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173 ÆßÇÁÀÇ Á¾·ù¿Í ¿ëµµ ¿î¿µÀÚ 02-01 19185 02-01
172 [À¯Ã¼¿ªÇÐ] Darcy's Friction Factor ±¸Çϱ⠽ºÅ×Æijë 03-05 168 03-0
171 [¼ö·ÂÇÐ] Partially Filled Pipe Flow Calculation_MANNIN¡¦ ½ºÅ×Æijë 05-25 2780 05-2
170 [È­°ø] Typical Tray Efficiency of Distillation /Absorpt¡¦ ½ºÅ×Æijë 05-21 2944 05-2
169 [±¹Á¦Ç¥ÁØ] 2019³â º¯°æ ±¹Á¦Ç¥ÁØ ¹°¸®´ÜÀ§ÀÇ ±âÁØ ½ºÅ×Æijë 11-25 2561 11-2
168 [À¯Ã¼¿ªÇÐ] ÆßÇÁÀÇ NPSH ¸¶Áø (Typical NPSH Margins Recom¡¦ ½ºÅ×Æijë 11-08 4439 11-0
167 [È­°ø] ÀúÀåÅÊÅ© ¿­¼Õ½Ç °è»ê ¹× Steam Coil±æÀÌ ÃßÁ¤ (1) ½ºÅ×Æijë 11-09 5478 11-09
166 [ROT] Shell & Tube ¿­±³È¯±â Tube °¹¼ö Àü¿­¸éÀû ÃßÁ¤Çϱâ (3) ½ºÅ×Æijë 10-17 5329 11-2
165 [ROT] ¿­±³È¯±â ±ÇÀåÀ¯¼Ó Recommended Shell and Tube Velo¡¦ ½ºÅ×Æijë 10-14 3934 10-14
164 [µ¿·Â] µ¿·Â = ¿¡³ÊÁö/½Ã°£ (5) ½ºÅ×Æijë 09-06 2807 11-1
163    [ȯ°æ] Æó¼öó¸®Àå ¹Ì»ý¹° À϶÷ Hamtouch 08-22 2080 08-22
162 [Àü±â] Motion Control Motor Types (1) ½ºÅ×Æijë 08-09 2279 08-09
161 [¹è°ü½Ç¹«] ¹è°ü¾Ð·Â¼Õ½Ç °è»ê ÀÚ·á (1) ½ºÅ×Æijë 07-11 5627 07-11
160 [±¹Á¦Ç¥ÁØ] Ç¥ÁØ»óÅÂ, Ç¥ÁØ´ë±â »óÅ (1) ½ºÅ×Æijë 11-10 4811 11-10
159 [È­°ø] Áø°ø ´©¼³·® °è»ê¹æ¹ý ½ºÅ×Æijë 10-05 5933 10-05
158    Economic pipe diameter for Liquid ÇÏ´ÃÀ»³¯°Å¡¦ 09-06 3262 09-06
157 [È­ÇÐ] Named Organic Reactions & Mechanisms - À¯±âÈ­ÇÐ ¡¦ ½ºÅ×Æijë 04-28 4821 04-28
156 [È­°ø] ÀÌ»ó±âüÀÇ ¹ýÄ¢°ú ÀÌ»ó±âü»ó¼ö (1) ½ºÅ×Æijë 01-13 7400 11-10
155       ³Ã°¢Å¾ ¼±Á¤¹æ¹ý ·Î¼¼ 12-09 3373 12-09
154    [¹°¸®] Çѱ¹ °íÀ¯ÀÇ ´ÜÀ§ (1) ½Ã´Þ 12-04 4310 01-13
153    ½ºÆÀÅͺó ´ÜÈ¿À² °è»ê¹æ¹ý HOHO 11-10 3726 11-10
152    ¹è°üÀÇ º¸¿Â°ú º¸³Ã ·¹µåk½ÇÀå 11-26 3809 11-26
151    Á¤À¯¼®À¯ÇÐÇаøÁ¤ ¼³¸í ¼ö¿ø±è»ó¹« 08-29 4328 08-29
150    ³Ã°¢Å¾ ¼±Á¤¹æ¹ý ±è»ç¶û½ÇÀå 05-28 3961 05-28
149    ¼¼°è ¿£Áö´Ï¾î CODE ¼Ò°³ ±è»ç¶û½ÇÀå 05-28 3675 05-28
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