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  Steam À¯¼Ó ¹× À¯·® °è»ê
  ±Û¾´ÀÌ : ¾Æ¸Þ¸®Ä«³ë   °íÀ¯ID : pbccap     ³¯Â¥ : 10-10-11 11:02     Á¶È¸ : 12658    
¾È³çÇϼ¼¿ä.
 
Àú´Â ÇöÀç ¼®À¯È­ÇÐ °èÅë °øÀå¿¡¼­ ÀÏÇÏ°í Àִµ¥¿ä.
 
Compressor  TurbineÀÇ Steam Bypass LineÀ» È®°üÇÏ´Â °ÍÀ» °ËÅäÇÏ´Ù°¡
 
´ÙÀ½°ú °°Àº Àǹ®ÀÌ µé¾î¼­ Áú¹® ¿Ã¸³´Ï´Ù.
 
* ÇöÀç Á¶°Ç
 
Line : 1"
¾Ð·ÂÂ÷ : 30 kg/cm2 (ÃßÃø)
±æÀÌ : 1.5 m(equivalent length °¡Á¤)
À¯Ã¼(Inlet) : HPS Steam (370'C 42kg)
´ÙÀ½ Á¶°Ç¿¡¼­ È帣´Â À¯Ã¼ÀÇ À¯¼Ó°ú À¯·®Àº ¾î¶»°Ô ¾Ë¼ö ÀÖÀ»Áö ±Ã±ÝÇÕ´Ï´Ù.
 
Ȥ½Ã À¯·®°ú À¯¼ÓÀ» °è»êÇØ ÁֽǼö ÀÖ³ª¿ä.
 
°¨»çÇÕ´Ï´Ù.

ÀåÇö¼ö jddast   10-10-11 13:35
ÀúÀÇ ÂªÀº »ý°¢À¸·Î´Â À§ Á¶°ÇÀ¸·Î À¯·®°ú À¯¼ÓÀ» ±¸ÇÒ ¼ö´Â ¾øÀ» µí ÇÕ´Ï´Ù.
´Ù¸¸, 1"¿¡ È带¼öÀÖ´Â ÃÖ´ë À¯·®°ú ±× À¯¼ÓÀº ±¸ÇÒ ¼ö ÀÖÀ» °Í °°½À´Ï´Ù.

¿ì¼± À¯·®ÀÇ ÃʱⰪÀ» °¡Á¤ÇÏ°í ¹è°ü¿¡ È帣´Â friction loss¸¦ °è»êÇÕ´Ï´Ù. Friction loss´Â Darcy Equation µîÀ» ÅëÇØ ±¸ÇÕ´Ï´Ù. À¯·®À» ¾Ë¸é (Áú·®À¯·®=¹Ðµµ*¼Ó·Â*´Ü¸éÀû) °ø½ÄÀ¸·Î À¯¼ÓÀº ±¸ÇÏ½Ç ¼ö ÀÖ°ÚÁö¿ä. ±×·± ´ÙÀ½ °¢Á¾ ȸ»ç³ª ¹®ÇåÀÇ Line size guide ¹× criteria¸¦ º¸¸é HP steamÀÇ ÃÖ´ë À¯¼Ó Çã¿ëÄ¡¸¦ ã½À´Ï´Ù. ÃÖ´ëÀ¯¼ÓÇã¿ëÄ¡¸¦ ÃÖ´ë·Î ¸¸Á·ÇÒ¶§ ±îÁö À¯·®ÀÇ ÃʱⰪÀ» ¹Ù²ã°¡¸é¼­ ¸¸Á·ÇÏ´Â °ªÀ» ãÀ¸¸é ÃÖ´ë À¯·®À» ±¸ÇÏ½Ç ¼ö ÀÖÀ»°Í °°½À´Ï´Ù.

¸íÈ®ÇÏÁö ¾Ê°Å³ª Ʋ¸° ºÎºÐÀÌ ÀÖ´Ù¸é ¸»¾¸ÇØ ÁÖ¼¼¿ä.
½ºÅ×Æijë Stefano   10-10-11 14:40
(1) ÃÊÀ½¼Ó µµ´Þ ºÒ°¡
1"°üÀ» ÅëÇØ 42 kg/cm2 gÀÇ HP SteamÀÌ Èê·¯µé¾î¿Í ¾Ð·ÂÂ÷ 30 kg/cm2·Î È帣´Â °üÀÌ ÀÖ´Ù°í Çصµ ±× °üÀÇ Ãⱸ¿¡¼­´Â ½ÇÁ¦·Î ¾Ð·ÂÂ÷°¡ ±×¸®Å©°Ô ³ªÅ¸³ª¸ç Èê·¯°¥ ¼ö°¡ ¾ø½À´Ï´Ù. 

¿Ö³ÄÇϸé 43.03 kg/cm2 absÀÇ ¾à 1/2ÀÎ 21.5 kg/cm2 a (=20.5 kg/cm2 g) Á¤µµ¿¡¼­ À½¼Ó¿¡ µµ´ÞÇϱ⠶§¹®ÀÔ´Ï´Ù. 
µû¶ó¼­ 1"°ü Ãⱸ°¡ (43.03-30.00) Áï 13.03 kg/cm2 a ¾Ð·ÂÀÌ µÇ´õ¶óµµ 1"°ü ¸»´Ü Á÷ÀüÀÇ ¾Ð·ÂÀº 26.06 kg/cm2 a Á¤µµ°¡ µÉ °ÍÀÌ°í ÀÌ ¾Ð·Â¿¡¼­ À½¼ÓÀ¸·Î ¹èÃâµÉ °ÍÀÔ´Ï´Ù. 

(2) ÃÖ´ë È帧 À¯·®
µû¶ó¼­ 26 kg/cm2 a Á¶°Ç¿¡¼­ ºÎÇÇÀ¯·®À¸·Î 
Q at 26 kg/cm2 a ~ 173¡É = (1"°ü ´Ü¸éÀû, A m^2)*(HPS 26.06 kg/cm2 a¿¡¼­ÀÇ À½¼Ó, Vs m/s).......................(1)
°¡ È带 °ÍÀÌ°í ÀÌ ¶§ÀÇ ¿Âµµ´Â 43 kg/cm2 a¿¡¼­ 26.06 kg/cm2 a µµ ´Ü¿­ÆØâ½Ã ¿ÂµµÀΠ 173µµ Á¤µµ°¡ µÉ °ÍÀÔ´Ï´Ù.

(3) ¼öÁõ±â ¼Ó¿¡¼­ÀÇ À½¼Ó
173µµ 26.06 kg/cm2 a¿¡¼­ÀÇ ¼öÁõ±â ¼Ó¿¡¼­ÀÇ À½¼ÓÀ» ¾Ë¾Æ¾ß ÇÏ°Ú½À´Ï´Ù. 

À½¼Ó, m/s = ..................................(2)

À½¼Ó°è»êÀº ÀÌ°÷À» ã¾Æ º¸¼¼¿ä
http://www.google.co.kr/#hl=ko&source=hp&biw=1266&bih=833&q=sonic+velocity+calculation&aq=1&aqi=g2&aql=&oq=Sonic+velo&gs_rfai=&fp=15221fb4bfe47fe9


Using the ideal gas law to replace p with nRT/V, and replacing ¥ñ with nM/V, the equation for an ideal gas becomes:

Speed of Sound, C = ¡î(¥ã  k T / m)

where
cideal is the speed of sound in an ideal gas.
R (approximately 8.3145 J¡¤mol−1¡¤K−1) is the molar gas constant.[1]
k is the Boltzmann constant,  1.380 6504(24) ¡¿ 10^−23  J/K 
¥ã (gamma) is the adiabatic index (sometimes assumed 7/5 = 1.400 for diatomic molecules from kinetic theory, assuming from quantum theory a temperature range at which thermal energy is fully partitioned into rotation (rotations are fully excited), but none into vibrational modes. Gamma is actually experimentally measured over a range from 1.3991 to 1.403 at 0 degrees Celsius, for air. Gamma is assumed from kinetic theory to be exactly 5/3 = 1.6667 for monoatomic molecules such as noble gases).
T is the absolute temperature in kelvins.
M is the molar mass in kilograms per mole. The mean molar mass for dry air is about 0.0289645 kg/mol.
m is the mass of a single molecule in kilograms.
ÀåÇö¼ö jddast   10-10-11 16:28
±×·¡¼­ Á¦°¡ ¾Æ¹«¸® ¾Ð·ÂÂ÷¸¦ Á൵ 21kg/cm2a ÀÌÇϷδ ¾È³»·Á°¡´Â °Å¿´³×¿ä.

1) ±×·±µ¥ 1"°ü ¸»´Ü Á÷ÀüÀÇ ¾Ð·Â 26.06kg/cm2a´Â ¾î¶²°Ô ³ª¿Â ¼öÄ¡ÀÎÁö ±Ã±ÝÇÕ´Ï´Ù.

2)  43->26kg/cm2g·Î ´Ü¿­ÆØâ¿Âµµ°¡ 173µµ Á¤µµ¶ó°í Çϼ̴µ¥ Á¦ »ý°¢¿£ ´Ü¿­·Î ÆØâÇÑ´ÙÇÏ´õ¶óµµ 350µµ Á¤µµ·Î..  ´Ü¿­À̴ϱñ ¶³¾îÁø ¾Ð·ÂÁ¶°Ç¿¡¼­ °°Àº ¿£Å»ÇÇÀÎ ¿Âµµ¸¦ ±¸ÇÑ °ªÀÔ´Ï´Ù. Á¦°¡ ¹» Ʋ·È´ÂÁö,, ¾î¶»°Ô ±¸ÇÑ °ªÀÎÁö ¾Ë°í ½Í½À´Ï´Ù.
Stefano    10-10-11 19:53
1) Sonic Velocity´Â ¹Ù·Î ºÐÀÚµéÀÌ Á÷Á¢ Áøµ¿Çϸ鼭 À̵¿ÇÒ¶§ÀÇ ÃÖ´ë ¼ÓµµÀε¥ ºÐÀÚÀÇ Áøµ¿¼Óµµº¸´Ù ´õ ºü¸£°Ô À¯Ã¼°¡ À̵¿ÇÒ ¼ö°¡ ¾ø´Â ÀÌÀ¯´Â ÁøÇà¹æÇâÀ¸·Î ºÐÀÚµéÀÇ Ãæµ¹¿¡ ÀÇÇØ ÀúÇ×ÀÌ Å©°Ô °É¸®±â ¶§¹®ÀÔ´Ï´Ù.  ÃÊÀ½¼Ó ¹°Ã¼´Â °¡½ºÀÇ ¼Óµµº¸´Ù ´õ ºü¸¥ ¼Óµµ·Î °¡½º¸¦ Á¦Ä¡°í ³¯¾Æ°¡´Â °ÍÀÌÁö¸¸ À¯Ã¼´Â ÃÊÀ½¼ÓÀÌ»óÀ¸·Î Èê·¯°¥ ¼ö°¡ ¾ø½À´Ï´Ù.

ÀÔ±¸ÀÇ Àý´ë¾Ð·Â¿¡ ´ëÇÑ ÃⱸÀÇ ¾Ð·ÂÀÇ ºñ°¡ ¾î´À Á¤µµ µÇ´À³Ä¿¡ µû¶ó À½¼Ó¿¡ µµ´ÞÇϴ°¡¸¦ ¾Ë ¼ö ÀÖ´Â ¼ö½ÄÀÌ Àִµ¥ ÀÌ´Â Isentropic Exponent°ª¿¡ µû¶ó ´Þ¶óÁý´Ï´Ù.  ¿©·¯¹ø ÀÌ°÷ °Ô½ÃÆÇ¿¡ ¼Ò°³ÇÑ ÀûÀÌ Àִµ¥  ¥ã°ª¿¡ µû¸¥ (Ãⱸ¾Ð/ÀÔ±¸¾Ð)ÀǺñ¸¦ ÀÌ°÷¿¡¼­ ã¾Æº¸¼¼¿ä.
http://www.chemeng.co.kr/site/bbs/board.php?bo_table=xqna&wr_id=12990&page=7

2) ÀÌ»ó±âü¶ó°í °¡Á¤ÇÏ°í °¡½º¸¦ ´Ü¿­ÆØâÇÏ°Ô µÇ¸é Àý´ë¿Âµµ¿Í ¾Ð·Â°£ÀÇ °ü°è¼ö½ÄÀº

(T2/T1)=(P2/P1)^{(¥ã-1)/¥ã} ............(4)ÀÇ °ü°è°¡ ÀÖ½À´Ï´Ù.  À̷κÎÅÍ °è»êÇϸé T2¸¦ ±¸ÇÒ ¼ö ÀÖ½À´Ï´Ù.
ÀåÇö¼ö jddast   10-10-12 08:55
°¨»çÇÕ´Ï´Ù.

1) HP steamÁ¶°Ç¿¡¼­ Isentropic exponent, k=1.388 À̴ϱñ °ø±â(1.4)¿Í °°´Ù°í ÇÑ´Ù¸é ÀÔ°è¾Ð·Âºñ´Â 0.5283ÀÔ´Ï´Ù.
Áï, ÀÔ°è¾Ð·Âºñ¸¦ ³ÑÀ» ¼ö ¾ø±â¿¡ Ãⱸ¾Ð·ÂÀÌ 43.03*0.5283=22.7kg/cm2a ¿¡¼­ À½¼Ó¿¡ µµ´ÞÇÏ°Ô µË´Ï´Ù. ±×·¡¼­ ÃⱸÁ÷ÀüÀÌ ¾à 26kg/cm2a¶ó°í ÇÑ´Ù¸é ÀÌ ¾Ð·Â¿¡¼­ À½¼ÓÀ¸·Î ¹èÃâµÇ¾î ³ª°¡°Ô µË´Ï´Ù.

2) À§ Isentropic EquiationÀº ´Ü¿­¾ÐÃà(compressor)¿¡¼­ ¾²ÀÌ´Â ½ÄÀ̶û °°Àº ³»¿ëÀÎ °Í °°½À´Ï´Ù. ±×·¡¼­ Àúµµ °è»êÀ» ÇغþúÁö¸¸ ½ºÅ×Æijë´ÔÀÇ °è»ê°á°ú¶û È®¿¬È÷ Â÷ÀÌ°¡ ÀÖ½À´Ï´Ù.
T2=T1*(P2/P1)^{(k-1)/k} = (273+370)*(26.06/43.03)^{(1.388-1)/1.388}=559K (=286µµ)

Á¦°¡ ÀÌÇØÇÑ ³»¿ëÀÔ´Ï´Ù. ¿©·¯¹ø ¼Ò°³ÇÏ°í °¡¸£Ä§ÁÖ¼ÌÁö¸¸ È®½ÇÈ÷ ¾Ë°í ½Í½À´Ï´Ù.
Ʋ¸° ºÎºÐÀÌ ¹«¾ùÀÎÁö °¡¸£ÃÄ ÁÖ½Ã¸é °¨»çÇÏ°Ú½À´Ï´Ù.
Stefano    10-10-12 12:35
¥ã°ªÀÌ 1.388ÀÌ°í ÀÓ°è¾Ð·Âºñ°¡ 0.5283À̶ó°í Çϸé ()¾ÈÀÇ °ªÀ» 0.5283À» »ç¿ëÇؼ­ °è»êÇÏ¸é µÇ°ÚÁö¿ä.  ´Ü (4)ÀÇ ¼ö½ÄÀº ÀÌ»ó±âüÀÌ°í ¿ÏÀü ´Ü¿­»óÅÂÀÎ °æ¿ì¿¡ ´ëÇØ Àû¿ëÇÕ´Ï´Ù.

Ãⱸ¿Âµµ= (273+370)*(0.5283)^(0.388/1.388)-273= 264 ¡É

½ºÅ×Æijë´Â ( )¾ÈÀÇ ÀÓ°è¾Ð·Âºñ¸¦ ´ë·« 0.5·Î ±×¸®°í k°ªÀ» 1.4 Á¤µµ·Î °³·«°è»êÇß´ø °ÍÀε¥ °è»êÀÌ À߸øµÈ °ÍÀ¸·Î º¸ÀÔ´Ï´Ù.    ½ºÅ×Æijë (°³·«)°è»ê : (273+370)*(0.5)^(0.4/1.4)-273 = 254 ¡É
ÀåÇö¼ö    10-10-12 13:13
°¨»çÇÕ´Ï´Ù.

È®½ÇÈ÷ ¹è¿ö°©´Ï´Ù.
   

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