Thermohydraulic Analysis of Shell-and-Tube Heat Exchanger with Segmental Baffles

<table>Variation of <svg height="8.0500002" id="M17" style="vertical-align:-0.1638pt" version="1.1" viewbox="0 0 10.975 8.0500002" width="10.975" xmlns="http://www.w3.org/2000/svg" xmlns:xlink="http://www.w3.org/1999/xlink">
<g transform="matrix(.017,-0,0,-.017,.062,7.775)"><path d="M615 290q0 -148 -114 -245q-65 -57 -125 -57q-39 0 -62 27t-29 70q-31 -41 -72 -69t-74 -28q-49 0 -82.5 43t-33.5 124q0 97 55 174.5t148 124.5l15 -24q-59 -45 -94 -113t-35 -146q0 -58 19.5 -88.5t48.5 -30.5q33 0 62 34.5t45 101.5q16 73 20 135l80 17l5 -6
q-11 -37 -23.5 -100t-12.5 -92q0 -47 16.5 -71.5t44.5 -24.5q62 0 95.5 67t33.5 160q0 107 -63 152l1 9q14 14 45 14q29 0 57.5 -44t28.5 -114z" id="x1D714"></path></g>
</svg> with Reynolds number (for cold water inlet).</table>

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fig6

Figure 6

Figure 6: Thermohydraulic Analysis of Shell-and-Tube Heat Exchanger with Segmental Baffles 