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Control Valve Sizing¿¡ ´ëÇؼ Áú¹® »çÇ×ÀÌ ÀÖ½À´Ï´Ù.
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Ãʼø¼ö
08-06
3430
08-07
1104
Butterfly valve·Î À¯·®Á¶ÀýÇÒ ¶§ opening
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ÁÖ¿ìÁÖ¿õ
08-06
3098
08-07
1103
¾ÈÀü¹ëºê ¿ë·® °è»ê½Ã ÃàÀû¾Ð·Â Àû¿ë °ü·Ã
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±¸¹ß
08-06
3509
08-07
1102
Pro/ll Áõ·ùž ¼³°è¸¦ °øºÎÇÏ°í ÀÖ´Â ÇлýÀÔ´Ï´Ù. Áõ·ùž ¡¦
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08-07
3358
08-07
1101
IPA ¹®ÀÇ
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08-07
2581
08-07
1100
Pro/ii °øÁ¤¼³°è¸ð»ç±â heat exchanger
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08-07
3289
08-08
1099
±Û¸®¼¼·Ñ·ÎºÎÅÍ »ý¼ºµÇ´Â ¼ö¼Ò,¿¡Åº¿Ã °ü·Ã ½ÇÇè Áú¹®µå¸³¡¦
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08-08
2295
08-08
1098
cost estimation°ú design temperature
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08-08
5514
08-09
1097
pro/ii µ¹¸±¶§ dehydration°ú distillation °üÇÏ¿© Áú¹®ÇÕ¡¦
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08-04
2851
08-13
1096
HEAT EXCHANGER ÀÇ COST ESTIMATION ÀÌ ±Ã±ÀÇÕ´Ï´Ù.
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08-12
2470
08-13
1095
HS¿Í LSÀÇ Áõ¹ßÀá¿¿¡ °üÇؼ..
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08-12
3927
08-13
1094
Duty VS External Heat
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08-13
3227
08-14
1093
SC Pumping TrapÀÇ °³¼±»çÇ׿¡ ±Ã±ÝÁõÀÌ ÀÖ½À´Ï´Ù.
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¹Ì³ªÅäÀÚÅ°¡¦
08-13
7713
08-14
1092
compressor performance curve °ü·Ã Áú¹® µå¸³´Ï´Ù.
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pneuma
08-01
4302
08-15
1091
hydraulic complex factor Áú¹®ÀÔ´Ï´Ù.
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08-15
3073
08-16
1090
°øÁ¤°³¼±À» ÇÔ¿¡ ÀÖ¾î¼ ÀúÀÇ »ý°¢ÀÌ ÇÕ´çÇÑ°¡ ±Ã±ÝÇÕ´Ï´Ù.
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08-14
3159
08-16
1089
RO vs. FE(orifice type) °ü·Ã Áú¹®µå¸³´Ï´Ù.
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intheron
08-12
10912
08-20
1088
À¯Ã¼ÀÇ È帧 ¼Óµµ°è»ê
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khsvirgo
08-22
4953
08-22
1087
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08-24
1086
Distillation columnÀÇ Total, Partial vapor¿¡ ´ëÇÑ Áú¹®
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08-23
3729
08-24
1085
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Á¾ÇǸ®
08-24
2679
08-25
1084
Crude desulter system °ü·Ã Áú¹®
(11)
ÇÎÅ©¼ÖÆ®
08-19
3388
08-27
1083
FT(Flow Transmitter), LT(Level Transmitter) Type ¹× ves¡¦
(4)
pneuma
08-28
3185
08-28
1082
Aspen Plus¸¦ ÀÌ¿ëÇÑ radfrac reboiler ¿Âµµ Á¶Àý¿¡ °üÇÏ¿©
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neo
08-08
3299
08-29
1081
Aspen simulation ÁøÇà ½Ã components ¼±Á¤ ÁúÀÇ
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¾¾¾çÀÌÁú
08-28
3028
08-29
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