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Liquid Culture Systems for in vitro Plant Propagation

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156 Annette Hohe & Ralf Reski<br />

projects have been started <strong>in</strong> order to analyse gene functions on a large scale<br />

(Nishiyama et al., 2001; Egener et al., 2002). Additionally, Physcomitrella is<br />

an ideal organism <strong>for</strong> physiological analyses because of its clearly separated<br />

and well-def<strong>in</strong>ed developmental stages (e.g. Bhatla et al., 2002). Moreover,<br />

it is used also <strong>in</strong> applied plant biotechnology as a production system <strong>for</strong><br />

heterologous prote<strong>in</strong>s (Reutter and Reski, 1996).<br />

Thus, bioreactor cultures of Physcomitrella protonema suspensions have<br />

been established <strong>for</strong> several reasons: i) protonema suspensions are used <strong>for</strong><br />

protoplast isolation <strong>for</strong> large scale trans<strong>for</strong>mation (Hohe et al., 2001; Hohe<br />

and Reski, 2002). ii) Bioreactor cultures represent a ‘conta<strong>in</strong>ed environment’<br />

<strong>for</strong> the production of heterologous compounds (Reutter and Reski, 1996). iii)<br />

Bioreactor culture offers a unique possibility <strong>for</strong> study<strong>in</strong>g the effect of<br />

environmental conditions on growth and development (Hohe et al., 2002).<br />

This, <strong>in</strong> turn, is the basis <strong>for</strong> physiological studies as well as <strong>for</strong> the<br />

optimisation of culture conditions <strong>for</strong> the production of heterologous<br />

compounds.<br />

In this paper we report on the effect of physical and chemical growth<br />

conditions, i.e. gas atmosphere, light <strong>in</strong>tensity and pH, on the growth and<br />

development of bioreactor cultures of Physcomitrella protonema.<br />

2. Materials and methods<br />

Protonema suspension cultures of Physcomitrella patens were grown <strong>in</strong> a<br />

modified Knop medium conta<strong>in</strong><strong>in</strong>g 4.24 mmol Ca(NO3)2, 1.02 mmol KCl,<br />

1.84 mmol KH2PO4, 3.36 mmol MgSO4 and 0.045 mmol FeSO4, pH 5.8<br />

(Reski and Abel, 1985). For batch cultures <strong>in</strong> bioreactors the medium was<br />

additionally supplemented with 2.5 mmol ammonium tartrate.<br />

Bioreactor cultures were done <strong>in</strong> glass vessels with a work<strong>in</strong>g volume of<br />

either 5 or 10 litres, respectively (Applikon, Schiedam, The Netherlands).<br />

<strong>Culture</strong>s were aerated with 0.3 vvm air or air supplemented with 2 % (v/v)<br />

CO2 and stirred with a mar<strong>in</strong>e impeller runn<strong>in</strong>g with 400 (10-litre vessel) or<br />

500 rpm (5-litre vessel). Light <strong>in</strong>tensity was 190 (10-litre vessel) or<br />

120 µmol s -1 m -2 (5-litre vessel) provided by fluorescent tubes (Philips<br />

TLD 25) either cont<strong>in</strong>uously or with a light/dark periodicity of 16/8 hours.<br />

Control of pH was by automatic titration of 0.5 N KOH or HCl (ADI 1030<br />

control device, Applikon, Schiedam, The Netherlands).<br />

Growth was determ<strong>in</strong>ed by measur<strong>in</strong>g the dry weight of the cultures; two<br />

50 ml samples were taken per day and the cell material dried to constant<br />

weight at 105°C <strong>for</strong> 2 hours.<br />

<strong>Culture</strong> was either done as a batch culture start<strong>in</strong>g with approximately<br />

30 mg l -1 dry weight, or as semi cont<strong>in</strong>uous culture, i.e. <strong>in</strong> a daily rhythm a

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