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  Vapor-Liquid separator sizing ¹æ¹ý
  ±Û¾´ÀÌ : ¸ð¹ü»ý   °íÀ¯ID : mbsahg     ³¯Â¥ : 10-11-22 19:16     Á¶È¸ : 7053    

¾È³çÇϽʴϱî
¸Å¹ø ÀÎÅÍ³Ý È­ÇаøÇп¡¼­ µµ¿òÀ» ¹Þ°í ÀÖ´Â ¸ð¹ü»ýÀÔ´Ï´Ù.
»ó±â Á¦¸ñ°ú °ü·ÃÇÏ¿© ¼ö °è»êÀ¸·Î Vessel sizingÀ» ÇÏ´ø Áß ¸·È÷´Â ºÎºÐÀÌ ÀÖ¾î ÀÌ·¸°Ô ±ÛÀ» ¿Ã¸³´Ï´Ù.
Âü°íÀÚ·á´Â API 12J ÀÔ´Ï´Ù.
 

DESIGN CONDITION

Operating Temp. = 43¡É

Operating Press. = 12kg/cm2

Gas flow rare = 30kg/hr

Liquid flow rate = 1000kg/hr

Density of gas = 4kg/m3 =0.25lb/ft3

Density of liquid = 800kg/m3 =49.94lb/ft3

K-factor = 0.3

TL x TL = 8000mm

H(Liquid level)  =  20% =1600mm

 

CALCULATION

ù°, Max. allowable superficial velocity ±¸ÇÔ. 

Va = K[(dL-dG)/dG]^0.5

Va= Max. allowable superficial velocity(ft/s) 

K = Constant

dL = Liquid of density(lb/ft3)

dG = Gas of density(lb/ft3)

µû¶ó¼­  Va = 0.3{(49.94-0.25)/0.25}^0.5= 4.23ft/s =1.29m/s

 

 µÑ°, Min. gas flow area¸¦ ±¸ÇÔ.

A = Gas flowrate/ Max. allowable superficial velocity

= (30kg/hr)/(4kg/m3)/(1.29m/s) = 5.81m2

 

¼Â°, Min. ID of separator¸¦ ±¸ÇÔ.

D = (4*A/pi)^0.5 = {4*(5.81m2)/3.14}^0.5 = 2.72m

 

³Ý°, Liquid volume(excluding bottom head)À» ±¸ÇÔ.

VL = pi*D*H/4

 

´Ù¼¸Â°, Liquid capacity¸¦ ±¸ÇÔ.

W = 1440*(VL)/t/24

W= Liquid capacity (bbl/hr)

t = Retention time (min.)

µû¶ó¼­ W = 1440*(29.26bbl)/(1min)/24

        = 1755.4 bbl/hr = 11.63m3

 

Vessel size´Â ID 2720 x TL 8000À¸·Î °è»êµË´Ï´Ù.

¿©±â¼­ ±Ã±ÝÇÑ °ÍÀº Liquid capacityÀÇ Àǹ̴ ¹«¾ùÀ̸ç Áö±Ý °è»êÇÑ VesselÀº

Vertical typeÀε¥ Horizontal typeÀÏ ¶§´Â SizingÇÒ °æ¿ì ¾î¶² Á¡ÀÌ ¼öÁ¤µÇ¾î¾ß

ÇÏ´ÂÁö ±Ã±ÝÇÕ´Ï´Ù.

°í¼ö´ÔµéÀÇ ´äº¯ ºÎŹµå¸³´Ï´Ù.

 

 


Stefano    10-11-23 15:51
(1) Liquid Capacity´Â Liquid Volume Flow¸¦ ÀǹÌÇϴµ¥ Liquid Holding TimeÀÇ °æ¿ì¿¡µµ ¾×»ó¿¡ Æ÷ÇԵǾî ÀÖ´ø ±âÆ÷°¡ ±â»óÀ¸·Î ¸ðµÎ ¶°¿Ã¶ó ºÐ¸®µÉ ¼ö ÀÖ´Â Holding TimeÀ» À¯ÁöÇØ¾ß ÇÒ °ÍÀ̹ǷΠÀüü Separator Å©±â¸¦ °áÁ¤Çϴµ¥ ÇÊ¿äÇÑ µ¥ÀÌÅÍÀÔ´Ï´Ù.   

(2)Horizontal SeparatorÀÎ °æ¿ì °°Àº ¹æ¹ýÀ¸·Î ÇϵÇ,
Kh = 1.25 Kv¸¦ ÃëÇÏ°í
Varpor Space ºÎºÐÀÌ ÀüüÀÇ 20% ÀÌ»óÀÌ µÇµµ·Ï ÇÏ°í
L/D°ªÀÌ 3~5¹üÀ§¸¦ ÃÊ°úÇÏ¸é ´Ù½Ã °è»êÇÏ¿© °áÁ¤Çϵµ·Ï ÇÕ´Ï´Ù.

Âü°í: 
R.N. Watkins,  Sizing Separator and Accumulators, Hydrocarbon Processing Nov 1967
C.R. Branan ROT for Chem Engineers, GPC, 1994
¸ð¹ü»ý mbsahg   10-11-23 20:20
½ºÅ×Æijë´ÔÀÇ ´äº¯¿¡ °¨»çµå¸³´Ï´Ù.

´äº¯ 2)¿¡¼­ Kh = 1.25Kv´Â Vertical typeº¸´Ù ºÐ¸®ÀÇ È¿°ú°¡ ÁÁ±â¶§¹®¿¡ Kh°ªÀÌ Ä¿Áö´Â°ÍÀ¸·Î ÀÌÇØÇß½À´Ï´Ù.
Vapor Space ºÎºÐÀº Vertical Type¿¡¼­ ±¸ÇÑ ¹æ¹ýÀ¸·Î A_vapor = Gas flowrate/ Max. allowable superficial velocity°ª¿¡¼­ A_total_Min. = (A_vapor)/0.2À» °ªÀ¸·Î  ±¸ÇÏ´Â°Í °°½À´Ï´Ù.(Rule of Thumb for Chemical Engineers ÂüÁ¶) ¿©±â¼­ ¿ì¼± Horizontal typeÀÇ A_vapor°ªÀº Vapor¿Í LiqiudÀÇ ÃÖ¼Ò¸éÀûÀε¥ 20%ÀÇ °ªÀº Vessel¿¡¼­ Vapor°¡ Â÷ÁöÇÏ´Â ¸éÀûÀ» ÀǹÌÇÏ´Â°Í °°Àºµ¥ ¸éÀûÀ¸·Î A_total°ªÀÌ È¿¿ëÀÌ ÀÖ´ÂÁö ±Ã±ÝÇÕ´Ï´Ù.

±×¸®°í VesselÀÇ L/DÀÇ °ªÀÌ 3~5ÀÇ ¹üÀ§¿¡¼­ »ç¿ëÇϴµ¥ VesselÀÇ ¾Ð·Â¿¡ µû¶ó ¾Ð·ÂÀÏ Å¬¼ö·Ï °ªÀ» Å©°Ô °¡Áö¶ó´Â ¹®ÇåÀ» ¿¹Àü¿¡ º¸¾Ò´Âµ¥ ±× ÀÌÀ¯°¡ ÀûÇôÀÖÁö ¾Ê¾Ò½À´Ï´Ù. ±× ÀÌÀ¯¸¦ ¹«¾ùÀÎÁö ±Ã±ÝÇÕ´Ï´Ù.
½ºÅ×Æijë Stefano   10-11-23 22:38
(1) Kh=1.25 KvÀÇ Àǹ̴ Horizontal Separator´Â Vertical ¹æÇâÀ¸·Î ²ø¾î¿Ã¸®´Â È¿°ú(Upward Drag of the Vapor)°¡ Àû±â¶§¹®¿¡ Vertical º¸´Ù À¯¼ÓÀ» (´ë·«)25% Á¤µµ ´õ Å°¿öµµ ¹®Á¦ ¾ø´Ù´Â ¶æÀÔ´Ï´Ù. 

(2) Disengaging Space 20%
  Vapor°¡ Â÷ÁöÇÏ´Â ¸éÀûÀº ¹Ù·Î Vapor Space ºÎÇǸ¦ ¶æÇϴµ¥ Vapor Space 20% Á¤µµ´Â Liquid°¡ °¡µæ ä¿öÁ® ÀÖÀ» ¶§ ÃÖ¼ÒÇÑÀÇ Vapor °ø°£À» ÀǹÌÇÕ´Ï´Ù.  ÀÌ ¼öÄ¡´Â ¿ø·¡ Watkins ¾¾°¡ Á¦¾ÈÇÑ °ªÀÌÁö¿ä. ½ÇÁ¦·Î´Â Knock-Out DrumÀ¸·Î »ç¿ëµÇ´Â Vessel¿¡¼­ ±×¸® ¾×¸éÀÌ ³ô°Ô ¿îÀüµÇ´Â Separator´Â °ÅÀÇ ¾øÀ» °ÍÀÔ´Ï´Ù.  ´ë½Å, 20%°ø°£ÀÌ Vapor°ø°£À̶ó°í Çϸé Vertical Drumº¸´Ù´Â Horizontal DrumÀÌ È¿°úÀûÀ̶ó´Â Àǹ̸¦ ³»Æ÷ÇÕ´Ï´Ù 

(3) "5<L/D<3 ÀÎ °æ¿ì" ÀÌ´Â L/D<3 À̰ųª  L/D>5ÀÎ °æ¿ì¸¦ Çѹø¿¡ ³ªÅ¸³½ °ÍÀε¥  ÀÌ´Â ¼öÇÐÀû ¼ö½ÄÀ¸·Î´Â ¼º¸³ÇÒ ¼ö ¾ø´Â Ʋ¸° Ç¥ÇöÀÔ´Ï´Ù.  ÀÌ ¹üÁÖ¸¦ ¹þ¾î³ª¸é, Áï ³Ê¹« ¶×¶×Çصµ ³Ê¹« ȦÂßÇصµ "(°æÁ¦¼º, È¿À²¼º ¸é¿¡¼­) º°·Î È¿°úÀûÀÌÁö ¸øÇÏ´Ù"´Â °ÍÀ» ÀǹÌÇÕ´Ï´Ù.  ¾Ð·ÂÀÌ ³ôÀ¸¸é L/D°ªÀ» Å©°ÔÇÏ´Â °ÍÀÌ À¯¸®ÇÏÁö¸¸ ÀúÀå¿ë·®À» Á¤Çصΰí ÀåÄ¡Á¦ÀÛºñ¿ë¸¸ µûÁ³À» ¶§ ±×·¸´Ù´Â À̾߱âÀÌ°í ±â-¾×ºÐ¸®±âó·³ °¢°¢ÀÇ È¥ÇÕ»ó¿¡¼­ "Settling È¿°ú"¸¦ ³íÇÏ´Â °æ¿ì¿Í´Â ´Ù¸¨´Ï´Ù. 

½ºÆ÷Ã÷ Á¾¸ñÀÇ °æ¿ì¿¡µµ ´Þ¸®±â ¼±¼ö¿Í ¿ªµµ¼±¼ö´Â üÇüÀÌ ÀüÇô ´Ù¸£´Ù´Â °ÍÀ» ¿¬»óÇØ º¸¸é ÀÌÇØ°¡ µÉ °ÍÀÔ´Ï´Ù.
   

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