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The application of principles of heat transfer to the design of equipment to accomplish a certain engineering objective is of extreme importance In a heat exchanger, heat transfer from one uid to another occurs either by direct contact or through an intervening wall The following section deals with the recuperative-type heat exchanger in which the uids exchange heat through a wall One uid ows through a series of tubes and the other through a shell surrounding them (shell-and-tube heat exchanger) Flow may be either parallel (Fig 99) (both uids moving in the same direction) or counter ow (Fig 910) ( uids moving in opposite directions) Another possibility is the cross ow arrangement in which the ows are at right angles

Here s what is happening behind the scenes when you add a COM reference to your application: A copy of the component is placed in the project directory A proxy is generated for the COM component The proxy is called a Runtime Callable Wrapper (RCW), and it essentially makes the COM component look like a NET assembly

Other types have more complex ows: eg, the multi-pass and mixed- ow types The heat transfer rate is calculated from Eq 98 where U is the overall heat transfer coef cient given by Eq 911; A is heat transfer area (surface area of tubes) The following relations give the heat transferred, the logarithmic mean temperature difference Tm and the effectiveness Tm T2 T2 ln T1 Tc2 Th1 Tc1 Tc1 T1 (933)

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actual heat transfer maximum possible heat transfer where heat transfer is q and U 1 1 / ha 1 / hc U A Tm

Figure 21-13

(934)

Although Visual Studio NET does the preceding things for you, you may be asked on the Microsoft exam to prove your expertise with the command tool that allows you to manually generate the NET proxy The tool is called TtlbImpexe, and it is the Type Library Importer The importer will convert the definitions in the COM library to equivalent definitions in CLR The tool will create an assembly that can be looked at by using Ildasmexe, which is the MSIL disassembler utility The syntax for using the Type Library Importer tool is as follows:

assuming that the main resistance to heat transfer is on the uid side, ie, the heat transfer conduction resistance through the tube wall is much smaller A ha hc mean surface area of tubes heat transfer coefficient for hot fluid side heat transfer coefficient for cold fluid side

tlbimp <name of file containing the COM type library> [options]

It is important to note that if one of the uids is a condensing vapor or a boiling liquid, the temperature is constant on that side, T1 T2 Counter Flow (Fig 910) For this case the temperature range possible is greater than for the parallel- ow type (Fig 99) The same formulas apply Cross Flow Instead of using Tm as above, Tm F is used, where F is a factor obtained from tables (see Ref 9) q U A F Tm Tm is the same as for

Figure 21-14

The subjects of thermodynamics and heat transfer are highly complementary, although some fundamental differences exist between them Although thermodynamics is concerned with heat interaction and the vital role that it plays in the rst and second laws, it considers neither the basic mechanisms that provide for heat

Since no even numbers are in the sequence, FirstOrDefault returns the zero default value. On the other hand, the LastOrDefault operator looks for the last odd number in the sequence and finds the number 9. Figure 1-24 shows the output.

exchange nor the methods that exist for computing the rate of heat exchange3,7 Thermodynamics is concerned with equilibrium states More speci cally, thermodynamics may be used to determine the amount of energy required in the form of heat for a system to pass from one equilibrium state to another The discipline of heat transfer does what thermodynamics is inherently unable to do It considers the rate at which heat transfer occurs in terms of thermal nonequilibrium This is done through the introduction of a new set of physical principles These principles are transport laws, which are not a part of the subject of thermodynamics They include Fourier s law, the Stefan-Boltzmann law, and Newton s law of cooling, which were de ned earlier In summary, it is important to remember that a description of heat transfer requires that the additional principles be combined with the rst law of thermodynamics

/asmversion:versionnumber /help or / /out:filename /namespace:namespace /primary /publickey:filename /verbose /unsafe /reference:filename /silent Table 21-2

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