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930 Control valve failure½Ã PSV sizing basis (2) MedalofHon¡¦ 09-10 8545 09-10
929 ¹°Áú¼öÁö¸¦ ¼¼¿ì°í, ÆÛ¼¾Æ® ³óµµ¸¦ ±¸ÇÏ´Â ¹®Á¨µ¥ Ç®´Ù°¡ ¡¦ µµ¿òÀ» ¿ä¡¦ 00-00 8547 00-00
928 ÆßÇÁÀÇ GPM ±¸ÇÏ´Â ¹æ½ÄÀ» ¾Æ½Ã´ÂÁö¿ä? (1) Kate 10-23 8548 10-23
927 À¯,¹«±â¹° ¼¼Á¤¿ë ¾àÇ°¿¡ ´ëÇØ(±¸¿¬»ê,Â÷¾Æ¿°¼Ò»ê³ªÆ®·ý) (1) Àº¼º±¤ 04-01 8550 04-01
926 stern-volmer ¹æÁ¤½Ä (1) Ã߽°ï 02-28 8550 02-28
925 PSV sizing for Gas Expasion °ü·ÃÇÏ¿© Áú¹® µå¸³´Ï´Ù. (4) thisyear 09-15 8553 09-15
924 ¹°:1729¸®ÅÍ+ NaOH(25%):101¸®ÅÍ =? ³óµµ? (1) ¹®ÁØÈ£ 00-00 8554 00-00
923 Áõ·ùž ¸®Ç÷°½º ¿Âµµ °ü·Ã ¹®ÀÇ (5) ³ª·¡±â 11-08 8556 11-08
922 DMF ³»ÀÇ Total Amine ºÐ¼®¹æ¹ý (1) ±è´ë¹Î 10-03 8562 10-03
921 ¼öÁõ±â ºÎÇÇ°¡ ¹°ÀÇ 1.05¹è? (3) ±ÇÇõÁ¾ 00-00 8563 00-00
920 Bunker C Oil ÇöÁ¦ ½Ã¼¼¸¦ ¾Ë ¼ö ÀÖÀ»±î¿ä? (3) ±èÅÂÇü 02-07 8572 02-07
919 Ȳ»ê°úÁú»êÈ¥ÇÕ¹°ÀûÁ¤ (2) stjeh 07-07 8573 07-07
918 Joule-Thomson È¿°ú¸¦ ÀÌ¿ëÇÑ ¼³ºñ (1) ±è¼®¿­ 06-01 8574 06-01
917 Áú·®¼Óµµ(kg/h) ¹× ±âüppm ±¸ÇÏ´Â ¹æ¹ý ¾Ë·ÁÁÖ¼¼¿ä. (2) Áö´Ï2 06-03 8574 06-03
916 double-pipe heat exchanger¼³°è¿¡ °üÇؼ­¿ä (4) Áö¾Ð¼±³à 09-21 8575 09-21
915 ·ÎÁø °ø½Ä¿¡ ´ëÇؼ­.. (5) ¸ô¶ó 05-29 8577 05-29
914 ½ºÅ×Æijë´Ô²² ÀÚ¹® ±¸ÇÕ´Ï´Ù(³Ãµ¿´É·Â °è»êÇϴ¹æ¹ý) (2) »ïµ¹ÀÌÁ¤ 09-07 8577 09-07
913 PSV relieving temperature (6) iminproces¡¦ 01-12 8580 01-12
912 PUMP ¾çÁ¤ ¹®ÀÇ °Ç (3) PCº¸ÀÏ·¯¼³¡¦ 05-17 8584 05-17
911 PMMA ¿Í PVCAÀÇ ¹°¼º¿¡ °üÇÑÀÚ·á Á» ¾Ë·ÁÁÖ¼¼¿ä. (1) ¿ÀÁöÀº 00-00 8585 00-00
910 ÀÔÀÚ(particle) ³óµµ °è»ê¿¡ °üÇØ Áú¹® µå¸³´Ï´Ù. (3) kepman 10-09 8592 10-09
909 ºÐ¹è°è¼ö... (1) ¸ð¸§ 00-00 8595 00-00
908 polytropic exponent °è»ê (9) ¾Æ¸Þ¸®Ä«³ë 06-20 8604 06-20
907 ²À Á» ºÎŹµå¸±²²¿ä.. ºÎµð ´äº¯ ¹Ù¶ø´Ï´Ù.. (1) ±ÞÇÑÀÌ 10-05 8606 10-05
906    ¾×üºÎÇÇÆØâ¾Ð·Â (7) ´ÙÀ­ 09-11 8606 09-11
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