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173 [¼ö·ÂÇÐ] Partially Filled Pipe Flow Calculation_MANNIN¡¦ ½ºÅׯijë 05-25 2271 05-2
172 [È­°ø] Typical Tray Efficiency of Distillation /Absorpt¡¦ ½ºÅׯijë 05-21 2380 05-2
171 [±¹Á¦Ç¥ÁØ] 2019³â º¯°æ ±¹Á¦Ç¥ÁØ ¹°¸®´ÜÀ§ÀÇ ±âÁØ ½ºÅׯijë 11-25 2070 11-2
170 [À¯Ã¼¿ªÇÐ] ÆßÇÁÀÇ NPSH ¸¶Áø (Typical NPSH Margins Recom¡¦ ½ºÅׯijë 11-08 3762 11-0
169 [È­°ø] ÀúÀåÅÊÅ© ¿­¼Õ½Ç °è»ê ¹× Steam Coil±æÀÌ ÃßÁ¤ ½ºÅׯijë 11-09 4543 11-09
168 [ROT] Shell & Tube ¿­±³È¯±â Tube °¹¼ö Àü¿­¸éÀû ÃßÁ¤Çϱâ (3) ½ºÅׯijë 10-17 4776 11-2
167 [ROT] ¿­±³È¯±â ±ÇÀåÀ¯¼Ó Recommended Shell and Tube Velo¡¦ ½ºÅׯijë 10-14 3376 10-14
166 [µ¿·Â] µ¿·Â = ¿¡³ÊÁö/½Ã°£ (5) ½ºÅׯijë 09-06 2387 11-1
165 [Àü±â] Motion Control Motor Types (1) ½ºÅׯijë 08-09 1814 08-09
164 [¹è°ü½Ç¹«] ¹è°ü¾Ð·Â¼Õ½Ç °è»ê ÀÚ·á (1) ½ºÅׯijë 07-11 4947 07-11
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162 [È­°ø] ÀÌ»ó±âüÀÇ ¹ýÄ¢°ú ÀÌ»ó±âü»ó¼ö (1) ½ºÅׯijë 01-13 6764 11-10
161 [È­°ø] Áø°ø ´©¼³·® °è»ê¹æ¹ý ½ºÅׯijë 10-05 5328 10-05
160 [È­ÇÐ] Named Organic Reactions & Mechanisms - À¯±âÈ­ÇÐ ¡¦ ½ºÅׯijë 04-28 4270 04-28
159 [Àü±â] Àü±â±âÃÊ ÀÌ·Ð Á¤¸® ÃÖ°í°ü¸®ÀÚ 01-29 25043 01-29
158 [ȯ°æ] Water Á¾·ù (1) ÃÖ°í°ü¸®ÀÚ 01-29 19972 01-29
157 [ȯ°æ] DO/BOD/COD ¿ë¾î ¼³¸í (1) ÃÖ°í°ü¸®ÀÚ 01-29 15664 01-29
156 [Àü±â] ¼¼°èÀÇ Àü¾Ð ÇöȲ ÃÖ°í°ü¸®ÀÚ 01-29 14891 01-29
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154    [¹°¸®] °øÇдÜÀ§ ȯ»êÀ϶÷Ç¥ ·Ô°Ç°øÁ¤ 07-05 7074 07-05
153 [¹°¸®] Çѱ¹ °íÀ¯ÀÇ ´ÜÀ§ (1) ÃÖ°í°ü¸®ÀÚ 01-29 11569 01-29
152    [¹°¸®] Çѱ¹ °íÀ¯ÀÇ ´ÜÀ§ (1) ½Ã´Þ 12-04 3724 01-13
151 [ȯ°æ] ¹°ÀÇ °æ¼ö¿Í ¿¬¼ö Á¤¸® (1) ÃÖ°í°ü¸®ÀÚ 01-29 13644 01-29
150 [¹°¸®] ÇØ¼ö¸é»óÀÇ Ç¥ÁØ´ë±âÀÇ ±âº»Æ¯¼ºÄ¡ ÃÖ°í°ü¸®ÀÚ 01-29 10174 01-29
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