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[A£«] Final-lab report for Batch Reactor, CSTR (ÆÄÀ̳Π·¹Æ÷Æ® Batch Reactor, CSTR) / 1. Results 2. Discussion 3. Reference / 1. Results Batch Reactor¿Í CSTRÀÇ °á°ú´Â °¢ ¹ÝÀÀ±â À¯ÇüÀÇ ¿î¿µ Ư¼º°ú Ãâ·Â Ư¼º¿¡¼ ¶Ñ·ÇÇÑ Â÷À̸¦ º¸¿©ÁØ´Ù. Batch ReactorÀÇ °æ¿ì, ¹ÝÀÀ¹°ÀÇ ÀüºÎ°¡ ÀÏ°ýÀûÀ¸·Î ¹ÝÀÀ±â¿¡ ÅõÀԵǰí, ÁöÁ¤µÈ ½Ã°£ µ¿¾È ¹ÝÀÀÀÌ ÀÌ·ç¾îÁø ´ÙÀ½, ÃÖÁ¾ »ý¼º¹°ÀÌ ¡¦ |
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·¹Æ÷Æ® >
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3p age   | 
3,000 ¿ø
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[A£«] Pre-lab report for Batch Reactor, CSTR (ÇÁ¸®·¦ ·¹Æ÷Æ® ȸºÐ½Ä ¹ÝÀÀ±â, CSTR) / 1. Introduction 1) Purpose of the experiment 2. Theoretical Background 1) Definition 2) Equations, Chemical reaction 3) Precautions on experiment 3. Experiment 1) Materials 2) Procedure 4. Reference / 1. Introduction ȸºÐ½Ä ¹ÝÀÀ±â(Batch Reactor)¿Í ¿¬¼Ó È¥ÇÕ ±â°è(CSTR¡¦ |
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È°ø°èÃø½ÇÇè Pre-Report -CSTR and Tubular Flow Reactor / 1.½ÇÇè Á¦¸ñ 2.½ÇÇè ¸ñÀû 3.ÀÌ·Ð ¹× ¹è°æÁö½Ä 4.½ÇÇè Àåºñ 5.½ÇÇè ¼ø¼ 6.Âü°í¹®Çå / 1.½ÇÇè Á¦¸ñ CSTR ¹× °ü·ù ¹ÝÀÀ±â ½ÇÇèÀº ÈÇаøÁ¤¿¡¼ Áß¿äÇÑ °øÁ¤ ´ÜÀ§·Î °£ÁֵǴ ÀÌ µÎ °¡Áö ¹ÝÀÀ±âÀÇ µ¿ÀÛ ¿ø¸®¿Í Ư¼ºÀ» ÀÌÇØÇÏ°í, ÀÌ·ÐÀû ¿¹Ãø°ú ½ÇÁ¦ ½ÇÇè °á°ú¸¦ ºñ±³ÇÏ¿© ¹ÝÀÀ±âÀÇ ¼º´ÉÀ» Æò°¡ÇÏ´Â µ¥ ÃÊÁ¡À» ¸ÂÃß°í ÀÖ´Ù¡¦ |
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È°ø½ÇÇè ·¹Æ÷Æ® CSTR / ¥°. ¼·Ð ¥±. ÀÌ·Ð ¥². ½ÇÇèÀåÄ¡ ¹× ¹æ¹ý ¥³. ½ÇÇè°á°ú ¹× °íÂû ¥´. °á·Ð ¥µ. Âü°í¹®Çå / ¥°. ¼·Ð ÈÇÐ °øÁ¤¿¡¼ ¹ÝÀÀ ¼Óµµ¸¦ Á¦¾îÇÏ°í »ý»ê¼ºÀ» ±Ø´ëÈÇϱâ À§ÇØ ´Ù¾çÇÑ ¹ÝÀÀ±â ¼³°è°¡ ÇÊ¿äÇÏ´Ù. ±×Áß¿¡¼µµ ¿¬¼Ó È¥ÇÕ ÅÊÅ© ¹ÝÀÀ±â(CSTR, Continuous Stirred-Tank Reactor)´Â ÈÇÐ °øÁ¤¿¡¼ ³Î¸® »ç¿ëµÇ´Â ÇüÅ Áß Çϳª·Î, ¿ë¾×ÀÌ Áö¼ÓÀûÀ¸·Î ÁÖÀÔµÇ°í¡¦ |
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·¹Æ÷Æ® >
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5p age   | 
3,000 ¿ø
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CSTR °á°úº¸°í¼ / 1. ¼·Ð (½ÇÇè°³¿ä , ¸ñÀû, Çʿ伺 µîÀ» ¼¼ú) 2. ½ÇÇè¹æ¹ý 3. ½ÇÇè°á°ú 1) T=50¡ÉÀÏ ¶§ 2) T=60¡ÉÀÏ ¶§ 3) k0¿Í Ea±¸Çϱâ 4. ½ÇÇè°á°úºÐ¼® ¹× °íÂû 5. °á·Ð / 1. ¼·Ð (½ÇÇè°³¿ä , ¸ñÀû, Çʿ伺 µîÀ» ¼¼ú) 2xxx³âµµ CSTR °á°úº¸°í¼´Â ¿¬¼Ó È帧 Stirred Tank Reactor(CSTR)ÀÇ ¿î¿µ ¹× ¼º´É ºÐ¼®À» ÅëÇØ ÈÇÐ °øÁ¤ÀÇ È¿À²¼º°ú »ý»ê¼ºÀ» Æò°¡ÇÏ´Â °ÍÀ»¡¦ |
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[OK] (2xxx³âµµ A£«) CSTR °á°úº¸°í¼ / 1. ¼·Ð (½ÇÇè°³¿ä , ¸ñÀû, Çʿ伺 µîÀ» ¼¼ú) 2. ½ÇÇè¹æ¹ý 3. ½ÇÇè°á°ú 1) T=50¡ÉÀÏ ¶§ 2) T=60¡ÉÀÏ ¶§ 3) k0¿Í Ea±¸Çϱâ 4. ½ÇÇè°á°úºÐ¼® ¹× °íÂû 5. °á·Ð / 1. ¼·Ð (½ÇÇè°³¿ä , ¸ñÀû, Çʿ伺 µîÀ» ¼¼ú) 2xxx³âµµ CSTR °á°úº¸°í¼´Â ¿¬¼Ó È帧 Stirred Tank Reactor(CSTR)ÀÇ ¿î¿µ ¹× ¼º´É ºÐ¼®À» ÅëÇØ ÈÇÐ °øÁ¤ÀÇ È¿À²¼º°ú »ý¡¦ |
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[°øÁ¤½ÇÇè] CSTR¿¡¼ ¹ÝÀÀ¼Óµµ»ó¼ö ÃøÁ¤ °á°úº¸°í¼ / 1. ½ÇÇè°á°ú ¹× °á°ú ³íÀÇ 1) 1 CSTRÀÇ ¹ÝÀÀ¼Óµµ»ó¼ö °è»ê 2) Arrhenius equationÀ» ÀÌ¿ëÇÑ ºñ´©È ¹ÝÀÀÀÇ È°¼ºÈ ¿¡³ÊÁö 3) Series CSTRÀÇ ÃÖÁ¾ÀüȯÀ²ÀÇ ¿ÀÂ÷ 4) »ó¿Â¿¡¼ 1 CSTR°ú series CSTRÀÇ ´ÜÀ§ ºÎÇÇ´ç ÃÖÁ¾ ÀüÈÀ² ºñ±³ 5) 1°³ÀÇ PFRÀ» ÀÌ¿ëÇÏ¿© Series CSTRÀÇ ÃÖÁ¾ÀüȯÀ² º¸¿Ï¹æ¹ý 2. Open question 1) ¹ÝÀÀ ½ÃÀÛ¡¦ |
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·¹Æ÷Æ® >
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10p age   | 
3,000 ¿ø
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[ÀÎÇÏ´ë A£« ½ÇÇ躸°í¼] ÈÇаøÇнÇÇè CSTR °á°úº¸°í¼ / 1.¼·Ð(½ÇÇè°³¿ä, ¸ñÀû, Çʿ伺 µîÀ» ¼¼ú) 2.½ÇÇè¹æ¹ý 3.½ÇÇè°á°ú ¨çEthyl acetate, NaOH¸¦ 0.1MÀÇ ³óµµ·Î 11L Á¦Á¶ ¨èÀ¯Ãâ¿ë¾×ÀÇ ÀûÁ¤ °á°ú ¨éMass balance¸¦ ÅëÇØ CSTR¿¡¼ÀÇ ¹ÝÀÀ¼Óµµ½Ä À¯µµ ¨êÀ¯µµµÈ ¹ÝÀÀ¼Óµµ½Ä°ú ½ÇÇèµ¥ÀÌÅ͸¦ »ç¿ëÇÏ¿© ¹ÝÀÀÂ÷¼ö ¹× ¹ÝÀÀ¼Óµµ»ó¼ö °è»ê ¨ë50¡É¿Í 60¡É¿¡¼ÀÇ ½ÇÇèµ¥ÀÌÅÍ¿Í ¾Æ·¹´Ï¡¦ |
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¹ÝÀÀÇö»ó½ÇÇè CSTR °á°ú·¹Æ÷Æ® / 1. ¸ñÀû 2. ÀÌ·Ð 1) CSTR(Continuous Stirred Tank Reactor) 2) Macroscopic Mass Balance 3) ÀüµµµµÀÇ ÃøÁ¤ 3. ½ÇÇè ÀåÄ¡ 4. ½ÇÇè Áغñ¹° 5. ½ÇÇè ¹æ¹ý 5. ½ÇÇè °á°ú / 1. ¸ñÀû CSTR(Continuous Stirred Tank Reactor) ¹ÝÀÀÇö»ó ½ÇÇèÀÇ ¸ñÀûÀº ¿¬¼ÓÀûÀ¸·Î ¹ÝÀÀ¹°°ú »ý¼º¹°ÀÌ ÁÖÀÔµÇ°í ¹èÃâµÇ´Â ½Ã½ºÅÛ¿¡¼ÀÇ ÈÇÐ ¹ÝÀÀ ¼Óµµ ¹× ¹ÝÀÀ¡¦ |
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¹ÝÀÀÇö»ó CSTR ½ÇÇè / 1. ¸ñÀû 2. ÀÌ·Ð 3. ½ÇÇè ÀåÄ¡ 4. ½ÇÇè Áغñ¹° 5. ½ÇÇè ¹æ¹ý 6. ½ÇÇè °á°ú 7. °á°ú°ªÀÇ °íÂû 8. °³ÀÎ °íÂû / 1. ¸ñÀû CSTR(Continuous Stirred Tank Reactor) ½ÇÇèÀÇ ¸ñÀûÀº ¹ÝÀÀ ½Ã½ºÅÛÀÇ µ¿Àû Ư¼º°ú ¹ÝÀÀ ¼Óµµ¿¡ ´ëÇÑ ÀÌÇظ¦ µ½°í, À̸¦ ¹ÙÅÁÀ¸·Î ÈÇÐ ¹ÝÀÀ °øÁ¤ÀÇ ÃÖÀûÈ ¹× ¼³°è¿¡ ÇÊ¿äÇÑ ±âÃÊ µ¥ÀÌÅ͸¦ È®º¸ÇÏ´Â °ÍÀÌ´Ù. CSTR´Â ¿¬¼ÓÀûÀ¸·Î ¹ÝÀÀ¹°¡¦ |
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