2009
DOI: 10.1016/j.biortech.2009.01.022
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Intensification of biodiesel synthesis using zigzag micro-channel reactors

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Cited by 155 publications
(100 citation statements)
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“…Depending on the reactional scheme and the thermokinetic properties of the system, continuous processes may withdraw existing obstacles of batch processes such as numerous steps, secondary reactions, stable equilibria and difficulties to separate the reaction products. Several works on biodiesel production using microreactors have recently been published [11][12][13][14]. The methanolysis system is complex due to changing phase equilibria [15]: two 4 immiscible phases are present at the beginning (vegetable oil and methanol), then a single phase appears after a few minutes of reaction.…”
Section: Introductionmentioning
confidence: 99%
“…Depending on the reactional scheme and the thermokinetic properties of the system, continuous processes may withdraw existing obstacles of batch processes such as numerous steps, secondary reactions, stable equilibria and difficulties to separate the reaction products. Several works on biodiesel production using microreactors have recently been published [11][12][13][14]. The methanolysis system is complex due to changing phase equilibria [15]: two 4 immiscible phases are present at the beginning (vegetable oil and methanol), then a single phase appears after a few minutes of reaction.…”
Section: Introductionmentioning
confidence: 99%
“…For instance, 98% soybean conversion was achieved at 60°C with contact time 180 s [60]. This result was further improved to 99.5% conversion at 56°C and 28 s contact time by improving the microreactor configuration, with zig-zag channels and optimised micromixers [61].…”
Section: -Organometallic and Enzyme-catalysed Reactions In Organic Symentioning
confidence: 94%
“…Some of the technologies have been applied successfully in commercial production (Qiu et al, 2010) where the reaction rate is greatly enhanced and thus residence time may be reduced. To reduce the limitations of mass and heat transfer in chemical reactions, literature recommends to conduct such reactions in micro-reactors (Pohar and Plazl, 2008;Hessel et al, 2005;Wen et al, 2009) and in packed bed reactors (Yu et al, 2010;Santacesaria et al, 2011;Su, 2011) or assisted reaction with hydrodynamic cavitation (Gogate et al, 2008;Sedahmed et al, 2011;, microwave (Gole and Gogate, 2013) and ultrasound Gole and Gogate, 2013;Gobikrishnan et al, 2013).…”
Section: Intensification Technologies In Continuous Mode For Scmmentioning
confidence: 99%
“…Higher conversion and selectivity were obtained in a shorter reaction time as compared to batch system. Wen et al (2009) reported the influence of the main geometric parameters on the performance of the zigzag micro-channel reactors in the continuous alkali-catalyzed biodiesel synthesis. The authors concluded that the high reaction efficiency of the zigzag micro-channel reactor can be attributed to the intensification of the overall volumetric mass transfer by passive mixing at the microscale.…”
Section: Intensification Technologies In Continuous Mode For Scmmentioning
confidence: 99%