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  PSV SIZING FOR GAS OR VAPOR RELIEF ¿¡¼­ FLOW BEHAVIOR SELECTION¿¡ °üÇÑ Áú¹®
  ±Û¾´ÀÌ : ÀÓÈ«Àç   °íÀ¯ID : hanwonclub2     ³¯Â¥ : 13-02-07 13:29     Á¶È¸ : 5816    
¾È³çÇϼ¼¿ä~ ¿À·£¸¸¿¡ µé¾î¿Í¼­ ±ÛÀ» ³²±é´Ï´Ù~^^ °ð ¼³¿¬ÈÞ°¡ ½ÃÀÛÀε¥ ȸ¿ø¿©·¯ºÐ ¸ðµÎ Áñ°Å¿î ¼³À» º¸³»½Ã±æ ¹Ù¶ø´Ï´Ù!
 
(1) Áú¹®Àº À§ÀÇ Á¦¸ñ°ú °°ÀÌ API 520 PART 1¿¡ ³ª¿Â PSV SIZINGÀ» ÇÒ ¶§ GAS OR VAPOR RELIEF ÀÇ °æ¿ì CRITICAL FLOW PRESSURE RATIO¿¡ µû¶ó FLOW BEHAVIOR À» SELECTION ÇؾßÇϴµ¥ ±× ±âÁØÀ» ¸íÈ®È÷ ¾Ë°íÀÚ ±ÛÀ» ¿Ã¸³´Ï´Ù. ¿ì¼± API STD 520 8Th EDITION, DEC 2008  PART 1 ÀÇ 5.6.2.5ÀýÀ» ¿Ã·Áº¸°Ú½À´Ï´Ù. "The sizing equations for pressure relief devices in vapor or gas service fall into two general categories depending on whether the flow is critical or subcritical. If the pressure downstream of the nozzle is less than, or equal to, the critical flow pressure, Pcf, then critical flow will occur, and the procedures in 5.6.3 should be applied. If the downstream pressure exceeds the critical flow pressure, Pcf , then subcritical flow will occur, and the procedures in 5.6.4 or 5.6.5 should be applied. See Table 7 for typical critical flow pressure ratio values." ¿¡¼­ ºÓÀº»ö ±Û¾¾·Î µÈ the pressure downstream of the nozzle°ú the downstream pressure ÀÇ ¸íÈ®ÇÑ Àǹ̸¦ ¸ð¸£°Ú½À´Ï´Ù. Á¦°¡ ÃßÃøÇϱâ·Î´Â PSVÀÇ OUTLET LINEÀÇ  TOTAL BACKPRESSURE¸¦ ÀǹÌÇÏ´Â °Í °°Àºµ¥, BACKPRESSUREµµ SUPER-IMPOSED BACKPRESSURE¿Í BUILT UP BACKPRESSURE°¡ Àֱ⿡ µÑ Áß Çϳª¸¦ ÀǹÌÇÒ ¼öµµ ÀÖ´Ù´Â »ý°¢µµ µé°í, Á¤È®È÷ ¾î¶² °ÍÀ» ÀǹÌÇÏ´Â ´Ü¾îÀÎÁö¸¦ Àß ¸ð¸£°Ú½À´Ï´Ù. ¾Ë°í °è½Å ºÐÀ̳ª ½ºÅ͵ðÇϽŠºÐµéÀÇ °í°ßÀ» ¿©Âã°íÀÚÇÏ¿À´Ï ¸¹Àº °¡¸£Ä§ ºÎŹµå¸³´Ï´Ù!

½ºÅ×Æijë Stefano   13-02-07 18:32
µ¶ÀÚµéÀÌ ½±°Ô ÀÐÀ» ¼ö ÀÖµµ·Ï Àû´çÇÑ ÁٹٲÞÀ» »ç¿ëÇÏ¿© ´Ü¶ôÀ» ³ª´©¾î ±ÛÀ» ´Ù½Ã ¿Ã·ÁÁÖ¼¼¿ä.  ÇÚÀçÀÇ »óÅ·δ ´«À» ¾ÆÁÖ ÇÇ°ïÇÏ°Ô ÇÕ´Ï´Ù. 
ÀÓÈ«Àç hanwonclub2   13-02-13 10:39
´ä±ÛÀÌ ´Þ¸° ±ÛÀº ¼öÁ¤ÀÌ ºÒ°¡´ÉÇÏ¿© ¼öÁ¤ÇÑ ±ÛÀ» ¸ñ·Ï¿¡ ´Ù½Ã ¿Ã·È½À´Ï´Ù.
   

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