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173 ÆßÇÁÀÇ Á¾·ù¿Í ¿ëµµ ¿î¿µÀÚ 02-01 18012 02-01
172 [¼ö·ÂÇÐ] Partially Filled Pipe Flow Calculation_MANNIN¡¦ ½ºÅׯijë 05-25 1512 05-2
171 [È­°ø] Typical Tray Efficiency of Distillation /Absorpt¡¦ ½ºÅׯijë 05-21 1652 05-2
170 [±¹Á¦Ç¥ÁØ] 2019³â º¯°æ ±¹Á¦Ç¥ÁØ ¹°¸®´ÜÀ§ÀÇ ±âÁØ ½ºÅׯijë 11-25 1408 11-2
169 [À¯Ã¼¿ªÇÐ] ÆßÇÁÀÇ NPSH ¸¶Áø (Typical NPSH Margins Recom¡¦ ½ºÅׯijë 11-08 2816 11-0
168 [È­°ø] ÀúÀåÅÊÅ© ¿­¼Õ½Ç °è»ê ¹× Steam Coil±æÀÌ ÃßÁ¤ ½ºÅׯijë 11-09 3567 11-09
167 [ROT] Shell & Tube ¿­±³È¯±â Tube °¹¼ö Àü¿­¸éÀû ÃßÁ¤Çϱâ (3) ½ºÅׯijë 10-17 3825 11-2
166 [ROT] ¿­±³È¯±â ±ÇÀåÀ¯¼Ó Recommended Shell and Tube Velo¡¦ ½ºÅׯijë 10-14 2642 10-14
165 [µ¿·Â] µ¿·Â = ¿¡³ÊÁö/½Ã°£ (5) ½ºÅׯijë 09-06 1903 11-1
164    [ȯ°æ] Æó¼öó¸®Àå ¹Ì»ý¹° À϶÷ Hamtouch 08-22 1068 08-22
163 [Àü±â] Motion Control Motor Types (1) ½ºÅׯijë 08-09 1272 08-09
162 [¹è°ü½Ç¹«] ¹è°ü¾Ð·Â¼Õ½Ç °è»ê ÀÚ·á (1) ½ºÅׯijë 07-11 3903 07-11
161 [±¹Á¦Ç¥ÁØ] Ç¥ÁØ»óÅÂ, Ç¥ÁØ´ë±â »óÅ (1) ½ºÅׯijë 11-10 3496 11-10
160 [È­°ø] Áø°ø ´©¼³·® °è»ê¹æ¹ý ½ºÅׯijë 10-05 4531 10-05
159    Economic pipe diameter for Liquid ÇÏ´ÃÀ»³¯°Å¡¦ 09-06 2402 09-06
158 [È­ÇÐ] Named Organic Reactions & Mechanisms - À¯±âÈ­ÇÐ ¡¦ ½ºÅׯijë 04-28 3616 04-28
157 [È­°ø] ÀÌ»ó±âüÀÇ ¹ýÄ¢°ú ÀÌ»ó±âü»ó¼ö (1) ½ºÅׯijë 01-13 5949 11-10
156       ³Ã°¢Å¾ ¼±Á¤¹æ¹ý ·Î¼¼ 12-09 2460 12-09
155    [¹°¸®] Çѱ¹ °íÀ¯ÀÇ ´ÜÀ§ (1) ½Ã´Þ 12-04 3173 01-13
154    ½ºÆÀÅͺó ´ÜÈ¿À² °è»ê¹æ¹ý HOHO 11-10 2752 11-10
153    ¹è°üÀÇ º¸¿Â°ú º¸³Ã ·¹µåk½ÇÀå 11-26 2850 11-26
152    Á¤À¯¼®À¯ÇÐÇаøÁ¤ ¼³¸í ¼ö¿ø±è»ó¹« 08-29 3289 08-29
151    ³Ã°¢Å¾ ¼±Á¤¹æ¹ý ±è»ç¶û½ÇÀå 05-28 3052 05-28
150    ¼¼°è ¿£Áö´Ï¾î CODE ¼Ò°³ ±è»ç¶û½ÇÀå 05-28 2781 05-28
149    ½ºÅÙ·¹½º°­ Ç¥±â¹æ¹ý ÇÑ¿ï¾Æºü 01-16 3033 01-16
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