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Design, Development and
Evaluation of an ‘Oscillatory Flow Bioreactor’
(OFBR)
Oscillatory baffled
reactors (OBR)
are a relatively new design of ‘intensified’
plug flow reactors. They provide a new type of
mixing device, which can be used for continuous
or batch applications (Jian and Ni, 2003).
In contrast to the
conventional plug flow reactor, the oscillatory
baffled reactor has equally spaced orifice plate
baffles (Stonestreet and Harvey, 2002). The
baffles divide the tubular reactor into single
chambers. When the fluid is oscillated, the
baffles cause the formation of vortices, which
leads to both radial and axial mixing. Thus, the
chambers each act like a single stirred tank
reactor, while the fluid is streaming through
them. The chaotic flow patterns lead to
instability and turbulence within the reactor
and provide intensive, uniform mixing.
Oscillation can be carried
out in two different ways: by oscillating the
fluid itself or the baffled device.
The OBR has
a number of advantages over other reactors which
might make it useful for special applications.
One major advantage is the good, uniform mixing,
which provides a good heat and mass transfer. The good mixing in OBR also
results in shorter reaction times. Shorter
reaction times lead to a reduced
length-to-diameter ratio in comparison to
conventional plug flow reactors and therefore a
more compact design. Thus the OBR is ideal for
long reactions. The shear in OBRs is more
uniform than in stirred tanks, which might be an
advantage especially for biological
applications. Scalability is a particular
advantage of the OBR because the mixing does not
change with scale, which makes a linear scale-up
possible and predictable.
As the technology can easily
be configured to suspend particles and for gas
contacting, the oscillatory baffled reactor
seems to be a valuable invention for different
types of process industries such as
pharmaceutical production, polymerisation and
biochemical engineering (Jian and Ni, 2003).
One of the most commercially
important classes of long reactions are
fermentations. Currently, new methods of
continuous fermentation are required to allow
conversion of a range of batch fermentation
processes to inherently more efficient
continuous processing.
As one major advantage of
the OBR is very good uniform mixing, providing a
good mass and oxygen transfer, it seems ideal
for microbial purposes. The possibility of
continuous fermentation is a second advantage as
it will minimise the substrate and product
inhibition.
Lower shear rates compared
to a stirred tank reactor may be an additional
advantage depending on the shear sensitivity of
cultures such as mammalian, insect and plant
cells, fungi and certain types of algae.
This project will initially
entail some design consideration of the new
design features required when bioreactions, as
opposed to chemical reactions, are to be
performed. That design will then be fabricated,
and the reactor assessed for a range of
applications provided by other partners within ‘Bioproduction’
and compared to conventional technology, to
determine when and how the OBR is a good
solution.
The main emphasis herein
will be to evaluate the reactor for bioprocesses
(various, including microbial production of
intermediates and functional biomaterials e.g.
biopolymers and enzymic biotransformations).
For
more information please contact
Prof Adam Harvey.
References
-
Harvey, A.P., Mackley, M.R.
and Seliger, T.: Process intensification of
biodiesel production using a continuous
oscillatory baffled reactor, Journal of Chemical
Technology and Biotechnology 78 (2003): 338 –
341
-
Jian, H. and Ni, X.-W.: On
modelling turbulent flow in an oscillatory
baffled column -RANS model or large-eddy
simulation? Journal of Chemical Technology and
Biotechnology 78 (2003): 321 - 325
-
Stonestreet, P. and Harvey,
A.P.: A mixing-based design methodology for
continuous oscillatory baffled reactors, Trans
IchemE 80 (A) (2002): 31 - 44
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