Residence time distribution of dispersed liquid and solid phase in a continuous oscillatory flow baffled crystallizer

2017 ◽  
Vol 317 ◽  
pp. 413-423 ◽  
Author(s):  
Rohit Kacker ◽  
Sven I. Regensburg ◽  
Herman J.M. Kramer
2014 ◽  
Vol 68 (3) ◽  
pp. 363-379 ◽  
Author(s):  
Danijela Slavnic ◽  
Branko Bugarski ◽  
Nikola Nikacevic

Global market competition, increase in energy and other production costs, demands for high quality products and reduction of waste are forcing pharmaceutical, fine chemicals and biochemical industries, to search for radical solutions. One of the most effective ways to improve the overall production (cost reduction and better control of reactions) is a transition from batch to continuous processes. However, the reactions of interests for the mentioned industry sectors are often slow, thus continuous tubular reactors would be impractically long for flow regimes which provide sufficient heat and mass transfer and narrow residence time distribution. The oscillatory flow reactors (OFR) are newer type of tube reactors which can offer solution by providing continuous operation with approximately plug flow pattern, low shear stress rates and enhanced mass and heat transfer. These benefits are the result of very good mixing in OFR achieved by vortex generation. OFR consists of cylindrical tube containing equally spaced orifice baffles. Fluid oscillations are superimposed on a net (laminar) flow. Eddies are generated when oscillating fluid collides with baffles and passes through orifices. Generation and propagation of vortices create uniform mixing in each reactor cavity (between baffles), providing an overall flow pattern which is close to plug flow. Oscillations can be created by direct action of a piston or a diaphragm on fluid (or alternatively on baffles). This article provides an overview of oscillatory flow reactor technology, its operating principles and basic design and scale - up characteristics. Further, the article reviews the key research findings in heat and mass transfer, shear stress, residence time distribution in OFR, presenting their advantages over the conventional reactors. Finally, relevant process intensification examples from pharmaceutical, polymer and biofuels industries are presented.


2017 ◽  
Vol 92 (8) ◽  
pp. 2178-2188 ◽  
Author(s):  
Danijela S Slavnić ◽  
Luka V Živković ◽  
Ana V Bjelić ◽  
Branko M Bugarski ◽  
Nikola M Nikačević

2021 ◽  
Vol 32 (2) ◽  
pp. 611-618
Author(s):  
Atena Dehghani Kiadehi ◽  
Mikel Leturia ◽  
Franco Otaola ◽  
Aissa Ould-Dris ◽  
Khashayar Saleh

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