Thermodynamic and Transport Properties of Fluids

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Superheated steam has a pressure and temperature of 40 bar and 400 oC respectively. Using the steam tables (Rogers and Mayhew, 1995, 5th Edition), determine the: Using the steam tables (Rogers and Mayhew, 1995, 5th Edition), determine the: The saturated steam tables give infor- mation about the two-phase region while the superheated tables give information about the vapor phase. Since we know from part (a) that our point lies in the vapor phase, we will use the superheated steam Reproduced from Rogers, G. F. C., and Mayhew, Y. R., Engineering Thermydt~namics, Work and Heat Transfer (Longman, 1992). By definition: = u' + p6 and g" = K- TS gand ii are virtually independent of pressure and in the following will be treated as such: hence

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Steam table a 1 thermodynamics lecture handout docsity steam tables fifth edition by rogerayhew steam tables steam tables Whats people lookup in this blog: Steam Table Thermodynamics Pdf Upload the PDF file you should eSign. Do that by pulling it from the internal storage or the cloud. Steam tables, namely “Thermodynamic and transport properties of fluids, SI units arranged by Rogers & Mayhew” will be provided. Please note that these tables are Molar (universal) gas constant: a = 8.3 145 kJ/kmol K t = 1.986 Btu/lb-mol R = 1545 ft Ibf/lb-mol R

c -refers to a property in the critical state f -refers to a property of the saturated liquid, or to a value of formation g -refers to a property of the saturated vapour fg -refers to a change of phase at constant p I -refers to a property of the saturated solid s -refers to a saturation temperature or pressure N2 - 28 kg/kmol 0.79 0.767 0, - 32 kg/kmol 0.2 1 0.233 N2/02 3.76 3.29 Molar mass 6 = 29 kg/kmol Specific gas constant R = 0.287 kJ/kg K

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National Engineering Laboratory, Sream Tables 1964 (Her Majesty's Stationery Office 1964) (reproduced by courtesy of the Controller of Her Majesty's Stationery Office). The specific heat capacities of atomic H. N and 0 are given with adequate accuracy by r;, = 2 k , ~