In this paper a rotor-stator spinning disk
reactor for intensified biodiesel synthesis is described and numerically simulated.
The reactor consists of two flat disks, located coaxially and parallel to each
other with a gap ranging from 0.1 mm to 0.2 mm between the disks. The upper
disk is located on a rotating shaft while the lower disk is stationary. The
feed liquids, triglycerides (TG) and methanol are introduced coaxially along
the center line of rotating disk and stationary disk, respectively. Fluid
hydrodynamics in the reactor for synthesis of biodiesel from TG and methanol in
the presence of a sodium hydroxide catalyst are simulated, using
convection-diffusion-reaction species transport model by the CFD software ANSYS?
Fluent v. 13.0. The effects of upper disk’s spinning speed and gap size are
evaluated.
References
[1]
Stankiewicz, A.I. and Moulijn, J.A. (2000) Process Intensification: Transforming Chemical Engineering. Chemical Engineering Progress, 96, 22-34.
[2]
Jachuck, R. (1995) Process Intensification for Responsive Processing. Trans IChemE, 80, 233-238.
http://dx.doi.org/10.1205/026387602753581980
[3]
Owen, J.M. and Rogers, R.H. (1989) Flow and Heat Transfer in Rotating-Disc Systems, Rotor-Stator Systems in Engineering Design Series, 1, John Wiley & Sons, Inc.
[4]
de Beer, M.M., Keurentjes, J.T.F., Schouten, J.C. and van der Schaaf, J. (2014) Engineering Model for Single-Phase Flow in a Multistage Rotor-Stator Spinning Disc Reactor. Chemical Engineering Journal, 242, 53-61.
http://dx.doi.org/10.1016/j.cej.2013.12.052
[5]
Qiu, Z.Y., Petera, J. and Weatherley, L.R. (2012) Biodiesel Synthesis in an Intensified Spinning Disk Reactor. Chemical Engineering Journal, 210, 597-609. http://dx.doi.org/10.1016/j.cej.2012.08.058
[6]
Freedman, B., Butterfield, R.O. and Pryde, E.H. (1994) Transesterification Kinetics of Soybean Oil. Journal of the American Oil Chemists’ Society, 63, 1375-1380. http://dx.doi.org/10.1007/BF02679606
[7]
Noureddini, H. and Zhu, D. (1997) Kinetics of Transesterification of Soybean Oil. Journal of the American Oil Chemists’ Society, 74, 1457-1463. http://dx.doi.org/10.1007/s11746-997-0254-2
[8]
Qiu, Z.Y. (2010) Intensification of Liquid-Liquid Contacting Processes. Ph.D. Thesis, University of Kansas, USA.