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258 Benčina et al.<br />

1. Introduction<br />

Enzymes immobilized on solid-phase matrices have found various applications<br />

in biotechnology, molecular biology and molecular diagnostics and can<br />

serve as industrial catalysts and as specific reagents for analytical procedures. The<br />

advantages of using immobilized enzymes instead of an enzyme solution include<br />

increased stability and an opportunity to work with a continuous system over long<br />

periods of time. A wide range of supports have been utilized for immobilization<br />

among which particle-based supports are the most commonly implemented. The<br />

typeofsupportusedforimmobilizationisoneofthekeyconsiderationsinpractical<br />

application due to different immobilization efficiency, ligand utilization and mass<br />

transfer regime. The mass transfer between the mobile phase and the stationary<br />

phase has a pronounced effect on the performance. In the case of particulate porous<br />

supports, the substrate has to diffuse from the mobile phase into the pores in order<br />

to reach the catalytic sites of the immobilized enzyme. Because the diffusion,<br />

especially for large molecules, is commonly slower than the reaction process at<br />

the active site, the overall kinetic behavior of the immobilized enzyme is governed<br />

by mass transfer, causing a decrease in efficiency.<br />

To overcome this drawback, a new group of supports called monoliths was<br />

introduced (1). Contrary to conventional stationary phases that are in the form<br />

of a few micrometer particles, monoliths are made of a single piece of porous<br />

material. Pores are highly interconnected forming a channel network through<br />

which the mobile phase flows. As the main transport mechanism is convection,<br />

mass transfer resistance can be neglected under operating conditions. Consequently,<br />

the overall behavior of the immobilized ligand reflects its intrinsic<br />

reaction kinetics. Therefore, such an immobilized system is expected to allow<br />

higher throughput because of higher enzyme efficiency, especially pronounced<br />

for macromolecular substrates having low mobility.<br />

Among different types of monoliths, methacrylate-based monoliths were<br />

most frequently used for immobilization of various ligands. As such, they<br />

were used either as an affinity support for purification of target compounds<br />

(2,3) or as bioreactors (2,4,5). In this work, some examples of macromolecular<br />

bioreactors based on Convective Interaction Media (CIM) ® (CIM is a registered<br />

trademark of BIA Separations, Ljubljana, Slovenia) supports (methacrylatebased<br />

monoliths) are presented.<br />

2. Materials<br />

1. CIM Convective Interaction Media ® epoxy groups containing poly (glycidyl<br />

methacrylate-co-ethylene dimethacrylate) monolithic columns (BIA Separations)<br />

with a diameter of 12 mm and thickness of 3 mm (monolith volume 0.34 ml)<br />

having median pore size of approximately 1.5 or 6 μm (CIM epoxy disk).

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