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173 [À¯Ã¼¿ªÇÐ] Darcy's Friction Factor ±¸Çϱ⠽ºÅ×Æijë 03-05 1026 03-0
172 [¼ö·ÂÇÐ] Partially Filled Pipe Flow Calculation_MANNIN¡¦ ½ºÅ×Æijë 05-25 3607 05-2
171 [È­°ø] Typical Tray Efficiency of Distillation /Absorpt¡¦ ½ºÅ×Æijë 05-21 3810 05-2
170 [±¹Á¦Ç¥ÁØ] 2019³â º¯°æ ±¹Á¦Ç¥ÁØ ¹°¸®´ÜÀ§ÀÇ ±âÁØ ½ºÅ×Æijë 11-25 3368 11-2
169 [À¯Ã¼¿ªÇÐ] ÆßÇÁÀÇ NPSH ¸¶Áø (Typical NPSH Margins Recom¡¦ ½ºÅ×Æijë 11-08 5483 11-0
168 [È­°ø] ÀúÀåÅÊÅ© ¿­¼Õ½Ç °è»ê ¹× Steam Coil±æÀÌ ÃßÁ¤ (1) ½ºÅ×Æijë 11-09 6926 11-0
167 [ROT] Shell & Tube ¿­±³È¯±â Tube °¹¼ö Àü¿­¸éÀû ÃßÁ¤Çϱâ (3) ½ºÅ×Æijë 10-17 6247 10-1
166 [ROT] ¿­±³È¯±â ±ÇÀåÀ¯¼Ó Recommended Shell and Tube Velo¡¦ ½ºÅ×Æijë 10-14 4934 10-1
165 [µ¿·Â] µ¿·Â = ¿¡³ÊÁö/½Ã°£ (5) ½ºÅ×Æijë 09-06 3562 09-0
164 [Àü±â] Motion Control Motor Types (1) ½ºÅ×Æijë 08-09 3408 08-0
163 [¹è°ü½Ç¹«] ¹è°ü¾Ð·Â¼Õ½Ç °è»ê ÀÚ·á (1) ½ºÅ×Æijë 07-11 6949 07-1
162 [±¹Á¦Ç¥ÁØ] Ç¥ÁØ»óÅÂ, Ç¥ÁØ´ë±â »óÅ (1) ½ºÅ×Æijë 11-10 5893 11-1
161 [È­°ø] ÀÌ»ó±âüÀÇ ¹ýÄ¢°ú ÀÌ»ó±âü»ó¼ö (1) ½ºÅ×Æijë 01-13 8536 01-1
160 [È­°ø] Áø°ø ´©¼³·® °è»ê¹æ¹ý ½ºÅ×Æijë 10-05 6960 10-0
159 [È­ÇÐ] Named Organic Reactions & Mechanisms - À¯±âÈ­ÇÐ ¡¦ ½ºÅ×Æijë 04-28 5728 04-2
158 [Àü±â] Àü±â±âÃÊ ÀÌ·Ð Á¤¸® ÃÖ°í°ü¸®ÀÚ 01-29 26617 01-2
157 [ȯ°æ] Water Á¾·ù (1) ÃÖ°í°ü¸®ÀÚ 01-29 21623 01-2
156 [ȯ°æ] DO/BOD/COD ¿ë¾î ¼³¸í (1) ÃÖ°í°ü¸®ÀÚ 01-29 17072 01-2
155 [Àü±â] ¼¼°èÀÇ Àü¾Ð ÇöȲ ÃÖ°í°ü¸®ÀÚ 01-29 16287 01-2
154 [¹°¸®] °øÇдÜÀ§ ȯ»êÀ϶÷Ç¥ (1) ÃÖ°í°ü¸®ÀÚ 01-29 18999 01-2
153    [¹°¸®] °øÇдÜÀ§ ȯ»êÀ϶÷Ç¥ ·Ô°Ç°øÁ¤ 07-05 8537 07-0
152 [¹°¸®] Çѱ¹ °íÀ¯ÀÇ ´ÜÀ§ (1) ÃÖ°í°ü¸®ÀÚ 01-29 13017 01-2
151    [¹°¸®] Çѱ¹ °íÀ¯ÀÇ ´ÜÀ§ (1) ½Ã´Þ 12-04 5152 12-0
150 [ȯ°æ] ¹°ÀÇ °æ¼ö¿Í ¿¬¼ö Á¤¸® (1) ÃÖ°í°ü¸®ÀÚ 01-29 15094 01-2
149 [¹°¸®] Çؼö¸é»óÀÇ Ç¥ÁØ´ë±âÀÇ ±âº»Æ¯¼ºÄ¡ ÃÖ°í°ü¸®ÀÚ 01-29 12014 01-2
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