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6074 Distillation columnÀÇ Total, Partial vapor¿¡ ´ëÇÑ Áú¹® (3) Kininarima¡¦ 08-23 3582 08-24
6073 ÀÌ·± Áú¹®À» µå¸®°í ½Í³×¿ä..¹ÝÇÕ¼º¼¶À¯¸¦ ¸¸µå´Â ÀÌÀ¯.. (3) ¾Æ¿ö³Ê Äù¡¦ 00-00 5761 08-24
6072 À¯Ã¼ÀÇ È帧 ¼Óµµ°è»ê (1) khsvirgo 08-22 4705 08-22
6071 RO vs. FE(orifice type) °ü·Ã Áú¹®µå¸³´Ï´Ù. (37) intheron 08-12 10831 08-20
6070 °øÁ¤°³¼±À» ÇÔ¿¡ À־ ÀúÀÇ »ý°¢ÀÌ ÇÕ´çÇÑ°¡ ±Ã±ÝÇÕ´Ï´Ù. (3) ¹Ì³ªÅäÀÚÅ°¡¦ 08-14 3058 08-16
6069 hydraulic complex factor Áú¹®ÀÔ´Ï´Ù. (2) rndtkdwlwl¡¦ 08-15 2976 08-16
6068 compressor performance curve °ü·Ã Áú¹® µå¸³´Ï´Ù. (2) pneuma 08-01 4067 08-15
6067 SC Pumping TrapÀÇ °³¼±»çÇ׿¡ ±Ã±ÝÁõÀÌ ÀÖ½À´Ï´Ù. (17) ¹Ì³ªÅäÀÚÅ°¡¦ 08-13 7558 08-14
6066 Duty VS External Heat (5) ¾ö¸¶³ªµµ¼­¡¦ 08-13 3094 08-14
6065 HS¿Í LSÀÇ Áõ¹ßÀá¿­¿¡ °üÇؼ­.. (7) ¹Ì³ªÅäÀÚÅ°¡¦ 08-12 3771 08-13
6064 HEAT EXCHANGER ÀÇ COST ESTIMATION ÀÌ ±Ã±ÀÇÕ´Ï´Ù. (1) ¾È´¨¾È´¨ 08-12 2379 08-13
6063 pro/ii µ¹¸±¶§ dehydration°ú distillation °üÇÏ¿© Áú¹®ÇÕ¡¦ (4) ¾È´¨¾È´¨ 08-04 2740 08-13
6062 cost estimation°ú design temperature (1) ¾È´¨¾È´¨ 08-08 5371 08-09
6061 ±Û¸®¼¼·Ñ·ÎºÎÅÍ »ý¼ºµÇ´Â ¼ö¼Ò,¿¡Åº¿Ã °ü·Ã ½ÇÇè Áú¹®µå¸³¡¦ (1) Á¾ÇǸ® 08-08 2206 08-08
6060 Pro/ii °øÁ¤¼³°è¸ð»ç±â heat exchanger (2) ¾ö¸¶³ªµµ¼­¡¦ 08-07 3188 08-08
6059 IPA ¹®ÀÇ (1) ´õºí¸®À¯ 08-07 2477 08-07
6058 Pro/ll Áõ·ùž ¼³°è¸¦ °øºÎÇÏ°í ÀÖ´Â ÇлýÀÔ´Ï´Ù. Áõ·ùž ¡¦ (2) ¿ë»ó¾Æ¸® 08-07 3177 08-07
6057 ¾ÈÀü¹ëºê ¿ë·® °è»ê½Ã ÃàÀû¾Ð·Â Àû¿ë °ü·Ã (1) ±¸¹ß 08-06 3373 08-07
6056 Butterfly valve·Î À¯·®Á¶ÀýÇÒ ¶§ opening (1) ÁÖ¿ìÁÖ¿õ 08-06 2965 08-07
6055 Control Valve Sizing¿¡ ´ëÇؼ­ Áú¹® »çÇ×ÀÌ ÀÖ½À´Ï´Ù. (2) Ãʼø¼ö 08-06 3305 08-07
6054 °áÇÕÂ÷¼ö ¹×, ÀüÀÚ¹èÄ¡ °ü·Ã Áú¹®ÀÔ´Ï´Ù^^; (2) Á¤Ç๮ 10-16 7773 08-05
6053 ReactorÀÇ CostingÀ» ÇÏ´Â ¹æ¹ý¿¡¼­ Àǹ®ÀÌ »ý°Ü Áú¹®µå¸³¡¦ (5) °øÁ¤ÃÖÀûÈ­ 08-02 3323 08-03
6052 pro/ii¿¡¼­ column size¸¦ ¾îµð¼­ È®ÀÎÇÒ ¼ö ÀÖ´ÂÁö ±Ã±ÝÇÕ¡¦ (1) Áî¿ÀÃ÷¸® 08-01 2840 08-01
6051 water seal Áø°øÆßÇÁ Áú¹®µå¸³´Ï´Ù. (2) Á¾ÇǸ® 08-01 4196 08-01
6050 ÇÁ·ÎÇÊ·»(propylene, C3H6) ¿£Å»ÇÇ °ª (2) ¹®°æÈñ 07-31 3135 07-31
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