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 ±¸À±¸ð ( ÎýëÈÙÈ / Yoon-Mo Koo )  

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 1953 . 10

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 1987 . 09 . 01

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 860-7513  /  2S117  /  »ý¹°³ª³ë°øÁ¤°øÇÐ ¿¬±¸½Ç

E-Mail

 ymkoo@inha.ac.kr

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 A.I.Ch.E., Çѱ¹»ê¾÷¹Ì»ý¹°ÇÐȸ, Çѱ¹»ý¹°°øÇÐȸ, Çѱ¹È­ÇаøÇÐȸ

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 1975.02 ¼­¿ï´ëÇб³(Çлç) / È­ÇаøÇÐ
 1977.02 Çѱ¹°úÇбâ¼ú¿ø(¼®»ç) / È­ÇаøÇÐ
 1985.12 Purdue Univ.(¹Ú»ç) / È­ÇаøÇÐ

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 1977.03~1980.06 Çѱ¹°úÇбâ¼ú¿¬±¸¼Ò / ¿¬±¸¿ø
 1986.01~1987.08 Purdue ´ëÇб³ / Res.Assoc
 1991.07~1992.06 Univ.of California, lrvine / ¹æ¹®±³¼ö

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- Size Exclusion Cyclic Separation, 1985.

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- Porcine Liver Esterase¸¦ ÀÌ¿ëÇÑ ±¤Çм±ÅÃÀûÀÎ ·¹º¸Ç÷ϻç½ÅÀÇ »ý»ê, Çѱ¹»ý¹°°øÇÐȸÁö, 15±Ç 3È£, pp313-317, 2000.
- On-line recovery of large molecules from mixture solution using semi-continuous size exclusion chromatography , Progress in Biotechnology, Vol. 16, pp21-24, 2000.
- ¼¶À¯¼ÒºÐÇØÈ¿¼Ò¿¡ ÀÇÇÑ Áß±Ô¸ð °í±ÞÆóÁöÀç»ý Å»¹¬°øÁ¤, Çѱ¹È­ÇаøÇÐȸÁö, 38±Ç 3È£, pp434-439, 2000.
- Interconversion and disproportionation reaction among cyclodextrin homologues in aqueous two-phase forming solution, BIOTECHNOLOGY LETTERS, 22±Ç, pp651-654, 2000.
- On-line Recovery of Large Molecules and Concentration of Small Molecules using Reciprocating Size Exclusion Chromatography with Temperature Swing, Biotech. Tech. , Vol.13, pp, 1999.
- On-line separation of solute mixtues using reciprocating size exclusion chromatography, Biotech. Tech., Vol.13, No.10, pp715-717, 1999.
- È¥ÇÕ¼¼Æ÷¸¦ ÀÌ¿ëÇÑ Aerated Slurry Bioreactor¿¡¼­ÀÇ in vitro Glutathione »ý»ê, Çѱ¹»ý¹°°øÇÐȸÁö, 14±Ç,4È£, pp445-451, 1999.
- Cellulase Production in Fed-Batch Culture by Trichoderma reesei Rut C-30, J. of Microbiology and Biotechnology, Vol.9, No.1, pp44-49, 1999.
- Cellulase Production by Trichoderma reesei Rut C-30 with Batch and Fed-batch Fermentation, , Vol.25, No.1, pp16-19, 1999.
- On-line recovery of large molecules from mixtures using reciprocating size exclusion chromatography, Biotech. Tech., Vol.13, pp211-214, 1999.
- ¿¡Åº¿ÃÀ» Á¶¿ë¸Å·Î »ç¿ëÇÑ ºÐº°°áÁ¤È­¿¡ ÀÇÇÑ CyclodextrinÀÇ ºÐ¸®Á¤Á¦, Çѱ¹È­ÇаøÇÐȸÁö, Vol.36,No.6, pp968-971, 1998.
- Production of Cellulose by Trichoderma reesei Rut C-30 in a Batch Fermenter, J. Microbiol. Biotechnol., 8±Ç,6È£, pp575-580, 1998.
- Trichoderma reesei Rut C-30 À¯·¡ cellulase¿¡ ÀÇÇÑ °í±ÞÆóÁöÀç»ý¿¡ °ü, Çѱ¹È­ÇаøÇÐȸÁö, 36±Ç,5È£, pp759-763, 1998.
- Effect of Feeding Method on the Production of Glutathione by High Cell Density Cultivation of Recombinant Escherichia coli, Chinese J. of Biotech., Vol.14, No.4, pp452-455, 1998.
- È¿¸ðÀÇ ATPÀç»ý»ê°è¿Í ´ëÀå±Õ À¯·¡ÀÇ ÀçÁ¶ÇÕ »ý»êÈ¿¼Ò¸¦ ÀÌ¿ëÇÑ in vitro ±Û·çŸġ¿Â »ý»ê, Çѱ¹»ê¾÷¹Ì»ý¹°ÇÐȸÁö, 26±Ç,3È£, pp213-220, 1998.
- Effect of Additives and Fed-batch Culture Strategies on the Production of Glutathione by Recombinant Escherichia coli, Process Biochemistry, Vol.33, No.7, pp709-714, 1998.
- Trichoderma reesei¸¦ ÀÌ¿ëÇÑ ¼¶À¯¼Ò ºÐÇØÈ¿¼ÒÀÇ »ý»ê¿¡ À־ È¥ÇÕź¼Ò¿øÀÇ ¿µÇâ, The Kor. J. of Mycology, 26(2), pp239-245, 1998.
- Production of Cellulase by Trichoderma reesei Rut C30 in Wheat Bran-containing Media, J. Microbiolo. Biotechnol., 8±Ç,3È£, pp208-213, 1998.
- Recovery of beta-Galactosidase from E. coli Double Lysogen using Aqueous Two-Phase System, Biotech. Tech., 12±Ç,6È£, pp455-458, 1998.
- Cellulase Production by Trichoderma reesei Rut C-30 in Submerged Fermentation, J. of Wuxi Univ. of Light Ind., 17±Ç,2È£, pp6-10, 1998.
- Effect of Precursor Amino Acids and ATP on the Production of Glutathione by Recombinant Escherichia coli, J. of Wuxi Univ. of Light Ind., 17±Ç,2È£, pp11-15, 1998.
- À̿±³È¯ Å©·Î¸¶Åä±×·¡ÇǸ¦ ÀÌ¿ëÇÑ GlutathioneÀÇ ºÐ¸®, Çѱ¹»ý¹°°øÇÐȸÁö, 13±Ç,1È£, pp77-82, 1998.
- Trichoderma reesei QM9414ÀÇ ¼¶À¯¼Ò ºÐÇØÈ¿¼Ò »ý»êÀ» À§ÇÑ Á¶Àýº¯ÀÌÁÖÀÇ ºÐ¸® ¹× Ư¼º¿¡ °üÇÑ ¿¬±¸, The Kor. J. of Mycology, 26±Ç,1È£, pp127-133, 1998.
- The Cellulase Production by Trichoderma reesei in Submerged Fermentation, Food and Fermentation Industries, 24±Ç,1È£, pp20-25, 1998.
- Optimization of Cellulase Production in Batch Fermentation by Trichoderma reesei, Biotech. and Bioproc. Eng., 3±Ç,1È£, pp44-47, 1998.
- Production of Cyclodextrin Homologues using Aqueous Two-Phase System, Biotech. & Bioprocess Eng., 2±Ç, pp97-100, 1997.
- ±Û·çŸġ¿Â »ý»ê ÀçÁ¶ÇÕ ´ëÀå±ÕÀÇ °í³óµµ ¹è¾ç¿¡ °üÇÑ ¿¬±¸, Çѱ¹È­ÇаøÇÐȸÁö, 35±Ç,4È£, pp526-531, 1997.
- Mathematical Modeling for the Estimation of Lipase Activity by Agar Diffusion Method, Kor. J. of Chem. Eng., 14±Ç,3È£, pp179-183, 1997.
- ħÀü¹ý°ú Àü±âÅõ¼®À» ÀÌ¿ëÇÑ Glutathione ºÐ¸®, Çѱ¹»ý¹°°øÇÐȸÁö, 12±Ç,2È£, pp255-259, 1997.
- È¥ÇÕ¼¼Æ÷°è °íÁ¤È­ ¹ÝÀÀ±â¿¡ ÀÇÇÑ Glutathione »ý»ê, Çѱ¹»ý¹°°øÇÐȸÁö, 12±Ç,2È£, pp151-158, 1997.
- ¼ö¼ºÀÌ»ó°è¸¦ ÀÌ¿ëÇÑ Cyclodextrin HomologuesÀÇ »ý»ê, Biotech. & Bioprocess Eng., 2±Ç, pp97-100, 1997.
- ±Û·çŸġ¿Â »ý»ê ÀçÁ¶ÇÕ ´ëÀå±ÕÀÇ °í³óµµ ¹è¾ç¿¡ °üÇÑ ¿¬±¸, Çѱ¹È­ÇаøÇÐȸÁö, 35(4), pp526-531, 1997.
- Increased Production of ¥â-Cyclodextrin using Aqueous Two Phase System, Biotech. Tech., 10±Ç,6È£, pp395-400, 1996.
- Controlled lysis of Escherichia coli double-lysogen of bacteriophages lambdaHL1 and phi434, Kor. J. of Chem. Eng., 13±Ç,2È£, pp202-206, 1996.
- Phage Lysogen°ú Expanded Bed AdsorptionÀ» ÀÌ¿ëÇÑ ¼¼Æ÷³» È¿¼ÒÀÇ È¸¼ö, Çѱ¹»ý¹°°øÇÐȸÁö, 11±Ç,6È£, pp663-668, 1996.
- Àü±âÅõ¼®¿¡ ÀÇÇÑ ÃÊ»êÀÇ À̵¿Æ¯¼º, Çѱ¹»ý¹°°øÇÐȸÁö, Vol.11,No.3, pp360-366, 1996.
- Lipase¸¦ »ý»êÇÏ´Â ÀçÁ¶ÇÕ ´ëÀå±ÕÀÇ Phage¿¡ ÀÇÇÑ Á¶ÀýÀû ¿ë±Õ, Çѱ¹»ý¹°°øÇÐȸÁö, 10±Ç,5È£, pp575-581, 1995.
- ºñ¿ë¸Å ÷°¡¹ýÀ» ÀÌ¿ëÇÑ Dextran ºÐº°Ä§Àü¿¡ °üÇÑ ¿¬±¸, Çѱ¹»ý¹°°øÇÐȸÁö, 10±Ç,3È£, pp257-263, 1995.
- ÀçÁ¶ÇÕ ´ëÀå±Õ°ú È¿¸ðÀÇ °íÁ¤È­ È¥ÇÕ¼¼Æ÷°è¿¡ ÀÇÇÑ ¥ã-Glutamylcysteine »ý»ê, Çѱ¹»ý¹°°øÇÐȸÁö, 10±Ç,3È£, pp249-256, 1995.
- Àڿܼ±¿¡ ÀÇÇÑ E. coli Double-lysogen ¿ëÇØ¿¡ ´ëÇÑ ¼öÇÐÀû ¸ðµ¨, Çѱ¹È­ÇаøÇÐȸÁö, 33±Ç,3È£, pp386-393, 1995.
- Analysis of a Nonlinear, Coupled Chromatographic System, Kor. J. Chem. Eng., 11±Ç,4È£, pp227-231, 1994.
- Controlled Lysis of E. coli Double-Lysogen by UV-Irradiation, Biotech. Letters, 6±Ç,10È£, pp1007-1010, 1994.
- Dextransucrase¿¡ ÀÇÇÑ Dextran »ý¼º±âÀÛ¿¡ °üÇÑ ¿¬±¸, Çѱ¹»ý¹°°øÇÐȸÁö, 9±Ç,1È£, pp1-7, 1994.
- Mechanism of Simultaneous Solutes Separation and Concentration by Size Exclusion Cyclic Separation, Kor. J. Chem. Eng., 10±Ç,1È£, pp49-55, 1993.
- Concentration of High Molecular Weight Solute byClinical Dextran using Two-stage Reactor, Biotechnology Techniques, 6±Ç,4È£, pp377-380, 1992.
- Continuous Production of Clinical Dextran using Two-stage Reactor, Biotechnology Letters, 14(5), pp379-384, 1992.
- ¿ª¹Ì¼¿À» ÀÌ¿ëÇÑ Bacillus licheniformis ¹ßÈ¿¾×À¸·ÎºÎÅÍ ¾ËÄ®¸®¼º ´Ü¹éÁú ºÐÇØÈ¿¼ÒÀÇ ÃßÃâ¿¡ °üÇÑ¿¬±¸, Çѱ¹»ý¹°°øÇÐȸÁö, 6±Ç,1È£, pp105-109, 1991.
- Estimation of Fiber Radii and Lengths of Sephadex Gel by the Modified Ogston Model, Kor. J. Chem. Eng., 6±Ç,3È£, pp254-258, 1989.
- Sephadex G Gel ¼¶À¯ÀÇ ¹Ý°æ°ú ±æÀÌ, Çѱ¹»ý¹°°øÇÐȸÁö, 4±Ç,1È£, pp15-17, 1989.
- Modeling of Size Exclusion Parametric Pumping, Sep. Sci. & Tech., 23, pp413-417, 1988.
- Scaling Rules for Isocratic Elution Chromatography, AIChE J., 34, pp1006-1019, 1988.
- Molecular Structure of Dextran Gel, Çѱ¹»ýÈ­ÇÐȸÁö, 21±Ç,1È£, pp22-30, 1988.
- Size Exclusion Parametric Pumping, Ind. & Eng. Sci. Fund., 24, pp108-112, 1985.
- 2´Ü ¿¬¼Ó½Ä ¹ßÈ¿ ¹æ½Ä¿¡ ÀÇÇÑ ¼ÖºñÅç·ÎºÎÅÍÀÇ ¼Öº¸Áî »ý»êÁ¶¾÷Á¶°ÇÀÇ ÃÖÀûÈ­, Çѱ¹È­ÇаøÇÐȸÁö, 18±Ç,5È£, pp333-342, 1980.
- Kinetics of Esterification for Octylphenylphosphoric Acids, Inorg. Nucl. Chem. Letters, 14, pp405-409, 1978.

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- ¿¬¼Ó ¿Õº¹½Ä Å©±â¹èÁ¦ Å©·Î¸¶Åä±×¶óÇÇ ½Ã½ºÅÛ ¹× À̸¦ ÀÌ¿ëÇÑ °íºÐÀÚ ¹°ÁúÀÇ ºÐ¸®¹æ¹ý, 1998
- ´Ü¹éÁú Á¦Á¶¿Í ¼¼Æ÷¿ëÇØ¸¦ µ¿Àϰ賻(in-situ)¿¡¼­ ¼öÇàÇÏ´Â ¹æ¹ý, 1998

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