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Water and Solute Permeability of Plant Cuticles: Measurement and ...

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54 3 Permeance, Diffusion <strong>and</strong> Partition Coefficients: Units <strong>and</strong> Their Conversion<br />

Pressure in receiver (mm Hg)<br />

0.4<br />

0.3<br />

0.2<br />

0.1<br />

t e<br />

slope: 2 x 10 −3 mm Hg/min<br />

0.0<br />

0 50 100 150 200 250 300<br />

Time (min)<br />

Fig. 3.1 <strong>Water</strong> vapour transport across an ethyl cellulose (EC) membrane at 25 ◦ C. The pressure<br />

increase in the receiver compartment was plotted vs time. (Redrawn from Yasuda <strong>and</strong> Stannett<br />

1962)<br />

an increase in pressure <strong>of</strong> the receiver, <strong>and</strong> this was used to calculate the flux. The<br />

steady state flux was obtained by keeping the pressure difference between donor <strong>and</strong><br />

receiver practically constant (steady state). Gas or vapour pressures were measured<br />

in cm mercury (cmHg). Vapour pressure greatly depends on temperature, which<br />

necessitates rigorous temperature control. In this book, we shall deal with permeability<br />

<strong>of</strong> membranes to water <strong>and</strong> water vapour. Penetration <strong>of</strong> permanent gases<br />

(O2, N2, CO2) has been reviewed by Lendzian <strong>and</strong> Kerstiens (1991). While the following<br />

conversions also apply to permanent gases, we shall simply use the term<br />

vapour. A typical example is steady state diffusion <strong>of</strong> water vapour at 25 ◦ C across<br />

an ethyl cellulose (EC) membrane, as shown in Fig. 3.1.<br />

After some time the flux becomes steady, <strong>and</strong> from these data the extrapolated<br />

hold-up time (te) <strong>and</strong> the steady state flux (amount per unit area <strong>and</strong> time) can<br />

be calculated. Volumes <strong>of</strong> gases or vapours greatly depend on temperature, <strong>and</strong><br />

fluxes were expressed as volume at st<strong>and</strong>ard temperature (273.15 K) <strong>and</strong> pressure<br />

(101,325 Pa), abbreviated as STP. For calculating permeability (PHg), the volume<br />

<strong>of</strong> gas or vapour at STP (Jv) was multiplied by membrane thickness (ℓ in cm) <strong>and</strong><br />

divided by the pressure in the donor (pdonor in cmHg)<br />

PHg = Jvℓ<br />

pdonor<br />

= cm3 (STP)cm−2s−1cm . (3.1)<br />

cmHg<br />

In words, this permeability coefficient has the dimension cubic centimetres <strong>of</strong><br />

vapour at STP passing per second under a gradient <strong>of</strong> 1 cmHg per centimetre membrane<br />

thickness <strong>and</strong> square centimetre <strong>of</strong> membrane area. Before converting this<br />

rather awkward unit to the SI system, we shall present an example taken from<br />

Yasuda <strong>and</strong> Stannett (1962).

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