| ²é¿´: 984 | »Ø¸´: 4 | |||
| ±¾Ìû²úÉú 1 ¸ö ·ÒëEPI £¬µã»÷ÕâÀï½øÐв鿴 | |||
¼ñÀÖʰ»¶Í³æ (³õÈëÎÄ̳)
|
[ÇóÖú]
Ò»¸öÕªÒª·Òë³ÉººÓ½ñÌì¾ÍÒª£¬
|
||
| A continuous-flow bubble column reactor for biodiesel production by non-catalytic transesterification of triglycerides has been developde.The principle of a bubble column reactor for transesterification is similar to reactive distillation,where the reaction products in the gas phase are continuously removed from the reactive zone,while oil,as the reactant,is retained in the reactive zone(liquid phase).A dedicated laboratory-scale continuous-floe bubble column reactor,with a predetermined 200ml liquid volume of palm oil in the reactor ,has been used for this study.In this study,the effects of the methanol feed flow rates(1.5,3.0,and6.0ml/min) and reaction temperatures (250,270,and 290¡æ) on the biodiesel productivity increased with MeOH feed flow rate and reaction temperature correspondingly.On the other hand, the purity of the methyl ester in the biodiesel product decreased. |
» ²ÂÄãϲ»¶
ÓжàÉÙÈËÊǽñÌì²éϵͳ֪µÀ½á¹ûµÄ£¿
ÒѾÓÐ18È˻ظ´
Ϊʲô×ÊÖúÊý¸÷´ó¸ßУ¶¼´´Ð¸ߣ¬×Ô¼ºÉêÇëÔõô¾ÍÕâôÄÑ
ÒѾÓÐ12È˻ظ´
ÓÐûÓÐÈÔûÊÕµ½ÐÅÏ¢µÄ
ÒѾÓÐ3È˻ظ´
µ¼Ê¦Í²ۣºÎÒÔõô̯ÉÏÁËÕâô¸ö¼«Æ·Ñо¿Éú£¡
ÒѾÓÐ8È˻ظ´
»ù½ð²»ÖУ¬¹²Ãã
ÒѾÓÐ11È˻ظ´
Â鷳ר¼ÒÃÇ¿´¿´ÆÀίÃǵÄÒâ¼û£¨F¿ÚÃæÉÏ£©
ÒѾÓÐ9È˻ظ´
2026ÄêÒ¶ÆóËï»ù½ð
ÒѾÓÐ6È˻ظ´
¹ú×ÔÈ»ÃæÉϸ´ÅÌ~»¶ÓÌÖÂÛ
ÒѾÓÐ13È˻ظ´
»ù½ðϵͳʲôÄÚÈÝҲûÓÐ
ÒѾÓÐ9È˻ظ´
Ôõô²é°¡
ÒѾÓÐ6È˻ظ´

8814402
ÖÁ×ðľ³æ (Ö°Òµ×÷¼Ò)
- ·ÒëEPI: 509
- Ó¦Öú: 18 (СѧÉú)
- ¹ó±ö: 0.381
- ½ð±Ò: 12921.1
- É¢½ð: 47
- ºì»¨: 16
- Ìû×Ó: 4185
- ÔÚÏß: 357.9Сʱ
- ³æºÅ: 1184404
- ×¢²á: 2011-01-06
- רҵ: Ò©ÎïѧÆäËû¿ÆÑ§ÎÊÌâ
¡¾´ð°¸¡¿Ó¦Öú»ØÌû
¡ï
sltmac: ½ð±Ò+1 2012-06-01 15:00:39
sltmac: ½ð±Ò+1 2012-06-01 15:00:39
|
A continuous-flow bubble column reactor for biodiesel production by non-catalytic transesterification of triglycerides has been developde.¿ª·¢ÁËÒ»ÖÖͨ¹ý¸ÊÓÍÈýõ¥µÄ·Ç´ß»¯õ¥½»»»·´Ó¦²úÉúÉúÎï²ñÓ͵IJ»¶ÏÁ÷ÅÝÕÖËþ·´Ó¦Æ÷¡£The principle of a bubble column reactor for transesterification is similar to reactive distillation,where the reaction products in the gas phase are continuously removed from the reactive zone,while oil,as the reactant,is retained in the reactive zone(liquid phase).õ¥½»»»·´Ó¦ËùÓõÄÁ÷ÅÝÕÖËþ·´Ó¦Æ÷µÄÔÀíÓë·´Ó¦ÐÔÕôÁóÏàËÆ£¬ÆøÏà·´Ó¦²úÎï²»¶Ï´Ó·´Ó¦Çø±»ÒƳý£¬¶ø×÷Ϊ·´Ó¦ÎïµÄÓÍÔòÁôÔÚ·´Ó¦ÇøÒºÏàÖС£ ÓàϵÄÏÂÎç¸øÄ㣬»Ø¼ÒÁË |
2Â¥2012-06-01 11:45:15
¼ñÀÖʰ»¶
ͳæ (³õÈëÎÄ̳)
- Ó¦Öú: 0 (Ó×¶ùÔ°)
- ½ð±Ò: 2.3
- Ìû×Ó: 45
- ÔÚÏß: 23.6Сʱ
- ³æºÅ: 1435711
- ×¢²á: 2011-10-10
- ÐÔ±ð: MM
- רҵ: ÖÐÒ©ÖÆ¼Á

3Â¥2012-06-01 12:08:39
|
4Â¥2012-06-01 12:14:12
8814402
ÖÁ×ðľ³æ (Ö°Òµ×÷¼Ò)
- ·ÒëEPI: 509
- Ó¦Öú: 18 (СѧÉú)
- ¹ó±ö: 0.381
- ½ð±Ò: 12921.1
- É¢½ð: 47
- ºì»¨: 16
- Ìû×Ó: 4185
- ÔÚÏß: 357.9Сʱ
- ³æºÅ: 1184404
- ×¢²á: 2011-01-06
- רҵ: Ò©ÎïѧÆäËû¿ÆÑ§ÎÊÌâ
¡¾´ð°¸¡¿Ó¦Öú»ØÌû
¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï
¼ñÀÖʰ»¶: ½ð±Ò+30, ·ÒëEPI+1, ¡ï¡ï¡ï¡ï¡ï×î¼Ñ´ð°¸ 2012-06-01 15:50:57
¼ñÀÖʰ»¶: ½ð±Ò+30, ·ÒëEPI+1, ¡ï¡ï¡ï¡ï¡ï×î¼Ñ´ð°¸ 2012-06-01 15:50:57
| The principle of a bubble column reactor for transesterification is similar to reactive distillation,where the reaction products in the gas phase are continuously removed from the reactive zone,while oil,as the reactant,is retained in the reactive zone(liquid phase).õ¥½»»»·´Ó¦ËùÓõÄÁ÷ÅÝÕÖËþ·´Ó¦Æ÷µÄÔÀíÓë·´Ó¦ÐÔÕôÁóÏàËÆ£¬ÆøÏà·´Ó¦²úÎï²»¶Ï´Ó·´Ó¦Çø±»ÒƳý£¬¶ø×÷Ϊ·´Ó¦ÎïµÄÓÍÔòÁôÔÚ·´Ó¦Çø¡£A dedicated laboratory-scale continuous-floe bubble column reactor,with a predetermined 200ml liquid volume of palm oil in the reactor ,has been used for this study.±¾ÊµÑéÖвÉÓÃÁËÒ»Ì×ʵÑéÊÒ¹æÄ£µÄ²»¶ÏÁ÷ÅÝÕÖËþ·´Ó¦Æ÷£¬Ô¤ÏȼÓÈë200mLÒº×´×ØéµÓÍ¡£In this study,the effects of the methanol feed flow rates(1.5,3.0,and6.0ml/min) and reaction temperatures (250,270,and 290¡æ) on the biodiesel productivity increased with MeOH feed flow rate and reaction temperature correspondingly.ÊÔÑé½á¹û±íÃ÷£¬ÉúÎï²ñÓ͵IJúÂÊËæ¼×´¼¹©ÒºËٶȺͷ´Ó¦Î¶ÈÔö¼Ó¶øÏàÓ¦Ôö¼Ó¡£On the other hand, the purity of the methyl ester in the biodiesel product decreased.ÁíÒ»·½Ã棬²úÎïÖм×õ¥µÄ´¿¶ÈÏàӦϽµ¡£ |
5Â¥2012-06-01 15:01:38









»Ø¸´´ËÂ¥
ͶƱ:
10