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TABLA 5-11<br />

PERDIDAS DE CALOR EN LAS TUBERIAS<br />

DiAmetro Temperatura de Espesor del ?Ardida de calor, Eficiencia<br />

de It <strong>la</strong> superficia, ais<strong>la</strong>miento, (Btuipie/hr) del<br />

tuberfa, F pulgadas Sin aisi. Con.aisl. ais<strong>la</strong>miento<br />

pulgadas<br />

4 200 1 1/2 300 70 76.7<br />

300 2 800 120 85.0<br />

400 2 1/2 1500 150 90.0<br />

6 200 1 1/2 425 95 78.7<br />

300 2 1300 180 85.8<br />

400 2 1/2 2000 195 90.25<br />

8 200 1 1/2 550 115 79.1<br />

300 2 1500 200 86.7<br />

400 2 1/2 2 750 250 91.0

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