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2015.05.23
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Á¦¸ñ : DME »ý»ê°øÁ¤¿¡¼­ º¹ÇÕ¸·À» ÀÌ¿ëÇÑ ÀÌ»êȭź¼Ò Á¦°Å°øÁ¤ Àü»ê¸ð»ç ÀúÀÚ : ³ë»ó±Õ
¹ßÇàÇÐȸ : Çѱ¹»êÇбâ¼úÇÐȸ [The Korea Academia-industrial cooperation Society]
¹ßÇàÁ¤º¸ : Çѱ¹»êÇбâ¼úÇÐȸ³í¹®Áö Á¦ 15±Ç 7È£ pp.4698-4706(9 pages)
¹ßÇà³âµµ : 2014

ÀúÀ۽ñâ : 2014³â 7¿ù

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1. ¼­ ·Ð
2. ÀÌ·Ð
3. Áß°ø»ç º¹ÇÕ¸·ÀÇ ¼ø¼ö ±âüÅõ°úµµ
4. ºÐ¸®¸·À» ÀÌ¿ëÇÑ CO2 Á¦°Å°øÁ¤ Àü»ê¸ð»ç
5. °á·Ð
References

º»¹®³»¿ë

º» ¿¬±¸¿¡¼­´Â µð¸ÞÆ¿¿¡Å׸£(dimethyl ether)
»ý»ê °øÁ¤¿¡ Æ÷ÇÔµÈ ÀÌ»êȭź¼Ò Á¦°Å°øÁ¤¿¡¼­ ÀÌ»êȭź¼Ò Á¦°Å ¹æ¹ýÀ¸·Î º¹ÇÕ¸·(composite membrane)À» »ç¿ëÇÏ´Â °øÁ¤¿¡ ´ëÇØ °øÁ¤±¸¼º°ú ¸ð»ç¸¦ ¼öÇàÇÏ¿´´Ù. º¹ÇÕ¸·Àº (ÁÖ)¿¡¾î·¹Àο¡¼­ Á¦Á¶ÇÑ PEI-PDMS(polyetherimide-polydimethyl siloxane) º¹ÇÕ¸·À» ´ë»óÀ¸·Î ÇÏ¿´À¸¸ç º¹ÇÕ¸· °øÁ¤À» ¸ðµ¨¸µÇϱâ À§Çؼ­ »ó¿ë¼º È­ÇаøÁ¤ ¸ð»ç±âÀÎ Invensys »çÀÇ PRO/II with PROVISION 9.2¸¦ »ç¿ëÇÏ¿´´Ù. ±×¸®°í º¹ÇÕ¸· °øÁ¤À» ¸ð»çÇϱâ À§ÇØ ÇÊ¿äÇÑ °¢ ¼ø¼ö¼ººÐµéÀÇ Åõ°úµµ »ó¼ö´Â (ÁÖ)¿¡¾î·¹Àο¡¼­ ¼öÇàÇÑ ½ÇÇè µ¥ÀÌÅ͸¦ ȸ±ÍºÐ¼® ÇÏ¿© »õ·Ó°Ô °áÁ¤ ÇÏ¿´´Ù. °á±¹ ½ÇÇèÀ»ÅëÇØ ¾òÀº Åõ°úµµ »ó¼ö¿Í »ó¿ë¼º È­ÇаøÁ¤ ¸ð»ç±â¸¦ È°¿ëÇÏ¿© ÀÌ»êȭź¼Ò¸¦ Á¦°ÅÇϱâ À§ÇÑ º¹ÇÕ¸· °øÁ¤À» ±¸¼ºÇÏ°í Á¦°Å¿¡ÇÊ¿äÇÑ ºÐ¸®¸· ¸éÀû°ú Utility ºñ¿ëÀ» µµÃâÇÏ¿´´Ù.

In this study, the simulation
was performed for the CO removal process using a composite membrane inDME production. The composite membrane, PEI-PDMS (polyetherimide- polydimethyl siloxane) manufactured byAirrane Co. Ltd., was used in the modeling through a commercial simulation design program, PRO/II withPROVISION 9.2 by Invensys. To simulate the process, the permeability constants of each of the pure component fromAirrane Co. Ltd. were determined by regression analysis from the experimental data. The required separationmembrane area and utility cost in the CO removal process were obtained using a chemical process simulator andcomposite membrane with a compatible permeability constant.   (ÀÌÇÏ »ý·«)

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