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  ºÐ¸®°øÁ¤¿¡¼­ ȸºÐÁõ·ù¿¡ °üÇÑ Áú¹®ÀÔ´Ï´Ù.
  ±Û¾´ÀÌ : ¸¸Ã¶   °íÀ¯ID : kmcgogo     ³¯Â¥ : 07-11-26 00:32     Á¶È¸ : 6227    
ȸºÐÁõ·ù¿¡ °üÇÑ ºÎºÐ¿¡¼­ ¹®Á¦¸¦ Ç®´Ù ¸·È÷´Â ºÎºÐÀÌ À־ ÀÌ·¸°Ô Áú¹®À» µå¸³´Ï´Ù.
 
¸ÕÀú ¹®Á¦¸¦ ¾Ë·Áµå¸®¸é,
 
- ÃÑ 25¸ôÀÇ È¥ÇÕ¹° Áß¿¡¼­ ¸ôºÐÀ²ÀÌ 0.35ÀÎ º¥Á¨°ú Åç·ç¿£ÀÇ È¥ÇÕ¹°À» Áõ·ù°ü¿¡ ÃæÀüÇÏ¿´´Ù. °°Àº Á¶¼ºÀ» °¡Áø °ø±Þ¹°À» 7mol/h·Î °ø±ÞÇÏ°í ¿­°ø±Þ ¼Óµµ¸¦ Á¶ÀýÇÏ¿© Áõ·ù°üÀÇ ¾×ü ³ôÀ̸¦ °°°Ô À¯ÁöÇÏ¿´´Ù. ¾Æ¹«·± ¾×üµµ Áõ·ù°üÀ» ¶°³ªÁö ¾ÊÀ¸¸ç ¥á = 2.5 ÀÌ´Ù. Áõ·ù¹° Á¶¼ºÀÌ º¥Á¨ 0.45 ¸ôºÐÀ²·Î ¶³¾îÁú ¶§±îÁö ½Ã°£ÀÌ ¾ó¸¶³ª °É¸±±î?
 
 
ȸºÐÁõ·ù¸¦ °øºÎÇϸ鼭, feedµµ ¾ø´Â ¹ÌºÐ½Ä Áõ·ù¸¸À» ¹è¿ü´Âµ¥ ÀÌ°°Àº ÀÀ¿ë ¹®Á¦¸¦ Á¢ÇÏ°Ô µÇ´Ï
¿©·¯¹æ¸éÀ¸·Î »ý°¢À» Çغôµ¥ ¸¹ÀÌ ³­ÇØÇÏ´õ±º¿ä.
 
Á¦ ³ª¸§´ë·Î´Â,
 
 
Áõ·ù°ü ¼Ó º¥Á¨¾çÀ» B¶ó ÇÏ°í Åç·ç¿£¾çÀ» T¶óÇϸé,
 
(MB/MB0) = (MA/MA0)^(1/¥áA,B) ½ÄÀ» ÀÌ¿ëÇϸé,
 
 
MB0 = 16.25
 
MB = 16.25 + 0.65 x 7t - 0.55 x 7 t
 
MA0 = 8.75
 
MA = 8.75 + 0.35 x 7 t - 0.45 x 7 t
 
 
·Î¼­, ½Ã°£´ç º¯È­ÇÏ´Â ¾çÀ» Àú·¸°Ô µÎ¾ú°í,
 
ÀÌ°É ½Ä¿¡ ´ëÀÔÇÏ¿© Ç®¾îº¸¸é, ¾È³ª¿À´õ±º¿ä.
 
ÀÏ´Ü, ÁÖ¾îÁø Á¶°ÇÀ» ¾î¶»°Ô ÀÌ¿ëÇؾßÇÏ´ÂÁö ¹®Á¦¸¦ Àß ÀÌÇØÇÏÁö ¸øÇϰڳ׿ä.
 
¹®Á¦¸¦ Ç®¾î°¨¿¡ ÀÖ¾î, µµ¿òÀ» ÁÖ¼ÌÀ¸¸é ÇÕ´Ï´Ù.
 
Âü°í·Î ÀÌ ¹®Á¦ÀÇ Á¤´äÀº t = 2.14 ÀÔ´Ï´Ù.

½ºÅ×Æijë Stefano   07-11-27 10:23
(1) ÁÖ¾îÁø Á¶°Ç
Feed = F =7 mole/h
Vaporization Rate = V = 7 mole/h (Still Liquid Level ÀÏÁ¤)

Mole Fraction Benzene in Feed = Xf = 0.35
Total Moles in Still = M = 25 moles

X = Mole Fraction Benzene in Still, -
Y = Mole Fraction Benzene in Vapor, -
t  = Run Time, h

Initial Condition, Xo = 0.35
End of Run Condition, Xe = 0.45

(2) ¹°Áú¼öÁö

(Input)-(Output)=(Accumulation)

Xf*F*dt - V*Y*dt = - M dX -----------------------(1)

 À­ ½Ä¿¡¼­ º¯¼ö´Â X, Y, t ÀÌ°í Xf, F, V, MÀº ¸ðµÎ »ó¼ö

(3) Relative Volatility, ¥á

¥á  = (Y/X)/{(1-Y)/(1-X)} ...........................(2)


(4) ¹®Á¦Ç®ÀÌ´Â (2)½Ä¿¡¼­ Y¸¦ ¥á¿Í X·Î ³ªÅ¸³»°í À̸¦ (1)½Ä¿¡ ´ëÀÔÇÏ°í
X = Xo~Xe,  t = 0~t ±îÁö ÀûºÐÇؼ­ t¸¦ ±¸Çغ¸¼¼¿ä.
   

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