اولين سايت تخصصي آموزش و نگهداري و تعميرات ديگ بخار، ديگ آبگرم، ديگ روغن داغ و آموزش نگهداري و طراحي تاسيسات در ايران به صورت کاملا فارسي، و با استناد به آخرين دستاوردهي تکنولوژي ديگ هاي بخار و تاسيسات مربوطه، در جهان.

 

 

 


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HEAT TRANSFER IN THE RADIANT SECTION OF PETROLEUM HEATERS (part2): 1 - 2 - 3 - 4

 
 

DISCUSSION OF RESULTS

In order to arrive at a definite conclusion regarding the respective merits of the Wilson, Lobo and Hottel empirical equation and the theoretical equation, the heat absorbed by the oil in the radiant section as predicted by these two equations has been compared to the actually observed heat absorption.

figure 9
figure 10

The radiant section will be defined as that section in which the heat is liberated and in which the heat transfer is primarily by radiation from the hot gas mass and the hot refractory surfaces. The cold or ultimate heat-receiving surface is considered to consist of those tubes which can "see" to a greater or less extent the main gas mass. This emphasis has been made because in the case of certain furnaces the first rows of tubes in the convection section can see the main gas mass. The plane area * of these tubes, Acp' must be considered as a part of the radiant section equivalent cold plane surface, aAcp' In furnaces where the convection section is placed behind a bridge wall, out of sight of the main gas mass, the projected area of the convection section is not considered to be part of the radiant section cold surface. <-- page 4 (part2) -- page 2 -->

 


 

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