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152 Consider a steady-flow process in which the following gas-phase reaction takes place: CO ;o2-+ C 0 2 The surroundings are at 300 K ( a ) What is Wideal when the reactants enter the process as pure carbon monoxide and as air containing the stoichiometric amount of oxygen, both at 29815 K (25 C) and 1 bar, and the products of complete combustion leave the process at the same conditions (6) The overall process is exactly the same as in (a), but the CO is here burned in an adiabatic reactor at 1 bar What is Wideal the process of cooling the flue gases to for 29815 K (25"C) What is the irreversible feature of the overall process What is its thermodynamic efficiency What has increased in entropy, and by how much

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try { String query = new String ("SELECT SUM(Quantity) " + "FROM Orders "); DataRequest = DatabasecreateStatement(); Results = DataRequestexecuteQuery (query); DisplayResults (Results);

The remainder of this chapter discusses each element in detail, including a complete description of the element, a table that lists the element s usage rules, a usage example for the element, and if applicable, a usage example of associated annotations In the tables that describe each element s usage rules, pay special attention to the JSF Versions rule, which specifies the JSF versions to which the given element is applicable

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The absolute-ordering element encapsulates the set of elements that specify the absolute order by which named JSF XML configuration files are to be loaded This element may only be used in the application s /WEB-INF/faces-configxml file It may not be used in any /META-INF/faces-configxml file found in a jar or in any file listed in javaxfacesCONFIG_ FILES key in webxml This element has no other use than to denote the beginning and end of absolute ordering details

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153 A plant has saturated steam available at 2700 kPa, but there is little use for this steam Rather, steam at 1000 kPa is required Also available is saturated steam at 275 kPa A suggestion is that the 275 kPa steam be compressed to 1000 kPa, using the work of expanding of the 2700 kPa steam to 1000 kPa The two streams at 1000 kPa would then be mixed Determine the rates at which steam at each initial pressure must be supplied to provide enough steam at 1000 kPa so that upon condensation to saturated liquid heat in the amount of 300 kW is released, ( a ) If the process is carried out in a completely reversible manner ( b ) If the higher-pressure steam expands in a turbine of 78% efficiency and the lowerpressure steam is compressed in a machine of 75% efficiency Make a thermodynamic analysis of this process 154 Make a thermodynamic analysis of the refrigeration cycle of Ex 9l(b) 155 Make a thermodynamicanalysis of the refrigeration cycle described in one of the parts of Pb 99 Assume that the refrigeration effect maintains a heat reservoir at a temperature 55 K (55"C) above the evaporation temperature and that T, is 55 K (55"C) below the condensation temperature 156 Make a thermodynamic analysis of the refrigeration cycle described in the first paragraph of Pb 912 Assume that the refrigeration effect maintains a heat reservoir at a temperature 55 K (55"C) above the evaporation temperature and that T, is 55 K (55"C)below the condensation temperature 157 A colloidal solution enters a single-effect evaporator at 37315 K (100 C) Water is vaporized from the solution, producing a more concentrated solution and 05 kg s-' of steam at 37315 K (100 C) This steam is compressed and sent to the heating coils of the evaporator to supply the heat required for its operation For a minimum heat-transfer driving force across the evaporator coils of 10 K (lO C),for a compressor efficiency of 75%, and for adiabatic operation, what is the state of the steam leaving the heating coils of the evaporator For a surroundings temperature of 300 K, make a thermodynamic analysis of the process 158 Make a thermodynamic analysis of the process described in Pb 88 T, = 30015 K (27 C) 159 Make a thermodynamic analysis of the process described in Ex 93 To = 295 K.

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