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1422 Vapor sulfur hexafluoride SF6 at pressures of about 1600 kPa is used as a dielectric in large primary circuit breakers for electric transmission systems As liquids, SF6and H 2 0 are essentially immiscible, and it is therefore necessary to specify a low enough moisture content in the vapor SF6 so that if condensation occurs in cold weather a liquid-water phase will not form first in the system For a preliminary determination, assume the vapor phase an ideal gas and prepare the phase diagram [Fig 1420(a)] for H20(1)lSF6(2) at 1600 kPa in the composition range up to 1000 parts per mega parts of water (mole basis) The following approximate equations for vapor pressure are adequate:

Description Specifies the fully qualified class name of a javaxfacesapplicationNavigationHandler implementation class that will replace the JSF implementation s default navigation handler implementation Encapsulates the set of elements that specify navigation rule configuration details Encapsulates any elements specific to the JSF implementation for a given navigation-rule element See the section Extension Elements Indicates that the property defined by the enclosing element must be initialized to null Encapsulates the set of elements that specify the relative order by which named JSF XML configuration files are to be loaded Specifies that all other JSF XML configuration files are to be loaded as part of the parent absoluteordering or relative ordering scheme Specifies the fully qualified class name of a javaxfacescontextPartialViewContextFactory implementation class that will replace or decorate the JSF implementation s default partial view context factory implementation Specifies the fully qualified class name of a javax faceseventPhaseListener implementation class that will be notified of all phase changes during the JSF request processing lifecycle Encapsulates the set of elements used to specify the details for a property Specifies the fully qualified class name for a property s value Encapsulates any elements specific to a JSF implementation for a given property element See the section Extension Elements Specifies the logical name for a property Specifies the fully qualified class name of a javax faceselPropertyResolver implementation class that will replace the JSF implementation s default property resolver implementation

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try { String query = new String (" SELECT FirstName, LastName, OrderNumber, ProductName, Quantity " + " FROM Customers,Orders, Products " + " WHERE ProdNumber = ProductNumber " + " AND CustomersCustNumber = OrdersCustomerNumber"); DataRequest = DatabasecreateStatement(); Results = DataRequestexecuteQuery (query); DisplayResults (Results); DataRequestclose(); } private void DownRow ( ResultSet DisplayResults ) throws SQLException { int OrderNum, Quantity; String FirstName = new String(); String LastName = new String(); String ProductName = new String(); String printrow = new String(); FirstName = DisplayResultsgetString ( 1 ) ; LastName = DisplayResultsgetString ( 2 ) ; OrderNum = DisplayResultsgetInt ( 3 ) ; ProductName = DisplayResultsgetString ( 4 ) ; Quantity = DisplayResults getInt ( 5 ) ; printrow = FirstName + " " + LastName + " " + OrderNum + " " + ProductName + " " + Quantity ; Systemoutprintln(printrow); }

1423 In Ex 144 a plausibility argument was developed from the LLE equilibrium equations to demonstrate that positive deviations from ideal-solution behavior are conducive to liquid/liquid phase splitting (a) Use one of the binary stability criteria to reach this same conclusion (b) Is it possible in principle for a system exhibiting negative deviations from ideality to form two liquid phases 1424 Toluene(1) and water(2) are essentially immiscible as liquids Determine the dewpoint temperatures and the compositions of the first drops of liquid formed when vapor mixtures of these species with mole fractions zl = 02 and zl = 07 are cooled at the constant pressure of 10133 kPa What is the bubble-point temperature and the composition of the last drop of vapor in each case See Table 102, p 346, for vaporpressure equations 1425 n-Heptane(1) and water(2) are essentially immiscible as liquids A vapor mixture containing 65-mol-% water at 37315 K (100 C) and 101325 Wa is cooled slowly at constant pressure until condensation is complete Construct a plot for the process showing temperature vs the equilibrium mole fraction of heptane in the residual vapor See Table 102, p 346, for vapor-pressure equations 1426 Consider a binary system of species 1 and 2 in which the liquid phase exhibits partial miscibility In the regions of miscibility, the excess Gibbs energy at a particular temperature is expressed by the equation:

JSF Versions 10, 11, 12, 20

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