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912 A vapor-compression refrigeration system is conventional except that a countercurrent heat exchanger is installed to subcool the liquid from the condenser by heat exchange with the vapor stream from the evaporator The minimum temperature difference for heat transfer is 56 K (56"C) Tetrafluoroethane is the refrigerant (Table 91, Fig G2), evaporating at 26615 K (-7 C) and condensing at 30015 K (27 C) The heat load on the evaporator is 2110 kW If the compressor efficiency is 75%, what is the power requirement How does this result compare with the power required by the compressor if the system operates without the heat exchanger How do the refrigerant circulation rates compare for the two cases 913 Consider the vapor-compression refrigeration cycle of Fig 91 with tetrafluoroethane as refrigerant (Table 91, Fig G2) If the evaporation temperature is 26115 K (- 12"C), show the effect of condensation temperature on the coefficient of performance by making calculations for condensation temperatures of 28875 K (156"C), 30015 K (27 C) and 31115 K(38"C) (a) Assume isentropic compression of the vapor (b) Assume a compressor efficiency of 75% 914 A heat pump is used to heat a house in the winter and to cool it in the summer During the winter, the outside air serves as a low-temperature heat source; during the summer, it acts as a high-temperature heat sink The heat-transfer rate through the walls and roof of the house is 075 kW for each kelvin of temperature difference between the inside and outside of the house, summer and winter The heat-pump motor is rated,at 15 kW Determine the minimum outside temperature for which the house can be maintained at 29315 K (20 C) during the winter and the maximum outside temperature for which the house can be maintained at 29815 K (25 C) during the summer 915 Dry methane is supplied by a compressor and precooling system to the cooler of a Linde liquid-methane system (Fig 96) at 180 bar and 300 K The low-pressure methane leaves the cooler at a temperature 6 K (6 C) lower than the temperature of the incoming high-pressure methane The separator operates at 1 bar, and the product is saturated liquid at this pressure What is the maximum fraction of the methane entering the cooler that can be liquefied Perry's Chemical Engineers' Handbook (footnote 7) is a source of data for methane.

TIP If you wait about an hour, you should see a mail message from the carpaldsh script You can use the mail program from the command line by typing:

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916 Rework the preceding problem for methane entering at 200 bar, and precooled to 240 K by external refrigeration An advertisement is noted in a rural newspaper for a dairy-barn unit that combines a milk cooler with a water heater Milk must, of course, be refrigerated, and hot water is required for washing purposes The usual barn is equipped with a conventional air-cooled electric refrigerator and an electric-resistance water heater The new unit is said to provide both the necessary refrigeration and the required hot water at a cost for electricity about the same as the cost of running just the refrigerator in the usual installation To assess this claim, compare two refrigeration units: The advertised unit takes 1465 kW from a milk cooler at 27215 K (-l0C), and discards heat through a

[root@fedora-serverA ~]# mail Mail version 81 6/6/93 Type for help "/var/spool/mail/root": 1 message 1 new >N 1 root@serverAexample Fri Aug 30 11:49 1/6 "Carpal Tunnel Warning" &

as derived from the LeeIKesler correlation as functions of T, and P,, thus providing a threeparameter generalized correlation for fugacity coefficients Tables E13 and E15 for #' can be used alone as a two-parameter correlation which does not incorporate the refinement introduced by the acentric factor

At times, you may find that you simply don t need a particular service to be started at boot time This is especially important if you are configuring the system as a server and need only specific services and nothing more As described in the preceding sections, you can cause a service not to be started by simply renaming the symbolic link in a particular runlevel directory; rename it to start with a K instead of an S Once you are comfortable working with the command line, you ll quickly find that it is easy to enable or disable a service The startup runlevels of the service/program can also be managed using the chkconfig utility To view all the runlevels in which the carpaldsh program is configured to start up, type

Figure 18-17. The words Not Pressed will display if the variable has a value of False. Finally, I drop in an NXT BUTTON WAIT block to wait until the left button is pressed; this will give me time to view the results on the screen (see Figure 18-18).

A useful generalized correlation for In # results when the simplest form of the virial equation is valid Equations (358) and (359) combine to give:

If you check the list of runlevels for the carpaldsh program again, you will see that the field for runlevel 2 has been changed from 2:off to 2:on Type

Substitution in Eq (1162) and integration yield:

Graphical user interface (GUI) tools are available that will help you manage which services start up at any given runlevel In Fedora and other Red Hat type systems (including RHEL), one such tool is the system-config-services utility (see Figure 6-1) To launch the program, type

This equation, used in conjunction with Eqs (361) and (362), provides reliable values of 4 for any nonpolar or slightly polar gas when applied at conditions where Z is approximately linear in pressure Figure 315 again serves as a guide to its suitability

Named functions, HRB(TR,PR,OMEGA) and SRB(TR,PR,OMEGA), for evaluation of H R / RT, and S R / R by the generalized virial-coefficient correlation were described in Sec 67 Similarly, we introduce here a function named PHIB(TR,PR,OMEGA) for evaluation of 4:

On a system running OpenSuSE Linux, the equivalent GUI program (see Figure 6-2) can be launched by typing:

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