Question: Information from table C.1 * * * * * * * [1] Steam at 900 F and 65 psia is expanded reversibly & adiabatically through

Information from table C.1

* * * * * * * [1] Steam at 900 F and 65 psia is expanded reversibly & adiabatically through a steam turbine until the pressure is reduced to ambient pressure. Find the final temperature with the following methods: a) Calculation: Equation 5.10 using the constants in Table C.1 b) Interpolation: the steam tables Find the isentropic work output of the turbine using steam tables. Table C.1: Heat Capacities of Gases in the Ideal-Gas State Constants in equation C IR = A + BT+CT+r for T (K) from 298 K tomu Chemical species T. 108 10fc 10-D CHU CH CH CHO CH CH CH CH 1500 1500 1500 1500 1500 1500 1500 1500 1500 4217 6369 9.011 11.928 11.901 14731 17.350 20.361 21.174 L702 1131 1213 1.935 1.672 2.164 1.025 2370 4.108 9.08 19.225 28.785 36.915 37.853 45 151 31722 62.127 70.567 -2.164 -5.561 -8.24 11:02 11.945 - 14.11 16.791 -19.486 -22 208 CH CH CH CH30 CH 1500 1500 1500 1500 1500 1500 1500 5.325 7.792 10.520 13:412 16.240 19.053 21.868 1424 1.637 1.967 2.691 3220 3.768 4124 14.394 2706 31.600 19.753 48.189 36.58 64.960 4.392 6.913 -9.87 12447 -15.157 -17.847 -20.52 17.978 I - 158 1.299 Alkaner Methane Ethane Propane -Butane -Butane Pentne -Hexane -Heptanc -Octane 1 Alkemes: Ethylene Propylene 1-Butene 1-Pentene 1- Herne 1-Heptene 1-Octen Miscellaneous arganics Acetaldehyde Acetylene Benzene 1.3 Busdienc Cyclohexane Ethan Ethylbenzene Ethylenc oxide Formaldehyde Methanol Styren Toluene Miscellaneous inorganics Air Ammonia nomine Carbon monoxide Carbon dioxide Carbon disulfide Chlorine Hydrogen Hydrogen sulfide Hydrogen chloride Hydrogen cyanide Nitrogen Nitrous oxide Nitric oxide Nitrogen dioxide Dinitrogen letroxide Oxygen Sulfur dioxide Sulfur trioxide Water CHO , CH CHE CH CHO CHO CHO CHO CH CH 1000 1500 1500 1500 1500 1500 1500 1000 1500 1500 1500 1500 6506 5.253 10.259 10.720 11.121 8.9.18 15.993 5.784 4191 3.547 15.534 12.922 1.693 6.132 -0.206 2.734 - 1876 3.518 1.124 -0,385 1.952 39.064 26.786 03249 20,001 55.180 23.463 7.022 12.216 50.192 47.052 13.30 -8.882 -0.92 6.00 -18,426 -9.996 -1.827 -3.450 -16,662 -15.716 2211 2050 0.200 20XXI 1800 3000 3.509 4.2009 4337 3.507 4.467 2500 2000 TROX 30XX 3000 2300 5332 4082 146 NH Bry CO CO: CS CI: H HS HCI HCN NA NO NO NO NO 0 SO, SO HO 3.355 7578 4.493 2376 5,457 6311 4442 240 2.931 3.156 4.736 3.30 3.328 1387 4082 11.660 3.639 5.699 8.000 3470 3512 1 3.502 4.616 3.590 407 9.198 3.535 4296 6.09 4038 0.375 3.020 0.056 0.557 1045 0.05 DONS 0.422 1,490 0.622 1350 0.593 1214 0.629 1.195 2.257 0.506 OSI 1.056 1450 -0.016 -018 -0.154 -0.031 1.157 0906 - OON 0212 0.151 0225 0.000 0928 0014 -0.792 -2757 0.222 2015 2028 0.121 2000 2000 2000 2000 2000 2000 Selected from H. M. Spencer de Chem., vol. pp. 2152-2154. 1948-K R Kelley, 08 Bull CV * * * * * * * [1] Steam at 900 F and 65 psia is expanded reversibly & adiabatically through a steam turbine until the pressure is reduced to ambient pressure. Find the final temperature with the following methods: a) Calculation: Equation 5.10 using the constants in Table C.1 b) Interpolation: the steam tables Find the isentropic work output of the turbine using steam tables. Table C.1: Heat Capacities of Gases in the Ideal-Gas State Constants in equation C IR = A + BT+CT+r for T (K) from 298 K tomu Chemical species T. 108 10fc 10-D CHU CH CH CHO CH CH CH CH 1500 1500 1500 1500 1500 1500 1500 1500 1500 4217 6369 9.011 11.928 11.901 14731 17.350 20.361 21.174 L702 1131 1213 1.935 1.672 2.164 1.025 2370 4.108 9.08 19.225 28.785 36.915 37.853 45 151 31722 62.127 70.567 -2.164 -5.561 -8.24 11:02 11.945 - 14.11 16.791 -19.486 -22 208 CH CH CH CH30 CH 1500 1500 1500 1500 1500 1500 1500 5.325 7.792 10.520 13:412 16.240 19.053 21.868 1424 1.637 1.967 2.691 3220 3.768 4124 14.394 2706 31.600 19.753 48.189 36.58 64.960 4.392 6.913 -9.87 12447 -15.157 -17.847 -20.52 17.978 I - 158 1.299 Alkaner Methane Ethane Propane -Butane -Butane Pentne -Hexane -Heptanc -Octane 1 Alkemes: Ethylene Propylene 1-Butene 1-Pentene 1- Herne 1-Heptene 1-Octen Miscellaneous arganics Acetaldehyde Acetylene Benzene 1.3 Busdienc Cyclohexane Ethan Ethylbenzene Ethylenc oxide Formaldehyde Methanol Styren Toluene Miscellaneous inorganics Air Ammonia nomine Carbon monoxide Carbon dioxide Carbon disulfide Chlorine Hydrogen Hydrogen sulfide Hydrogen chloride Hydrogen cyanide Nitrogen Nitrous oxide Nitric oxide Nitrogen dioxide Dinitrogen letroxide Oxygen Sulfur dioxide Sulfur trioxide Water CHO , CH CHE CH CHO CHO CHO CHO CH CH 1000 1500 1500 1500 1500 1500 1500 1000 1500 1500 1500 1500 6506 5.253 10.259 10.720 11.121 8.9.18 15.993 5.784 4191 3.547 15.534 12.922 1.693 6.132 -0.206 2.734 - 1876 3.518 1.124 -0,385 1.952 39.064 26.786 03249 20,001 55.180 23.463 7.022 12.216 50.192 47.052 13.30 -8.882 -0.92 6.00 -18,426 -9.996 -1.827 -3.450 -16,662 -15.716 2211 2050 0.200 20XXI 1800 3000 3.509 4.2009 4337 3.507 4.467 2500 2000 TROX 30XX 3000 2300 5332 4082 146 NH Bry CO CO: CS CI: H HS HCI HCN NA NO NO NO NO 0 SO, SO HO 3.355 7578 4.493 2376 5,457 6311 4442 240 2.931 3.156 4.736 3.30 3.328 1387 4082 11.660 3.639 5.699 8.000 3470 3512 1 3.502 4.616 3.590 407 9.198 3.535 4296 6.09 4038 0.375 3.020 0.056 0.557 1045 0.05 DONS 0.422 1,490 0.622 1350 0.593 1214 0.629 1.195 2.257 0.506 OSI 1.056 1450 -0.016 -018 -0.154 -0.031 1.157 0906 - OON 0212 0.151 0225 0.000 0928 0014 -0.792 -2757 0.222 2015 2028 0.121 2000 2000 2000 2000 2000 2000 Selected from H. M. Spencer de Chem., vol. pp. 2152-2154. 1948-K R Kelley, 08 Bull CV

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