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1660 º£¼¿ÀÇ ¾Ð·Â ÀúÇÏ °è»ê (3) À¯´Ï 10-20 5773 10-2
1659 ±âÈ­¿­ ±¸Çϱâ (1) ¿£½Ã¾Æ 10-22 5675 10-2
1658 H2S¿Í CO2 Á¦°Å °øÁ¤¿¡ ´ëÇØ ¹®ÀÇÇÕ´Ï´Ù (4) À̼±¸í 10-22 7005 10-2
1657 °øÁ¤µµ¿¡¼­.. (3) ±è±â¿õ 10-26 4878 10-2
1656 ³Ã°¢½Ã½ºÅÛ COP¸¦d ±¸ÇÏ°í½Í½À´Ï´Ù (3) Á¤Çö¼ö 10-26 4965 10-2
1655 ºÒÈ°¼º°¡½º ÁÖÀԽà breakdown ¹ß»ý (2) Áö³ª°¡´ÂÀÌ 10-27 3987 10-2
1654 Blowdown valve ÀÇ isolation (1) °¾ 10-27 4120 10-2
1653 Distillation column Hot vapor bypass °ü·Ã Áú¹®ÀÇ °Ç (1) È­°øÃʺ¸ 11-04 8149 11-0
1652 boil off gas calculation Áú¹® (1) ¸Þ¿ì½º 11-09 4097 11-0
1651 Ball tank¿¡¼­ÀÇ Boil off gas °è»êÇÏ´Â ¹æ¹ý (1) HOHO 11-02 5732 11-0
1650 NH3 (¾Ï¸ð´Ï¾Æ) ³óµµ º¯È¯ ppb - ppbv (4) ¿ëÇü 11-03 6610 11-0
1649 HTRI ¹°¼ºÄ¡ ÀԷ½à HTRI VS VMGTThermo V8.0 ÀÇ Â÷ÀÌÁ¡?? (1) ¾Æ³îµåº¸½º 11-05 4216 11-0
1648 nozzle set-in, set-on ¿¬°áÀÇ ±âÁØ? (1) ¾Æ³îµåº¸½º 11-05 4208 11-0
1647 HTRI gasoline composition ÀÔ·Â (°í¼ö´ÔÀÇ Á¶¾ð ºÎŹ µå¸³¡¦ (3) ¾ÆÁ÷µµ°øºÎ¡¦ 11-19 4097 11-1
1646 50# ½ºÆÀ Vent(½Ã°£´ç 15Åæ)·Î ½Ã°£´ç 650# ½ºÆÀ 20Åæ Vent¡¦ (1) ¼º¹Ú»ç 11-19 3860 11-1
1645 [Áú¹®]Áõ·ùž ¿îÀü¿¡ ´ëÇØ ±Ã±ÝÇÑ°Ô »ý°Ü ¹®Àǵ帳´Ï´Ù. (1) »ð»ì°³ 11-11 4838 11-1
1644 Á¤Á¦ TOWER ÀÌ»ó Çö»ó (6) ¿À·£Áö 11-14 5143 11-1
1643 Jet flooding % ¿Í D/C clearance ¿¡ ´ëÇÑ °ü°è (1) °øÁ¤¿£Áö´Ï¡¦ 11-15 5185 11-1
1642 Blended Gasoline Tank Type (1) éÌÜó 11-10 3785 11-1
1641 Åͺó È¿À² ±¸ÇÒ¶§ ÀÌ·Ð ÅäÃâÃø ¿£Å»ÇÇ °è»ê ¹æ¹ý¿¡ ´ëÇØ ¹®¡¦ (1) HOHO 11-19 6085 11-1
1640 2oo3 voting and degradation °ü·Ã (2) ÇöÀåFE 11-17 8680 11-1
1639 HTRI ¿À·ù ¸Þ½ÃÁö Áú¹®ÀÔ´Ï´Ù. (1) ¾Æ³îµåº¸½º 11-18 4149 11-1
1638 Hydraulic¿¡¼­ ÈÄ´Ü ¾Ð·Â °è»ê ¹æ¹ý (9) °õµ¹ÀÌǪ 11-18 9652 11-1
1637 ¿­±³È¯±â Approach Temperature Áú¹®µå·Á¿ä (½ºÅ×Æijë´Ô ´ä¡¦ (1) Ä«À̴нº 11-18 6454 11-1
1636 extraction¿¡¼­ ÃßÁ¦°¡ °ú´ÙÇÒ °æ¿ì (1) È­°ø´ë»ý 11-22 3974 11-2
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