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Enzymatic microreactors in chemical analysis and kinetic studies

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the hydrolysis of p-nitrophenylphosphate <strong>and</strong> urea catalyzed<br />

by alkal<strong>in</strong>e phosphatase <strong>and</strong> urease, respectively.<br />

Yadavalli et al. (2004) presented a microarray-based<br />

system with immobilized enzymes which enabled<br />

screen<strong>in</strong>g of low concentrations of enzyme substrates.<br />

The hydrogel arrays were prepared photolithographically<br />

on silicon surfaces. In earlier work, Zhan et al.<br />

(2002) developed a similar method for the monitor<strong>in</strong>g<br />

of the reactions catalyzed by glucose oxidase <strong>and</strong><br />

horseradish peroxidase entrapped <strong>in</strong> a hydrogel matrix<br />

(Fig. 5). The oxidation of glucose was followed by<br />

decomposition of Amplex red dye (a substrate of horseradish<br />

peroxidase) which resulted <strong>in</strong> formation of fluorescent<br />

resoruf<strong>in</strong>. It was concluded that the pores <strong>in</strong> the<br />

hydrogels were sufficiently small to reta<strong>in</strong> the enzymes<br />

<strong>and</strong> the reporter dyes, <strong>and</strong> it was suggested that the<br />

method could be applied to immobilization <strong>and</strong> monitor<strong>in</strong>g<br />

of reactions of other prote<strong>in</strong>s.<br />

Recently Rondelez et al. (2005) managed to follow<br />

the reaction catalyzed by s<strong>in</strong>gle molecules of h-galactosidase<br />

<strong>and</strong> horseradish peroxidase entrapped between<br />

glass/PDMS slides, <strong>in</strong> a non-microfluidic system. This<br />

was facilitated by a fluorescence assay <strong>and</strong> watch<strong>in</strong>g<br />

the product detection with<strong>in</strong> a few m<strong>in</strong>utes.<br />

Any k<strong>in</strong>d of biocatalysis imag<strong>in</strong>g <strong>in</strong> enzymatic<br />

<strong>microreactors</strong> is dependent on the existence of appropriate<br />

assays, usually <strong>in</strong>volv<strong>in</strong>g fluorescence spectrometry.<br />

UV-Vis imag<strong>in</strong>g is possible <strong>in</strong> pr<strong>in</strong>ciple, but would<br />

require the use of channels <strong>and</strong> supports made of a<br />

material such as silica which is transparent over the<br />

wavelength range used.<br />

Fig. 5. Micrographs of hydrogel micropatches with<strong>in</strong> a microfluidic<br />

channel: (A) optical micrograph; (B) fluorescence micrograph of the<br />

same micropatches shown <strong>in</strong> (A). Fluorescence arises from the dye<br />

SNAFL-1 entrapped with<strong>in</strong> the hydrogel. Repr<strong>in</strong>ted with permission<br />

from Zhan et al. (2002). Copyright (2002) American Chemical<br />

Society.<br />

3. Conclusions <strong>and</strong> future trends<br />

So far, very few enzymes have been applied with<strong>in</strong><br />

<strong>microreactors</strong>, although it seems the new devices will be<br />

developed not only as model systems but they will also<br />

be directed to specific problems, as already happens <strong>in</strong><br />

the case of tryptic digestion <strong>and</strong> PCR <strong>microreactors</strong>.<br />

There are few published patents describ<strong>in</strong>g construction<br />

of enzymatic <strong>microreactors</strong> (Fujii <strong>and</strong> Hosokawa, 1998;<br />

Combette <strong>and</strong> Constant<strong>in</strong>, 2003; Miyazaki <strong>and</strong> Maeda,<br />

2004a,b), which <strong>in</strong>dicates that developments of applications<br />

<strong>in</strong> this field are still <strong>in</strong> the <strong>in</strong>itial stage.<br />

One applications-oriented example of use of enzymatic<br />

<strong>microreactors</strong> is the hydrolysis of used grease <strong>and</strong><br />

its conversion to diesel fuel (Hsu et al., 2002). This also<br />

po<strong>in</strong>ts to the bgreenQ aspects of <strong>microreactors</strong>, due to<br />

their low ma<strong>in</strong>tenance requirements, as well as applications<br />

<strong>in</strong> environmental protection. There is a huge commitment<br />

by the pharmaceutical <strong>in</strong>dustry to the search for<br />

new potent <strong>in</strong>hibitors of lipases, that can be employed <strong>in</strong><br />

the treatment of obesity (Müller <strong>and</strong> Petry, 2004), <strong>and</strong><br />

fast analytical procedures for these biocatalysts are required.<br />

A variety of immobilized lipases available from<br />

a range of suppliers (e.g. Sigma Aldrich, Amano, Bio-<br />

Chemika, Novozymes) may be used <strong>in</strong> microsystems<br />

produced for fast screen<strong>in</strong>g of <strong>in</strong>hibitors of these<br />

enzymes. Other immobilized enzymes are already<br />

used <strong>in</strong> <strong>in</strong>dustrial syntheses (Buchholz et al., 2005).<br />

Various aspects of enzyme immobilization <strong>in</strong>clud<strong>in</strong>g<br />

stability issues have been discussed by Cao (2005).<br />

<strong>Enzymatic</strong> <strong>microreactors</strong> have the potential for <strong>in</strong>troduction<br />

<strong>in</strong>to <strong>in</strong>dustrial-scale synthesis. They can be<br />

easily <strong>in</strong>corporated <strong>in</strong> systems operat<strong>in</strong>g <strong>in</strong> the external<br />

number<strong>in</strong>g-up mode, where the reaction subunits are<br />

cased separately <strong>and</strong> put together externally. This<br />

mode of scal<strong>in</strong>g up reactions provides good adjustability<br />

<strong>and</strong> control over the process, due to repetition of the<br />

fluidic path while the transport properties <strong>and</strong> hydrodynamics<br />

are preserved (Hessel et al., 2004). Any microreactor<br />

units conta<strong>in</strong><strong>in</strong>g enzyme found to be lack<strong>in</strong>g<br />

sufficient activity can be easily replaced with new<br />

ones, with m<strong>in</strong>imal effects on the performance of the<br />

whole system.<br />

The s<strong>in</strong>e qua non-condition for any large scale use of<br />

enzymatic <strong>microreactors</strong> is of ease of use <strong>and</strong> robustness,<br />

together with commercialization of microsystem<br />

components. Robustness <strong>in</strong> part governed by the enzyme<br />

stability, <strong>and</strong> lipases have the advantages of<br />

stability at ambient temperatures whether immobilized<br />

<strong>and</strong> stored dry or <strong>in</strong> an organic solvent.<br />

The other important issue is sett<strong>in</strong>g up the <strong>in</strong>terface<br />

systems to operate the <strong>microreactors</strong>. Such systems

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