Biotechnology Advances 24 (2006) 42 – 57
www.elsevier.com/locate/biotechadv
Research review paper
Enzymatic microreactors in chemical analysis and kinetic studies
Pawel L. Urban a, David M. Goodall a,*, Neil C. Bruce b
a
b
Department of Chemistry, University of York, Heslington, York, YO10 5DD, UK
CNAP, Department of Biology, University of York, Heslington, York, YO10 5YW, UK
Received 30 May 2005; accepted 3 June 2005
Available online 1 August 2005
Abstract
The fields of application of microreactors are becoming wider every year. A considerable number of papers have been published
recently reporting successful application of enzymatic microreactors in chemistry and biochemistry. Most are devices with enzymes
immobilized on beads or walls of microfluidic channels, whilst some use dissolved enzymes to run a reaction in the microfluidic
system. Apart from model systems, mostly with glucose oxidase, horseradish peroxidase and alkaline phosphatase, the principal
fields of application of microreactors are tryptic digestion of proteins and polymerase chain reaction in automated analyses of
proteomic and genetic material, respectively. Enzymatic microreactors also facilitate characterization of enzyme activity as a
function of substrate concentration, and enable fast screening of new biocatalysts and their substrates. They may constitute key
parts of lab-on-a-chip and ATAS, assisting the analysis of biomolecules. This review provides systematic coverage of examples of
reports on enzymatic microreactors published recently, as well as relevant older papers.
D 2005 Elsevier Inc. All rights reserved.
Keywords: Characterization of proteins and DNA; Enzyme immobilization; Lab-on-a-chip; Microfluidic systems; Microreactors
Contents
1.
2.
Introduction . . . . . . . . . . . . . . . . . . . . . . . . . . .
Applications of enzymatic microreactors . . . . . . . . . . . .
2.1. Analysis of chemical species. . . . . . . . . . . . . . .
2.1.1. Homogeneous and heterogeneous biocatalysis .
2.1.2. Analysis of proteins . . . . . . . . . . . . . . .
2.1.3. Analysis of nucleic acids . . . . . . . . . . . .
2.1.4. Model enzymatic systems . . . . . . . . . . . .
2.2. Other applications . . . . . . . . . . . . . . . . . . . .
2.2.1. Kinetic studies. . . . . . . . . . . . . . . . . .
2.2.2. Imaging of biotransformations in microreactors .
3. Conclusions and future trends. . . . . . . . . . . . . . . . . .
Acknowledgements. . . . . . . . . . . . . . . . . . . . . . . . . .
References . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
* Corresponding author. Tel.: +44 1904 435 328; fax: +44 1904 432 516.
E-mail address: dmg1@york.ac.uk (D.M. Goodall).
0734-9750/$ - see front matter D 2005 Elsevier Inc. All rights reserved.
doi:10.1016/j.biotechadv.2005.06.001
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
43
44
44
44
44
46
48
48
48
51
52
53
53
P.L. Urban et al. / Biotechnology Advances 24 (2006) 42–57
1. Introduction
Microreactors are usually defined as miniaturized
reaction systems fabricated by using, at least partially,
methods of microtechnology and precision engineering
(Ehrfeld et al., 2000). The term bmicroreactorQ is the
proposed name for a wide range of devices having
small dimensions, and a further division according to
size into nano, micro and minireactors is hardly ever
used (Ehrfeld et al., 2000). Most of the currently constructed microreaction devices take advantage of microfluidics and nanofluidics, which enables use of micro
and nanolitre volumes of reactive species and ensures
high efficiency as well as repeatability of biocatalytic
processes. Microreactors find applications in organic
synthesis (Haswell and Watts, 2003; Hessel et al.,
2004). An example of an application in biotechnology
is the fast multi-step synthesis of peptides (Watts et al.,
2001). The main benefits of application of microreactors in industry are: faster transfer of results of development work into production, earlier start of production
at lower costs, easier scale-up of production capacity,
smaller plant size, lower costs for transportation, materials and energy, and more flexible response to market
demands (Ehrfeld et al., 2000).
Though the majority of papers describe microreactors as components of microfluidic devices, this term is
also used in context of self-organised systems such as
reverse micelles (Madamwar et al., 1988; Chopineau et
al., 1998; Carvalho and Cabral, 2000), liposomes (Oberholzer et al., 1999; Walde and Ichikawa, 2001) and
microemulsions (Garti et al., 1997; Garti, 2003). Selforganised systems will not be discussed in this review.
Analytical systems which comprise microreactors are
expected to be characterized by outstanding repeatability
and reproducibility, due to replacing batch iterative steps
and discrete sample treatment by flow injection systems.
The possibility of performing similar analyses in parallel
is an attractive feature for screening and routine use.
Microreactors have been integrated into automated analytical systems (Pfohl et al., 2003), and as well as providing benefits from system automation this also
eliminates errors associated with manual protocols. Further advantages of the use of microreactors in analytical
chemistry are that they can be coupled with numerous
detection techniques (Schwarz and Hauser, 2001; Verpoorte, 2003a,b), and that pretreatment of the samples
can be carried out on the chip (de Mello and Beard, 2003;
Chiesl et al., 2005). Methods of injection of the fluids
into microchannels, and connecting and interfacing
microreactors with other system components, are also
being improved. This should help eliminate any remain-
43
ing obstacles to more widespread uptake of the technology (Fang, 2004). Miniaturized analytical assays are
useful in many branches of biotechnology (Guijt-van
Duijn et al., 2003). The influence of nanotechnology in
the development of biosensors has been reviewed by
Jianrong et al. (2004). Whilst recently published books
cover industrial applications of microreactors (Ehrfeld et
al., 2000; Hessel et al., 2004, 2005a,b), analytical applications are of increasing importance and are therefore
also surveyed in the present review.
Enzymatic microreactors have been developed in
order to facilitate routine work in biochemical analysis,
and also have applications in biocatalysis. A low expenditure of the enzyme is often a result of its immobilization. However, the range of immobilized enzymes
available with satisfactory characteristics is still limited
(Buchholz et al., 2005), which inevitably decreases the
number of potential applications. The following immobilized enzymes are used on an industrial scale: glucose
isomerase, sucrose mutase, h-galactosidase, penicillin
acylase, d-amino acid oxidase, glutaryl amidase, thermolysin, nitrilase, aminoacylase and hydantoinases
(Buchholz et al., 2005).
Enzymatic microreactors have been used for analytical applications as components of integrated systems,
often termed lab-on-a-chip or in micro total analysis
systems (ATAS) (Vilkner et al., 2004). Although the
first enzymatic microreactors were constructed in the
1970s and 1980s, the growth in their practical applications dates to the late 1990s. No examples of enzymatic
microreactors were included in the first comprehensive
book on microreactors published in 2000 (Ehrfeld et al.,
2000).
It is helpful to divide the analytical applications of
enzymatic microreactors into two classes. Firstly,
those which use biocatalysis in order to transform
an analyte difficult to measure into an easily measurable form. Secondly, microreactors designed for
screening of substrates, enzymes and examine their
kinetic characteristics. The first category is exemplified by the large number of microsystems designed
for digestion of proteins to convert them to morereadily measured peptides. Another example is oxidation of glucose by glucose oxidase followed by
measuring chemiluminescence of luminol oxidised
by hydrogen peroxide formed in the primary reaction
(L’Hostis et al., 2000). The second category is exemplified by work presented by Seong et al. (2003) to
quantitatively measure enzyme kinetics in a continuous-flow microfluidic system.
The aim of this review is to summarize recent
work in the field of enzymatic microreactors, which
44
P.L. Urban et al. / Biotechnology Advances 24 (2006) 42–57
constitutes a new branch of microtechnology. Objectives are to highlight new arising trends in the
development of enzymatic microreactors, to show
their present applications in applied analytical chemistry and biochemical studies, and to consider possible implications of enzymatic microreactors in
biotechnology.
2. Applications of enzymatic microreactors
The achievements in chemical and biochemical
microreaction systems before 2000 have been highlighted by Haswell and Skelton (2000). Developments
in immobilized microfluidic enzymatic reactors have
been discussed by Krenková and Foret (2004). Girelli
and Mattei (2005) have recently reviewed the applications of immobilized enzyme reactors in high performance liquid chromatography: most of the constructed
reactors used enzymes bound covalently to the support,
and the functional groups involved in the binding were
amino, epoxyl, carboxyl, diol and phenolic. Examples
were given of enzyme-catalysed reactions carried out
before or after the column separation, as well as in the
column.
2.1. Analysis of chemical species
This section commences with coverage of the types
of microreactors used, with the classification into homogeneous and heterogeneous biocatalysis. All of the
examples of successful application of enzymatic microreactors with immobilized enzymes presented in this
review can be classified into the following groups: (i)
analysis of proteins, (ii) analysis of nucleic acids, and
(iii) model enzymatic systems. Separate subsections
describe each in turn.
2.1.1. Homogeneous and heterogeneous biocatalysis
Microreactors may use an immobilized enzyme, or
its solution may be injected to the reaction zone; the
two approaches encompass heterogeneous and homogenous biocatalysis, respectively. The majority of published applications refer to use of immobilised
enzymes. An example of homogeneous biocatalysis
on a microscale is electrophoretically mediated microanalysis (EMMA), first described by Bao and Regnier
(1992) and later referred to as EMMA (Regnier et al.,
1995), which makes use of different mobility of an
enzyme and its substrate in order to mix the zones of
both and to accomplish bioconversion of the substrate
to the product. The enzyme solution is injected into a
fused silica capillary followed by injection of its sub-
strate, and the capillary is considered as the microreactor (Avila and Whitesides, 1993; Van Dyck et al.,
2003). In spite of the apparent complexity, such a
configuration is suitable for automation and control of
the time of contact between the catalyst and its substrate. However, the EMMA method is only feasible in
the case of fast catalytic processes, since contact times
are typically in the range milliseconds to seconds.
EMMA is advantageous because the amounts of enzyme and substrate used are extremely small (Kanie
and Kanie, 2003).
Apart from enzymes, another chemical species (e.g.
an antibody) may be immobilized in the microchannel
and an enzyme involved in the specific reaction may be
injected to the system (Yakovleva et al., 2002). Further
examples of microsystems without immobilized
enzymes involve conversions catalyzed by alkaline
phosphatase (Liu et al., 2004; Moorthy et al., 2004),
glucose oxidase, catalase, urease (Zhang and Tadigadapa, 2004), glycosidase (Kanno et al., 2002) and laccase (Maruyama et al., 2003), illustrating a wide range
of enzymes that can be applied in such microsystems.
The mode of operation involving homogeneous catalysis is relatively easy to achieve, since there is no need
for immobilization of the enzyme. A drawback of using
homogeneous biocatalysis and injecting the enzyme
solution to the microreactor is the difficulty of enzyme
recycling, as well as the necessity of its continuous
dosage. Nevertheless, the use of microfluidic components allows the reactions to be achieved in nanolitre
volumes without excessive expenditure of biocatalytic
species.
Use of microreactors with enzymes immobilized
either on packed beads or on the inner wall of the
channel does not require continuous supply of the
biocatalyst within the run. The substrates are normally
moved through the channel by application of pressure.
An alternative is by use of electroosmotic flow (Haswell and Skelton, 2000), which is potentially attractive
with microchannels packed with small particles which
would provide high backpressure. More information on
the solid supports used in microreactors can be found in
the review by Peterson (2005).
2.1.2. Analysis of proteins
The greatest number of recent applications of enzymatic microreactors refer to protein and peptide mapping (Table 1), an essential process in the identification
and sequencing of proteins. The most frequently used
enzyme is trypsin, the enzyme catalyzing the process of
protein digestion through hydrolysis of peptide bonds at
a basic residue.
45
P.L. Urban et al. / Biotechnology Advances 24 (2006) 42–57
Table 1
Application of enzymatic microreactors in the analysis of proteins
Enzyme
Medium
Application
Reference
Chymotrypsin
Chymotrypsin,
trypsin, papain
Silicon
Magnetic microparticles
Ekström et al., 2000
Korecka et al., 2004
Pepsin
Gel on a photopolymerized
porous silica monolith
Protease
Protease
Trypsin
Fused-silica capillary (metal–ion
chelated adsorption )
Porous wall of a capillary
Controlled pore glass
Trypsin
Trypsin
Controlled pore glass
Fused-silica capillary
Trypsin
Trypsin
Fused-silica capillary
Fused-silica capillary
Trypsin
Trypsin
Peptide mapping
Jiang et al., 2000b
On-line frontal analysis
of enzymatic products
Digestion of insulin
Protein patterning
Jiang et al., 2000a
Trypsin
Gel beads
Glycidyl methacrylatemodified cellulose membrane
Glycidyl methacrylatemodified cellulose membrane
Glycidyl methacrylatemodified cellulose
Injected
Micropatterned sol–gel
structures in polydimethylsiloxane
microchannels
Monolith
Protein identification
Specific fragmentation
of high molecular-mass
and heterogeneous
glycoproteins
Protein digestion,
peptide separation,
and protein identification
Peptide mapping analysis
of proteins
Protein mapping
On-line protein digestion,
preconcentration, separation
and detection (in UV)
Peptide mapping
Analysis of proteins
and peptides
Digestion of proteins
On-column digestions
of small amounts of proteins
Digestion of proteins
Peptide mapping
Peterson et al., 2003
Trypsin
Trypsin
Monolith
Monolithic capillary column
Trypsin
Trypsin
Trypsin
Porous polymer monolith
Porous polymer monolith
Porous polymer monolith in
fused-silica capillary
Porous silicon
Enzyme digestion for
peptide mapping
Analysis of proteins
Digestion of picomoles
of proteins
Protein mapping
Peptide mass mapping
Peptide mass mapping
Bengtsson et al., 2002
Jiang and Lee, 2001
Trypsin
Trypsin
Trypsin
Trypsin
Trypsin, glucose
oxidase
Trypsin
Trypsin
PVDF membrane disk
Trypsin
Trypsin
Trypsin and pepsin
(proteases)
Trypsin
RP beads
Silica gel microchannels
Fused-silica capillary
High-speed on-line
protein digestion
Protein mapping
(lactate dehydrogenase)
Extraction of proteins
from 2D gels and digestion
Protein mapping
Proteomic research
Peptide mapping
poly(vinylidene fluoride)
in Poly(dimethylsiloxane)
channel
Rapid protein digestion,
peptide separation, and
protein identification
Porozyme
One example of such a system involves a homemade microreactor with trypsin immobilized on controlled pore glass (CPG) beads (Bonneil et al., 2000),
Kato et al., 2004
Guo et al., 2003
Guo et al., 2002
Bonneil and Waldron, 2000
Bonneil et al., 2000
Licklider et al., 1995
Licklider and Kuhr, 1998
Amankwa and Kuhr, 1992
Jin et al., 2003
Jiang et al., 2000c
Gottschlich et al., 2000
Kim et al., 2001
Xie et al., 1999
Ye et al., 2004
Peterson et al., 2002a
Palm and Novotny, 2004
Peterson et al., 2002b
Samskog et al., 2003
Cooper and Lee, 2004
Ekström et al., 2002
Qu et al., 2004
Licklider and Kuhr, 1994
Fig. 1. The microreactor was prepared by dry-packing
into a fused silica capillary (530 Am i.d.) under sonication. An HPLC column was used as a reservoir contain-
46
P.L. Urban et al. / Biotechnology Advances 24 (2006) 42–57
Fig. 1. Set-up for digestion in the immobilized-trypsin microreactor. Reprinted from Bonneil et al. (2000) with permission from Elsevier.
ing the trypsin-CPG beads. A low pressure of argon gas
was applied to drive the buffer solution containing a
protein sample through the capillary. The flow rate in
the system was calibrated by collecting and weighing
the amount of solution emerging from the microreactor
in a measured time. The system could be constructed in
30 min. A peptide map of h-casein was obtained within
the total time of 3 h (digestion and CE separation).
Microreactors can be easily attached to the nebuliser
for an electrospray ionisation (ESI) interface to mass
spectrometry (MS), providing an on-line system. Alternatively, the product fractions may be sampled prior to
off-line analysis by means of matrix assisted laser
desorption ionisation — time of flight (MALDITOF)-MS. Although trypsin is the most frequently
used catalyst for protein hydrolysis, other proteases
(e.g. chymotrypsin, pepsin and papain) may also be
utilised. The enzymes are immobilized on a variety of
media, either particles filling the microreactor cavity, or
bound to the inner walls of the capillary (Nashabeh and
Rassi, 1992; Verpoorte, 2003a). In the latter case, there
are no backpressure constraints during sample injection.
Enzyme immobilization on the walls of fused-silica
capillaries is also convenient because such capillaries
are widely available and inexpensive, and because electrophoretic separation can be carried out in the same
capillary as the enzymatic reaction. This approach can
in principle reduce systematic errors associated with
moving the sample from the microreactor into the
separation zone.
2.1.3. Analysis of nucleic acids
A notable achievement of microtechnology has been
setting up systems with microreactors for polymerase
chain reaction (PCR), enabling automation of DNA
amplification. This has allowed the construction of
high throughput systems for fast analysis of genetic
material. Typically, the substrates for PCR reaction
and polymerase enzyme are injected into the reaction
zone (Zhang and Yeung, 1998; Khandurina et al., 2000;
Lee et al., 2000; Nagai et al., 2001; Schneegass et al.,
2001; Ke et al., 2004), and a thermal cycling
P.L. Urban et al. / Biotechnology Advances 24 (2006) 42–57
programme is applied to enable amplification of the
DNA chain. Nagai et al. (2001) produced a microarray
with microchambers of dimensions 80 80 Am and
volume 85 pl. Each chamber could contain as little as
a single molecule prior to DNA amplification. Ke et al.
(2004) designed a silicon-based system with an internal
cavity volume of 7 Al for carrying fast detection of the
DNA sequence characteristic for Mycobacterium tuberculosis, based on mutation in the 81 bp region of rpoB
gene. In comparison with current methods for diagnosis
of tuberculosis, this provides significant savings in time
and cost of enzymes and reagents.
A few authors have described microdevices for further analysis of DNA, including its digestion with
restrictases (Washizu et al., 1996; Burns et al., 1998;
Katsura et al., 2004). Uptake of such systems could
improve automation in providing restriction maps for
plasmids, which are routinely required in many research
protocols in molecular biology. Fig. 2 shows the device
constructed by Burns et al., 1998. It incorporates PCR
as well as separation of the product with capillary
electrophoresis. As little as 10 ng Al 1 of DNA in
120 nl drops could be detected. DNA sequencing in
microsystems has been reviewed by Kan et al. (2004),
and Lagally and Mathies (2004) have covered recent
47
developments in technologies available for genetic
analysis on a microscale.
Chip-based devices for genomics and proteomics,
including PCR, have been discussed by Sanders and
Manz (2000). Schneegaß and Köhler (2001) reviewed
the development of a variety of devices and components for performing DNA amplification, and gave a
comparison of batch-process thermocyclers with reaction chambers and flow-through devices for different
purposes. They pointed out the advantages of using
microdevices, not only because of the size reduction
but also for their greater efficiency. The heating and
cooling elements possess small volumes and heat capacities, which yield high heating and cooling rates,
typically in the range 15–40 K s 1. Conventional thermocyclers achieve heating and cooling rates of approximately 2–10 K s 1, a factor of 4 or more lower than
the microdevices. Kricka and Wilding (2003) have
discussed general aspects of miniaturization trends
concerning PCR. Hashimoto et al. (2003) have described a ATAS for DNA analysis including amplification, purification, sequencing and separation, and have
recently highlighted the influence of flow rate on the
kinetics of the PCR reaction under continuous flow
conditions (Hashimoto et al., 2004).
Fig. 2. Schematic of integrated device with two liquid samples and electrophoresis gel for nanolitre analysis of DNA. Reprinted with permission
from Burns et al. (1998). Copyright (1998) AAAS.
48
P.L. Urban et al. / Biotechnology Advances 24 (2006) 42–57
2.1.4. Model enzymatic systems
A variety of immobilization techniques and microfluidic designs have been used to build enzymatic
microreactors designed for use in analysis of chemical
species (Table 2). The most widely-used supports for
immobilization of enzymes are beads of silicon or glass,
although there are numerous particular solutions including immobilization on the inner walls of microfluidic
channels and fused silica capillaries. The most popular
enzymes for testing immobilization efficiency and
assaying the microreaction process are glucose oxidase
(Murakami et al., 1993; Laurell and Rosengren, 1994;
Laurell et al., 1995; Drott et al., 1997; Folly et al., 1997;
Drott et al., 1999; Kulys, 1999; Niwa et al., 1999;
Bengtsson et al., 2000; L’Hostis et al., 2000; Strike et
al., 2000; Bengtsson et al., 2002; Mao et al., 2002; Park
and Clark, 2002; Wilhelm and Wittstock, 2002; Zhan et
al., 2002; Park et al., 2003; Holden et al., 2004;
Nomura et al., 2004; Xu and Fang, 2004), horseradish
peroxidase (Mao et al., 2002; Park and Clark, 2002;
Wilhelm and Wittstock, 2002; Zhan et al., 2002; Heule
et al., 2003; Lv et al., 2003; Seong et al., 2003; Holden
et al., 2004) and alkaline phosphatase (Mao et al., 2002;
Park et al., 2003; Gleason and Carbeck, 2004; Holden
et al., 2004; Koh and Pishko, 2005). These enzymes are
relatively cheap and easily accessible, and their chemical nature and the reactions catalyzed by them are well
understood. In work by L’Hostis et al. (2000) a microscale electrochemiluminescence (ECL) detector was
used to monitor the products of conversion of glucose
by glucose oxidase immobilized on glass beads with
luminol as a chelator. It allowed the detection of glucose within the biologically-relevant range 50–500 AM.
In the near future, it is expected that work using model
enzymes will be augmented by studies with other
enzymes useful for analytical assays.
2.2. Other applications
Apart from applications in analysis of chemical
species, several of the methods presented in the previous sections are also useful in kinetic characterization
of enzymes. This will be covered in Section 2.2.1.
There have been several attempts to use imaging techniques to directly visualize within the microchannel the
product formed in the course of reaction. Imaging
techniques applied with enzymatic microreactors are
discussed in Section 2.2.2.
2.2.1. Kinetic studies
Microreactors offer significant advantages for online monitoring of biocatalysis and characterisation of
kinetics of supported enzymes. Generally, such
enzymes are of better stability than when in free solution (Cao, 2005). Microreactors enable the key parameters characterising the kinetics, K m and v max, to be
determined for immobilized enzymes. Characterization
of new immobilized enzymes can be facilitated by
using miniaturized systems in continuous flow mode.
Results are obtained using very small quantities of
immobilized enzymes and the methods are readily amenable to automation of the protocols. Such methods
overcome problems with batch assays for immobilized
enzymes, e.g. the difficulty of mixing of the solid
particles containing supported enzyme with the substrate solution.
Seong et al. (2003) showed that the Michaelis constant determined with a microfluidic device with immobilized horseradish peroxidase was similar to the value
obtained during homogeneous catalysis in batch mode.
An interesting method for determining K m and v max
was presented by Jiang et al. (2000a), who applied online frontal analysis of peptides originating from the
digestion by trypsin immobilized on glycidyl methacrylate-modified cellulose. The Lineweaver–Burke diagrams were easily constructed, based on the effects of
injection of different concentrations and variation of
flow rate of the substrate solution. Bilitewski et al.
(2003) highlighted the application of microfluidic systems to enzymatic reactions.
In many cases, an enzymatic reaction is very fast and
can reach equilibrium within a single passage of substrate stream through the microreaction channel. However, several biotransformations, for example those
catalyzed by lipases, are slower. In these cases, a recirculating system can be constructed using a loop of
tubing together with the reactor, as in Fig. 3 (Pijanowska et al., 2001). The substrate solution was
pumped through the system with a peristaltic pump.
Three types of immobilization were tested, and high
performance of the units was demonstrated with either
glass beads or nitrocellulose sheets as enzyme carrier,
while entrapment within alginate gel beads was shown
to give unsatisfactory results. Hydrolysis of the substrate was measured by change of pH during the initial
phase of the reaction over a 25 min period; the time to
reach the steady-state was estimated at 110 min. Use of
pH measurement to monitor progress of the reaction
was shown to be sensitive, 0.478 pH/mM for tributyrin
(b4 mM). Scaling down the dimensions of the microreactor, and immobilizing the enzyme (lipase) inside a
fused silica capillary leads to very short times for the
hydrolysis (Kaneno et al., 2004). This shows that application of microreactors with immobilized lipases
49
P.L. Urban et al. / Biotechnology Advances 24 (2006) 42–57
Table 2
Model enzymatic systems involving microreactors
Enzyme
Medium
Application
Refs.
Acetylcholinesterase, urease
Poly(ethylene glycol) hydrogel
Yadavalli et al., 2004
Alanine aminotransferase,
glutamate oxidase
Alkaline phosphatase
Sieved porous glass beads
Biotransformation in
hydrogel arrays
Determination of l-alanine,
a-ketoglutarate and l-glutamate
Development of microscale
steady-state kinetic analysis
Method for photopatterning
well-defined patches of enzymes
inside a microfluidic device
Glass slide
Alkaline phosphatase
and bienzymatic system
(glucose oxidase and
horseradish peroxidase)
Alkaline phosphatase
and bienzymatic system
(glucose oxidase
and peroxidase)
Alkaline phosphatase,
glucose oxidase,
horseradish peroxidase
Poly(dimethylsiloxane)/glass
Alkaline phosphatase, urease
Hydrogel copolymerized
with enzymes
Silicon
Silicon wafer
Fused-silica capillary
Ascorbate oxidase
Aatalase, penicillinase
Cucumisin, l-lactic
dehydrogenase
Different enzymes
Glucose dehydrogenase
Glucose oxidase
Glucose oxidase
Glucose oxidase
Glucose oxidase
Janasek and Spohn, 1999
Gleason and Carbeck, 2004
Holden et al., 2004
Nitrocellulose membrane on glass
Method for immobilizing
enzymes without chemical
modification of a microchannel
Park et al., 2003
Phospholipid bilayers inside
poly(dimethylsiloxane)
microchannels
Rapid determination of
enzyme kinetics at many
different substrate concentrations
by carrying out laminar flowcontrolled dilution on-chip
pH-sensitive fluorophore
used to monitor changes of pH
Glutamate monitoring
Sensing of microlitre samples
Development of immobilization
techniques
Direct incorporation of the
enzyme onto the wall material
Study of PQQ-dependent
quinoprotein (use of scanning
electrochemical microscopy)
Determination of glucose
Mao et al., 2002
Determination of glucose
Determination of codeine
and glucose
Glucose measurement by FIA
Strike et al., 2000
L’Hostis et al., 2000
l-glutamate monitoring
Glucose monitoring
Influence of the matrix
depth investigated
Determination of glucose
Glucose measurement in flow
Continuous glucose monitoring
in a microdialysis-based system
Glucose and glutamate monitoring,
myoglobin cleavage
Determination of glucose
Niwa et al., 1999
Drott et al., 1997
Drott et al., 1999
Polydimethylsiloxane cast
on silicon/SU-8 moulds
Streptavidin-coated
paramagnetic beads
Aminopropyl controlledpore glass particles
Controlled-pore glass
Controlled-pore glass beads
Glucose oxidase
Glucose oxidase
Glucose oxidase
Enzyme-immobilized
magnetic microparticles
Fused silica
Porous silicon
Porous silicon
Glucose oxidase
Glucose oxidase
Glucose oxidase
Silica
Silicon chip
Silicon wafer
Glucose oxidase,
ascorbate oxidase, trypsin
Glucose oxidase,
horseradish peroxidase
Glucose oxidase,
horseradish peroxidase
Glucose oxidase, invertase
Porous silicon
Glass-supported aminopropyl
Horseradish peroxidase
Sapphire wafer
Horseradish peroxidase,
uricase
Sol–gel
Hydrogel copolymerized
with enzymes
Polycrystalline gold and glass
Formation of micropatterns
of enzymes
Determination of glucose
and sucrose
Use of homovanillic acid
fluorescence assay
Determination of uric acid
Koh and Pishko, 2005
Collins et al., 2001
Xie et al., 1992
Miyazaki et al., 2004
Jones et al., 2002
Zhao and Wittstock, 2004
Xu and Fang, 2004
Nomura et al., 2004
Kulys, 1999
Murakami et al., 1993
Laurell et al., 1995
Bengtsson et al., 2000
Zhan et al., 2002
Wilhelm and Wittstock, 2002
Folly et al., 1997
Heule et al., 2003
Lv et al., 2003
(continued on next page)
50
P.L. Urban et al. / Biotechnology Advances 24 (2006) 42–57
Table 2 (continued)
Enzyme
Medium
Application
Refs.
Horseradish peroxidase,
h-galactosidase
Lipase
Microbeads
Seong et al., 2003
Glass beads, alginate gel
beads, nitrocellulose sheets
SiO2-coated microcapillary
Sol–gel arrays
Measurement of enzyme kinetics
(fluorescence imaging)
Hydrolysis of triacetin,
tributyrin and triolein
Hydrolysis of umbelliferone acetate
Screening of proteins (enzymes)
Silicon wafer
Ni-NTA agarose beads
Silica monolith
Aminopropyl glass particles
Polydimethylsiloxane
Porous silicon
Continuous glucose measurements
Rapid hydroxylation of macrolides
Transesterification (glycidol, n-butyrate)
Quantification of trehalose
High urea conversion in continuous flow
Determination of sucrose
Laurell and Rosengren, 1994
Srinivasan et al., 2004
Kawakami et al., 2005
Bachinski et al., 1997
Jones et al., 2004
Lendl et al., 1997
Lipase
Lipases, proteases,
glucose oxidase,
horseradish peroxidase
Peroxidase, glucose oxidase
PikC hydroxylase
Protease
Trehalase
Urease
B-Fructosidase
offers a great advantage by shortening the analysis time.
In batch reactions, completion of enzyme-catalysed
transesterification may take days for some supported
lipases (Kamal et al., 2002).
On account of reproducible distribution of the products formed along the axes of the microreactor, the
enzymatic process can be visualized by fluorescence
microscopy in order to acquire data on the concentration
patterns inside the device. Such an approach was presented by Seong et al. (2003), and fluorescence images
of the reaction zone together with scaled numerical
results from the cross-sections of input and output
streams are shown in Fig. 4. The method provided
high sensitivity for product detection and short response
time, and kinetic graphs of the reaction catalyzed by the
enzyme (horseradish peroxidase) were obtained. The
Lilly–Hornby model was used to characterize the kinet-
Pijanowska et al., 2001
Nakamura et al., 2004
Park and Clark, 2002
ics of biocatalysis in the packed microcolumn, and
results were compared with those for kinetics of the
enzyme in homogeneous solution. The Michaelis constants were found to be similar to those obtained from
the Lineweaver–Burke model for the homogeneous catalysis. In comparison with standard assays, the amount
of enzyme used was very small: Seong et al. (2003)
estimated that 200 pmol (3 109 molecules of enzyme)
were required for the analysis. The current trend in
biochemical analysis is to decrease the amount of biocatalyst used. Recently, Moore et al. (2004) presented an
assay for 500 lipase molecules, capable of application to
single cells. Rondelez et al. (2005) described an assay
for monitoring reaction catalyzed by a single molecule
of h-galactosidase and horseradish peroxidase.
The kinetics model described by Lilly et al. (1966) is
appropriate for systems with continuous flow of the
Fig. 3. Schematic for continuous-flow reaction and monitoring of hydrolysis of esters using microreactor packed with lipase immobilized onto either
nitrocellulose sheets or glass beads coated with keratin. Reprinted from Pijanowska et al. (2001) with permission from Elsevier.
P.L. Urban et al. / Biotechnology Advances 24 (2006) 42–57
51
Fig. 4. (A) Horse radish peroxidase-catalyzed reaction between non-fluorescent amplex red and H2O2 to yield fluorescent resorufin. (B)
Fluorescence micrograph of the microreactor during continuous-flow operation. The substrate solution contained 5 AM H2O2 and 10 AM amplex
red in 50 mM Tris-HCl buffer (pH 7.4) and was introduced into the microreactor from left to right. Flow rate, 0.5 Al min- 1. (C) Normalized
fluorescence intensity line scans obtained at locations indicated by the dashed lines in (B). The excitation and maximum emission wavelengths were
563 and 587 nm, respectively. Reprinted with permission from Seong et al. (2003). Copyright (2003) American Chemical Society.
substrate and under steady-state conditions, and can be
summarized by the following equation:
Ps0 ¼ KmV lnð1 PÞ þ C=Q
ð1Þ
where P is the fraction of substrate reacted in the
column, s 0 the substrate concentration at the beginning,
KVm the apparent Michaelis constant, C the reaction
capacity of the reactor, and Q the flow rate of the
substrate. This formula allows determination of the
apparent Michaelis constant of the catalytical process
when all other parameters are known. If any masstransfer effects contribute to dynamics, an extrapolation
to zero flow rate is required to obtain the value of the
Michaelis constant for comparison with that of free
enzyme (Seong et al., 2003).
Mass transfer is always an important issue when
considering enzymes entrapped in supports, and the
ideal situation is when diffusion of substrate and product into and out of the bulk solution is not the rate
limiting process. Koh and Pishko (2005) determined
Michaelis constants of enzymes entrapped in hydrogel
micropatches in microfluidic channels using Lineweaver–Burke graphs. Values were found to be lower, by
approximately an order of magnitude, than those
obtained from experiments using the homogeneous
enzymes. The influence of entrapment in the hydrogel
nanostructure on the kinetic properties of the enzymes
was discussed.
2.2.2. Imaging of biotransformations in microreactors
Apart from the study described in Section 2.2.1.
(Seong et al., 2003), up to now there have been few
other attempts to image the enzymatic reaction zone. In
the continuous flow mode, imaging allows comparison
of the signals at inlet and outlet of the microreactor, and
hence data on the rate of substrate conversion in a
single pass of the reactor. Koh and Pishko (2005)
used seminaphthofluorescein (SNAFL-1) as a pH indicator and enzymes copolymerized with poly(ethylene
glycol) to monitor biocatalytic processes resulting in a
change of acidity. Variations in the fluorescence intensity were monitored by fluorescence microscopy during
52
P.L. Urban et al. / Biotechnology Advances 24 (2006) 42–57
the hydrolysis of p-nitrophenylphosphate and urea catalyzed by alkaline phosphatase and urease, respectively.
Yadavalli et al. (2004) presented a microarray-based
system with immobilized enzymes which enabled
screening of low concentrations of enzyme substrates.
The hydrogel arrays were prepared photolithographically on silicon surfaces. In earlier work, Zhan et al.
(2002) developed a similar method for the monitoring
of the reactions catalyzed by glucose oxidase and
horseradish peroxidase entrapped in a hydrogel matrix
(Fig. 5). The oxidation of glucose was followed by
decomposition of Amplex red dye (a substrate of horseradish peroxidase) which resulted in formation of fluorescent resorufin. It was concluded that the pores in the
hydrogels were sufficiently small to retain the enzymes
and the reporter dyes, and it was suggested that the
method could be applied to immobilization and monitoring of reactions of other proteins.
Recently Rondelez et al. (2005) managed to follow
the reaction catalyzed by single molecules of h-galactosidase and horseradish peroxidase entrapped between
glass/PDMS slides, in a non-microfluidic system. This
was facilitated by a fluorescence assay and watching
the product detection within a few minutes.
Any kind of biocatalysis imaging in enzymatic
microreactors is dependent on the existence of appropriate assays, usually involving fluorescence spectrometry. UV-Vis imaging is possible in principle, but would
require the use of channels and supports made of a
material such as silica which is transparent over the
wavelength range used.
Fig. 5. Micrographs of hydrogel micropatches within a microfluidic
channel: (A) optical micrograph; (B) fluorescence micrograph of the
same micropatches shown in (A). Fluorescence arises from the dye
SNAFL-1 entrapped within the hydrogel. Reprinted with permission
from Zhan et al. (2002). Copyright (2002) American Chemical
Society.
3. Conclusions and future trends
So far, very few enzymes have been applied within
microreactors, although it seems the new devices will be
developed not only as model systems but they will also
be directed to specific problems, as already happens in
the case of tryptic digestion and PCR microreactors.
There are few published patents describing construction
of enzymatic microreactors (Fujii and Hosokawa, 1998;
Combette and Constantin, 2003; Miyazaki and Maeda,
2004a,b), which indicates that developments of applications in this field are still in the initial stage.
One applications-oriented example of use of enzymatic microreactors is the hydrolysis of used grease and
its conversion to diesel fuel (Hsu et al., 2002). This also
points to the bgreenQ aspects of microreactors, due to
their low maintenance requirements, as well as applications in environmental protection. There is a huge commitment by the pharmaceutical industry to the search for
new potent inhibitors of lipases, that can be employed in
the treatment of obesity (Müller and Petry, 2004), and
fast analytical procedures for these biocatalysts are required. A variety of immobilized lipases available from
a range of suppliers (e.g. Sigma Aldrich, Amano, BioChemika, Novozymes) may be used in microsystems
produced for fast screening of inhibitors of these
enzymes. Other immobilized enzymes are already
used in industrial syntheses (Buchholz et al., 2005).
Various aspects of enzyme immobilization including
stability issues have been discussed by Cao (2005).
Enzymatic microreactors have the potential for introduction into industrial-scale synthesis. They can be
easily incorporated in systems operating in the external
numbering-up mode, where the reaction subunits are
cased separately and put together externally. This
mode of scaling up reactions provides good adjustability
and control over the process, due to repetition of the
fluidic path while the transport properties and hydrodynamics are preserved (Hessel et al., 2004). Any microreactor units containing enzyme found to be lacking
sufficient activity can be easily replaced with new
ones, with minimal effects on the performance of the
whole system.
The sine qua non-condition for any large scale use of
enzymatic microreactors is of ease of use and robustness, together with commercialization of microsystem
components. Robustness in part governed by the enzyme stability, and lipases have the advantages of
stability at ambient temperatures whether immobilized
and stored dry or in an organic solvent.
The other important issue is setting up the interface
systems to operate the microreactors. Such systems
P.L. Urban et al. / Biotechnology Advances 24 (2006) 42–57
involve sampling, injection, flow control (e.g. pumping) and monitoring of the product. Many of these steps
can be realized by incorporating enzymes in the structure of lab-on-a-chip which then can be integrated
within portable analytical devices. Nevertheless, appropriate interfacing between macro and micro instruments
is indispensable (Fredrickson and Fan, 2004). Microreactors have already been used within analytical
instruments, e.g. capillary electrophoresis, high performance liquid chromatography and mass spectrometry.
Fabrication of such systems on the industrial scale will
facilitate parallel analyses and obviate the need for
construction of home-made set-ups with syringe
pumps and capillary detectors.
High resolution screening (HRS) is a generic term
for methods based on high performance separation of a
mixture of compounds followed by on-line affinity
recognition, usually achieved with an enzymatic assay
and MS detection. HRS is an advantageous technique
in drug discovery (Irth et al., 2004) since it enables
evaluation of their affinity for target enzymes. Whilst
the enzyme is usually injected into the system following
separation of the mixture components using HPLC, an
alternative is to connect a microreactor with an immobilized enzyme to the output of an HPLC column.
These approaches facilitate investigation of the action
of enzymes towards new drug candidates, and other
targets in analysis and synthesis (Girelli and Mattei,
2005). Ma et al. (2000) demonstrated a system where
the enzyme (lactate dehydrogenase) was injected into
96 wells, incubated (30–1477 min), and the contents of
the wells sampled and separated by capillary electrophoresis in 96 multiplexed capillaries. This parallel
assay approach allowed rapid evaluation of the effects
of change of pH and enzyme concentration, and optimization of reaction conditions.
There is an undoubted need for development of
microreactors and multiplexed methodologies with all
the enzymes which are frequently used, especially in
biochemical enzymatic methods, so that optimization
can be performed quickly. A desirable goal is for highthroughput screening of enzymes, their substrates and
inhibitors. Use of microreactors with parallel microfluidic streams could facilitate the selection from an array
of enzymes of a specific enzyme for optimum transformation of the chosen substrate. Prospective fields of
application of microreactors are quite wide and include
biotechnology, as well as combinatorial chemistry and
enzyme-targeted drug search.
This review of the recent development of enzymatic
reaction technology has shown that such miniaturized
systems find applications in many fields, especially in
53
the analysis of proteins and nucleic acids. The development of this field is in part limited by the availability
of enzymes immobilized on solid supports, as well as
by the range of assays that permit monitoring progress
of the reactions on a microscale. Use of microreactors
also facilitates kinetic studies of immobilized enzymes,
using extremely small quantities of biocatalyst material.
Since supported enzymes can be used in continuous
biocatalytic processes, they have the potential to replace homogeneous catalysis protocols. Whilst most of
the examples given in this review are of research
applications, adoption of the techniques in standard
analytical and micropreparative procedures would undoubtedly be aided by the commercialization of enzymatic microreactors.
Acknowledgements
The authors would like to acknowledge the financial
support of the European Community received as a part of
the project bCHEMCELL: Chemical Biology in Reactors and CellsQ (Contract No. MEST-CT-2004-504345).
References
Amankwa LN, Kuhr WG. Trypsin-modified fused-silica capillary
microreactor for peptide-mapping by capillary zone electrophoresis. Anal Chem 1992;64:1610 – 3.
Avila LZ, Whitesides GM. Catalytic activity of native enzymes during
capillary electrophoresis — an enzymatic microreactor. J Org
Chem 1993;58:5508 – 12.
Bachinski N, Martins AS, Paschoalin VMF, Panek AD, Paiva CLA.
Trehalase immobilization on aminopropyl glass for analytical use.
Biotechnol Bioeng 1997;54:33 – 9.
Bao J, Regnier FE. Ultramicro enzyme assays in a capillary electrophoretic system. J Chromatogr 1992;608:217 – 24.
Bengtsson M, Ekström S, Drott J, Collins A, Csoregi E, Marko-Varga
G, et al. Applications of microstructured porous silicon as a biocatalytic surface. Phys Status Solidi, A Appl Res 2000;182:495 – 504.
Bengtsson M, Ekström S, Marko-Varga G, Laurell T. Improved
performance in silicon enzyme microreactors obtained by homogeneous porous silicon carrier matrix. Talanta 2002;
56:341 – 53.
Bilitewski U, Genrich M, Kadow S, Mersal G. Biochemical analysis with microfluidic systems. Anal Bioanal Chem 2003;
377:556 – 69.
Bonneil E, Waldron KC. On-line system for peptide mapping by
capillary electrophoresis at sub-micromolar concentrations.
Talanta 2000;53:687 – 99.
Bonneil E, Mercier M, Waldron KC. Reproducibility of a solid-phase
trypsin microreactor for peptide mapping by capillary electrophoresis. Anal Chim Acta 2000;404:29 – 45.
Buchholz K, Kasche V, Bornscheuer UT. Biocatalysts and enzyme
technology. Weinheim7 Wiley-VCH; 2005.
Burns MA, Johnson BN, Brahmasandra SN, Handique K, Webster
JR, Krishnan M, et al. An integrated nanoliter DNA analysis
device. Science 1998;282:484 – 7.
54
P.L. Urban et al. / Biotechnology Advances 24 (2006) 42–57
Cao L. Immobilized enzymes: science or art? Curr Opin Chem Biol
2005;9:217 – 26.
Carvalho CML, Cabral JMS. Reverse micelles as reaction media for
lipases. Biochimie 2000;82:1063 – 85.
Chiesl TN, Shi W, Barron AE. Poly(acrylamide-co-alkylacrylamides)
for electrophoretic DNA purification in microchannels. Anal
Chem 2005;77:772 – 9.
Chopineau J, Robert S, Fénart L, Cecchelli R, Lagoutte B, Paitier S, et
al. Monoacylation of ribonuclease A enables its transport across
an in vitro model of the blood-brain barrier. J Control Release
1998;56:231 – 7.
Collins A, Mikeladze E, Bengtsson M, Kokaia M, Laurell T,
Csöregi E. Interference elimination in glutamate monitoring
with chip integrated enzyme microreactors. Electroanalysis
2001;13:425 – 31.
Combette, Ph., Constantin, O., 2003. Microreactor, method for preparing same, and method for producing a biochemical or biological reaction. Patent No. WO03097229.
Cooper JW, Lee CS. Integrated and ultrasensitive gel protein identification. Anal Chem 2004;76:2196 – 202.
de Mello AJ, Beard N. Dealing with drealT samples: sample pretreatment in microfluidic systems. Lab Chip 2003;3:11N – 9N.
Drott J, Lindstrom K, Rosengren L, Laurell T. Porous silicon as the
carrier matrix in microstructured enzyme reactors yielding high
enzyme activities. J Micromech Microeng 1997;7:14 – 23.
Drott J, Rosengren E, Lindstrom K, Laurell T. Porous silicon carrier
matrices in micro enzyme reactors — influence of matrix depth.
Microchim Acta 1999;131:115 – 20.
Ehrfeld W, Hessel V, Löwe H. Microreactors. Weinheim7 WileyVCH; 2000.
Ekström S, Önnerfjord P, Nilsson J, Bengtsson M, Laurell T,
Marko-Varga G. Integrated microanalytical technology enabling
rapid and automated protein identification. Anal Chem
2000;72:286 – 93.
Ekström S, Malmström J, Wallman L, Löfgren M, Nilsson J, Laurell
T, et al. On-chip microextraction for proteomic sample preparation
of in-gel digests. Proteomics 2002;2:413 – 21.
Fang Q. Sample introduction for microfluidic systems. Anal Bioanal
Chem 2004;378:49 – 51.
Folly R, Salgado A, Valdman B, Valero F. The development of
enzymatic sensors for the continuous monitoring of glucose and
sucrose. Braz J Chem 1997;14.
Fredrickson CK, Fan ZH. Macro-to-micro interfaces for microfluidic
devices. Lab Chip 2004;4:526 – 33.
Fujii, T., Hosokawa, K., 1998. Microreactor for biochemical reaction.
Patent No. JP10337173.
Garti N. Microemulsions as microreactors for food applications. Curr
Opin Colloid Interface Sci 2003;8:197 – 211.
Garti N, Lichtenberg D, Silberstein T. The hydrolysis of phosphatidylcholine by phospholipase A2 in microemulsion as
microreactor. Colloids Surf, A Physicochem Eng Asp
1997;128:17 – 25.
Girelli AM, Mattei E. Application of immobilized enzyme reactor in
on-line high performance liquid chromatography: a review. J
Chromatogr B 2005;819:3 – 16.
Gleason NJ, Carbeck JD. Measurement of enzyme kinetics using
microscale steady-state kinetic analysis. Langmuir 2004;20:
6374 – 81.
Gottschlich N, Culbertson CT, McKnight TE, Jacobson SC, Ramsey
JM. Integrated microchip-device for the digestion, separation and
postcolumn labeling of proteins and peptides. J Chromatogr B
2000;745:243 – 9.
Guijt-van Duijn RA, Moerman R, Kroon A, van Dedem GWK, van
den Doel R, van Vliet L, et al. Miniaturized analytical assays in
biotechnology. Biotechnol Adv 2003;21:431 – 44.
Guo Z, Zhang QC, Lei ZD, Kong L, Mao XQ, Zou HF. Studies
on rapid micro-scale peptide mapping analysis using a capillary micro-reactor. Chem J Chin Univ — Chin 2002;23:
1277 – 80.
Guo Z, Xu SY, Lei ZD, Zou HF, Guo BC. Immobilized metalion chelating capillary microreactor for peptide mapping analysis of proteins by matrix assisted laser desorption/ionizationtime of flight-mass spectrometry. Electrophoresis 2003;24:
3633 – 9.
Hashimoto M, He Y, Yeung ES. On-line integration of PCR and cycle
sequencing in capillaries: from human genomic DNA directly to
called bases. Nucleic Acids Res 2003;31:41.
Hashimoto M, Chen PC, Mitchell MW, Nikitopoulos DE, Soper SA,
Murphy MC. Rapid PCR in a continuous flow device. Lab Chip
2004;4:638 – 45.
Haswell SJ, Skelton V. Chemical and biochemical microreactors.
Trends Anal Chem 2000;19:389 – 95.
Haswell SJ, Watts P. Green chemistry: synthesis in micro reactors.
Green Chem 2003;5:240 – 9.
Hessel V, Hardt S, Löwe H. Chemical micro process engineering.
Weinheim7 Wiley-VCH; 2004.
Hessel V, Hardt S, Löwe H, Müller A, Kolb G. Chemical Micro
Process Engineering. Weinheim7 Wiley-VCH; 2005a.
Hessel V, Löwe H, Müller A, Kolb G. Chemical micro process
engineering. Processing and plants. Weinheim7 Wiley-VCH;
2005b.
Heule M, Rezwan K, Cavalli L, Gauckler LJ. A miniaturized enzyme
reactor based on hierarchically shaped porous ceramic microstruts.
Adv Mater 2003;15:1191 – 4.
Holden MA, Jung SY, Cremer PS. Patterning enzymes inside microfluidic channels via photo attachment chemistry. Anal Chem
2004;76:1838 – 43.
Hsu A-F, Jones K, Foglia TA, Marmer WN. Immobilized lipasecatalysed production of alkyl esters of restaurant grease as biodiesel. Biotechnol Appl Biochem 2002;36:181 – 6.
Irth H, Long S, Schenk T. High-resolution screening in an expanded
chemical space. Curr Drug Discov 2004:19 – 23.
Janasek D, Spohn U. Chemiluminometric flow injection analysis
procedures for the enzymatic determination of l-alanine, alphaketoglutarate and l-glutamate. Biosens Bioelectron 1999;14:
123 – 9.
Jiang Y, Lee CS. On-line coupling of micro-enzyme reactor with
micro-membrane chromatography for protein digestion, peptide
separation, and protein identification using electrospray ionization
mass spectrometry. J Chromatogr A 2001;924:315 – 22.
Jiang H, Zou H, Wang H, Ni J, Zhang Q, Zhang Y. On-line characterization of the activity and reaction kinetics of immobilized
enzyme by high-performance frontal analysis. J Chromatogr A
2000a;903:77 – 84.
Jiang HH, Zou HF, Wang HL, Ni JY, Zhang Q. Covalent immobilization of trypsin on glycidyl methacrylate-modified cellulose
membrane as enzyme reactor. Chem J Chin Univ — Chin
2000b;21:702 – 6.
Jiang HH, Zou HF, Wang HL, Zhang Q, Ni JY, Zhang QC, et al.
Combination of MALDI-TOF mass spectrometry with immobilized enzyme microreactor for peptide mapping. Sci China, Ser B
Chem Life Sci Earth Sci 2000c;43:625 – 33.
Jianrong Ch, Yuqing M, Nongyue H, Xiaohua W, Sijiao L. Nanotechnology and biosensors. Biotechnol Adv 2004;22:505 – 18.
P.L. Urban et al. / Biotechnology Advances 24 (2006) 42–57
Jin LJ, Ferrance J, Sanders JC, Landers JP. A microchip-based
proteolytic digestion system driven by electroosmotic pumping.
Lab Chip 2003;3:11 – 8.
Jones F, Lu ZH, Elmore BB. Development of novel microscale
system as immobilized enzyme bioreactor. Appl Biochem Biotechnol 2002;98:627 – 40.
Jones F, Forrest S, Palmer J, Lu ZH, Elmore J, Elmore BB. Immobilized enzyme studies in a microscale bioreactor. Appl Biochem
Biotechnol 2004;113:261 – 72.
Kamal A, Sandbhor M, Ramana KV. One-pot lipase-catalyzed synthesis of enantiopure secondary alcohols from carbonyl compounds: a new protocol for lipase-mediated resolution.
Tetrahedron: Asymmetry 2002;13:815 – 20.
Kan CW, Fredlake CP, Doherty EAS, Barron AE. DNA sequencing
and genotyping in miniaturized electrophoresis systems. Electrophoresis 2004;25:3564 – 88.
Kaneno J, Kohama R, Miyazaki M, Uehara M, Kanno K, Fujii M, et
al. Development of surface modification method and its application for preparation of enzyme-immobilized microreactor. Kagaku
Kogaku Ronbunshu 2004;30:154 – 8.
Kanie Y, Kanie O. Electrophoretically mediated microanalysis: enzyme analyses at a nanoliter scale. Beckman Coulter PACE Setter
2003;7:1 – 4.
Kanno K, Maeda H, Izumo Sh, Ikuno M, Takeshita K, Teshiro A, et
al. Rapid enzymatic transglycosylation and oligosaccharide synthesis in a microchip reactor. Lab Chip 2002;2:15 – 8.
Kato M, Sakai-Kato K, Jin HM, Kubota K, Miyano H, Toyo’oka T, et
al. Integration of on-line protein digestion, peptide separation, and
protein identification using pepsin-coated photopolymerized sol–
gel columns and capillary electrophoresis/mass spectrometry.
Anal Chem 2004;76:1896 – 902.
Katsura Sh, Harada N, Maeda Y, Komatsu J, Matsuura Sh, Takashima
K, et al. Activation of restriction enzyme by electrochemically
released magnesium ion. J Biosci Bioeng 2004;98:293 – 7.
Kawakami K, Sera Y, Sakai Sh, Ono T, Ijima H. Development and
characterization of a silica monolith immobilized enzyme microbioreactor. Ind Eng Chem Res 2005;44:236 – 40.
Ke C, Berney H, Mathewson A, Sheehan MM. Rapid amplification
for the detection of Mycobacterium tuberculosis using a noncontact heating method in a silicon microreactor based thermal
cycler. Sens Actuators, B, Chem 2004;102:308 – 14.
Khandurina J, McKnight TE, Jacobson SC, Waters LC, Foote RS,
Ramsey JM. Integrated system for rapid PCR-based DNA analysis in microfluidic devices. Anal Chem 2000;72:2995 – 3000.
Kim YD, Park CB, Clark DS. Stable sol–gel microstructured and
microfluidic networks for protein patterning. Biotechnol Bioeng
2001;73:331 – 7.
Koh W-G, Pishko M. Immobilization of multi-enzyme microreactors
inside microfluidic devices. Sens Actuators, B, Chem
2005;106:335 – 42.
Korecka L, Bilkova Z, Holeapek M, Kralovsky J, Benes M, Lenfeld J,
et al. Utilization of newly developed immobilized enzyme reactors
for preparation and study of immunoglobulin G fragments. J
Chromatogr B 2004;808:15 – 24.
Krenková J, Foret F. Immobilized microfluidic enzymatic reactors.
Electrophoresis 2004;25:3550 – 63.
Kricka LJ, Wilding P. Microchip PCR. Anal Bioanal Chem
2003;377:820 – 5.
Kulys J. The carbon paste electrode encrusted with a microreactor as
glucose biosensor. Biosens Bioelectron 1999;14:473 – 9.
Lagally ET, Mathies RA. Integrated genetic analysis microsystems. J
Phys, D, Appl Phys 2004;37:R245 – 61.
55
Laurell T, Drott J, Rosengren L. Silicon-wafer integrated enzyme
reactors. Biosens Bioelectron 1995;10:289 – 99.
Laurell T, Rosengren L. A micromachined enzyme reactor in (110)oriented silicon. Sens Actuators, B, Chem 1994;19:614 – 7.
Lee TMH, Hsing I-M, Lao AIK, Carles MC. A miniaturized DNA
amplifier: its application in traditional Chinese medicine. Anal
Chem 2000;72:4242 – 7.
Lendl B, Schindler R, Frank J, Kellner R. Fourier transform infrared
detection in miniaturized total analysis systems for sucrose analysis. Anal Chem 1997;69:2877 – 81.
L’Hostis E, Michel PE, Fiaccabrino GC, Strike DJ, de Rooij NF,
Koudelka-Hep M. Microreactor and electrochemical detectors
fabricated using Si and EPON SU-8. Sens Actuators, B, Chem
2000;64:156 – 62.
Licklider L, Kuhr WG. Optimization of online peptide-mapping by
capillary zone electrophoresis. Anal Chem 1994;66:4400 – 7.
Licklider L, Kuhr WG. Characterization of reaction dynamics in a
trypsin-modified capillary microreactor. Anal Chem 1998;70:
1902 – 8.
Licklider L, Kuhr WG, Lacey MP, Keough T, Purdon MP, Takigiku R.
Online microreactors/capillary electrophoresis/mass-spectrometry
for the analysis of proteins and peptides. Anal Chem
1995;67:4170 – 7.
Lilly MD, Hornby WE, Crook EM. Kinetics of carboxymethylcellulose-ficin in packed beds. Biochem J 1966;100:718 – 23.
Liu DJ, Perdue RK, Sun L, Crooks RM. Immobilization of DNA onto
poly(dimethylsiloxane) surfaces and application to a microelectrochemical enzyme-amplified DNA hybridization assay. Langmuir 2004;20:5905 – 10.
Lv Y, Zhang Z, Chen F. Chemiluminescence microfluidic system
sensor on a chip for determination of glucose in human serum
with immobilized reagents. Talanta 2003;59:571 – 6.
Ma L, Gong X, Yeung ES. Combinatorial screening of enzyme
activity by using multiplexed capillary electrophoresis. Anal
Chem 2000;72:3383 – 7.
Madamwar DB, Bhatt JP, Ray RM, Srivastava RC. Activation and
stabilization of invertase entrapped into reversed micelles of
sodium lauryl sulfate and sodium tauroglycocholate in organic
solvents. Enzyme Microb Technol 1988;10:302 – 5.
Mao HB, Yang TL, Cremer PS. Design and characterization of
immobilized enzymes in microfluidic systems. Anal Chem
2002;74:379 – 85.
Maruyama T, Uchida J, Ohkawa T, Futami T, Katayama K, Nishizawa
K, et al. Enzymatic degradation of p-chlorophenol in a two-phase
flow microchannel system. Lab Chip 2003;3:308 – 12.
Miyazaki M, Maeda H. Microreactor and method for producing the
same. Patent No. JP2004267097;2004a.
Miyazaki M, Maeda H. Microreactor with enzyme reversibly bonded
therein and its production method. Patent No. JP2004160273;
2004b.
Miyazaki M, Kaneno J, Kohama R, Uehara R, Kanno K, Fujii M, et
al. Preparation of functionalized nanostructures on microchannel
surface and their use for enzyme microreactors. Chem Eng J
2004;101:277 – 84.
Moore BD, Stevenson L, Watt A, Flitsch S, Turner NJ, Cassidy C, et
al. Rapid and ultra-sensitive determination of enzyme activities
using surface-enhanced resonance Raman scattering. Nat Biotechnol 2004;22:1133 – 8.
Moorthy J, Mensing GA, Kim D, Mohanty S, Eddington DT, Tepp
WH, et al. Microfluidic tectonics platform: a colorimetric, disposable botulinum toxin enzyme-linked immunosorbent assay system. Electrophoresis 2004;25:1705 – 13.
56
P.L. Urban et al. / Biotechnology Advances 24 (2006) 42–57
Müller G, Petry S. Lipases and phospholipases in drug development:
from biochemistry to molecular pharmacology. Weinheim7 WileyVCH; 2004.
Murakami Y, Takeuchi T, Yokoyama K, Tamiya E, Karube I, Suda M.
Integration of enzyme-immobilized column with electrochemical
flow cell using micromachining techniques for a glucose detection
system. Anal Chem 1993;65:2731 – 5.
Nagai H, Murakami Y, Yokoyama K, Tamiya E. High-throughput
PCR in silicon based microchamber array. Biosens Bioelectron
2001;16:1015 – 9.
Nakamura H, Li X, Wang H, Uehara M, Miyazaki M, Shimizu H, et
al. A simple method of self assembled nano-particles deposition
on the micro-capillary inner walls and the reactor application for
photo-catalytic and enzyme reactions. Chem Eng J 2004;101:
261 – 8.
Nashabeh W, Rassi ZE. Enzymophoresis of nucleic acids by tandem
capillary enzyme reactor-capillary zone electrophoresis. J Chromatogr A 1992;596:251 – 64.
Niwa O, Kurita R, Horiuchi T, Torimitsu K. Continuous monitoring of
l-glutamate released from cultured rat nerve cells with a microfabricated on-line sensor at a slow flow rate. Electroanalysis
1999;11:356 – 61.
Nomura A, Shin S, Mehdi OO, Kauffmann JM. Preparation, characterization, and application of an enzyme-immobilized magnetic
microreactor for flow injection analysis. Anal Chem 2004;76:
5498 – 502.
Oberholzer T, Meyer E, Amato I, Lustig A, Monnard P-A. Enzymatic
reactions inside liposomes using the detergent-induced liposome
loading method. Biochim Biophys Acta 1999;1416:57 – 68.
Palm AK, Novotny MV. Analytical characterization of a facile porous
polymer monolithic trypsin microreactor enabling peptide mass
mapping using mass spectrometry. Rapid Commun Mass Spectrom 2004;18:1374 – 82.
Park CB, Clark DS. Sol–gel encapsulated enzyme arrays for highthroughput screening of biocatalytic activity. Biotechnol Bioeng
2002;78:229 – 35.
Park SS, Joo HS, Cho SI, Kim MS, Kim YK, Kim BG. Multi-step
reactions on microchip platform using nitrocellulose membrane
reactor. Biotechnol Bioprocess Eng 2003;8:257 – 62.
Peterson DS. Solid supports for micro analytical systems Solid supports for micro analytical systems. Lab Chip 2005;5:132 – 9.
Peterson DS, Rohr T, Svec F, Fréchet JMJ. High-throughput
peptide mass mapping using a microdevice containing trypsin
immobilized on a porous polymer monolith coupled to MALDI
TOF and ESI TOF mass spectrometers. J Proteome Res
2002a;1:563 – 8.
Peterson DS, Rohr T, Svec F, Fréchet JMJ. Enzymatic microreactoron-a-chip: protein mapping using trypsin immobilized on porous
polymer monoliths molded in channels of microfluidic devices.
Anal Chem 2002b;74:4081 – 8.
Peterson DS, Rohr T, Svec F, Fréchet JMJ. Dual-function microanalytical device by in situ photolithographic grafting of porous
polymer monolith: integrating solid-phase extraction and enzymatic digestion for peptide mass mapping. Anal Chem
2003;75:5328 – 35.
Pfohl T, Mugele F, Seemann R, Herminghaus S. Trends in microfluidics with complex fluids. Chemphyschem 2003;4:1291 – 8.
Pijanowska DG, Baraniecka A, Wiater R, Ginalska G, oobarzewski J,
Torbicz W. The pH-detection of triglycerides. Sens Actuators, B,
Chem 2001;78:263 – 6.
Qu HY, Wang HT, Huang Y, Zhong W, Lu HJ, Kong JL, et al. Stable
microstructured network for protein patterning on a plastic micro-
fluidic channel: strategy and characterization of on-chip enzyme
microreactors. Anal Chem 2004;76:6426 – 33.
Regnier FE, Patterson DH, Harmon BJ. Electrophoretically-mediated microanalysis (EMMA). Trends Anal Chem 1995;14:
177 – 181.
Rondelez Y, Tresset G, Tabata KV, Arata H, Fujita H, Takeuchi Sh, et
al. Highly coupled ATP synthesis by F-1-ATPase single molecules. Nat Biotechnol:20 – 2.
Samskog J, Bylund D, Jacobsson SP, Markides KE. Miniaturized online proteolysis-capillary liquid chromatographymass spectrometry for peptide mapping of lactate dehydrogenase. J Chromatogr A
2003;998:83 – 91.
Sanders GHW, Manz A. Chip-based microsystems for genomic and
proteomic analysis. Trends Anal Chem 2000;19:364 – 78.
Schneegass I, Brautigam R, Kohler JM. Miniaturized flow-through
PCR with different template types in a silicon chip. Lab Chip
2001;1:42 – 9.
Schneegah I, Köhler JM. Flow-through polymerase chain reactions in
chip thermocyclers. Rev Mol Biotechnol 2001;82:101 – 21.
Schwarz MA, Hauser PC. Recent developments in detection
methods for microfabricated analytical devices. Lab Chip
2001;1:1 – 6.
Seong GH, Heo J, Crooks RM. Measurement of enzyme kinetics
using a continuous-flow microfluidic system. Anal Chem
2003;75:3161 – 7.
Srinivasan A, Bach H, Sherman DH, Dordick JS. Bacterial P450catalyzed polyketide hydroxylation on a microfluidic platform.
Biotechnol Bioeng 2004;88:528 – 35.
Strike DJ, Fiaccabrino G-C, Koudelka-Hep M, de Rooij NF. Enzymatic microreactor using Si, glass and EPON SU-8. Biomed
Microdev 2000;2:175 – 8.
Van Dyck S, Kaale E, Nováková S, Glatz Z, Hoogmartens J, Van
Schepdael A. Advances in capillary electrophoretically mediated
microanalysis. Electrophoresis 2003;24:3868 – 78.
Verpoorte E. Beads and chips: new recipes for analysis. Lab Chip
2003a;3:60N – 8N.
Verpoorte E. Chip vision — optics for microchips. Lab Chip
2003b;3:42N – 52N.
Vilkner T, Janasek D, Manz A. Micro total analysis systems Recent
developments. Anal Chem 2004;76:3373 – 86.
Walde P, Ichikawa S. Enzymes inside lipid vesicles: preparation,
reactivity and applications. Biomol Eng 2001;18:143 – 77.
Washizu M, Yamamoto T, Kurosawa O, Suzuki S, Shimamoto N.
Molecular surgery of DNA using enzyme-immobilized particles.
Trans IEE Jpn 1996;116-E:196 – 202.
Watts P, Wiles C, Haswell SJ, Pombo-Villar E, Styring P. The
synthesis of peptides using micro reactors. Chem Commun
2001:990 – 1.
Wilhelm T, Wittstock G. Generation of periodic enzyme patterns by
soft lithography and activity imaging by scanning electrochemical
microscopy. Langmuir 2002;18:9485 – 93.
Xie B, Danielsson B, Norberg P, Winquist F, Lundström I. Development of a thermal micro-biosensor fabricated on a silicon chip.
Sens Actuators, B, Chem 1992;6:127 – 30.
Xie Sh, Svec F, Fréchet JMJ. Design of reactive porous polymer
supports for high throughput bioreactors: poly(2-vinyl-4,4dimethylazlactone-co-acrylamide-co-ethyl dimethacrylate) monoliths. Biotechnol Bioeng 1999;62:30 – 5.
Xu Z-R, Fang Z-L. Composite poly(dimethylsiloxane)/glass microfluidic system with an immobilized enzymatic particle-bed reactor
and sequential sample injection for chemiluminescence determinations. Anal Chim Acta 2004;507:129 – 35.
P.L. Urban et al. / Biotechnology Advances 24 (2006) 42–57
Yadavalli VK, Koh W-G, Lazur GJ, Pishko MV. Microfabricated
protein-containing poly(ethylene glycol) hydrogel arrays for biosensing. Sens Actuators, B, Chem 2004;97:290 – 7.
Yakovleva J, Davidsson R, Lobanova A, Bengtsson M, Eremin S,
Laurell T, et al. Microfluidic enzyme immunoassay using silicon
microchip with immobilized antibodies and chemiluminescence
detection. Anal Chem 2002;74:2994 – 3004.
Ye M, Hu Sh, Schoenherr RM, Dovichi NJ. On-line protein digestion
and peptide mapping by capillary electrophoresis with post-column labeling for laser-induced fluorescence detection. Electrophoresis 2004;25:1319 – 26.
57
Zhan W, Seong GH, Crooks RM. Hydrogel-based microreactors as a
functional component of microfluidic systems. Anal Chem
2002;74:4647 – 52.
Zhang N, Yeung ES. On-line coupling of polymerase chain reaction
and capillary electrophoresis for automatic DNA typing and HIV1 diagnosis. J Chromatogr B 1998;714:3 – 11.
Zhang YY, Tadigadapa S. Calorimetric biosensors with integrated
microfluidic channels. Biosens Bioelectron 2004;19:1743 – 73.
Zhao CA, Wittstock G. Scanning electrochemical microscopy of
quinoprotein glucose dehydrogenase. Anal Chem 2004;76:
3145 – 54.