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Liquid Culture Systems for in vitro Plant Propagation

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42 Anne Kathr<strong>in</strong>e Hvoslef-Eide et al.<br />

1. Introduction<br />

Internationally, there is considerable <strong>in</strong>terest <strong>in</strong> develop<strong>in</strong>g vegetative<br />

propagation methods that could facilitate rapid propagation of elite material<br />

(Preil, 1991; Takayama and Akita, 1994). Consider<strong>in</strong>g the cost of labour <strong>in</strong><br />

Western Europe, propagation <strong>in</strong> liquid culture, especially <strong>in</strong> bioreactors, is a<br />

possible way to produce clonal propagules at a low cost. One of the<br />

advantages of grow<strong>in</strong>g cell cultures <strong>in</strong> bioreactors is the opportunity to<br />

control the oxygen supply accurately <strong>in</strong> the liquid. This communication<br />

describes a self-constructed and self-built set of six identical bioreactors to<br />

provide controlled experimental conditions <strong>for</strong> cell cultures.<br />

The designed bioreactors are closed systems or so-called batch<br />

bioreactors, which are the most frequently used s <strong>in</strong> biotechnological<br />

productions (Siebel, 1992; Glick and Pasternak, 1998). Hav<strong>in</strong>g identical<br />

bioreactors provides the possibility to run factorial experiments to reveal<br />

<strong>in</strong>teractions between the experimental parameters. The aim of the<br />

construction was to take advantage of experience from cell cultures grown <strong>in</strong><br />

commercially-available bioreactors and to construct a bioreactor with<br />

exceptionally low shear <strong>for</strong>ces, at the lowest possible price. The bioreactors<br />

on the commercial market have been designed to provide optimal growth <strong>for</strong><br />

bacteria, yeast and, to some extent, plant cell cultures <strong>for</strong> secondary<br />

metabolite production. When aim<strong>in</strong>g to grow somatic embryos <strong>for</strong> largescale<br />

propagation, the effect of shear <strong>for</strong>ces is more critical than <strong>for</strong> cell<br />

cultures <strong>for</strong> secondary metabolites. First, we designed a prototype, tested<br />

this out, improved it and then built a set of six identical “improved”<br />

bioreactors. There are two features with our bioreactors that make them<br />

more gentle to the cultured plant cells than various commercial designs; (1)<br />

the aeration system and (2) the stirr<strong>in</strong>g device. Both are designed to allow<br />

slow, gentle movement of the suspension, without allow<strong>in</strong>g cell settlement <strong>in</strong><br />

quiet zones <strong>in</strong> the bioreactors. So far, we have grown embryogenic cultures<br />

of carrot (Daucus carota) (Nissen, unpublished results), Norway spruce<br />

(Picea abies) (Kvaalen, 1997), birch (Betula pendula) (Hvoslef-Eide, 2000),<br />

cyclamen (Cyclamen persicum) (Hvoslef-Eide and Munster, 1997, 1998) and<br />

shoot cultures of Christmas begonia (Begonia x cheimantha) (Hvoslef-Eide,<br />

unpublished results) <strong>in</strong> our bioreactors.<br />

For a more general and comprehensive description of plant cell<br />

bioreactor design than is provided <strong>in</strong> this article, see the book chapter by<br />

Heyerdahl et al. (1995).

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