Continuous enzymatic biodiesel production from coconut oil in two-stage packed-bed reactor incorporating an extracting column to remove glycerol formed as by-product

2016 ◽  
Vol 39 (10) ◽  
pp. 1611-1617 ◽  
Author(s):  
William Costa e Silva ◽  
Larissa Freitas ◽  
Pedro C. Oliveira ◽  
Heizir F. de Castro
Keyword(s):  
Coconut Oil ◽  
Packed Bed ◽  
Biodiesel Production ◽  
Packed Bed Reactor ◽  
Two Stage

A two-stage enzymatic ethanol-based biodiesel production in a packed bed reactor

2012 ◽  
Vol 162 (4) ◽  
pp. 407-414 ◽  
Author(s):  
Yuan Xu ◽  
Mathias Nordblad ◽  
John M. Woodley
Keyword(s):  
Packed Bed ◽  
Biodiesel Production ◽  
Packed Bed Reactor ◽  
Two Stage

scholarly journals Continuous biodiesel production under subcritical condition of methanol – Design of pilot plant and packed bed reactor with MnCO3/Na-silicate catalyst

2018 ◽  
Vol 168 ◽  
pp. 494-504 ◽  
Author(s):  
Hui Liu ◽  
Ivana Lukić ◽  
Marija R. Miladinović ◽  
Vlada B. Veljković ◽  
Miodrag Zdujić ◽  
...  
Keyword(s):  
Pilot Plant ◽  
Packed Bed ◽  
Biodiesel Production ◽  
Packed Bed Reactor ◽  
Subcritical Condition

Lipase Acrylic Resin Catalyzed Interesterification of Sewage Sludge in Micro Packed Bed Reactor: Box-Behnken Design

2020 ◽  
Vol 870 ◽  
pp. 81-96
Author(s):  
Ali A. Jazie ◽  
Riyam Imad Jaddan ◽  
Mohamed F. Al-Dawody ◽  
Suhad A. Abed
Keyword(s):  
Enzyme Activity ◽  
Sewage Sludge ◽  
Ethyl Acetate ◽  
Acrylic Resin ◽  
Packed Bed ◽  
Biodiesel Production ◽  
Packed Bed Reactor ◽  
Heating Process ◽  
Optimum Conditions ◽  
Box Behnken Design

Ethyl acetate as acyl accepter have been used for sewage sludge biodiesel production in micro packed bed reactor. Lipase acrylic resin enzyme activity was investigated in the interesterification reaction of converting the sewage sludge into a biodiesel product. The main parameters affecting the process was adjusted via the design of Box-Behnken and approach of response surface then the optimum conditions were as follow (reaction time=15 h, ethyl acetate/oil ratio=24:1, temperature=40 °C and enzyme quantity=18 wt%) providing 95.78 % biodiesel yield. The lipase acrylic resin was examined under the optimum conditions for the reusability. the flow effect and the heating process of the micro packed bed reactor was investigated. The product biodiesel physicochemical properties were evaluated according to the ASTM D-6751-2 and found acceptable comparable to the mineral diesel properties.

Biodiesel production from soybean soapstock acid oil by hydrolysis in subcritical water followed by lipase-catalyzed esterification using a fermented solid in a packed-bed reactor

2013 ◽  
Vol 81 ◽  
pp. 15-23 ◽  
Author(s):  
Diniara Soares ◽  
Andrei Ferreira Pinto ◽  
Alan Guilherme Gonçalves ◽  
David Alexander Mitchell ◽  
Nadia Krieger
Keyword(s):  
Subcritical Water ◽  
Packed Bed ◽  
Biodiesel Production ◽  
Packed Bed Reactor ◽  
Acid Oil
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