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Çѱ¹¼öÀÚ¿øÇÐȸ / v.41, no.3, 2008³â, pp.243-249
½ÀÁöÀÇ ¼öÁú°ü¸®¸¦ À§ÇÑ ¿¬¼Ó±³¹ÝÅÊÅ©¹ÝÀÀ±â ¸ðµ¨ÀÇ Àû¿ë
( Application of Continuous Stirred Tank Reactor Model for Water Quality Control and Management in Wetland Treatment )
±è°æ¼·;¾ÈÅÂÁø;±è¹Î¼ö; ±¹¸³ÇѰæ´ëÇб³ ȯ°æ°øÇаú;±¹¸³ÇѰæ´ëÇб³ Åä¸ñ°øÇаú;±¹¸³ÇѰæ´ëÇб³ ȯ°æ°øÇаú;
 
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º» ¿¬±¸¿¡¼­´Â ÁöÇ¥È帧 ½ÀÁöÀÇ ¼öÁú°ü¸®¸¦ À§ÇÏ¿© ½ÀÁö ³» ¿À¿°¹°ÁúÀ» ÀûÀýÈ÷ ¸ðÀÇÇÒ ¼ö ÀÖ´Â ¿¬¼Ó±³¹ÝÅÊÅ©¹ÝÀÀ±â(CSTR) ¸ðµ¨À» ±¸ÃàÇÏ¿´´Ù. ÀÌ ¸ðµ¨Àº 4Â÷ Runge-Kutta¹ýÀ» »ç¿ëÇϰí, ½ÇÃøÄ¡¿Í °è»êÄ¡ÀÇ Â÷À̸¦ ÃÖ¼ÒÈ­ ÇÏ´Â ÃÖÀûÈ­ ±â¹ýÀ¸·Î ÇØ¸¦ ±¸Çϸç, ¹Ì±¹ EPA ½ÀÁö µ¥ÀÌÅͺ£À̽º¿¡ ¼ö·ÏµÈ ÀÚ·áÁß ¼öÁú ¹× ¼ö¸®ÀÚ·á°¡ ÃæºÐÇϸç, ºÐ¼®ÀÌ ¿ëÀÌÇÑ ÇϳªÀÇ ¼ö»ý´ë¸¦ °®´Â ½ÀÁö¸¦ ¼±ÅÃÇÏ¿©, ¼öÁúÇ׸ñÁß °ü½Éµµ°¡ ³ôÀº BOD, TSS (Total Suspended Solid)ÀÇ ¸ðÀÇ¿¡ Àû¿ëÇÏ¿´´Ù. ½ÀÁöÀÇ Ã¼ÀûÀÌ ÀÏÁ¤ÇÒ °æ¿ì¿Í üÀû ¹× À¯·®ÀÌ ÀÏÁ¤ÇÒ °æ¿ì °¢°¢¿¡ ´ëÇØ ¹ÝÀÀ¼Óµµ»ó¼ö¸¸À» °í·ÁÇÒ °æ¿ì, ¹°ÁúÈ帧¾ç¸¸À» °í·ÁÇÒ °æ¿ì ¹× ¹ÝÀÀ¼Óµµ»ó¼ö¿Í ¹°ÁúÈ帧¾ç ¸ðµÎ¸¦ °í·ÁÇÒ °æ¿ì·Î ³ª´©¾î ¸ðÀǸ¦ ½Ç½ÃÇÏ¿´´Ù. ¸ðÀÇ °á°ú ±âÁ¸ÀÇ ¹ÝÀÀ¼Óµµ»ó¼ö¸¸À» °í·ÁÇÑ °æ¿ìº¸´Ù ¹ÝÀÀ¼Óµµ»ó¼ö ¹× ¹°ÁúÈ帧¾ç ¸ðµÎ¸¦ °í·ÁÇÏ´Â °ÍÀÌ ½ÇÁ¦Çö»óÀ» Àß ³ªÅ¸³ÂÀ¸¸ç, ½ÀÁöÀÇ TSS ħ°­¼Óµµ´Â $0.3{sim}0.4;m/d$ÀÇ °ªÀ» ³ªÅ¸³»´Â °ÍÀ¸·Î ÆÄ¾ÇµÇ¾ú´Ù. ÀÌ ¸ðµ¨Àº ½ÀÁöÀÇ ¼öÁú°ü¸®¿¡ ÀûÀýÈ÷ Ȱ¿ëÇÒ ¼ö ÀÖÀ» °ÍÀ¸·Î ÆÇ´ÜµÈ´Ù.
Continuous stirred tank reactor(CSTR) model which can be applied to control and management of the surface flow wetland is developed to simulate the water quality in this research. The model solution is obtained from the optimization model using the least-squares and 4th-order Runge-Kutta methods. The model is applied to simulate BOD and TSS in the wetland database of U.S. EPA, in which the hydraulic and water quality data are enough and the number of pond is just one for simple analysis of running results. The model is tested in two different cases, one constant volume case and another constant volume and flow rate case considering only reaction term, mass flux term and both reaction and mass flux terms respectively. It is found that the model simulates the real water quality very well with both reaction and mass flux terms rather than only reaction term and the settling velocity of TSS becomes $0.3{sim}0.4;m/d$. The model can be applied in wetlands treatment efficiently.
 
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½ÀÁö;CSTR ¸ðµ¨;¹°Áú¼öÁö;ÃÖÀûÈ­ ¸ðµ¨;ÃÖ¼ÒÀڽ¹ý;wetland;CSTR model;mass balance;optimization model;least-squares method;
 
Çѱ¹¼öÀÚ¿øÇÐȸ³í¹®Áý / v.41, no.3, 2008³â, pp.243-249
Çѱ¹¼öÀÚ¿øÇÐȸ
ISSN : 1226-6280
UCI : G100:I100-KOI(KISTI1.1003/JNL.JAKO200814256113753)
¾ð¾î : Çѱ¹¾î
³í¹® Á¦°ø : KISTI Çѱ¹°úÇбâ¼úÁ¤º¸¿¬±¸¿ø
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