| *Critical Factors for the Industrial Application of Catalysis 1. Chemoselectivity, regioselectivity and enantioselectivity (Ratio (by weight) of the by-products to the desired product) 2. Catalyst productivit | ||
| Ä«Å×°í¸®: Àü¹®ÀÚ·á > ¼¼¹Ì³ªÀÚ·á > Àü¹®Çмú ¤Ó µî·ÏÀÏ: 2004/08/26 ¤Ó µî·ÏÀÚ: realseminar ¤Ó Æò°¡¾øÀ½ | ||
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| *¿Ü±¹ÀÇ ÇöȲ -¹Ì±¹, À¯·´, ÀϺ»ÀÇ ±â¼ú ¼±Áø±¹µéÀº µµÀå±â±â ¹× ¼³ºñÀÇ Àú°øÇØÈ, °íÈ¿À²È, ¿¡³ÊÁö Àý¾à ¿¡ ÁÖ·Â -Àü¹®¾÷ü:±×·¹ÀÌÄÚ, ³ëµå½¼, ¿Í±×³Ê, À̿͟ µî ±¹³» ÇöȲ -Ãë¾àÇÑ ±â¼ú ±â¹Ý ¿Ü±¹ Á¦Ç°ÀÇ ¸ð¹æ ¹× ¿ª¼³°è ÀúºÎ°¡°¡Ä¡ÀÇ µµÀå±â±â¸¸ ±¹»êȵǰí, °í°¡ ¹× °í¼º´ÉÀÇ µµÀå ±â±â´Â Àü·® ¼öÀÔ ±¹³» µ¶ÀÚ | ||
| Ä«Å×°í¸®: Àü¹®ÀÚ·á > ¼¼¹Ì³ªÀÚ·á > Àü¹®Çмú ¤Ó µî·ÏÀÏ: 2004/08/26 ¤Ó µî·ÏÀÚ: realseminar ¤Ó Æò°¡¾øÀ½ | ||
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| *±âÁ¸³¯¿°°øÁ¤ *ºñÈ¿À²ÀûÀÎ ÀÛ¾÷ °øÁ¤ Àå±â°£ÀÇ »ùÇÃ/½ÃÁ¦Ç° »ý»ê °úÁ¤ ½Å»óǰ ½ÃÀå »çÀüÁ¶»ç ºÎÁ· ½ÃÁð ÈÄ °úµµÇÑ Àç°í ºÎ´ã/°¡°Ý Ç϶ô °í°´ ¿ä±¸»çÇ×ÀÇ ´ëÀÀ·Â ºÎÁ· ´Ù¾çÇÑ µðÀÚÀÎ »ùÇà »ý»ê ´ÙǰÁ¾ ¼Ò·® ÁÖ¹® Áõ°¡ | ||
| Ä«Å×°í¸®: Àü¹®ÀÚ·á > ¼¼¹Ì³ªÀÚ·á > Àü¹®Çмú ¤Ó µî·ÏÀÏ: 2004/08/26 ¤Ó µî·ÏÀÚ: realseminar ¤Ó Æò°¡¾øÀ½ | ||
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| *¿¬±¸µ¿Çâ -Calvert µî(1998)Àº Àý»èÀ¯¿Í °ü·ÃµÈ ¾Ï¹ß»ý¿¡ ´ëÇÑ 40¿©Æí ÀÌ»óÀÇ ¿ªÇבּ¸ °á°úµéÀ» Á¾ÇÕÀûÀ¸·Î °íÂûÇÑ °á°ú ÈĵÎ(larynx), Á÷Àå(rectum), ÃéÀå(pancreas), ÇǺÎ(skin), À½³¶(scrotum), ¹æ±¤(bladder)¿¡¼ÀÇ ¾Ï¹ß»ý°ú À¯ÀÇÇÑ °ü°è°¡ ÀÖ´Ù°í ºÐ¼®ÇÔ. -1998³â NIOSHµµ "Criteria for a Recomm | ||
| Ä«Å×°í¸®: Àü¹®ÀÚ·á > ¼¼¹Ì³ªÀÚ·á > Àü¹®Çмú ¤Ó µî·ÏÀÏ: 2004/08/26 ¤Ó µî·ÏÀÚ: realseminar ¤Ó ±¸¸ÅÆò°¡ D | ||
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| º» ½ÇÇèÀÇ °á°ú·ÎºÎÅÍ ´ÙÀ½°ú °°Àº °á·ÐÀ» ¾òÀ» ¼ö ÀÖ¾ú´Ù. °ðÀº ¿øÅëÇü ±â°øÀ» °®´Â ºÐ¸®¸·¿¡¼ O/W ¿¡¸ÖÁ¯ÀÇ ºÐ¸®¸· Åõ°ú¿µ¿ªÀº ¼¼ ºÎºÐÀ¸·Î ³ª´ ¼ö ÀÖ´Ù. ¸ÕÀú Àú¾Ð ¿µ¿ªÀÇ °æ¿ì, ÀϹÝÀûÀÎ ºñº¯Çü¼º ÀÔÀÚÀÇ ºÐ¸®¸· Åõ°ú°Åµ¿À» µû¸¥´Ù. ÀÌ °æ¿ì ºÐ¸®¸·ÀÇ Ç¥¸é¿¡ ÃàÀûµÇ´Â O/W ¿¡¸ÖÁ¯ÀÌ »óÀüÀ̰¡ ÀϾÁö ¾ÊÀ» Á¤µµÀÇ ÃæÀü ¹Ðµµ¸¦ °¡Á®¾ß ÇϹǷΠ¸Å¿ì ³·Àº ¿îÀü¾Ð·Â ¹üÀ§°¡ µÇ¾ú´Ù | ||
| Ä«Å×°í¸®: Àü¹®ÀÚ·á > ¼¼¹Ì³ªÀÚ·á > Àü¹®Çмú ¤Ó µî·ÏÀÏ: 2004/08/26 ¤Ó µî·ÏÀÚ: realseminar ¤Ó Æò°¡¾øÀ½ | ||
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| *Membrane Separation Technology Filtration Membrane Dialysis Affinity Membrane Bio Membrane Membrane Contactor Facilitated Transport Membrane Membrane Reactor *Summary of Membrane Contactor Processes M | ||
| Ä«Å×°í¸®: Àü¹®ÀÚ·á > ¼¼¹Ì³ªÀÚ·á > Àü¹®Çмú ¤Ó µî·ÏÀÏ: 2004/08/26 ¤Ó µî·ÏÀÚ: realseminar ¤Ó Æò°¡¾øÀ½ | ||
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| *Membrane contactor processes • Membrane Absortion(MA)/Desorption(MD) - Gas absorption and stripping(CO2, SO2, H2S, NH3 • • •.) - Supercritical extraction - Waste water treatment • Me | ||
| Ä«Å×°í¸®: Àü¹®ÀÚ·á > ¼¼¹Ì³ªÀÚ·á > Àü¹®Çмú ¤Ó µî·ÏÀÏ: 2004/08/26 ¤Ó µî·ÏÀÚ: realseminar ¤Ó Æò°¡¾øÀ½ | ||
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| *1976 Kalundborg -Industrial symbiosis web of materials and energy exchanges among companies (and with the community) has developed since 1976 in Kalundborg, Denmark. -Originally, the motivation behind most o | ||
| Ä«Å×°í¸®: Àü¹®ÀÚ·á > ¼¼¹Ì³ªÀÚ·á > Àü¹®Çмú ¤Ó µî·ÏÀÏ: 2004/08/25 ¤Ó µî·ÏÀÚ: realseminar ¤Ó Æò°¡¾øÀ½ | ||
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| *µµ±ÝÀ̶õ? Ç¥¸é󸮾÷ÀÇ ÀÏÁ¾À¸·Î¼ ÁÖ·Î ½À½Ä¹ý¿¡ ÀÇÇØ Àü±âÀû ȤÀº ÈÇÐÀû ¿¡³ÊÁö¸¦ Ȱ¿ëÇÏ¿© ¼ÒÀçÀÇ Ç¥¸é¿¡ ¼ö ³»Áö ¼ö½Ê ¸¶ÀÌÅ©·Ð µÎ²²ÀÇ ±Ý¼Ó ¹Ú¸·À» ¾ò´Â °øÁ¤ÀÌ´Ù. *µµ±ÝÀÇ ¸ñÀû Á¦Ç°ÀÇ ¼ö¸í ¿¬Àå, ³»½Ä¼º µîÀÇ ±â´É ºÎ¿©, ¿Ü°ü °³¼± µî. *µµ±Ý »ê¾÷ÀÇ Æ¯Â¡ -¼³ºñ ÅõÀÚ Àû°í, °¡°ø ¾àÁ¦¸¦ ºñ·ÔÇÑ ¿î¿µºñ°¡ Å©´Ù. -ÀÛ¾÷ȯ°æÀ̳ª ȯ°æ¿¡ ´ëÇÑ ÀνÄÀÌ ¿¾ÇÇÏ¿© ´ë°³ | ||
| Ä«Å×°í¸®: Àü¹®ÀÚ·á > ¼¼¹Ì³ªÀÚ·á > Àü¹®Çмú ¤Ó µî·ÏÀÏ: 2004/08/25 ¤Ó µî·ÏÀÚ: realseminar ¤Ó ±¸¸ÅÆò°¡ C | ||
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| ÀϹÝÀûÀ¸·Î ¼¾¹°(Ìãâ©, h ar d wat er )Àº °ÅǰÀ» ³»´Âµ¥ ¸¹Àº ¾çÀÇ ºñ´©¸¦ ÇÊ¿ä·Î Çϸç, ¶Ç ¿Â¼ö ÆÄÀÌÇÁ, ³¹æÀåÄ¡, º¸ÀÏ·¯¿Í ±âŸ ¹°ÀÇ ¿Âµµ¸¦ Å©°Ô ¿Ã¸®´Â µ¥ »ç¿ëÇÏ´Â ÀåÄ¡¿¡ ½ºÄÉÀÏÀ» »ý¼ºÇÏ´Â ¹°À» ÀÏÄ´´Ù. ÀϹÝÀο¡°Ô´Â °æÁ¦ÀûÀÎ Ãø¸éÀ̳ª ¼¼Å¹À» ÇÒ ¶§ °Þ°Ô µÇ´Â °ï¶õ ¶§¹®¿¡ ºñ´©»ç¿ë·®¿¡ °ü½ÉÀ» °¡Áö³ª, ¿£Áö´Ï¾î¿¡°Ô´Â ½ºÄÉÀϹ®Á¦°¡ °¡Àå Å« °ü½É»çÀÌ´Ù.ÇÕ¼º¼¼Á¦ÀÇ | ||
| Ä«Å×°í¸®: Àü¹®ÀÚ·á > ¼¼¹Ì³ªÀÚ·á > Àü¹®Çмú ¤Ó µî·ÏÀÏ: 2004/08/25 ¤Ó µî·ÏÀÚ: realseminar ¤Ó Æò°¡¾øÀ½ | ||
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| *Objective of the Study To Provide Roadmap and technology Tree for the Enhancement of Membrane Contactor Technologies By Identifying -Applicable Processes -Materials and Module Technologies -Contactor Proce | ||
| Ä«Å×°í¸®: Àü¹®ÀÚ·á > ¼¼¹Ì³ªÀÚ·á > Àü¹®Çмú ¤Ó µî·ÏÀÏ: 2004/08/25 ¤Ó µî·ÏÀÚ: realseminar ¤Ó Æò°¡¾øÀ½ | ||
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| *Foaming ability * PA type and SA type surfactant solution produce high foam and increase foam height with increasing EO content. * EO/PO type surfactant solution produce low foam but increase foam height | ||
| Ä«Å×°í¸®: Àü¹®ÀÚ·á > ¼¼¹Ì³ªÀÚ·á > Àü¹®Çмú ¤Ó µî·ÏÀÏ: 2004/08/25 ¤Ó µî·ÏÀÚ: realseminar ¤Ó Æò°¡¾øÀ½ | ||
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