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  Polytropic Process °ü·Ã Áú¹®
  ±Û¾´ÀÌ : éÌÜó   °íÀ¯ID : yongbong     ³¯Â¥ : 16-01-25 13:07     Á¶È¸ : 4412    

ÀÌÀü¿¡µµ °ü·Ã Áú¹®À» ¿Ã¸° ÀûÀÌ ÀÖÀ¸³ª Àǹ®Á¡ÀÌ ÇؼҵÇÁö ¾Ê¾Æ,

Á» ´Ù¸¥ °üÁ¡¿¡¼­ Áú¹®À» µå¸±±î ÇÕ´Ï´Ù.

 

GPSA 13-28 Polytropic Calculation ºÎºÐ¿¡ µû¶ó¼­ ¼³¸íÀ» ÇØ º¸°Ú½À´Ï´Ù.

 

1. Polytropic Efficiency

Åë»ó Centrifugal CompressorÀÇ Head³ª Power¸¦ °è»êÇÒ ¶§ Polytropic Efficiency¶ó´Â vendor¿¡°Ô¼­ ¹Þ´Â °ªÀ» »ç¿ëÇÕ´Ï´Ù.

ÀÌ Polytropic Efficiency´Â ¾î´À Á¤µµÀÇ ¹üÀ§´Â ÀÖÁö¸¸, Vendor¿¡ µû¶ó, ±â±â¿¡ µû¶ó, GasÀÇ Á¾·ù¿¡ µû¶ó, insulation Á¤µµ¿¡ µû¶ó ¸ðµÎ ´Ù¸¦ °ÍÀ¸·Î »ý°¢µË´Ï´Ù.

 

2. Polytropic Index Calculation

1¹ø¿¡¼­ ¾òÀº Polytropic Efficiency¸¦ °¡Áö°í º¸Åë nÀ¸·Î Ç¥½ÃÇÏ´Â Polytropic Index¸¦ ´ÙÀ½°ú °°ÀÌ ±¸ÇÕ´Ï´Ù.

n / (n-1) = k / (k-1) * ¥ç

 

3. Polytropic Head Calculation

2¹ø¿¡¼­ ¾òÀº Polytropic Index¸¦ °¡Áö°í ¾Æ·¡¿Í °°ÀÌ Polytropic Head¸¦ ±¸ÇÕ´Ï´Ù.

Hp = (ZRT1)/ [MW*(n-1)/n] * [ (P2/P1)^[(n-1)/n] - 1]  

 

4. Compressor Power Calculation

3¹ø¿¡¼­ ¾òÀº Polytropic Head¿Í 1¹ø¿¡¼­ ¾òÀº Polytropic Efficiency¸¦ °¡Áö°í ¾Æ·¡¿Í °°ÀÌ Power¸¦ ±¸ÇÕ´Ï´Ù.

GHP = (w*Hp) / (¥ç*3600000)

¿©±â¿¡ Shaftµî¿¡¼­ ¹ß»ýÇÏ´Â Mechanical Loss¸¦ °í·ÁÇϸé Actual Power°¡ °è»êµÇ°Ú½À´Ï´Ù.

 

±× µ¿¾È Àú¸¦ ±«·ÓÇû´ø °ÍÀº, À§ÀÇ 2¹ø °úÁ¤°ú 4¹ø °úÁ¤¿¡¼­ Polytropic Efficiency°¡ µÎ ¹ø ¾²Àδٴ °ÍÀ̾ú½À´Ï´Ù.

ÀÌ°ÍÀ» ¿ì¿¬À̶ó°í ÇÒ ¼ö´Â ¾ø°ÚÁö¿ä.

¿Ö ÀÌ·¯ÇÑ °úÁ¤À» °ÅÄ¡´ÂÁö, Áß°£¿¡ °è»êÇÑ Hp (Polytropic Head)°¡ ¹«½¼ Àǹ̰¡ Àֱ淡 ±× °úÁ¤À» °ÅÄ¡´ÂÁö´Â ¸ð¸£°Ú½À´Ï´Ù.

´Ù¸¸, »ý°¢ÇÒ ¼ö ÀÖ´Â À¯ÀÏÇÑ ¼³¸íÀº, °á±¹ Polytropic Head (¶Ç´Â Polytropic Path/Process)´Â ¾î¶² ÀÌ·ÐÀûÀÎ Àǹ̰¡ ÀÖ´Â °Íµµ ¾Æ´Ï°í, ¶ÇÇÑ ¹°¸®ÀûÀÎ Àǹ̰¡ ÀÖ´Â °Íµµ ¾Æ´Ï°í,

´Ü¼øÈ÷ °è»ê»ó ÆíÀǸ¦ À§Çؼ­ ¸¸µé¾î³½ Áß°£´Ü°è¶ó´Â °ÍÀÔ´Ï´Ù.

Áï, 2¹ø °úÁ¤°ú 4¹ø °úÁ¤¿¡¼­ »ç¿ëµÇ´Â Efficiency°¡ °°Àº °ªÀÌ µÇµµ·Ï ÇÏ´Â ÀÓÀÇÀÇ n°ªÀ» (ȤÀº Hp°ªÀ») ã´Â´Ù´Â °ÍÀÔ´Ï´Ù.

 
ÀÌ·¯ÇÑ ³í¸®ÀÇ Àü°³°¡ ¸Â´Â °ÍÀϱî¿ä?

½ºÅ×Æijë Stefano   16-01-27 17:26
(1) Polytropic Process

 Polytropic Compression °úÁ¤Àº ¹«¼öÈ÷ ¸¹Àº ¼öÈ¿ÀÇ ¹ÌºÐ´Ü¼öÀÇ ¾ÐÃà´Ü¿¡¼­  Isentropic(Reversible, Adiabatic) Enthalpy Difference¿Í Actual Enthalpy DifferenceÀÇ ºñ¸¦ ÀÏÁ¤ÇÏ°Ô À¯ÁöÇϸ鼭 ¾ÐÃàÇÏ´Â °úÁ¤À¸·Î Á¤Àdz»¸° °ÍÀε¥ À̸¦ ¼ö½ÄÀ¸·Î Ç¥ÇöÇϸé

v dP/dh = ÀÏÁ¤ºñ = ¥çp ...............(1)

ÀÌ Á¶°ÇÀ» À¯ÁöÇϸ鼭 ¾ÐÃàÇßÀ»¶§ Actual Enthalpy Difference¸¦ ±¸ÇÏ·Á¸é ´ÙÀ½ ¼ö½Ä¿¡¼­ ¥çp¸¦ »ó¼ö·Î µÎ°í (1)½ÄÀ» ÀûºÐÇؼ­ ±¸ÇØ¾ß ÇÕ´Ï´Ù.  ¹Ý¸é ´Ü¿­°úÁ¤¿¡¼­ÀÇ ºÎÇÇ v´Â  pv^n=constant

Áï p1v1^n = p2v2^n ..= p v^n ...................(2)

¥Äh = (Enthalpy Difference between Suction and Discharge) = (p1~p2±îÁö ÀûºÐ) ¡ò (v/¥çp) dp ........(3)

(2) Polytropic Head

À§ÀÇ (3)½ÄÀÇ v¸¦ p·Î ġȯÇÏ¿© ÀûºÐÇÏ¿© ¾ò¾îÁø Enthalpy Â÷ÀÌ´Â Polytropic Compression¿¡¼­ Irreversibility¿Í Adiabatic Á¶°ÇÀ» ¸¸Á·ÇÏ´Â ¾ÐÃà°úÁ¤¿¡¼­ ÇÊ¿ä·Î ÇÏ´Â Specific Head°¡ µÇ´Âµ¥ ÀÌ °ªÀÌ Polytropic Head°¡ µË´Ï´Ù.

yp= p1v1*(n/n-1)*[(p2/p1)^(n-1)/n -1]  =z R T1 *(n/n-1)*[(p2/p1)^(n-1)/n -1].......(4)

(3) Polytropic Efficiency

Polytropic Efficiency´Â (1)½Ä¿¡¼­¿Í °°ÀÌ ¹Ì¸® Á¤ÇصР°ªÀ̳ª ÀÌ´Â Á¦À۵Ǵ Compressor¸¶´Ù ¾à°£¾¿ ´Ù¸£±â ¶§¹®¿¡ Â÷ÀÌ°¡ ÀÖÀ» ¼ö ÀÖ°í °³·«ÀûÀ¸·Î ´ÙÀ½ ¼ö½ÄÀ¸·Î Ç¥ÇöµË´Ï´Ù. 

¥çp = {(k-1)/k}/((n-1)/n} .............................(5a)  ¶Ç´Â  ( n-1)/n  = (k-1) / (k*¥çp) .........(5b)

(4) Compression Power

GHP, W = (Weight Flow)*(Polytropic Head yp) / ¥çp ....................................(6)

µ¿·Â °è»êÀº À§¿Í °°Àº ¼ö½ÄÀ¸·Î °è»êÇÏ°Ô µÇ´Âµ¥ ¿©±â¼­ Polytropic Head yp °è»ê¿¡ ÀÌ¹Ì »ç¿ëÇÑ ¥çp°ªÀº Polytropic Compression °úÁ¤¿¡ÀÇ Theoretical Head¿¡ ÇØ´çÇÏ°í ´Ù½Ã ¼Ò¿ä ¾ÐÃൿ·Â°è»ê¿¡µµ ´Ù½Ã µ¿ÀÏ ¥çp¸¦ ´Ù½Ã Àû¿ëÇÏ°í ÀÖ´À³Ä´Â °ÍÀÌ Áú¹®ÀÇ ÇÙ½ÉÀε¥..

À§ÀÇ (5)Polytropic Head °è»ê¿¡ "Actual" Mechanical Efficiency°¡ ´©¶ôµÇ¾îÀÖ´Ù°í ºÁ¾ß ÇÒ °Í °°½À´Ï´Ù.  ³íÁ¡Àº (1) ½ÄÀÌ ÀǹÌÇÏ´Â ¹Ù¿¡ ±Í°áµÇ´Â °ÍÀε¥.. ÀÌ ½ÄÀÇ À¯µµ°úÁ¤À» ã¾Æº¸¸é ¾Ë¾Æ³¾ ¼öµµ ÀÖÁö ¾ÊÀ»±î »ý°¢ÇÕ´Ï´Ù.  Çѹø ã¾Æº¸µµ·Ï ÇÏÁö¿ä.
   

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