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  downcomer ¼±Á¤
  ±Û¾´ÀÌ : ¸ÚÁø±×´ë   °íÀ¯ID : rhkdskdbsp     ³¯Â¥ : 13-05-08 15:34     Á¶È¸ : 5343    
column internal ¼³°è¸¦ °øºÎÇÏ°í ÀÖ½À´Ï´Ù.

½ºÅ×Æijë´ÔÀÌ ¿©·¯¹ø ÃßõÇϽŠ¼­Àû Kister ÀÇ "distillation design"¿¡ column sizing ÇÏ´Â ³»¿ëÀÌ ÀÖ½À´Ï´Ù.
¹®Á¦Ç®À̸¦ ÅëÇØ sizing À» º¸¿©ÁÖ°í Àִµ¥,
¿©±â¼­ p341 downcomer layout (Chapter 6. Tray Design and Operation) ¼³¸í¿¡ ´ëÇØ Çò°¥¸®´Â ºÎºÐÀÌ ÀÖ¾î Áú¹®µå¸³´Ï´Ù.
    - top section ºÎºÐÀº 1 pass tray, bottom section ºÎºÐÀº 2 pass tray¸¦ ¼±Á¤ÇÏ¿´½À´Ï´Ù.

[ top sectionÀº downcomer top area ¿Í bottom area °¡ °°Áö¸¸, bottom sectionÀº downcomer top area¿Í bottom area °¡ ´Ù¸¨´Ï´Ù.  Ã¥ º»¹®¿¡´Â 'There is an incentive to reduce this area by using a sloped downcomer. A 2:1 top-to-bottom area ratio is appropriate (1).' (p341 downcomer layout ºÎºÐ 6¹ø° ÁÙ) ¶ó°í ¼³¸íÀÌ µÇ¾îÀÖ½À´Ï´Ù. ]

ÀÌ ºÎºÐ¿¡¼­ ÀÌÇØ°¡ °¡Áö ¾Ê¾Æ Áú¹®µå¸³´Ï´Ù. 

Q1. top section ÀÇ downcomer top/bottom area °¡ °°Àº ÀÌÀ¯¿Í bottom section ÀÇ downcomer top/bottom area °¡ ´Ù¸¥ ÀÌÀ¯°¡ ¹«¾ùÀԴϱî?
Q2. bottom section ÀÇ downcomer area°¡ ´Ù¸¦ ¶§, 2:1 ratio¸¦ Àû¿ëÇÏ´Â ±âÁØÀÌ ¹«¾ùÀԴϱî? 
Q3. slope downcomer¸¦ Àû¿ëÇÒ ¶§ ÀϹÝÀûÀ¸·Îµµ 2:1 ·Î¸¸ downcomer area ratio¸¦ ¼±Á¤ÇÏ´Â °ÍÀԴϱî? ¾Æ´Ï¸é ´Ù¸¥ Àû¿ë±âÁØÀÌ ÀÖ³ª¿ä?

´ä±Û ±â´Ù¸®°Ú½À´Ï´Ù. °¨»çÇÕ´Ï´Ù. 

½ºÅ×Æijë Stefano   13-05-08 19:25
(0) Downcomer´Â ±â-¾× Á¢ÃËÀ» À§ÇÑ ¸ñÀûÀ¸·Î »ç¿ëµÇ´Â °ÍÀÌ ¾Æ´Ï°í À­´Ü¿¡¼­ ±â-¾× ÆòÇüÀ» "¾î´À Á¤µµ" ÀÌ·ç°í ÇÏ´ÜÀ¸·Î¾×À» ³»·Áº¸³»´Â ±â´ÉÀ» °¡Áö´Âµ¥

(1)¿¹Á¦ÀÇ °æ¿ì Top Tray¿¡¼­´Â Liquid¿Í VaporÀÇ À¯·®ÀÌ À۾Ƽ­ 1 pass·Î °¡´ÉÇÏ°í Tray¸éÀûµµ ÃæºÐÇÏ¿© ±»ÀÌ Top Area¿Í Bottom Area¸¦ ´Ù¸£°Ô ¸¸µéÀÌÀ¯°¡ ¾ø´Â °æ¿ì¿¡ ÇØ´çÇÕ´Ï´Ù . ÀÌ´Â Áú¹® Q1¿¡¼­ °°Àº ÀÌÀ¯¿¡ ÇØ´çÇÏ°í ´Ù¸¥ ÀÌÀ¯¶ó¸é Tray ¸éÀûÀ» Downcomer·Î »ç¿ëÇϴµ¥ ´ú ÇÒ¾ÖÇØ¾ß ColumnÀÇ Á÷°æÀÌ ÀÛ¾ÆÁö±â ¶§¹®ÀÔ´Ï´Ù.

(2) Q2¿¡¼­ 2:1ÀÌ ¹ÝµåÀÌ µÇ¾î¾ß ÇÏ´Â ÀÌÀ¯´Â ¾ø½À´Ï´Ù.  ´Ù¸¸ ¸éÀûÀÌ ´Ù¸¥ ÀÌÀ¯¶ó¸é  DowncomerÀÇ »óºÎ¿Í ÇϺÎÀÇ È帧ÇüÅ°¡ ´Ù¸£±â ¶§¹®ÀÔ´Ï´Ù.  Top ºÎºÐÀº BubbleÀÌ ¸¹ÀÌ ¼¯¿©À־ ¹Ðµµ°¡ ³·¾Æ ºÎÇÇÀ¯·®ÀÌ »ó´ëÀûÀ¸·Î Å©°í BottomºÎºÐ¿¡´Â Bubble Æ÷ÇÔ·®ÀÌ °ÅÀÇ ¾øÀÌ È帣±â ¶§¹®¿¡ È帧Åë·Î°¡ Á¼¾ÆÁ®µµ È帧¿¡ Å«ÁöÀåÀÌ ¾øÀ¸³ª Top ºÎºÐÀº À¯¼ÓÀÌ ³·¾Æ¾ß Vapor-LiquidÀÇ ºÐ¸®°¡ ¿ëÀÌÇϱ⠶§¹®¿¡ ¸éÀûÀ» ´Þ¸®ÇÏ´Â °ÍÀÌ ÁÁ±â ¶§¹®¿¡ Tray Tower ¿¡¼­ ½ÇÁ¦·Î ÀÌ ¹æ¹ýÀÌ Á¦ÀÛÇ¥ÁØÀ¸·Î Á¤ÂøµÈ ¸éÀÌ ÀÖ½À´Ï´Ù.
 
(3) Top Face¿Í Bottom Face´Ü¸é¿¡¼­ÀÇ ºñ°¡ 2:1Àº Typical Value¶ó´Â °ÍÀÏ»Ó ´Ù¸¥ Reference¿¡¼­´Â ÀüÇô ´Ù¸¥ °ªÀ» »ç¿ëÇÏ°í ÀÖ½À´Ï´Ù.  µû¶ó¼­ Å« Àǹ̸¦ °¡Áö´Â °ÍÀº ¾Æ´Õ´Ï´Ù .

<ÂüÁ¶>
https://www.google.com/webhp?hl=ko&tab=mw#hl=ko&sclient=psy-ab&q=%22Downcomer+Area+Ratio%22&oq=%22Downcomer+Area+Ratio%22&gs_l=hp.3...10067.11594.2.11782.3.3.0.0.0.0.143.278.0j2.2.0...0.0...1c.1.12.psy-ab.848RaUIHBWQ&pbx=1&bav=on.2,or.r_qf.&bvm=bv.46226182,d.dGI&fp=ebbd3b77881672c7&biw=1240&bih=923
     
¸ÚÁø±×´ë rhkdskdbsp   13-05-09 09:38
´äº¯ °¨»çÇÕ´Ï´Ù.
Top ºÎºÐ¿¡ bubbleÀÌ ¸¹ÀÌ Çü¼ºµÇ±â ¶§¹®¿¡ ¿øÈ°ÇÑ È帧À» À§ÇØ downcomer area°¡ Ä¿¾ß ÇÑ´Ù´Â ¶æÀ̱º¿ä.

Ãß°¡ Áú¹®ÀÔ´Ï´Ù.

1) Á¦ÀÛÇ¥ÁØÀ¸·Î Á¤ÂøµÇ¾ú´Ù´Â ¶æÀº °ü·ÊÀûÀ¸·Î ȸ»ç¿¡¼­ ±×·¸°Ô »ç¿ëÇÑ´Ù´Â ÀǹÌÀΰ¡¿ä?

2) downcomer area ratio ¸¦ ±¸Çϱâ À§Çؼ­´Â
ÂüÁ¶ÁֽŠ»çÀÌÆ®¸¦ °Ë»öÇغ¸´Ï "Fortran: Programs for Chemical Process Design, Analysis, and Simulation" Ã¥°ú°ú "Ludwig's Applied Process Design for Chemical and Petrochemical Plants" Ã¥À» ãÀ» ¼ö ÀÖ¾ú½À´Ï´Ù. ¿©±â¼­ °øÅëÀûÀ¸·Î downcomer area ratio ±¸ÇÏ´Â ¹æ¹ýÀÌ Á¦½Ã µÇ¾îÀֳ׿ä.

      2-1). Ludwig Ã¥ p251 ¿¡ º¸¸é downcomer area ratio = (Adc)/(2(Adc)+(Ab)) ·Î Á¦½ÃµÇ¾î ÀÖ°í, TableÀ» Âü°í                      Çؼ­ ±¸ÇÏ´Â ¹æ¹ýµµ Á¦½ÃµÇ¾î ÀÖ½À´Ï´Ù. ÀÌ µÎ°¡Áö ¹æ¹ýÀ» ¸ðµÎ »ç¿ëÇÏ´Â °ÍÀΰ¡¿ä?
      2-2). ¶ÇÇÑ Multipass ¿¡µµ Àû¿ëÇÒ ¼ö ÀÖ´Â ¹æ¹ýÀÎÁö ±Ã±ÝÇÕ´Ï´Ù.
      2-3). ¿©±â¿¡ ³ª¿Â ±ÛÀ» º¸¸é downcomer area ratio = Ad/At ¶ó°í »ý°¢ÇÒ ¼ö Àִµ¥ ÀÌ°Ô Á¤È®È÷ ¾î¶² ÀǹÌÀÎÁö
              ¸ð¸£°Ú½À´Ï´Ù. ¾î¶»°Ô ÀÌ·± µîÈ£°¡ ¼º¸³µÉ ¼ö ÀÖ´ÂÁö ¾Ë°í ½Í½À´Ï´Ù.

 [ Adc : downcomer area
    Ab : À̺κÐÀº ãÀ» ¼ö°¡ ¾ø¾î¼­ Á¤È®ÇÏÁö´Â ¾ÊÁö¸¸ bubbling area °¡ ¾Æ´Ò±î ÃßÁ¤ÇÕ´Ï´Ù.
    At : total area ]
   

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