Baffled Reactors for Continuous Reaction and Crystallisation
Submitting Institution
Heriot-Watt UniversityUnit of Assessment
ChemistrySummary Impact Type
TechnologicalResearch Subject Area(s)
Chemical Sciences: Other Chemical Sciences
Engineering: Chemical Engineering, Interdisciplinary Engineering
Summary of the impact
Research at Heriot-Watt University (HWU) has led to the development of a
new continuous
oscillatory baffled reactor and crystalliser technology. This has direct
economic and environmental
impact in the chemical, pharmaceutical and food industries. Waste is
substantially reduced, while
the scale of the equipment and plant is dramatically decreased, reducing
time to market, start-up
and maintenance costs and on-going energy usage. The reactor/crystalliser
was taken to market
through a spinout, NiTech Solutions Ltd, with a peak of 16 employees in
the REF period. Genzyme
(now Sanofi) has implemented NiTech's technology for biopharmaceutical
manufacture since
2007, with multi-100 ton production and sales of multi-£100M pa. The
technology now underpins
the larger-scale joint venture, the Continuous Manufacture and
Crystallisation (CMAC) consortium,
launched in 2010. CMAC has attracted over £60M investment, much of it from
three major
industrial partners, GSK, AstraZeneca and Novartis, with additional
second-tier investors. CMAC is
accelerating the introduction of new process-intensification technologies
in the process industries.
Underpinning research
Traditional batch technologies for manufacture of fine chemicals are
inherently inefficient due to
the difficulties of consistently meeting product specifications. This
incurs significant financial
penalties and generates waste. The current norm is that for every 1 kg of
active pharmaceutical
ingredient (API) harvested, 50 to 200 kg of waste is produced. The typical
raw material cost for a
single batch of API is £1 to £5M. Many of these products (over 90% of
pharmaceuticals and 80%
of fine chemicals) are of crystalline form and involve a crystallisation
step in their production cycle.
The control of crystal purity, morphology and size distribution therefore
has a significant impact on
the efficiency and profitability of the overall production.
Research of Prof Xiongwei Ni at Heriot-Watt University has successfully
addressed the
underpinning physical principles that are responsible for these
limitations of traditional batch
reactors and crystallisers. The work was stimulated, in part, by the
results of a 9-year EPSRC-
funded project (part of which was carried out at HWU) `Chemicals Behaving
Badly'. This identified
that the key to delivering consistent product specifications included the
control of cooling (linear)
profile and the attainment of uniform mixing. However, neither of these
features is achievable in
industrial batch systems, due to the facts that mixing becomes less
efficient and the specific area
per unit volume for heat transfer decreases dramatically with scale. This
makes any controlled
cooling profiles problematic to implement in any industrial production.
Ni's research has focused on understanding the science of achieving
uniform mixing at all scales in
plug flow under laminar flow conditions1, 2 The
continuous oscillatory baffled reactor and crystalliser
technology developed as a result of this research combines both uniform
mixing with precise
temperature control, allowing any desired cooling profiles, e.g. linear,
nonlinear, step function,
parabolic, etc., to be achieved from lab to full scales. The applicability
of the technology has been
demonstrated for transport processes, reactions and crystallisation.3, 4
Major patents have been
filed on both apparatus and method.5 The technology eliminates
the two fundamental problems
encountered in traditional industrial scale crystallisers identified
above. It also enables kinetic
reaction time to be executed at all scales, shrinking the space required.
Unlike standard batch
systems, laboratory monitoring tools have been shown to be capable of
being implemented on
industrial scales without modification, facilitating smooth, direct and
fast transition from the
laboratory to production. Knowledge gained in the laboratory can be
applied directly in production,
again unlike in traditional full-scale operations due to the effects of
non-scalable mixing.
Trials with a large number of chemical, food and pharmaceutical compounds
(>60) from various
industrial companies have firmly reinforced that the technology delivers
consistent product quality,
e.g. size distribution, morphology, yield and purity, with significant
reductions (>90%) in process
time, waste and unwanted products, as well as in energy, utility, plant
size and inventory.6
Continuous reaction and crystallisation are now identified as critical
steps in process-intensification
drives to improve manufacturing in the chemical and pharmaceutical
industries, through more
efficient use of reagents, solvents and energy while minimizing side
reactions, unwanted products
and waste materials.
References to the research
(* = best indicates the quality of the underpinning research)
2. Ni X, Jian H and Fitch AW, Evaluation of turbulent integral length
scale in an oscillatory
baffled column using large-eddy simulation and digital particle image
velocimetry. Trans
IChemE 81: 842-853 (2003). http://dx.doi.org/10.1205/026387603322482086
3. Ni X, Valentine A, Liao A, Sermage SBC, Thomson GB and Roberts KJ, On
the crystal polymorphic forms of L-glutamic acid following temperature programmed
crystallisation in a batch oscillatory baffled crystalliser. Crystal Growth and
Design 4: 1129-1135 (2004).
http://dx.doi.org/10.1021/cg049827l
4.* Ni X and Liao A, Effects of cooling rate and solution
concentration on solution crystallisation
of L-glutamic acid in an oscillatory baffled crystalliser. Crystal
Growth and Design 8: 2875-2881
(2008). http://dx.doi.org/10.1021/cg7012039
5. Ni X, Laird I and Liao A, Improved apparatus and method for
temperature controlled processes. EU patent WO 2007060412 A8 (22 November 2006).
6.* Lawton S, Steele G, Shering P, Zhao L, Laird I and Ni X, Continuous
crystallisation of
pharmaceuticals using a continuous oscillatory baffled crystalliser.
Organic Process
Research & Development 13: 1357-1363 (2009). http://dx.doi.org/10.1021/op900237x
Research grants:
1998 - 2001 EPSRC GR/M31309/01 £233,423 with Bonar Polymers Ltd
and Professor David
Sherrington of Chemistry, Strathclyde University on application of the
oscillatory baffled reactor to
continuous polymerisation processes
2000 - 2003 EPSRC GR/M63447/01 £193,175 on fluid flow
measurement using high resolution
digital particle image velocimetry
2000 - 2002 £36,000 Yorkshire Water on continuous coagulation
using an oscillatory baffled
Reactor
2003 - 2003 £100,000 Department of Trade and Industry (DTI) and
James Robinson Ltd on
continuous production of a photochemical using oscillatory baffled
reactor
2004 - 2005 £50,000 SMART: Scotland Award on a feasibility
study of continuous production of
a family of nano particles using an oscillatory-baffled reactor
2005 - 2006 £40,897 SMART: Scotland Award on a feasibility
study of continuous crystallisation
of l-glutamic acid using an oscillatory-baffled crystalliser
2009 - 2010 £55,819 Technology Strategy Board (TSB) Award on achieving
greater consistency
in the modification of human recombinant proteins through scaleable
continuous-production
process technology
2009 - 2011 €28,245 out of €958,429 from a FP7 Project on development
of continuous
oscillatory baffled reactor to enable the creation of graduated radar
absorbing multi-layer structures
for wind turbine applications
2010 - 2014 £148,384 two PhD studentship by the Scottish Founding
Council on probing into
how nucleation was generated without seeds in oscillatory baffled
crystalliser while seeding was
essential in traditional batch crystalliser
2012 - 2012 £53,048 from Continuous Manufacturing and
Crystallisation (CMAC) Industrial
Consortium on the effect of seed size and quantity on crystal
properties
Details of the impact
NiTech Solutions Ltd was spun off from Heriot-Watt University in Dec
2004, aided by a SMART
award from Scottish Enterprise, with plug-flow crystallisation and
reaction as the key technologies
for chemical, pharmaceutical and food industries. A second SMART award on
continuous
crystallisation supported Dr Anting Liao, Xiongwei Ni's ex-PhD student
from HWU, to be employed
at NiTech to carry out the designed trials. Excellent results were
generated; for example,
consistent crystal morphology/size distribution/enhanced yield,
significantly reduced process time
and waste, and elimination of the use of milling machines. An example of
the impact of the
technology is the continuous crystallisation of one of the AstraZeneca's
blockbuster drug
ingredients. In their operation in traditional crystallisers, it takes 9
hours and 40 minutes for the
crystallisation step; the filtration rate is poor because of uneven sizes
of crystals generated due to
the difficulties, identified above, of controlling the crystallisation
environment. In order to obtain the
required size a milling machine is used as one of the key downstream unit
operations. When
applying NiTech continuous crystallising technology, the overall process
was shown to take only 12
minutes with uniform sizes, enhanced filtration rates (which eliminate the
use of the milling
machine) and significant savings in capital and operational costs (see ref
[6] above).
Another leading example is the production of a biopharmaceutical drug in
Genzyme (now Sanofi).
In less than two years from conception in 2005, full production was
commissioned at the Haverhill
site in April 2007 after successful trials and design at NiTech as well as
the certification of the
process by the FDA. NiTech technology was used to launch production of a
new active
pharmaceutical ingredient (API) via a three-phase reaction on the scale of
multi-hundred tons p.a.
with a value of multi-£100M p.a. The reaction is approximately 40 times
faster than a batch
process, with good flexibility to control throughput. The reactor was able
to fit into a small footprint
in an existing building, avoiding the traditional alternative of two large
pressure reactors and a new
building. There was a resultant saving of several million pounds in
capital expenditure and
approximately four times faster construction. Simplicity of operation and
reduced maintenance
costs have been sustained. Product quality is higher, with the ability to
continuously monitor and
control the reaction leading to a zero reject rate for this reaction step,
all contributing to a
competitive commercial advantage. Quoting a Senior Manager of Genzyme:
"This is believed to be the largest scale continuous manufacturing
plant for a patented API in the
world. Importantly, we were able to supply the market many months
earlier than would have been
the case with conventional batch processing. This was one of the best
investment decisions that I
have made! "
[text removed for publication]
NiTech has filed key patents on continuous crystallisation, worked with a
large number of chemical,
food and pharmaceutical companies on continuous crystallisation, including
seven out of the top
ten global pharma giants and two out of the top three global food
companies on edible oils. It has
received investments over £3M and employed more than 16 people.
Following discussions between NiTech, GSK, and members of the ScotCHEM
research pooling
and Chemical Sciences Scotland industry-academia collaborative initiatives
on how to further
exploit this technology, a joint demonstration project was established in
mid-2009. GSK provided
`model' crystallisation process and materials. Outstanding results were
obtained in these trials. It
was seen as an opportunity for Scotland to take the lead in meeting the
challenges facing chemical
manufacturing globally. This led to continuous crystallisation being the
platform technology in the
GSK-led Continuous Manufacture and Crystallisation (CMAC) consortium. CMAC
was established
in 2010 with £1M cash injection and £1M in kind each from GSK,
AstraZeneca and Novartis as the
tier-one members, plus £250k from tier two members including Fujifilm,
Genzyme, Croda,
Syngenta, Evonik, NiTech itself and others. In 2010/11, NiTech changed its
business model to
become an integrator and facilitator, focussing on collaboration with an
engineering company
rather than manufacturing the reactors itself. It is a critical part of
CMAC, indeed, according to a
member of the Board
"NiTech's technology is the technology that started it all off".
CMAC has now grown into a >£60M consortium with research grants from
EPSRC Centre for
Innovative Manufacturing (£9.1M), ESPRC DTC (£6.9M), Scottish Funding
Council (£1.5M), TSB
(1.75M), EPSRC ICT Platform (£4M), EU (£0.5M), and EPSRC RPIF (£34M). CMAC
is now the
largest and the most comprehensive centre in the world on continuous
crystallisation. It is focused
on helping industry to evaluate and trial leading edge process solutions
against their requirements
and to accelerate the introduction of new process-intensification
technologies to meet wider
industry needs.
Sources to corroborate the impact
A senior manager with technical responsibilities, Genzyme.
A member of the Board of NiTech Solutions.
A member of the Board of Chemical Sciences Scotland.
A senior manager in Investigational Materials Supply, GlaxoSmithKline.
www.nitechsolutions.co.uk