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Liquid Culture Systems for in vitro Plant Propagation

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Bioreactor design <strong>for</strong> propagation 49<br />

The pH can be controlled (very) precisely, but one problem then arises:<br />

acid and alkali are then more or less constantly added to ma<strong>in</strong>ta<strong>in</strong> the set<br />

po<strong>in</strong>t. This produces salt that may affect the biological processes <strong>in</strong> the<br />

bioreactor. To avoid unnecessary elevation of salt concentration, our<br />

controller implements a dead band around the set po<strong>in</strong>t. As long as the pH is<br />

with<strong>in</strong> the dead band, the controller will not activate the alkali or acid<br />

pumps. We have not used active pH regulation <strong>for</strong> our experiments <strong>in</strong> many<br />

cases, as the cells seem to be grow<strong>in</strong>g and develop<strong>in</strong>g well at the pH range<br />

provided. There<strong>for</strong>e, we have avoided pH regulation to simplify<br />

experimental design as much as possible. But the pH of the medium is a<br />

good <strong>in</strong>dicator <strong>for</strong> the condition of a cell suspension, and any <strong>in</strong>fection is<br />

usually first spotted as an abnormal pH read<strong>in</strong>g. Normally, with the medium<br />

we use, the pH reduces after <strong>in</strong>oculation, and then rises aga<strong>in</strong> (Figure 3).<br />

2.5 Stirr<strong>in</strong>g speed and stirrer direction<br />

The stirrer is a pitch blade stirrer made of sta<strong>in</strong>less steel (Figure 1B and<br />

1F). The shaft is held by a ball bear<strong>in</strong>g pressed <strong>in</strong>to a hole <strong>in</strong> the bioreactor<br />

lid. The bear<strong>in</strong>g provides enough stability <strong>for</strong> the stirrer. The grease of this<br />

bear<strong>in</strong>g can stand the autoclave temperature well and takes part <strong>in</strong> the sterile<br />

barrier. The motor and stirrer shaft are coupled by a slot and tap to allow <strong>for</strong><br />

easy removal of the motor when the vessel is taken away. The rotational<br />

speed can be varied from 0 - 100 rpm. The regular changes of direction are<br />

important to obta<strong>in</strong> a good mix<strong>in</strong>g at low speeds and hence reduce the shear<br />

<strong>for</strong>ces. A speed as low as 30 rpm is sufficient to provide good mix<strong>in</strong>g when<br />

chang<strong>in</strong>g the direction every 10s.<br />

2.6 Light quality provision<br />

It is possible to expose the cultures to different light qualities by us<strong>in</strong>g a<br />

light source provid<strong>in</strong>g near daylight spectrum (OFT bioLIGHTSYSTEMS,<br />

Strand Light<strong>in</strong>g, UK). This light can then be filtered through different<br />

coloured stagelight filters that will filter away parts of the light spectrum.<br />

We have used a blue filter (Strand filter No 419, primary dark blue) and a<br />

red filter (Strand filter No 406, primary red). All light treatments were at the<br />

same light quantity; 5 µmol m -1 s -2 <strong>for</strong> 18 h. Measur<strong>in</strong>g the light quantity<br />

<strong>in</strong>side the bioreactors and mov<strong>in</strong>g the light source closer or further away to<br />

provide the same quantum after filter<strong>in</strong>g can obta<strong>in</strong> this. The bioreactors can<br />

be covered with alum<strong>in</strong>ium foil to provide darkness.

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