Kirkbride equationÀ» È°¿ëÇÑ ÃÖÀû±Þ¼Û´Ü (Feed Stage) °è»êÀýÂ÷¿¡ ´ëÇÑ ³»¿ëÀÔ´Ï´Ù.
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Rigorous Model ÇüÅÂÀÇ Column °è»êÀ» ÇÏ°Ô µË´Ï´Ù.
º» »çÇ×Àº HYSYS¿¡¼ »ç¿ëÇÏ´Â ÃÖÀû±Þ¼Û´Ü °è»ê¹æ½ÄÀ» Approximate Method·Î °è»êÇÏ´Â
Kirkbride equation¸¦ ¼Ò°³ÇÏ´Â ³»¿ëÀÔ´Ï´Ù.
Tower ¸ðµ¨Áß Short-Cut Tower¸¦ º¸¸é ´õ¿í ÀÚ¼¼È÷ ¾Ë ¼ö Àֱ⠶§¹®¿¡ HYSYS ¿¹Á¦¸¦
÷ºÎÇÏ¿´½À´Ï´Ù. Âü°íÇϸé ÀÌÇØ°¡ ´õ ½±½À´Ï´Ù.
Kirkbride equation
Ln(m/p) = 0.206 * Ln[(B/D)*(Xf-HK/Xf-LK)*(Xb-LK/Xd-HK)^2]
m : Feed ´Ü¼ö±âÁØ »ó´ÜÀÇ ´Ü¼ö
p : Feed ´Ü¼ö±âÁØ ÇÏ´ÜÀÇ ´Ü¼ö
D : Distillate Product Flow
B : Bottom Product Flow
Xf-HK : Feed ¼ººÐÁß Heavy Key¿¡ ÇØ´çÇÏ´Â Á¶¼º [mol%]
Xf-LK : Feed ¼ººÐÁß Light Key¿¡ ÇØ´çÇÏ´Â Á¶¼º [mol%]
Xd-HK : Distillate Product ¼ººÐÁß Heavy Key¿¡ ÇØ´çÇÏ´Â Á¶¼º [mol%]
Xb-LK : Bottom Product ¼ººÐÁß Light Key¿¡ ÇØ´çÇÏ´Â Á¶¼º [mol%]
¿¹¸¦ µé¸é,
Feed, Top, Btm ¼ººÐ¿¡ ´ëÇÑ Á¶¼º(¸ôºÐÀ²)ÀÌ ´ÙÀ½°ú °°´Ù¸é (À¯Ã·µÈ HYSYS ÆÄÀÏ°ú µ¿ÀÏÇÑ ¼öÄ¡ÀÓ)
¼ººÐ Feed Á¶¼º Top Á¶¼º Btm Á¶¼º
========= ========= ========= =========
n-butane 26 mol% 98.6 mol% 1.0 mol%
n-pentane 35 mol% 1.4 mol% 46.6 mol%
n-hexane 26 mol% 0.0 mol% 3.5 mol%
n-heptane 13 mol% 0.0 mol% 17.4 mol%
========= ========= ========= =========
100 mol% 100 mol% 100 mol%
Feed Flow : 100 tmol/hr
Distillate Flow : 25.6 tmol/hr
Bottom Flow : 74.4 tmol/hr
Ln(m/p) = 0.206 * Ln[(B/D)*(Xf-HK/Xf-LK)*(Xb-LK/Xd-HK)^2]
m/p = [(B/D)*(Xf-HK/Xf-LK)*(Xb-LK/Xd-HK)^2] ^ 0.206
= ((74.4/25.6)*(0.35/0.26)*(0.01/0.014)^2)^0.206
= 1.153
m/p = »ó´Ü´Ü¼ö/Çϴܴܼö = 1.153
½ÇÁ¦ ¼³Ä¡µÈ ´Ü¼ö°¡ N = 20.52 ´ÜÀ̶ó¸é,
m = (N)/(1+1/m/p) = 20.52/(1+1/1.153) = 10.99 ´Ü
p = m / (m/p) = 10.99 / 1.153 = 9.53 ´Ü
Áï ÃÖÀûÀÇ ´Ü¼ö´Â 10.99´ÜÀÌ µÈ´Ù.
º» ½ÄÀ» È°¿ëÇϸé Tower ±Þ¼Û´ÜÀÌ ¿©·µÀÎ °æ¿ì ¶Ç´Â ±Þ¼Û´ÜÀ» º¯°æÇÏ°íÀÚ ÇÏ´Â °æ¿ì
Á¶¼ºº¯È¿¡ µû¸¥ ÃÖÀûÀÇ ±Þ¼Û´ÜÀ» »êÃâÇÒ ¼ö ÀÖ½À´Ï´Ù.