Posted by(ÀÛ¼ºÇϽŠºÐ) MaxMet Research Institute ( June 21, 2003 at 13:44:27: )
In Reply to(¿ø¹®) : flow behaviour index & consistency insdex
posted by(¿ø¹® ÀÛ¼ºÀÚ) : ±Ç¿À¼º/¿¬¼¼´ëÇб³ on June 11, 2003 at 23:50:09:
For the measurement of constancy index and flow index, you should use either
- rotational viscomster
- rheometer
with which you can measure the share stress value corresponding to the dedicated
shear rate(s-1).
plot S Stress vs S rate and you can find easily the K and n value in linear scale(in fact the
relation ship is non-linera but logarithmic).
Please refer to our consultation page as follows(in Korean)
(´äº¯)
ÆäÀÎÆ®, Carboxy Methyl Cellulose(CMC)´Â pseudoplastic°è
ºñ´ºÆ°¼º À¯Ã¼ÀÔ´Ï´Ù. ´ºÆ°¼ºÀ¯Ã¼(¹°, °ø±âµî°ú °°Àº À¯Ã¼)´Â
Àü´ÜÀ²°ú Àü´ÜÀÀ·ÂÀÇ ºñÀ²ÀÌ Àü´ÜÀ²ÀÇ º¯È¿¡ µû¶ó ÀÏÁ¤ÇÏÁö¸¸,
ºñ´ºÆ°¼º À¯Ã¼´Â ±× ºñÀ²ÀÌ Àü´ÜÀ²ÀÇ Å©±â¿¡ µû¶ó º¯ÈÇÕ´Ï´Ù.
µû¶ó¼ CMCÀÇ °æ¿ì¿Í °°Àº
ºñ´ºÆ°¼º À¯Ã¼ÀÇ Á¡µµ´Â ¿ÜºÎ ½ºÆ®·¹½ºÀÇ º¯È(¶Ç´Â ½ºÇɵéÀÇ
¼Óµµ)¿¡ µû¶ó ±× °ªÀÌ Æ²¸± ¼ö ¹Û¿¡ ¾ø½À´Ï´Ù.
¼ö¾øÀÌ rpmÀ» ¹Ù²Ù¾î À纸½Ã´õ¶óµµ ÃøÁ¤Ä¡´Â rpm¿¡ µû¶ó
°è¼Ó ´Þ¶óÁö´Â °ÍÀ» È®ÀÎÇÏ½Ç ¼ö ÀÖÀ¾´Ï´Ù
(ƽ¼ÒÆ®·ÎÇÇ¿¡ °üÇØ¼´Â À§ÀÇ ±ÛÀ» ÂüÁ¶ÇϽʽÿÀ).
À¯Ã¼ÀÇ Á¾·ù¸¦ ´ºÆ°ÀÇ ºÐ·ù¿¡ µû¶ó Á¤¸®ÇØ º¸¸é
´ÙÀ½°ú °°½À´Ï´Ù.
´ºÆ°¼º À¯Ã¼ : Àü´ÜÀÀ·Â =(ºñÀ²ÀÌ Ç×»óÀÏÁ¤) Á¡µµ x Àü´ÜÀ²
ºñ´ºÆ°¼º À¯Ã¼ : Àü´ÜÀÀ·Â =(ºñÀ²ÀÌ Àü´ÜÀ² Å©±â¿¡ µû¶ó º¯È) Á¡µµ x Àü´ÜÀ²
µû¶ó¼ ºñ´ºÆ°¼º À¯Ã¼´Â °Ñº¸±â Á¡µµÀÇ °³³äÀ» ÀÌ¿ëÇÏ¿©
Á¡µµ¸¦ ÃøÁ¤ÇÏ°í ±âÁذªÀ» ¸¶·ÃÇØ¾ß ÇÕ´Ï´Ù.
Àü´ÜÀÀ·Â = »ó¼öÁ¡µµ(consistency) x Àü´ÜÀ²^n
¿©±â¼ °Ñº¸±â Á¡µµ= Àý´ë°ª(»ó¼öÁ¡µµx Àü´ÜÀ²) ^ n-1
»ó¼öÁ¡µµ(consistency index)´Â ºñ´ºÆ°¼º À¯Ã¼ÀÇ Á¡µµ°ªÀ»
Ç¥ÇöÇÏ´Â °ªÀÔ´Ï´Ù.
Ç¥ÇöÇϽô º¯¼öµéÀº »ó¼öÁ¡µµ¿Í ÇÔ²² À¯µ¿Áö¼ö(flow behaviour index) ,
n°ªÀ» Á¦½ÃÇÕ´Ï´Ù.
n =1 ÀÏ °æ¿ì ´ºÆ°¼ºÀ¯Ã¼
n < 1 ÀÏ °æ¿ì ½´µµÇÃ¶ó½ºÆ½(psedo-plastic)
n > 1 ÀÏ °æ¿ì µô·¹ÀÌÅÏÆ®(dilatant)
µû¶ó¼ ÀÌ °æ¿ì ȸÀüÇü Á¡µµ°è¸¦ »ç¿ëÇÑ´Ù¸é ù¹øÂ° Ãßõ¹æ¹ýÀº
°Ñº¸±â Á¡µµ¸¦ µÎ°¡Áö ¶Ç´Â ±× ÀÌ»óÀÇ ½ºÇɵé¼Óµµ¿¡¼ ÃøÁ¤ÇÏ¿©
ºñ´ºÆ°¼º À¯Ã¼(»ùÇÃ)ÀÇ Æ¯¼ºÀ» ±Ô¸íÇØ µÎ½Ã´Â °ÍÀÔ´Ï´Ù.
Àü´ÜÀÀ·Â°ú Àü´ÜÀ²ÀÇ µµÇ¥¸¦ ÅëÇØ ÇØ´çÀ¯Ã¼ÀÇ ÀÏÁ¤¿Âµµ¿¡¼ÀÇ
»ó¼öÁ¡µµ¿Í n °ªÀ» ÃøÁ¤ÇÏ¿© ÀÌ °ªÀ» ±âÁØÀ¸·Î Ȱ¿ëÇϽøé
µË´Ï´Ù. ÀÌ °ª µÑÀº ¿©·¯ rpm¿¡¼ ÃøÁ¤ÇØ µÎ¸é ÇØ´çÀ¯Ã¼ÀÇ
¼ºÁúÀÌ º¯ÇÏÁö ¾Ê´Â ÇÑ ´ëÇ¥¼ºÀÌ ÀÖÀ¾´Ï´Ù(´Ü Á¤ÇØÁø ¿Âµµ¿¡¸¸ ÇØ´çµÇ¸ç,
½Ç ÇÁ·Î¼¼½ºÀÇ ¿ÂµµÀÇ ÀÚ·á°¡ ÇÊ¿äÇϸé, Á÷Á¢ÃøÁ¤
¶Ç´Â ³»¿Ü»ðÀÇ ¹æ¹ýÀ» »ç¿ëÇÒ ¼ö ÀÖ½À´Ï´Ù).
ÀÌ·¸°Ô ÇÏ¿© Á¤ÇØÁø ¿Âµµ¿¡¼ »ó¼öÁ¡µµ(consistency index)
¿Í À¯µ¿Áö¼ö nÀ» ÀÌ¿ëÇØ Á¡µµÀÇ ±âÁØÀ» ¸¶·ÃÇØ »ç¿ëÇϽʽÿÀ.
Âü°í
CMC 0.2 wt % with tap water consiostency index(mN s^n/M^2) 7.85 (at 19.5 C) n=0.946
CMC 0.4 wt% with tap water consiostency index(mN s^n/M^2) 27.12 (at 19.5 C) n=0.836
nota: the data can be dependent on the specific CMC polyer MW
ref;
C.H.Kim, "Liquid Phase Axial Dispersion Characteristics in Three-Phase Fluidized Beds",
MS thesis, Dept. Chem. Eng., KAIST(1981)
: ¿¬¼¼´ëÇб³ ȯ°æ°øÇаú ´ëÇпø»ýÀÔ´Ï´Ù.
: CMC solutionÀ» ÀÌ¿ëÇÑ ½ÇÇèÀ» Çϰí Àִµ¥
: CMC ³óµµ¿¡ µû¸¥ K(consistency index)¿Í n(flow behaviour index)¸¦ ±¸ÇϰíÀÚ ÇÕ´Ï´Ù.
: ÀϹÝÀûÀ¸·Î power law¸¦ ÀÌ¿ëÇÏ¿© shear rate °ú shear stress¸¦ ÃøÁ¤Çϸé À§ÀÇ µÎ °ªÀ» ½±°Ô °è»êÇÒ ¼ö ÀÖÀ» ÅÙµ¥..¾î¶»°Ô ÃøÁ¤ÇؾßÇÏ´ÂÁö ¸ð¸£°Ú±º¿ä.
: Á¦°¡ »ç¿ëÇϰí ÀÖ´Â Á¡µµ°è´Â TOKIMEC»çÀÇ BL-type(concentric cylinder type)ÀÔ´Ï´Ù.
: ¹Ù»Ú½Ã°ÚÁö¸¸, ´äº¯ ºÎʵ右´Ï´Ù.