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  ¿­±³È¯±â ³»¿¡¼­ À¯Ã¼ ¼Óµµ ±¸Çϱâ
  ±Û¾´ÀÌ : ´Þ³ª¶ó´ëÀå   °íÀ¯ID : precede3     ³¯Â¥ : 12-04-13 16:38     Á¶È¸ : 5750    
¿­±³È¯±â(shell&tube) ³»¿¡¼­ tube side¿Í shell sideÀÇ À¯Ã¼ÀÇ ¼Óµµ¸¦ ±¸ÇÏ°íÀÚ ÇÕ´Ï´Ù.
 
À¯Ã¼ÀÇ ¼Óµµ¸¦ °¡Áö°í, pressure dropµµ ±¸ÇÏ°í, ´Ù¸¥½Ä¿¡µµ ¼Óµµ°¡ ÇÊ¿äÇؼ­ ±¸ÇÏ°íÀÚ ÇÕ´Ï´Ù.
 
Áö±Ý Àú´Â Q=AVÀÇ ½ÄÀ» °¡Áö°í ´Ü¼øÈ÷ °è»êÀ» ÇÏ°í Àִµ¥, tube side¿¡¼­ÀÇ,
Q = volume flow rate (10.28 m3/hr)
A = surface area (0.066m2)ÀÌ ³ª¿Ô½À´Ï´Ù.
 
1" tube , 130°³°¡ ÀÖ´Ù°í Çؼ­ = (PI()*0.0254^2/4)*130 ÀÌ·¸°Ô Çߴµ¥, tubeÀÇ ´Ü¸éÀûÀº ÀÌ·¸°Ô ±¸Çϴ°ÍÀÌ ¾Æ´Ñ°¡¿ä?
 
±×¸®°í shellÀÇ ´Ü¸éÀûÀº shell diameter°¡ 0.49m ¶ó¼­, ¾Æ·¡¿Í °°ÀÌ shellÀÇ ´Ü¸éÀû¿¡¼­ tube´Ü¸éÀûÀ» »©ÁÖ¾ú´Âµ¥,
(PI()*0.49^2/4) - (PI()*0.0254^2/4)*130 = 0.122m2
 
¼Óµµ°¡
tube side : 0.04m/s
shell side : 0.02m/s
 
·Î ³ª¿Ô½À´Ï´Ù.
¼Óµµ°¡ ³Ê¹« ÀÛÀº°ÍÀÌ ¾Æ´Ñ°¡ Çؼ­¿ä.
 
Àоî Áּż­ °¨»çÇÕ´Ï´Ù.
 

½ºÅ×Æijë Stefano   12-04-16 23:03
1" Tube´Â ¿Ü°æÀÌ Á¤È®È÷ 1"°¡ µË´Ï´Ù.  ³»°æÀ» ã¾Æ¼­ °è»êÇØ º¸¼¼¿ä. ³»°æÀº Æ©ºêµÎ²²(BWG)¿¡ µû¶ó ´Þ¶óÁöÁö¿ä.
     
´Þ³ª¶ó´ëÀå precede3   12-04-18 09:52
¿¹~! °¨»çÇÕ´Ï´Ù. ³»°æÀÌ 0.87"À¸·Î °è»êÀ» ÇÏ´Ï 0.06 m/s °¡ ³ª¿É´Ï´Ù.
±×¸®µµ ³Ê¹« ÀÛÀº°Å °°³×¿ä..

shellÀÇ ´Ü¸éÀûÀº À§¿Í °°ÀÌ ±¸Çϴ°ÍÀÌ ¹æ¹ýÀΰ¡¿ä?
jslee jslee   12-04-18 04:27
»óº¯È­°¡ ¾ø´Ù¸é, ¿­Àü´Þ Ãø¸é¿¡¼­ ¼Óµµ°¡ ³Ê¹« ³·ÀºÁö´Â Reynolds number·Î ÆÇ´ÜÇÏ½Ã¸é ´õ ÁÁÀ» °Í °°½À´Ï´Ù.
(turbulent flowÀÎÁö ¿©ºÎ¸¦ º¸¸ç, laminar flowÀÏ °æ¿ì tubeÃøÀº ¿­Àü´ÞÈ¿À²ÀÌ ±Þ°ÝÈ÷ ¶³¾îÁü)
     
´Þ³ª¶ó´ëÀå precede3   12-04-18 09:56
´äº¯ °¨»çÇÕ´Ï´Ù~!

¾î¶² ¹®Çå¿¡ º¸´Ï tube passes ¸¦ ¼±Á¤ÇÒ¶§ Reynolds # ¸¦ 10000ÀÌ»óÀÌ µÇ°Ô²û Çؼ­ ¼³Á¤À» Ç϶ó´Â ½ÄÀ» ã¾Æ¼­ ±× ½ÄÀ¸·Î Çß½À´Ï´Ù.

±×·¡¼­ tube passes¸¦ 4·Î ¼±ÅÃÀ» Çß±¸¿ä.

Re = (4*m*Np) / (pi*Di*Nt*Á¡µµ) > 10000 ÀÌ ½ÄÀÌ¿´½À´Ï´Ù.

tube passes°¡ ´Ü¸éÀû°úÀÇ »ó°ü°ü°è°¡ ¾î¶»°Ô µÇ´ÂÁö¿ä...

          
jslee jslee   12-04-25 09:20
Tube pass ¼ö°¡ Áõ°¡ÇÏ¸é µ¿ÀÏ shell ID¿¡¼­ À¯Ã¼°¡ Áö³ª°¡´Â À¯·Î(tubes)ÀÇ ÃѴܸéÀû(tube´Ü¸éÀû*tube°¹¼ö)ÀÌ ±×¿¡ ¹Ýºñ·ÊÇØ °¨¼ÒÇÏ°Ô µË´Ï´Ù. Áï 100°³ÀÇ tube°¡ 1 pass·Î ¼³Ä¡µÇ¾î ÀÖ´Ù°¡ 2 pass°¡ µÇ¸é À¯Ã¼°¡ Áö³ª°¡´Â ÃÑ ´Ü¸éÀûÀº ¹ÝÀ¸·Î ÁÙ°Ô µË´Ï´Ù.

±×¸®°í, [ºÎÇÇÀ¯·®/´Ü¸éÀû=¼±¼Óµµ]À̹ǷΠ´Ü¸éÀûÀÌ Àý¹ÝÀ¸·Î ÁÙ¸é ¼±¼Óµµ´Â 2¹è°¡ µÇ°í, ±×¿¡ µû¶ó Reynolds #µµ µÎ¹è·Î Áõ°¡ÇÕ´Ï´Ù (Re = D*rho*v/mu). TubeÃø¿¡¼­ turbulent flow°¡ µÇ¾î¾ß ¿­Àü´ÞÈ¿À²ÀÌ ±Ø´ëÈ­µÇ¹Ç·Î, pass ¼ö¸¦ ´Ã¸²À¸·Î½á turbulent flow·Î ¸¸µå´Â °ÍÀÌ °¡´ÉÇÕ´Ï´Ù.

´Ü, ÁÖÀÇÇÒ Á¡Àº tube pass Áõ°¡½Ãų ¶§ tubeÃøÀÇ ¾Ð·Â°­Çϵµ Å©°Ô Áõ°¡ÇÑ´Ù´Â Á¡ÀÔ´Ï´Ù. TubeÃø ¾Ð·Â°­ÇÏ´Â ¼±¼ÓµµÀÇ Á¦°ö¿¡ ºñ·ÊÇÏ°í ¶Ç À¯Ã¼ÀÇ °æ·Î±æÀÌ¿¡µµ ºñ·ÊÇÕ´Ï´Ù. À§ÀÇ ¿¹¿¡¼­ pass¸¦ 1->2·Î Áõ°¡½Ã ¼±¼Óµµ°¡ 2¹è, °æ·Î±æÀ̵µ 2¹è·Î Áõ°¡ÇϹǷÎ, °á±¹ ¾Ð·Â°­ÇÏ´Â ±âÁ¸ÀÇ 8¹è·Î Áõ°¡ÇÏ°Ô µË´Ï´Ù.

Àúµµ ±â¾ïÀÌ °¡¹°°¡¹°Çؼ­ ÀÚ·á Á» ã¾Æº¸´À¶ó ´äº¯ÀÌ ´Ê¾ú³×¿ä. ÀÛÀº µµ¿òÀÌ¶óµµ µÇ¾úÀ¸¸é ÇÕ´Ï´Ù.
(Âü°íÀÚ·á: Lieberman, "Process Engineering for a Small Planet")
               
´Þ³ª¶ó´ëÀå precede3   12-04-26 18:15
´äº¯ °¨»çÇÕ´Ï´Ù^^ Á¤¸» ¸¹Àº µµ¿òÀÌ µÇ°íÀ־ °¨»çÇÕ´Ï´Ù~!

Á¦°¡ °á·ÐÀûÀ¸·Î ±¸ÇÏ°íÀÚ Çϴ°ÍÀº nozzleÀÇ sizeÀÔ´Ï´Ù~!
(Applied process design, vol 3, third edition P.111 ÀÇ fig 10.64¸¦ º¸°í ÀÖ½À´Ï´Ù.)

http://books.google.co.kr/books?id=T69gFnVmK4MC&printsec=frontcover&dq=Applied+Process+Design+for+Chemical+and+Petrochemical+Plants&hl=ko&sa=X&ei=HRGZT7_lNKrAiQeW3J2QBg&ved=0CDMQ6AEwAA#v=onepage&q=Applied%20Process%20Design%20for%20Chemical%20and%20Petrochemical%20Plants&f=false

ÀÌ ±×·¡ÇÁ¸¦ ÅëÇؼ­ nozzle size¸¦ ±¸Çϴ°ÍÀÌ ¾î´ÀÁ¤µµ ÇÕ´çÇÑ°¡¿ä?
Á¦ °è»ê¿¡ µû¸£¸é, shell ID °¡ 16.5in Àε¥, Ã¥À» ÅëÇؼ­ ±¸ÇÑ tube ÂÊ nozzle size°¡  6in °¡ ³ª¿É´Ï´Ù~!

³Ê¹« Å«°Í °°¾Æ¼­¿ä...

±×·³ °¨»çÇÕ´Ï´Ù~!
                    
jslee jslee   12-04-30 10:58
¸µÅ©ÀÇ Ã¥Ã³·³ ³ëÁñÅ©±â¸¦ ¼ÕÀ¸·Î °è»êÇغ¸Áö ¾Ê¾Æ¼­ ÇÕ´çÇÑ ¹æ¹ýÀÎÁö´Â ¸ð¸£°Ú½À´Ï´Ù¸¸,
³ëÁñ·ÎÀÇ ÃÖ´ëÀ¯¼ÓÇѰ踦 ±Ù°Å·Î ¸¸µç ±×·¡ÇÁ¶ó¸é ±âÁØÀ¸·Î »ïÀ» ¼ö ÀÖ°ÚÁö¿ä.
´Ù¸¸ »óÇÑ°ª¸¸ Á¦½ÃÇØÁÖ´Â °ÍÀ¸·Î º¸À̹ǷΠ¥ÄP°¡ Çã¿ëµÇ´Â ¹üÀ§ ³»¿¡¼­ ÁÙÀÏ ¼ö ÀÖÀ» °Í °°½À´Ï´Ù.
                         
´Þ³ª¶ó´ëÀå precede3   12-05-02 10:01
¿¹~! ´äº¯ Á¤¸» °¨»çÇÕ´Ï´Ù.
   

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