| 查看: 887 | 回复: 4 | |||
| 本帖产生 1 个 翻译EPI ，点击这里进行查看 | |||
[求助]
一个摘要翻译成汉语，今天就要，
|
|||
| 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℃) 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. |
回复此楼» 猜你喜欢
求调剂
已经有3人回复
-
一志愿北京化工大学，初试成绩350求调剂
已经有14人回复
-
复试调剂
已经有4人回复
-
323分（计算机视觉和大模型项目）能直接上手
已经有3人回复
-
311分 22408 求调剂
已经有3人回复
-
320分人工智能调剂
已经有7人回复
-
一志愿郑大0705求调剂
已经有4人回复
-
0703化学
已经有10人回复
-
301求调剂
已经有10人回复
-
306分材料与化工求调剂
已经有6人回复
8814402
至尊木虫 (职业作家)
- 翻译EPI: 509
- 应助: 18 (小学生)
- 贵宾: 0.381
- 金币: 12916.1
- 散金: 47
- 红花: 16
- 帖子: 4183
- 在线: 357.8小时
- 虫号: 1184404
- 注册: 2011-01-06
- 专业: 药物学其他科学问题
【答案】应助回帖
★
sltmac: 金币+1 2012-06-01 15:00:39
sltmac: 金币+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.开发了一种通过甘油三酯的非催化酯交换反应产生生物柴油的不断流泡罩塔反应器。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).酯交换反应所用的流泡罩塔反应器的原理与反应性蒸馏相似，气相反应产物不断从反应区被移除，而作为反应物的油则留在反应区液相中。 余下的下午给你，回家了 |
2楼2012-06-01 11:45:15
3楼2012-06-01 12:08:39
 |
4楼2012-06-01 12:14:12
8814402
至尊木虫 (职业作家)
- 翻译EPI: 509
- 应助: 18 (小学生)
- 贵宾: 0.381
- 金币: 12916.1
- 散金: 47
- 红花: 16
- 帖子: 4183
- 在线: 357.8小时
- 虫号: 1184404
- 注册: 2011-01-06
- 专业: 药物学其他科学问题
【答案】应助回帖
★ ★ ★ ★ ★ ★ ★ ★ ★ ★ ★ ★ ★ ★ ★ ★ ★ ★ ★ ★ ★ ★ ★ ★ ★ ★ ★ ★ ★ ★
捡乐拾欢: 金币+30, 翻译EPI+1, ★★★★★最佳答案 2012-06-01 15:50:57
捡乐拾欢: 金币+30, 翻译EPI+1, ★★★★★最佳答案 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).酯交换反应所用的流泡罩塔反应器的原理与反应性蒸馏相似，气相反应产物不断从反应区被移除，而作为反应物的油则留在反应区。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.本实验中采用了一套实验室规模的不断流泡罩塔反应器，预先加入200mL液状棕榈油。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℃) on the biodiesel productivity increased with MeOH feed flow rate and reaction temperature correspondingly.试验结果表明，生物柴油的产率随甲醇供液速度和反应温度增加而相应增加。On the other hand, the purity of the methyl ester in the biodiesel product decreased.另一方面，产物中甲酯的纯度相应下降。 |
5楼2012-06-01 15:01:38
