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173 [À¯Ã¼¿ªÇÐ] Darcy's Friction Factor ±¸Çϱ⠽ºÅ×Æijë 03-05 100 03-0
172 [¼ö·ÂÇÐ] Partially Filled Pipe Flow Calculation_MANNIN¡¦ ½ºÅ×Æijë 05-25 2699 05-2
171 [È­°ø] Typical Tray Efficiency of Distillation /Absorpt¡¦ ½ºÅ×Æijë 05-21 2861 05-2
170 [±¹Á¦Ç¥ÁØ] 2019³â º¯°æ ±¹Á¦Ç¥ÁØ ¹°¸®´ÜÀ§ÀÇ ±âÁØ ½ºÅ×Æijë 11-25 2480 11-2
169 [À¯Ã¼¿ªÇÐ] ÆßÇÁÀÇ NPSH ¸¶Áø (Typical NPSH Margins Recom¡¦ ½ºÅ×Æijë 11-08 4319 11-0
168 [È­°ø] ÀúÀåÅÊÅ© ¿­¼Õ½Ç °è»ê ¹× Steam Coil±æÀÌ ÃßÁ¤ (1) ½ºÅ×Æijë 11-09 5323 11-09
167 [ROT] Shell & Tube ¿­±³È¯±â Tube °¹¼ö Àü¿­¸éÀû ÃßÁ¤Çϱâ (3) ½ºÅ×Æijë 10-17 5237 11-2
166 [ROT] ¿­±³È¯±â ±ÇÀåÀ¯¼Ó Recommended Shell and Tube Velo¡¦ ½ºÅ×Æijë 10-14 3849 10-14
165 [µ¿·Â] µ¿·Â = ¿¡³ÊÁö/½Ã°£ (5) ½ºÅ×Æijë 09-06 2731 11-1
164 [Àü±â] Motion Control Motor Types (1) ½ºÅ×Æijë 08-09 2205 08-09
163 [¹è°ü½Ç¹«] ¹è°ü¾Ð·Â¼Õ½Ç °è»ê ÀÚ·á (1) ½ºÅ×Æijë 07-11 5517 07-11
162 [±¹Á¦Ç¥ÁØ] Ç¥ÁØ»óÅÂ, Ç¥ÁØ´ë±â »óÅ (1) ½ºÅ×Æijë 11-10 4726 11-10
161 [È­°ø] ÀÌ»ó±âüÀÇ ¹ýÄ¢°ú ÀÌ»ó±âü»ó¼ö (1) ½ºÅ×Æijë 01-13 7278 11-10
160 [È­°ø] Áø°ø ´©¼³·® °è»ê¹æ¹ý ½ºÅ×Æijë 10-05 5833 10-05
159 [È­ÇÐ] Named Organic Reactions & Mechanisms - À¯±âÈ­ÇÐ ¡¦ ½ºÅ×Æijë 04-28 4740 04-28
158 [Àü±â] Àü±â±âÃÊ ÀÌ·Ð Á¤¸® ÃÖ°í°ü¸®ÀÚ 01-29 25566 01-29
157 [ȯ°æ] Water Á¾·ù (1) ÃÖ°í°ü¸®ÀÚ 01-29 20505 01-29
156 [ȯ°æ] DO/BOD/COD ¿ë¾î ¼³¸í (1) ÃÖ°í°ü¸®ÀÚ 01-29 16140 01-29
155 [Àü±â] ¼¼°èÀÇ Àü¾Ð ÇöȲ ÃÖ°í°ü¸®ÀÚ 01-29 15353 01-29
154 [¹°¸®] °øÇдÜÀ§ ȯ»êÀ϶÷Ç¥ (1) ÃÖ°í°ü¸®ÀÚ 01-29 17999 01-29
153    [¹°¸®] °øÇдÜÀ§ ȯ»êÀ϶÷Ç¥ ·Ô°Ç°øÁ¤ 07-05 7563 07-05
152 [¹°¸®] Çѱ¹ °íÀ¯ÀÇ ´ÜÀ§ (1) ÃÖ°í°ü¸®ÀÚ 01-29 12059 01-29
151    [¹°¸®] Çѱ¹ °íÀ¯ÀÇ ´ÜÀ§ (1) ½Ã´Þ 12-04 4222 01-13
150 [ȯ°æ] ¹°ÀÇ °æ¼ö¿Í ¿¬¼ö Á¤¸® (1) ÃÖ°í°ü¸®ÀÚ 01-29 14150 01-29
149 [¹°¸®] Çؼö¸é»óÀÇ Ç¥ÁØ´ë±âÀÇ ±âº»Æ¯¼ºÄ¡ ÃÖ°í°ü¸®ÀÚ 01-29 10661 01-29
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