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173 ÆßÇÁÀÇ Á¾·ù¿Í ¿ëµµ ¿î¿µÀÚ 02-01 19207 02-01
172 [À¯Ã¼¿ªÇÐ] Darcy's Friction Factor ±¸Çϱ⠽ºÅ×Æijë 03-05 196 03-0
171 ¹ëºêÀÇ Á¾·ù (7) ¿î¿µÀÚ 08-07 17019 12-3
170 [ROT] Shell & Tube ¿­±³È¯±â Tube °¹¼ö Àü¿­¸éÀû ÃßÁ¤Çϱâ (3) ½ºÅ×Æijë 10-17 5360 11-2
169 ¾Ð·Â¿ë±â °³¿ä (1) ¿î¿µÀÚ 00-00 15985 06-2
168 Á¤À¯¼®À¯ÇÐÇаøÁ¤ ¼³¸í (6) ¿î¿µÀÚ 03-25 12624 06-1
167 À¯·®°è»êÀ» ÅëÇÑ Valve Sizing (4) ¿î¿µÀÚ 00-00 14901 05-2
166 Darcy-Weisbach Formula ±â¼úÀÚ·á (1) ¿î¿µÀÚ 08-07 11481 08-1
165 [È­°ø] Typical Tray Efficiency of Distillation /Absorpt¡¦ ½ºÅ×Æijë 05-21 2974 05-2
164 [¼ö·ÂÇÐ] Partially Filled Pipe Flow Calculation_MANNIN¡¦ ½ºÅ×Æijë 05-25 2809 05-2
163 [±¹Á¦Ç¥ÁØ] 2019³â º¯°æ ±¹Á¦Ç¥ÁØ ¹°¸®´ÜÀ§ÀÇ ±âÁØ ½ºÅ×Æijë 11-25 2593 11-2
162 [µ¿·Â] µ¿·Â = ¿¡³ÊÁö/½Ã°£ (5) ½ºÅ×Æijë 09-06 2823 11-1
161 [À¯Ã¼¿ªÇÐ] ÆßÇÁÀÇ NPSH ¸¶Áø (Typical NPSH Margins Recom¡¦ ½ºÅ×Æijë 11-08 4472 11-0
160 [È­°ø] ÀúÀåÅÊÅ© ¿­¼Õ½Ç °è»ê ¹× Steam Coil±æÀÌ ÃßÁ¤ (1) ½ºÅ×Æijë 11-09 5542 11-09
159 [ROT] ¿­±³È¯±â ±ÇÀåÀ¯¼Ó Recommended Shell and Tube Velo¡¦ ½ºÅ×Æijë 10-14 3967 10-14
158    [ȯ°æ] Æó¼öó¸®Àå ¹Ì»ý¹° À϶÷ Hamtouch 08-22 2095 08-22
157 [Àü±â] Motion Control Motor Types (1) ½ºÅ×Æijë 08-09 2302 08-09
156 [¹è°ü½Ç¹«] ¹è°ü¾Ð·Â¼Õ½Ç °è»ê ÀÚ·á (1) ½ºÅ×Æijë 07-11 5666 07-11
155 [Àü±â] ±×¸²°ú ÇÔ²²ÇÑ Ohm's Law (2) ÃÖ°í°ü¸®ÀÚ 01-29 12526 11-17
154 [È­°ø] ÀÌ»ó±âüÀÇ ¹ýÄ¢°ú ÀÌ»ó±âü»ó¼ö (1) ½ºÅ×Æijë 01-13 7425 11-10
153 [±¹Á¦Ç¥ÁØ] Ç¥ÁØ»óÅÂ, Ç¥ÁØ´ë±â »óÅ (1) ½ºÅ×Æijë 11-10 4849 11-10
152 [È­°ø] Áø°ø ´©¼³·® °è»ê¹æ¹ý ½ºÅ×Æijë 10-05 5956 10-05
151    Economic pipe diameter for Liquid ÇÏ´ÃÀ»³¯°Å¡¦ 09-06 3271 09-06
150 [È­ÇÐ] Named Organic Reactions & Mechanisms - À¯±âÈ­ÇÐ ¡¦ ½ºÅ×Æijë 04-28 4841 04-28
149    [¹°¸®] Çѱ¹ °íÀ¯ÀÇ ´ÜÀ§ (1) ½Ã´Þ 12-04 4334 01-13
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