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Liquid Culture Systems for in vitro Plant Propagation

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462 Michael B. Jackson<br />

CO 2 efflux (night)<br />

60 µmol kg -1 s -1<br />

CO 2 <strong>in</strong>flux (day)<br />

350 µmol kg -1 s -1<br />

CO efflux<br />

60 µmol kg-1 s-1 2<br />

2 2<br />

Ethylene efflux<br />

10 pmol kg-1 s-1 -<br />

Ethylene efflux<br />

10 pmol kg - -1 s -1<br />

O 2 <strong>in</strong>flux (night)<br />

60 µmol kg -1 s -1<br />

O 2 efflux (day)<br />

350 µmol kg -1 s -1<br />

O 2 <strong>in</strong>flux<br />

50 µmol kg -1 s -1<br />

Figure 1: Schematic illustration of the pattern and approximate scale of gas efflux and <strong>in</strong>flux<br />

that underlies normal plant growth and development. Sources <strong>for</strong> gas flux data <strong>in</strong>clude:<br />

Haupt-Hert<strong>in</strong>g and Fock (2002), Jackson (1980), Armstrong et al. (1991) and Poorter et al.<br />

(1991).<br />

3. Aeration by diffusion<br />

The pr<strong>in</strong>cipal mechanism that propels gas exchange <strong>in</strong> and out of a plant<br />

tissue is net diffusion down concentration gradients. The process is summed<br />

up by Fick's Law of Diffusion that can be expressed as Q/t = D � A (C<strong>in</strong> -<br />

Cout)/Th, where Q/t = amount of gas moved per second (flux density); D =<br />

diffusion coefficient of the medium through which the gas is mov<strong>in</strong>g; A =<br />

cross sectional area of diffusion pathway; C<strong>in</strong> = concentration at start of<br />

pathway; Cout = concentration at end of pathway; Th = length of diffusion<br />

pathway. Factors that <strong>in</strong>fluence the components of this equation and thus<br />

impact on the rate of gas transport (flux density) are now exam<strong>in</strong>ed.

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