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  Line Hydraulic°ü·Ã Áú¹®µå¸³´Ï´Ù.
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Line Hydraulic ½ºÅ͵ð Áß Two-phase Flow¿¡ °ü·ÃÇÏ¿© ±Ã±ÝÇÑ°Ô ÀÖ¾î Áú¹® µå¸³´Ï´Ù.
 
<HTFS Method>
ÇöÀç Homogeneous¸¦ °¡Á¤ÇÑ Duckler Method¸¦ °øºÎÇÏ°í ³ª¼­, Separted Flow ModelÀ» °øºÎÇÏ´ø Áß, HTFS°¡ °¡Àå ¿ÀÂ÷°¡ Àû´Ù´Â °ÍÀ» ¾Ë°Ô µÇ¾ú´Âµ¥¿ä. ÀúÈñ ȸ»ç¿¡¼­µµ Excel ÅøÀ» ÀÌ¿ëÇÏ¿© HTFS·Î Line SizingÀ» ÇÏ°í ÀÖ½À´Ï´Ù. ±×·±µ¥ ÀÌ°Í¿¡ Method¿¡ °ü·ÃµÈ ÀÌ·ÐÀûÀÎ Áö½ÄÀ» ¾Ë°í ½Í¾î¼­ µµ¿ò ¿äû µå¸³´Ï´Ù.
 
±âÁ¸ Áú¹®µé Áß¿¡ ºñ½ÁÇÑ °ÍÀÌ ÀÖ¾ú´Âµ¥ Wolverine TubeÞä¿¡¼­ ³ª¿Â Enginnering Data Book 3ÀÇ Ã©ÅÍ 13À» ¿­½ÉÈ÷ º¸¾ÒÁö¸¸ HTFSÀÇ ÀÌ·ÐÀûÀÎ Á¢±ÙÀÌ Àß µÇÁö ¾Ê½À´Ï´Ù... ±¸±Û °Ë»öÀ» ÅëÇؼ­µµ Àß ³ª¿ÀÁö ¾Ê¾Æ Ȥ½Ã µµ¿òÀ» Áֽøé Á¤¸» °¨»çÇÏ°Ú½À´Ï´Ù.
 
¿À´Ãµµ ÁÁÀºÇÏ·ç µÇ¼¼¿ä!

½ºÅ×Æijë Stefano   15-01-02 15:34
(1) HTFS¶ó´Â ¿­±³È¯±â ¼³°èÇÁ·Î±×·¥ÀÌ ¾î¶² ¹æ¹ýÀÇ Two-phase Flow Press DropÀ» »ç¿ëÇÏ´ÂÁö ¸ÕÀú ¾Ë¾Æº¼ ÇÊ¿ä°¡ ÀÖ½À´Ï´Ù.
ÃßÃøÄÁµ¥ HTFS ÇÁ·Î±×·¥ ³»¿¡ ¿©·¯ ¹æ¹ýÀ» ³»ÀåÇÏ°í ÀÖ°í ¼³°èÇÁ·Î±×·¥ »ç¿ëÀÚ°¡ ¼±ÅÃÇÏ¿© »ç¿ëÇÒ ¼ö ÀÖµµ·Ï µÇ¾î ÀÖÀ» °ÍÀ¸·Î º¾´Ï´Ù.

ÀÌ°÷(http://lhd52.files.wordpress.com/2011/09/group-3-pipe-segment.pdf,  p.5-20)¿¡´Â 14°³ÀÇ ¹æ¹ýÁß¿¡¼­ ¼±ÅÃÇϵµ·Ï µÇ¾î ÀÖ°í, ÀÌÁß HTFS´Â Homogeneous Model ȤÀº Liquid Slip ModelÀ» »ç¿ëÇÏ´Â °ÍÀ̳ª ÀÌµé ¹æ¹ýÀÇ ¿øõÀº ÀüÀÚ´Â Claxton (1972)ÀÇ The frictional pressure gradient method¿¡ÀÇÇÑ ¹æ¹ý, ÈÄÀÚ´Â Whalley¿Í Ward (1981)¿¡ ÀÇÇÑ Voild Fraction °ü°è½ÄÀ» ÀÌ¿ëÇÑ Liquid Slip ModelÀ̶ó°í ¼³¸íÇÏ°í ÀÖ½À´Ï´Ù 

(¹®Á¦´Â ¾î´À ¸ðµ¨¼ö½Äµµ +/- 25~50%Á¤µµÀÇ ¿ÀÂ÷¸¦ °¡Áö°í ÀÖ´Ù°í ÇϹǷΠÁÖÀÇÇØ¾ß ÇÑ´Ù°í ÇÕ´Ï´Ù.)

(2) Two-Phase Pressure Drop°ú °ü·ÃÇÏ¿© Àß ¿ä¾àµÈ °÷Àº ¿¹Àü¿¡µµ ¼Ò°³Çß¾ú°í Áú¹«ÀÚµµ ÀοëÇÑ  Wolverine TubeÞä¿¡¼­ ³ª¿Â Enginnering Data Book 3ÀÇ Ã©ÅÍ 13 ( http://ocw.kfupm.edu.sa/ocw_courses/user061/ME43701/Lecture%20Notes/db3ch13.pdf )¿¡ Àß ¿ä¾àµÇ¾î ÀÖ½À´Ï´Ù. 

(3) ¸¹ÀÌ »ç¿ëµÇ´Â Two-Phase Pressure Drop °è»ê ¹æ¹ýµé

i) Homegeneous Flow Model (±â-¾×ÀÇ ¼Óµµ°¡ µ¿ÀÏÇÏ°í ±ÕÀÏÇÏ°Ô ¼¯¿©È帥´Ù°í °¡Á¤ÇÑ ¸ðµ¨) - Duckler (??)
ii) Separated Flow Model-Two-Phase Multiplir¹ý (Liquid Flow Pressure Drop¿¡ ½Â¼ö °öÇÏ¿© °è»ê - Friedel (1979) 
iii) Separated Flow Model-Two-Phase Multiplier¹ý (Liquid ȤÀº Vapor Flow Pressure Drop¿¡ ½Â¼ö °öÇÏ¿© °è»ê)-Lockhart and Martinelli (1949)
iv) Separated Flow Model-Two-Phase Multiplier¹ý (Liquid Flow Pressure Drop¿¡ ½Â¼ö °öÇÏ¿© °è»ê)-Chisholm-Blasius Method (1973)
v) Homogeneous Liquid Model¿¡ Two-Phase Multiplier °ö¼À¹ý(±ÕÀÏ ¾×»ó Â÷¾Ð¿¡ Two-Phase ½Â¼ö °öÇÏ¿© °è»ê)-Bankoff (1960)
vi) Homogeneous Vapor Model¿¡ Two-Phase Multiplier °ö¼À¹ý(±ÕÀÏ ±â»ó Â÷¾Ð¿¡ Two-Phase ½Â¼ö °öÇÏ¿© °è»ê)-Chawla (1960)
vii) Separated Flow Model-Two-Phase Frictional Gradient ¹ý(Chisholm¹ý¿¡ ¾×»óÂ÷¾Ð°è¼ö, ±â»óÂ÷¾Ð°è¼ö¸¦ °öÇÏ¿© Á¶ÇÕ)-Mueller-Steinhagen & Heck(1986)

¸Ç ¸¶Á÷¸· ¹æ¹ýÀº ÀڽŵéÀÇ ¹æ¹ýÀÌ °¡Àå Àß µé¾î¸Â´Â´Ù°í ÁÖÀåÇÏ°í ÀÖ°í

http://www.eurotherm2008.tue.nl/Proceedings_Eurotherm2008/papers/Two-phase_Flow/TPF_10.pdf ¿¡¼­µµ ¾ð±ÞÇÏ°í ÀÖ´Â HTFS ¹ýÀ̶ó°í °ÍÀÌ °ú¿¬ ¹«¾ùÀÎÁö ÀÚ¼¼È÷´Â ¾Ë¼ö ¾øÁö¸¸  °è»ê¿¡ »ç¿ëÇÑ "Void Fraction"À̳ª "Vapor Fraction"ÀÇ ¹üÀ§°¡ °ú¿¬ ¾î´À Á¤µµÀÎÁö ¾Ë¾Æº¼ ÇÊ¿ä°¡ ÀÖ½À´Ï´Ù. 

(4) °á·ÐÀûÀ¸·Î..
°¢Á¾ Flow Pattern¿¡¼­ Àý´ëÀû Àß ¸Â´Â Two-Phase Pressure Drop Calculation ¹æ¹ýÀ̶ó´Â °ÍÀº ¾ÆÁ÷ Á¸ÀçÇÏÁö ¾Ê´Â´Ù°í º¾´Ï´Ù.  (Wolverrine Tube Inc.ÀÇ Engg. Data Book III p. 13-4 ÂüÁ¶)
Ź֠taming   15-01-05 16:02
Á¤¸» °¨»çÇÕ´Ï´Ù ½ºÅ×Æijë´Ô
°øÁ¤¼³°è¿¡¼­ °¡Àå Áß¿äÇÑ °ÍÀº À̷аú °æÇè¿¡ ÀÇÇÑ Model ¼±Á¤À̶ó°í ¾Ë°í Àִµ¥,
¾ÆÁ÷ ¸¹ÀÌ ºÎÁ·ÇÏ¿© ÀÌ·Ð °øºÎ¸¦ ÇÏ´Â Áß¿¡ µµ¿òÀÌ ¸¹ÀÌ µÇ¾ú½À´Ï´Ù.
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