Synthesis of palm based biolubricant in an oscillatory flow reactor (OFR)

2014 ◽  
Vol 52 ◽  
pp. 567-574 ◽  
Author(s):  
May Ying Koh ◽  
Tinia Idaty Mohd. Ghazi ◽  
Azni Idris
2012 ◽  
Vol 84 ◽  
pp. 544-551 ◽  
Author(s):  
S. Melendi ◽  
S. Bonyadi ◽  
P. Castell ◽  
M.T. Martinez ◽  
M.R. Mackley

2018 ◽  
Vol 18 (10) ◽  
pp. 5940-5946 ◽  
Author(s):  
Filipa Castro ◽  
António Ferreira ◽  
José A. Teixeira ◽  
Fernando Rocha

2020 ◽  
Vol 10 (3) ◽  
pp. 475-490 ◽  
Author(s):  
Pauline Bianchi ◽  
Jason D. Williams ◽  
C. Oliver Kappe

Abstract Oscillatory flow reactors (OFRs) superimpose an oscillatory flow to the net movement through a flow reactor. OFRs have been engineered to enable improved mixing, excellent heat- and mass transfer and good plug flow character under a broad range of operating conditions. Such features render these reactors appealing, since they are suitable for reactions that require long residence times, improved mass transfer (such as in biphasic liquid-liquid systems) or to homogeneously suspend solid particles. Various OFR configurations, offering specific features, have been developed over the past two decades, with significant progress still being made. This review outlines the principles and recent advances in OFR technology and overviews the synthetic applications of OFRs for liquid-liquid and solid-liquid biphasic systems.


2013 ◽  
Vol 378 ◽  
pp. 418-423
Author(s):  
Gang Liu ◽  
Jia Wu ◽  
Wei Li

The three-dimensional construct of concentration field in an oscillatory flow reactor (OFR) containing periodically spaced conic ring baffles was investigated by numerical simulation employing Reynolds-averaged Navier-Stokes equations. The computation covered a range of Oscillatory Reynolds number (Reo) from 623.32 to 3116.58 at Strouhal number (St) 0.995 and 1.99. The contour of concentration field showed that the concentration in the most part of the channel is relative uniform and a small retention area is found below the conic ring baffles, which means a region of relative poor mixing. In addition, the turbulent diffusion coefficient calculated from the simulation results implied the greater oscillatory amplitude and oscillatory frequency superimposed to the fluid, the stronger is the turbulence intensity.


2018 ◽  
Vol 4 (2) ◽  
pp. 1-15 ◽  
Author(s):  
F. Almeida ◽  
F. Rocha ◽  
A. Ferreira

In this research paper the residence time distribution (RTD) was monitored for a range of fluid oscillation, frequency, amplitude and flow rate in two oscillatory flow reactors (OFR) provided with 2D smooth periodic constrictions (2D-SPC) with different designs. It was studied the axial liquid dispersion using axial dispersion model and the mixing efficiency using tank-in-series model for continuous mode. Two cases, with and without fluid oscillation, were studied and determined the optimum conditions to ensure a close plug flow, an efficient mixing and a low axial liquid dispersion. The optimum operation conditions for the two 2D-SPC designs were found. Moreover, the effect of open cross-sectional area (a) on mixing and axial dispersion was also investigated. For low cross-sectional area values the mixing is higher. It was observed that fluid oscillation increases the mixing intensity even at lower flow rates, and the axial dispersion increases as the flow rate increases.


2013 ◽  
Vol 52 (29) ◽  
pp. 9816-9821 ◽  
Author(s):  
Filipa Castro ◽  
António Ferreira ◽  
Fernando Rocha ◽  
António Vicente ◽  
José António Teixeira

2007 ◽  
Vol 47 (1) ◽  
Author(s):  
Nasratun Masngut ◽  
Mohd Sobri Takriff ◽  
Abdul Wahab Mohammad ◽  
Mohd Sahaid Kalil ◽  
Abdul Amir Hassan Kadhum

2021 ◽  
Vol 9 (6) ◽  
pp. 106505
Author(s):  
Ana L. Gonçalves ◽  
Filipe Almeida ◽  
Fernando A. Rocha ◽  
António Ferreira

2012 ◽  
Vol 455-456 ◽  
pp. 121-126 ◽  
Author(s):  
Peng Wu ◽  
Jia Wu ◽  
Wei Li

In published papers, the experimental researches have been carried out on heat transfer in Oscillatory Flow Reac-tors (OFRs) with annular baffles in both batch and continuous modes. It’s found that even with low net flow rates (or without net flow) the heat transfer properties of OFR can match turbu-lent pipe flow. But there’s no paper shows the micro-structure of temperature field in OFRs to illustrate the heat transfer mechan-ism. In this paper, we report our 3-dimensional numerical simu-lation results of heat transfer of OFR with novel conic ring baf-fles which is particularly suitable for liquid-solid systems. The temperature field of conic baffled OFR was obtained by using the commercial CFD package CFX11.0. It’s found that in “soft” mix-ing region the maximum temperature gradient lies approximate-ly in the middle of each cell, i.e. between the two pairs of vortices. It can be speculated that the convection caused by the intense vortex interaction leads to heat transfer essentially. When it’s global mixing, severe bias flow occurs. The temperature field becomes more chaotic and the heat convection is caused by more disordered vortex interaction.


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