کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
687473 889323 2009 5 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Biodiesel production from rapeseed deodorizer distillate in a packed column reactor
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی تکنولوژی و شیمی فرآیندی
پیش نمایش صفحه اول مقاله
Biodiesel production from rapeseed deodorizer distillate in a packed column reactor
چکیده انگلیسی

In this study, a technical method investigating biodiesel production in a column reactor packed with cation exchange resin from rapeseed oil deodorizer distillate (RODD) was addressed. The results showed that D002 cation exchange resin presented more efficiently catalytic activity than 002CR and 732 resins in a packed column reactor. Biodiesel yield achieved over 96% under the optimal conditions: D002 resin catalyst dosage 18 wt.% (based on oil weight), oil to methanol molar ratio 1:9, reaction temperature 60 °C, and reaction time 4 h. When the packed resin catalyst was recovered, biodiesel yield was over 88% after 10 repeated batch cycles (40 h). The comparison of biodiesel production in a packed column reactor and catalyzed by traditional sulfuric acid from RODD was also studied. It was concluded that biodiesel synthesis in a packed column reactor would be a potential way for biodiesel production from RODD.

ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Chemical Engineering and Processing: Process Intensification - Volume 48, Issue 6, June 2009, Pages 1152–1156
نویسندگان
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