2684.3
3.4998 1.9911 5.4908
330
2499.2
12,858
13,707
14,601
15,541
16,529
0.001560 0.012979
1505.7
993.5
1525.8
1140.3
2666.0
3.5516 1.8906 5.4422
335
0.001597 0.011848
1537.5
945.5
2483.0
1559.4
1086.0
2645.4
3.6050 1.7857 5.3907
340
345
0.001638 0.010783
1570.7
893.8
2464.5
1594.6
1027.4
2622.0
3.6602 1.6756 5.3358
0.001685 0.009772
1605.5
837.7
2443.2
1631.7
963.4
2595.1
3.7179 1.5585 5.2765
350
0.001741 0.008806
1642.4
775.9
2418.3
1671.2
892.7
2563.9
3.7788 1.4326 5.2114
17,570
18,666
19,822
21,044
373.95 22,064
0.001808 0.007872
1682.2
1726.2
1777.2
355
706.4
2388.6
1714.0
812.9
2526.9
3.8442 1.2942 5.1384
360
0.001895 0.006950
625.7
2351.9
1761.5
720.1
2481.6
3.9165 1.1373 5.0537
365
0.002015 0.006009
526.4
2303.6
1817.2
605.5
2422.7
4.0004 0.9489 4.9493
370
0.002217
0.004953
1844.5
385.6
2230.1
1891.2
443.1
2334.3
4.1119 0.6890 4.8009
0.003106 0.003106
2015.7
2015.7
2084.3
2084.3
4.4070 0
4.4070

cen84959_ch18-ap01.qxd 8/11/06 1:21 PM Page 918
918 I
Thermodynamics
TABLE A-5
Saturated water-Pressure table
Internal energy,
Specific volume,
m/kg
Enthalpy,
kJ/kg
Entropy,
kJ/kg · K
St.
kJ/kg
Sat.
Sat.
Sat
Sat.
Sat.
Sat.
Sat.
St.
Evap.,
Press., temp., liquid,
P kPa
liquid,
liquid,
h;
vapor,
vapor,
Evap.,
vapor, liquid, Evap., vapor,
Tu °C V
he
S
1.0
6.97 0.001000 129.19
29.302 2355.2
2384.5
29.303 2484.4 2513.7 0.1059 8.8690 8.9749
13.02 0.001001 87.964
17.50 0.001001 66.990
1.5
54.686 2338.1
2392.8
54.688 2470.1 2524.7 0.1956 8.6314 8.8270
2.0
73.431 2325.5
2398.9
73.433 2459.5 2532.9 0.2606 8.4621 8.7227
2.5
21.08 0.001002 54.242
88.422 2315.4
2403.8
88.424 2451.0 2539.4 0.3118 8.3302 8.6421
3.0
24.08 0.001003 45.654
100.98 2306.9
2407.9
100.98
2443.9 2544.8 0.3543 8.2222 8.5765
4.0
28.96 0.001004 34.791
121.39
2293.1
2414.5
121.39
2432.3 2553.7 0.4224 8.0510 8.4734
5.0
32.87
0.001005 28.185
137.75
2282.1
2419.8
137.75
2423.0 2560.7 0.4762 7.9176 8.3938
7.5
40.29
0.001008 19.233
168.74
2261.1
2245.4
2429.8
168.75
2405.3 2574.0 0.5763 7.6738 8.2501
10
45.81 0.001010
14.670
191.79
2437.2 191.81
2392.1 2583.9 0.6492 7.4996 8.1488
15
53.97 0.001014
10.020
225.93
2222.1
2448.0 225.94
2372.3 2598.3 0.7549 7.2522 8.0071
60.06 0.001017
64.96 0.001020
2456.0 251.42
2462.4 271.96
20
7.6481
251.40
2204.6
2357.5 2608.9 0.8320 7.0752 7.9073
271.93
289.24
317.58
25
6.2034
2190.4
2345.5 2617.5 0.8932 6.9370 7.8302
30
69.09 0.001022
5.2287
2178.5
2467.7 289.27
2335.3 2624.6 0.9441 6.8234 7.7675
40
75.86 0.001026
3.9933
2158.8
2476.3 317.62
2318.4 2636.1 1.0261 6.6430 7.6691
50
81.32 0.001030
3.2403
340.49
2142.7
2483.2 340.54
2304.7 2645.2 1.0912 6.5019 7.5931
75
91.76 0.001037
2.2172
384.36
2111.8
2496.1
384.44
2278.0 2662.4 1.2132 6.2426 7.4558
100
99.61 0.001043
1.6941
417.40
2088.2
2505.6
417.51
2257.5 2675.0 1.3028 6.0562 7.3589
418.95
444.23
466.97
101.325 99.97 0.001043
1.6734
2087.0
2506.0 419.06
2256.5 2675.6 1.3069 6.0476 7.3545
105.97 0.001048
111.35 0.001053
2068.8
2513.0
2519.2 467.13
125
1.3750
444.36
2240.6 2684.9 1.3741 5.9100 7.2841
150
1.1594
2052.3
2226.0 2693.1 1.4337 5.7894 7.2231
175
116.04 0.001057
1.0037
486.82
2037.7
2524.5 487.01
2213.1 2700.2 1.4850 5.6865 7.1716
200
120.21 0.001061
0.88578 504.50
2024.6
2529.1
504.71
2201.6 2706.3 1.5302 5.5968 7.1270
123.97 0.001064
2012.7
2533.2
225
250
0.79329 520.47
520.71
2191.0 2711.7 1.5706 5.5171 7.0877
127.41 0.001067
0.71873 535.08
2001.8
2536.8
535.35
2181.2 2716.5 1.6072 5.4453 7.0525
275
130.58 0.001070
0.65732 548.57
1991.6
2540.1
548.86
2172.0 2720.9 1.6408 5.3800 7.0207
133.52 0.001073
0.60582 561.11
0.56199 572.84
0.52422 583.89
0.49133 594.32
2543.2 561.43
573.19
300
1982.1
2163.5 2724.9 1.6717 5.3200 6.9917
325
350
136.27 0.001076
1973.1
2545.9
2155.4 2728.6 1.7005 5.2645 6.9650
138.86 0.001079
584.26
2550.9 594.73
1964.6
2548.5
2147.7 2732.0 1.7274 5.2128 6.9402
375
141.30 0.001081
1956.6
2140.4 2735.1 1.7526 5.1645 6.9171
400
143.61 0.001084
0.46242 604.22
1948.9
2553.1 604.66
2133.4 2738.1 1.7765 5.1191 6.8955
450
147.90 0.001088
0.41392 622.65
1934.5 2557.1 623.14
2120.3 2743.4 1.8205 5.0356 6.8561
0.37483 639.54
0.34261 655.16
500
151.83
0.001093
1921.2
2560.7 640.09
2108.0 2748.1 1.8604 4.9603 6.8207
550
155.46 0.001097
1908.8
2563.9 655.77
2096.6 2752.4 1.8970 4.8916 6.7886
1897.1
2566.8 670.38
2569.4 684.08
600
158.83 0.001101
0.31560 669.72
2085.8 2756.2 1.9308 4.8285 6.7593
650
161.98 0.001104
0.29260 683.37
1886.1
2075.5 2759.6 1.9623 4.7699 6.7322
700
164.95
0.001108
0.27278 696.23
1875.6
2571.8 697.00
2065.8 2762.8 1.9918 4.7153 6.7071
750
167.75 0.001111
0.25552 708.40
1865.6 2574.0
709.24
2056.4 2765.7 2.0195 4.6642 6.6837

Expert Solution

This question has been solved!

Explore an expertly crafted, step-by-step solution for a thorough understanding of key concepts.

This is a popular solution!

SEE SOLUTION Check out a sample Q&A here

Step 1

VIEW

Step 2: Answer

VIEW

Trending now

This is a popular solution!

Step by step

Solved in 2 steps with 2 images

SEE SOLUTION Check out a sample Q&A here

Knowledge Booster

Learn more about

Need a deep-dive on the concept behind this application? Look no further. Learn more about this topic, mechanical-engineering and related others by exploring similar questions and additional content below.

Similar questions

what table and column are you looking at to get 103 kj for the enthalpy , and how are you getting the 163 , for 1866-163?.
Saturated Refrigerant-134a vapor Saturated liquid A tank occupied by saturated liquid-vapor mixture of refrigerant-134a at 3 MPa. If the fraction of the total volume occupied by vapor (Vsaturate vapor/ Vtotal) is O.94 determine quality of the mixture. Present your result as percent. (For example, if you find 0.952, enter your result to system as 95.2)
I3
quick please
A tank contains 192 kg of water at 113 kPa. 108 kg of water is in the liquid form and the rest is in the vapor form. The saturation temperature is 100.5 C, the specific volume of saturated liquid is 0.001040 m³/kg, and the specific volume of saturated vapor is 2.7808 m³/kg. a. Draw the P-v diagram to represent the phase transition from water, and specify the phase regions and lines explicitly. b. Mark the numerical values on the diagram, and determine the total volume of the mixture?
9d
3000 kJ of heat is given to 1 kg of water at 20 C. If steam with a pressure of 750 kPa is obtained as a result of this process, is this steam wet?institution? You should reach the result by typing the table values and operation steps. TIP: You should decide on enthalpy values using Thermodynamic Property Tables.
where are you finding v=0.0159939 m3/kg ? , when I look for the specific volume for saturate steam at 11000 kpa , I am finding vg=15.987 ?
How does steam at 350° C formed from water at 40°C,at 1atm. Explain in detail with the types of steams with diagrams. Draw also T-v diagram showing all parameters
Q4 Show that for a gas obeying van der Walls equation of state, 2a Cp – Cy = R + vT
Can anyone get correct answer for this?