help with the question pls Question 1This question requires the use of the Thermodynamic Property Tables supplied asadditional material.In addition, for steam, the specific ideal gas constant = 461.5 J/kg KA closed system is comprised of 10 kg of pure water substance initially at a temperature of400 °C and a pressure of 8.5 MPa (state 1).a) For state 1, show that the system is in the superheated yapour phase.(b) Evaluate the specific volume of the steam in state 1 using the thermodynamic propertytables supplied and compare it to the value obtained assuming the steam behaves asan ideal gas.Which value would you have most confidence in (give reasons for your choice).The system now undergoes an isentropic (constant entropy) adiabatic process during which itspressure drops to 100 kPa (state 2).c) For state 2 show that the system is now in the two-phase region.(d) Find the work done by the system on its surroundings during the process. Superheated Steam*P/[bar](T/C])200250300350400450500600[C]. 0.37484 2562h 2749$ 6.822v, 0.31564. 2568h 2757S, 6.761v, 0.2728. 2573h 2764S, 6,709D, 0.24034 2577, 2769$ 6.663, 0.2149. 2581h, 2774$ 6.623D. 0.194444 2584h. 2778i 6.586", 0.13172595h 2792S% 6.445, 0.09964. 2600h. 2799S, 6.340D. 0.06664. 2603h, 2803S% 6.186v. 0.0498и, 2602h, 2801S, 6.070", 0.03944, 2597h, 2794S% 5.9730.4252 0.4745 0.5226 0.5701 0.6172 0.6641 0.7108 0.804029633168 3272 33777.633 7.793 7.9445264428577.060272529627.271280430657.46028833045312934848.087330037028.351u(151.8)0.3522 0.3940 0.4344 0.4743 0.5136 0.5528 0.5919 0.66972881 29623166 32707.546 7.7076.(158.8)27222851 29586.968 7.1822640280130627.373304433763128 329934837.858 8.001 8.26737010.3001 0.3364 0.3714 0.4058 0.4397 0.4734 0.5069 0.57372636 2720 2800 28802846 2955 3060 3164 32696.888 7.106 7.298 7.473 7.634 7.786 7.929 8.195304333743127 32983482 37002961(165.0)0.2610 0.2933 0.3242 0.3544 0.3842 0.4138 0.4432 0.50188(170.4)2631 2716 2798284030423267 3373 3481 3699287829603126 329829513057 31626.817 7.040 7.233 7.409 7.571 7.723 7.866 8.1320.2305 0.2597 0.2874 0.3144 0.3410 0.3674 0.3937 0.4458262828356.753271429486.98027963055 31607.176 7.3522877 2959 3041 3126 32983372 3480 36997.667 7.811 8.077(175.4)32667.5150.20612623h0.2328 0.2580 0.2825 0.3065 0.3303 0.3540 0.4010295732647.46410271129446.926279430527.124287531587.3013040 3124 329733707.617(179.9)28296.6953478 36987.761 8.0280.1324 0.1520 0.1697269729256.7110.1865286831487.1020.2029 0.2191 0.2351 0.266729523256 33647.268 7.423 7.569 7.83815(198.3)259727966.452278430396.9193035 3120 32943473 36940.1115 0.1255 0.1386 0.1511 0.1634 0.1756 0.199526812904 3025 3138 3248 3357 3467 36906.547202774 2861 2946 30303116 3291(212.4)6.768 6.957 7.126 7.283 7.431 7.70130(233.8)0.0706 0.0812 0.0905 0.0993 0.1078 0.1161 0.1324264628586.2892751 2845 2933 3020 3108 328529956.541uh31176.7443231 3343 3456 36826.921 7.082 7.233 7.5070.0588 0.0664 0.0733 0.0800 0.0864 0.09882728 2828 2921 3010 3099 32793214 333040(250.3)h29636,36430946.58434456.769 6.935 7.089 7.36836740.0453 0.0519 0.0578 0.0632 0.0685 0.078650(263.9)2700 - 28102927 3070 3196 3316290730003090 327336667.258h34336.212 6.451 6.646 6.818 6.975". 0.03244. 2590h, 2784S. 5.890v, 0.02742581h. 2772S, 5.8140.0362 0.0422 0.0473 0.0521 0.0566 0.0652298833016.336 6.541 6.719 6.87960(275.6)2670 2792 28932887 3045 31776.07130813421326636577.166v/[m /kg]u/[kJ/kg]h/[kJ/kg]s/[kJ/kgk]0.0295 0.0352 0.0399 0.0441 0.0481 0.0556287931586.44870(285.8)263428415.934277230186.2312978 30733287 34106.632326036497.0886.796See footnote on p.6.

Question

help with the question pls Question 1This question requires the use of the Thermodynamic Property Tables supplied asadditional material.In addition, for steam, the specific ideal gas constant = 461.5 J/kg KA closed system is comprised of 10 kg of pure water substance initially at a temperature of400 °C and a pressure of 8.5 MPa (state 1).a) For state 1, show that the system is in the superheated yapour phase.(b) Evaluate the specific volume of the steam in state 1 using the thermodynamic propertytables supplied and compare it to the value obtained assuming the steam behaves asan ideal gas.Which value would you have most confidence in (give reasons for your choice).The system now undergoes an isentropic (constant entropy) adiabatic process during which itspressure drops to 100 kPa (state 2).c) For state 2 show that the system is now in the two-phase region.(d) Find the work done by the system on its surroundings during the process. Superheated Steam*P/[bar](T/C])200250300350400450500600[C]. 0.37484 2562h 2749$ 6.822v, 0.31564. 2568h 2757S, 6.761v, 0.2728. 2573h 2764S, 6,709D, 0.24034 2577, 2769$ 6.663, 0.2149. 2581h, 2774$ 6.623D. 0.194444 2584h. 2778i 6.586&#34;, 0.13172595h 2792S% 6.445, 0.09964. 2600h. 2799S, 6.340D. 0.06664. 2603h, 2803S% 6.186v. 0.0498и, 2602h, 2801S, 6.070&#34;, 0.03944, 2597h, 2794S% 5.9730.4252 0.4745 0.5226 0.5701 0.6172 0.6641 0.7108 0.804029633168 3272 33777.633 7.793 7.9445264428577.060272529627.271280430657.46028833045312934848.087330037028.351u(151.8)0.3522 0.3940 0.4344 0.4743 0.5136 0.5528 0.5919 0.66972881 29623166 32707.546 7.7076.(158.8)27222851 29586.968 7.1822640280130627.373304433763128 329934837.858 8.001 8.26737010.3001 0.3364 0.3714 0.4058 0.4397 0.4734 0.5069 0.57372636 2720 2800 28802846 2955 3060 3164 32696.888 7.106 7.298 7.473 7.634 7.786 7.929 8.195304333743127 32983482 37002961(165.0)0.2610 0.2933 0.3242 0.3544 0.3842 0.4138 0.4432 0.50188(170.4)2631 2716 2798284030423267 3373 3481 3699287829603126 329829513057 31626.817 7.040 7.233 7.409 7.571 7.723 7.866 8.1320.2305 0.2597 0.2874 0.3144 0.3410 0.3674 0.3937 0.4458262828356.753271429486.98027963055 31607.176 7.3522877 2959 3041 3126 32983372 3480 36997.667 7.811 8.077(175.4)32667.5150.20612623h0.2328 0.2580 0.2825 0.3065 0.3303 0.3540 0.4010295732647.46410271129446.926279430527.124287531587.3013040 3124 329733707.617(179.9)28296.6953478 36987.761 8.0280.1324 0.1520 0.1697269729256.7110.1865286831487.1020.2029 0.2191 0.2351 0.266729523256 33647.268 7.423 7.569 7.83815(198.3)259727966.452278430396.9193035 3120 32943473 36940.1115 0.1255 0.1386 0.1511 0.1634 0.1756 0.199526812904 3025 3138 3248 3357 3467 36906.547202774 2861 2946 30303116 3291(212.4)6.768 6.957 7.126 7.283 7.431 7.70130(233.8)0.0706 0.0812 0.0905 0.0993 0.1078 0.1161 0.1324264628586.2892751 2845 2933 3020 3108 328529956.541uh31176.7443231 3343 3456 36826.921 7.082 7.233 7.5070.0588 0.0664 0.0733 0.0800 0.0864 0.09882728 2828 2921 3010 3099 32793214 333040(250.3)h29636,36430946.58434456.769 6.935 7.089 7.36836740.0453 0.0519 0.0578 0.0632 0.0685 0.078650(263.9)2700 - 28102927 3070 3196 3316290730003090 327336667.258h34336.212 6.451 6.646 6.818 6.975&#34;. 0.03244. 2590h, 2784S. 5.890v, 0.02742581h. 2772S, 5.8140.0362 0.0422 0.0473 0.0521 0.0566 0.0652298833016.336 6.541 6.719 6.87960(275.6)2670 2792 28932887 3045 31776.07130813421326636577.166v/[m /kg]u/[kJ/kg]h/[kJ/kg]s/[kJ/kgk]0.0295 0.0352 0.0399 0.0441 0.0481 0.0556287931586.44870(285.8)263428415.934277230186.2312978 30733287 34106.632326036497.0886.796See footnote on p.6.

Accepted Answer

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