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33 Crude desulter system °ü·Ã Áú¹® (11) ÇÎÅ©¼ÖÆ® 08-19 3368 08-27
32 SC Pumping TrapÀÇ °³¼±»çÇ׿¡ ±Ã±ÝÁõÀÌ ÀÖ½À´Ï´Ù. (17) ¹Ì³ªÅäÀÚÅ°¡¦ 08-13 7690 08-14
31 ÇÁ·ÎÇÊ·»(propylene, C3H6) ¿£Å»ÇÇ °ª (2) ¹®°æÈñ 07-31 3246 07-31
30 Control Valve ¼±Á¤½Ã NOR, MAX À¯·®°ú Â÷¾Ð ¹®ÀÇ (8) ÄÚ³¢¸® 07-26 5067 05-1
29 µî¿£Å»ÇÇ °úÁ¤°ú µî¿£Æ®·ÎÇÇ °úÁ¤ Â÷ÀÌÁ¡ Áú¹®µå¸³´Ï´Ù. (1) thermo 05-28 7238 05-31
28 isothermal flash¿Í adiabatic flashÀÇ Â÷ÀÌ (3) Æĸ£µ¥½º 02-13 3605 02-24
27 ºÐ¸®°øÁ¤ Áú¹®µå¸³´Ï´Ù. (2) ¸¶µ¿¾² 01-23 3656 01-24
26 È­ÇаøÇп¡¼­ FlashÀÇ Á¤È®ÇÑ Á¤ÀǸ¦ ¾Ë°í ½Í½À´Ï´Ù. (4) ¼Öºû 12-06 7437 12-07
25 ÀÀÃà¼ö ¹è°üÀÇ water hammer (4) greentea 11-01 5655 05-2
24 Á¦¾î°ü·Ã ¹®ÀÇ (1) ÃÖ³²ÀÚ 08-31 3862 08-31
23 »óÆòÇü °ü·Ã Áú¹®µå¸³´Ï´Ù (6) ¸¶µ¿¾² 08-02 28 08-19
22 Thermal expansion Case (PSV(TRV))¿¡ ´ëÇÑ ÁúÀÇ (2) °øÁ¤ÀǽÃÀÛ 04-26 8625 04-29
21 Tank³» ¿ëÁ¸ »ê¼Ò Á¦°Å ¹æ¹ý Áú¹®µå¸³´Ï´Ù !! (1) ENG»õ³»±â 04-17 4425 04-18
20 Crude Distillation Column °ü·Ã ¹®ÀÇ »çÇ× (6) °õµ¹ÀÌǪ 04-05 6453 04-11
19 Product Tank »óºÎ condenser Capacity È®ÀÎ (4) Ä«°Ô·Î¿ì 01-13 5144 01-19
18 ¿­±³È¯±â °ü·Ã Áú¹®µå¸³´Ï´Ù. (2) ¸çÄ¥µÚ¸é 08-14 5558 08-14
17 RO ¼³Ä¡ ½Ã Noise ¹× Cavitation ÇØ°á ¹æ¾È (4) °¾ 08-13 3880 08-13
16 ÆØâ¹ëºê¿¡ °üÇؼ­ ÇÑ°¡ÁöÁ» ¿©ÂÞ°Ú½À´Ï´Ù. ¤Ð¤Ð (4) ce_cm 08-10 4065 08-10
15 Control Valve Áú¹®. (1) È­°øÅ׸® 08-09 4156 08-09
14 Ethylene filling (2) ±³Åä 08-03 3871 08-03
13 ¾È³çÇϼ¼¿ä! off gas °ü·ÃÇÏ¿© Áú¹®µå¸³´Ï´Ù. (1) ÂÞ²Ù¹Ì 08-01 3503 08-01
12 Liquid choke flow ¿Í RO sizing (5) °¾ 07-29 8358 07-29
11 Deaerator Steam Flash·® °è»ê (1) È­°øÅ׸® 07-09 5767 07-09
10 Relieving temperature Áú¹®µå¸³´Ï´Ù. (5) ±³Åä 07-02 5444 06-29
9 PSV Two phase HEM orifice sizing¿¡¼­.. (4) °¾ 04-23 5543 04-23
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