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µÄ¹æÄ££¬ÈçÈÈ´«µÝÄÜÁ¦»áÏÞÖÆ¼äЪ·´Ó¦Æ÷µÄ³ß´ç£¬ÈȽ»»»Æ÷±ØÐëÔÚÖÆÔì³§¶ø²»ÊÇÔÚÏÖ³¡¼Ó¹¤¡£ÕâÏÞÖÆÁ˲úÂÊÓÉÓÚÕâ¼äЪ·´Ó¦Æ÷¿ÉÒÔ±»¾¼ÃµØÀûÓ᣼äЪ·´Ó¦Æ÷Ò²±ØÐë×°ÁÏ¡¢Ð¶ÁϺÍÇåÏ´¡£ÎªÁ˼ӿ췴ӦÕâЩ·ÇÉú²úÐԵIJÙ×÷ÏûºÄÁ˶àÓÚ·´Ó¦±¾ÉíµÄʱ¼ä£¬Á¬Ðø»¯¹ý³Ì¿ÉÄܸüÓÐÎüÒýÁ¦¡£ 2. Semibatch Reactors (SBR) 2.°ë¼äЪ·´Ó¦Æ÷
Some reactions may yield a product in a different phase from the reaction mixture. Examples would be liberation of a gas from a liquid-phase reaction or the formation of a precipitate in a fluid-phase reaction. To drive the reaction to completion, it may be desirable to continuously separate the raw product phase. A semibatch operation may result as well from differing modes of feeding the individual reactants. For reasons we will discuss later, it may be desirable to charge one reactant to the reactor at the outset and bleed a second reactant in continuously over time. Such reactors have both a batch and a flow character and, like batch reactors, are useful for slow reactions and low production rates.
һЩ·´Ó¦Æ÷¿ÉÒÔ´Ó·´Ó¦»ìºÏÎïµÄ²»Í¬Ïà̬ÖÐÉú²ú³öijÖÖ²úÆ·¡£ÀýÈçÒºÏà·´Ó¦ÖÐÆøÌåµÄÊÍ·Å£¬»òÁ÷¶¯Ïà·´Ó¦ÖгÁµíµÄÉú³É¡£ÎªÁËÇýʹ·´Ó¦ÍêÈ«£¬Ï£Íû¼ÌÐø·ÖÀë´Ö²úÎïÏà¡£¸ö±ð·´Ó¦ÎïµÄ²»Í¬¼ÓÈ뷽ʽҲµ¼Ö°ëÁ¬Ðø²Ù×÷¡£ÔÒòÎÒÃÇÒÔºóÌÖÂÛ£¬¿ÉÏ£ÍûÒ»¿ªÊ¼¼ÓÈëÒ»ÖÖ·´Ó¦ÎïÒÔºóÁ¬Ðø¼ÓÈëµÚ¶þÖÖ·´Ó¦Îï¡£ÕâÀà·´Ó¦Æ÷ͬʱ¾ßÓÐÒ»¸ö¼äЪºÍÒ»¸öÁ÷¶¯µÄÌØÕ÷£¬Ïñ¼äЪ·´Ó¦Æ÷£¬ÊÊÓÃÓÚÂý·´Ó¦ºÍµÍ²úÂÊ¡£ 3. Continuous Stirred Tank Reactors (CSTR) 3. Á¬ÐøÁ÷¶¯½Á°è·´Ó¦Æ÷
It is a small step from the batch reactor to the CSTR. The same stirred vessel may be used with
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only the addition of piping and storage tanks to provide for the continuous in-and outflow. Faster reactions can be accommodated and larger production rates can be achieved because of the uninterrupted operation. CSTRs are most often used for liquid-phase reactions, such as nitration and hydrolysis, and multiphase reactions involving liquid with gases and/or solids. Examples would be chlorination and hydrogenation.
´Ó¼äЪ·´Ó¦Æ÷µ½Á¬ÐøÁ÷¶¯½Á°è·´Ó¦Æ÷ÊÇССµÄÒ»²½¡£Í¬ÑùµÄ½Á°èʽÈÝÆ÷µÄʹÓÿɽö½öÌí¼Ó¹ÜµÀºÍ´¢¹ÞÒÔÌṩÁ¬Ðø½øÁϺͳöÁÏ¡£ÒòΪÁ¬Ðø²Ù×÷¿É¼Ó¿ì·´Ó¦²¢Ìá¸ß²úÂÊ¡£Í¨³£´ó¶àÊýÁ¬ÐøÁ÷¶¯½Á°è·´Ó¦Æ÷ÓÃÓÚÒºÏà·´Ó¦£¬ÀýÈçÏõ»¯ºÍË®½â£¬¶àÏà·´Ó¦Æ÷Éæ¼°Òº-ÆøºÍ/»òÒº-¹Ì¡£ÀýÈçÂÈ»¯ºÍ¼ÓÇâ¡£ 4. CSTR in Series
4.¶à¼¶´®ÁªÁ¬ÐøÁ÷¶¯½Á°è·´Ó¦Æ÷
It was shown that considerable gains in production rate and economics can be achieved by passing the reacting mixture through a series of CSTRs. Again, we see how easy it is to achieve a gradual scale up, say for a specialty chemical for which is increasing. CSTRs in series are usually used for liquid-phase reactions.
ÊÂʵ֤Ã÷ͨ¹ýһϵÁж༶´®ÁªÁ¬ÐøÁ÷¶¯½Á°è·´Ó¦Æ÷µÄ»ìºÏÄܹ»»ñµÃ¸ß²úÂʺÍÖØ´óµÄ¾¼ÃÐ§Òæ¡£ÔÙÕߣ¬ÕâÖÖ·´Ó¦Æ÷ÈÝÒ×·Å´ó£¬ÀýÈçijÖÖ»¯Ñ§Æ·µÄÐèÇóÖð²½Ôö¼Óʱ³£ÕâÑù×ö¡£¶à¼¶´®ÁªÁ¬ÐøÁ÷¶¯½Á°è·´Ó¦Æ÷ͨ³£ÓÃÓÚÒºÏà·´Ó¦¡£ 5.Tubular Reactors 5.¹Üʽ·´Ó¦Æ÷
As the production rate requirement increases, batteries of CSTRs become increasingly complex
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and tubular reactors become attractive. With the transition to tubular reactors, some versatility is lost and more process integration is required. Nevertheless, tubular reactors find extensive application in liquid-phase reactions, for example, polymerization, and are almost always the continuous reactor of choice for gas-phase reactions, for example, pyrolysis. Exceedingly high production rates can be achieved with tubular reactors either by increasing the diameter of the tube or more commonly by using a sufficient number of tubes in parallel.
µ±²úÂÊÐèÒªÔö¼Óʱ£¬Ôö¼ÓÐí¶àÌ×Á¬Ðø½Á°èʽ·´Ó¦Æ÷±äµÃ¸´ÔÓ£¬¶ø¹Üʽ·´Ó¦Æ÷±äµÃÓÕÈË¡£×ª»¯³É¹Üʽ·´Ó¦Æ÷ʧȥÁËһЩͨÓÃÐÔ²¢ÒªÇó×ÛºÏÐí¶à²Ù×÷¡£¾¡¹ÜÈç´Ë£¬¹Üʽ·´Ó¦Æ÷ÔÚÒºÏà·´Ó¦ÖÐÆð׏㷺×÷Óã¬ÀýÈ磬¾ÛºÏ·´Ó¦£¬Æø-Òº·´Ó¦¼¸ºõ×ÜÊÇÑ¡ÔñÁ¬Ðø·´Ó¦Æ÷£¬ÀýÈ磬¸ßÎÂÁѽ⡣²ÉÓùÜʽ·´Ó¦Æ÷Äܹ»»ñµÃ·Ç³£¸ßµÄ²úÂÊ£¬ÒªÃ´Ôö¼Ó¹ÜµÄÖ±¾¶ÒªÃ´Í¨¹ýʹÓóä×ãÊýÁ¿µÄ²¢ÁйÜÌá¸ß¸ü´óµÄͨÓÃÐÔ¡£ 6. Recycle reactors 6. Ñ»··´Ó¦Æ÷
Recycle reactor can be batch, CSTR, tubular, and so on in nature with the purpose of the recycle varying from one case to the next. Many large-scale commercial processes incorporate the recycle of one or more streams back to an earlier point in the process to conserve raw materials. This practice often results in the accumulation of impurities, which in turn requires separation. Usually it is not simply the reactor outlet stream that is recycled back to the reactor inlet, but it can be. For example in a batch reactor the reacting mixture can be recycled, or pumped around, through a heat exchanger to provide thermal control.
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Recycle reactor have also found valuable application in the laboratory and pilot plant because of their special characteristics. At one extreme, in which all of the product is recycled (no net flow), the reactor is the exact equivalent of the well-stirred batch reactor. At the other extreme of no recycle, the reactor is simply the tubular variety. If there is some net flow but the recycle rate is high, the overall reactor performs like a CSTR. Yet the reaction tube itself behaves like differential tubular reactor. This versatility of the recycle reactor can be exploited to great advantage in research and development.
Ñ»··´Ó¦Æ÷ÓÉÓÚÆäÌØÊâµÄÌØÐÔÔÚʵÑéÊÒºÍÖÐÊÔ³µ¼äÒ²·¢ÏÖÁËÓ¦ÓüÛÖµ¡£Ò»¸ö¼«¶ËÊǽ«ËùÓеIJúÎïÑ»·£¨Ã»Óо»µÄÁ÷³ö£©£¬´Ëʱѻ··´Ó¦Æ÷ÑϸñµÈЧÓÚÈ«»ì¼äЪ·´Ó¦Æ÷¡£ÁíÒ»¸ö¼«¶ËÊÇûÓÐÑ»·£¬·´Ó¦Æ÷ÊǼòµ¥µÄ¹ÜʽÀà¡£¼ÙÈçÓÐһЩ¾»µÄÁ÷³öµ«Ñ»·Âʺܸߣ¬ËùÓеķ´Ó¦Æ÷ÔËÐÐÀàËÆÓÚÁ¬ÐøÁ÷¶¯½Á°è·´Ó¦Æ÷¡£È»¶ø·´Ó¦Æ÷±¾ÉíµÄ ÀàËÆÓÚ²»Í¬µÄ¹Üʽ·´Ó¦Æ÷¡£ÔÚÑо¿ºÍ·¢Õ¹ÖÐÑ»··´Ó¦Æ÷µÄͨÓÃÐÔÄܹ»¿ª·¢³ö¸ü´óµÄÓÅµã£¨ÊÆ£©¡£
¡ª¡ªBisio A. , Kabel R L. Scaleup of Chemical Processes. New York: John Wiley & Sons Inc. , 1985. 255~257
T 14 Styrene-Butadiene Copolymer µÚÊ®Ëĵ¥Ôª ¶¡¶þÏ©-±½ÒÒÏ©¹²¾ÛÎï
The synthetic rubber industry, based on the free-radical emulsion process, was created almost
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