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  ¿­±³È¯±â Shell Side Sizing ¹æ¹ýÁ» ºÎŹ µå·Á¿ä~
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Àü¿­¸éÀûÀº 5.2 m2, LMTD 44 µµ¾¾, ³Ã°¢¼ö À¯·® 1 m/s, Tube ¼ö 36°³ ÀÔ´Ï´Ù.
Tube O.D´Â 3/4 in À̱¸¿ä.

½ºÅ×Æijë Stefano   12-09-06 14:05
E. LudwigÀÇ APD(Applied Process Design for Chemical and Petrochemical Engineers) ³ª D.Q.KernÀÇ Process Heat Transfer¸¦ ã¾Æº¸¸é ¼ö°è»ê¿¡ ÀÇÇÑ ÀÚ¼¼ÇÑ ¼³°è¹æ¹ýÀÌ ¿¹Á¦¿Í ÇÔ²² ¼³¸íµÇ¾î ÀÖ½À´Ï´Ù. 

ShellÀÇ Inside Diameter¸¦ ÃßÁ¤ÇÏ´Â °è»ê ¹æ¹ýÀÇ ÇϳªÀÇ ¿¹¸¦ µé¸é ÀÌ°÷¿¡¼­ ã¾Æº¼ ¼ö ÀÖ½À´Ï´Ù.
Á÷Á¢ Çغ¸¼¼¿ä.
http://www.scribd.com/doc/52651083/Estimation-of-tubular-HE-internal-shell-diameter
   

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