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Liquid Culture Systems for in vitro Plant Propagation

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Application of Bioreactor Design Pr<strong>in</strong>ciples 23<br />

Table 1: Oxygen uptake rates (OUR) of plant tissues and plant tissue culture.<br />

<strong>Plant</strong> OUR (A)<br />

Alfalfa (Medicago sativa, germ<strong>in</strong>at<strong>in</strong>g seed, 18 o C) 44<br />

Wheat (Triticum aestivum, seedl<strong>in</strong>g, 18 o C) 8.8<br />

Corn (Zea mays, seedl<strong>in</strong>g, 18 o C) 6.3<br />

Pea (Pisum sativum, seed, 20 o C) 6.2<br />

Rye (Secale cereale, seedl<strong>in</strong>g, 18 o C) 5.0<br />

Potato (Solanum tuberosum, whole plant, 19 o C) 4.5<br />

Tobacco (Nicotiana tabacum, whole plant, 20 o C) 3.2<br />

<strong>Plant</strong> Tissue <strong>Culture</strong> (B), bulk tissue<br />

root meristem<br />

10-12<br />

200-300<br />

(A) Data from compilation reference (Altman and Dittmer, 1968); �mol O 2 g -1 FW·hr l -1 .<br />

(B) Average values from experimental measurements and quoted literature values.<br />

3. Oxygen transfer rate<br />

The average BOD can also be used to carry out an <strong>in</strong>itial “ball park”<br />

estimate of oxygen transfer rates (OTR) needed to supply oxygen. Under<br />

balanced equilibrium conditions, total demand will be equal the oxygen<br />

transfer rate from the gas to the media (OTRg-L):<br />

OTRg-L = BOD · �t · Vt = kLa (C* - CL) (Eqn. 1)<br />

Where �t is the tissue density (1.04 g ml -1 ; approximately water), Vt is the<br />

tissue volume, C* and CL are the equilibrium and actual medium dissolved<br />

oxygen concentrations, and kLa is a parameter used to characterize the rate of<br />

oxygen transfer from the gas phase to the medium. To provide <strong>for</strong> diffusion<br />

of oxygen <strong>in</strong>to the tissue it is reasonable to take C L � C*/2, there<strong>for</strong>e, an<br />

estimate <strong>for</strong> kLa of 8 hr -1 can be calculated as the mass transfer rate needed to<br />

supply a typical plant tissue culture BOD. This <strong>in</strong>itial calculation leads to a<br />

mislead<strong>in</strong>g conclusion, s<strong>in</strong>ce this rate of oxygen transfer should be easy to<br />

achieve <strong>in</strong> just about any bioreactor configuration (simple shake flasks or<br />

blow<strong>in</strong>g of bubbles <strong>in</strong> media would greatly exceed this level; Blanch and<br />

Clark, 1997). This apparent ease of supply<strong>in</strong>g oxygen is qualitatively<br />

consistent with the observation that slow-grow<strong>in</strong>g plant tissues should have<br />

much lower oxygen demand than microbial cultures, none-the-less,<br />

experimentation has shown that plant tissues very often display oxygenlimited<br />

behavior. For example, the doubl<strong>in</strong>g of O2 concentration <strong>in</strong> a flask

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