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Liquid Culture Systems for in vitro Plant Propagation

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28 Wayne R. Curtis<br />

C<br />

L<br />

y � P O2<br />

� C*<br />

�<br />

(Eqn. 5)<br />

H<br />

It is important to note that equilibrium dissolved oxygen (C * ) is almost never<br />

measured; <strong>in</strong>stead, probes are calibrated to give a percentage readout of this<br />

complex variable. Each of the parameters of oxygen mole fraction (yO 2 ),<br />

system pressure (P) and Henry’s Law coefficient (H) present different<br />

approaches to <strong>in</strong>creas<strong>in</strong>g oxygen availability.<br />

Bioreactor pressure will often enhance oxygen availability as an <strong>in</strong>direct<br />

consequence of bioreactor operation. In situ sterilisable bioreactors are<br />

pressure-rated autoclaves (sterilized @ ~18 p.s.i., 120 o C). The typical<br />

approach of operat<strong>in</strong>g at a head pressure of 5-10 p.s.i. not only reduces<br />

contam<strong>in</strong>ation risks from leaks, but can nearly double the equilibrium<br />

dissolved oxygen (1 atmosphere = 14.7 p.s.i.). In addition, the hydrostatic<br />

pressure (�H 2 0·g·depth) can be a significant contributor to oxygen transfer<br />

driv<strong>in</strong>g <strong>for</strong>ce (1 atmosphere � 33 feet of water). These observations have<br />

<strong>in</strong>terest<strong>in</strong>g implications <strong>for</strong> liquid culture micropropagation. The<br />

productivity of a reasonably efficient somatic embryogenic culture can<br />

generate large numbers of embryos <strong>in</strong> bioreactors smaller than 1000 l. S<strong>in</strong>ce<br />

scale-up would take place <strong>in</strong> tanks much smaller than traditional<br />

fermentation, the depth effect will be m<strong>in</strong>imal. Use of pressurization<br />

(beyond autoclave pressures) is usually avoided due to the prohibitive cost<br />

of pressure vessels (Curtis, 1999). However, s<strong>in</strong>ce ‘large-scale’<br />

micropropagation can be implemented at a small scale, the pressure rat<strong>in</strong>g of<br />

the vessel (and associated steel costs) will not dom<strong>in</strong>ate overall equipment<br />

costs, and use of pressure could be economically feasible if it provides a<br />

substantial improvement <strong>in</strong> micropropagule development.<br />

It is also apparent from equation 5, that an <strong>in</strong>crease <strong>in</strong> the Henry’s Law<br />

coefficient (H) will reduce the equilibrium dissolved oxygen pressure.<br />

Temperature has the greatest <strong>in</strong>fluence on H. As the temperature <strong>in</strong>creases,<br />

H <strong>in</strong>creases as thermal vibrations exclude oxygen, which decreases the<br />

maximum amount of oxygen that can dissolve <strong>in</strong> the media. Colder<br />

temperatures, there<strong>for</strong>e, favor oxygen solubility (15, 20, 25 and 30 o C<br />

correspond to 315, 283, 258, and 236 �mol O2 respectively <strong>in</strong> water). To<br />

take advantage of the <strong>in</strong>creased oxygen solubility at lower temperatures, an<br />

organism must be able to susta<strong>in</strong> metabolism rates. This is not generally the<br />

case <strong>for</strong> terrestrial plant tissues, there<strong>for</strong>e, a reduction <strong>in</strong> temperature will<br />

usually significantly reduce the BOD. A suppression of tissue development<br />

rates is generally not desirable s<strong>in</strong>ce it will <strong>in</strong>crease the time-frame required<br />

to produce micro-propagules. This observation may, however, be useful if it<br />

is desirable to ma<strong>in</strong>ta<strong>in</strong> aerobic respiration with<strong>in</strong> a tissue by simultaneously

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