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

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3.1 Units <strong>of</strong> <strong>Permeability</strong> 55<br />

3.1.1 Example<br />

Diffusion <strong>of</strong> water vapour across a polyethylene terephthalate (PET) membrane <strong>of</strong><br />

0.1 cm thickness was measured at 25 ◦ C. The vapour pressure in the donor chamber<br />

was 2.375 cmHg, which is the saturation vapour pressure <strong>of</strong> water at 25 ◦ C. Jv was<br />

4.2 × 10 −7 cm 3 vapour (STP) per cm 2 <strong>and</strong> s. From these data PHg can be calculated<br />

using (3.1):<br />

PHg = 4.2 × 10−7 cm 3 (STP) × 0.1cm<br />

cm 2 s × 2.375cmHg<br />

= 1.77 × 10 −8cm3 (STP)cm<br />

cm2 . (3.2)<br />

scmHg<br />

One might be tempted to simplify this dimension <strong>of</strong> PHg <strong>and</strong> write cm 2 s −1 , because<br />

in writing PHg driving force was 1 cmHg. This was never done, <strong>and</strong> we shall stick<br />

to the extended unit found in the literature, which does not use the suffix Hg to<br />

characterise this type <strong>of</strong> permeability coefficient.<br />

In biology, it is not customary to use fluxes based on vapour volume. Instead,<br />

mass fluxes (mol or kg) are used. Hence, we must convert the volume flux <strong>of</strong> gases<br />

or vapours (Jv) into mass fluxes (J). The volume <strong>of</strong> water vapour at STP can be converted<br />

to gram water by considering the vapour as an ideal gas, <strong>and</strong> this was always<br />

assumed when calculating Jv from experimental flux data expressed in pressure units<br />

(Fig. 3.1). The volume (V) <strong>of</strong> 1 mol <strong>of</strong> an ideal gas at STP can be calculated from<br />

the ideal gas law:<br />

V =<br />

n × R × T<br />

p<br />

= 1mol × 8.3143m3 Pa × 273.15K<br />

molK × 101,325Pa<br />

= 0.022414m 3 , (3.3)<br />

where R is the gas constant. One mol <strong>of</strong> water has a mass <strong>of</strong> 18 g, <strong>and</strong> the density <strong>of</strong><br />

water vapour (δwv) at STP is<br />

δwv = mass<br />

volume =<br />

18g<br />

22.414× 103 cm3 = 8.03 × 10−4gcm −3<br />

<strong>and</strong> the mass flux <strong>of</strong> water (Jw) can be calculated<br />

Jw = Jv × δwv = � 4.2 × 10 −7 cm 3 (STP) cm −2 s −1�� 8.03 × 10 −4 gcm −3�<br />

= 3.37 × 10 −10 gcm −2 s −1 .<br />

(3.4)<br />

(3.5)<br />

Before permeance or permeability can be calculated in SI units, the driving force<br />

must be converted. Yasuda <strong>and</strong> Stannett (1962) <strong>and</strong> others used cmHg, <strong>and</strong> conducted<br />

various experiments with different pressures in the donor. Results are shown<br />

in Fig. 3.2. The volume flux was proportional to pressure in cmHg or to partial<br />

pressure.<br />

In the SI system the driving force is <strong>of</strong>ten mass per volume, which is molm −3<br />

or kgm −3 . This is practically always the case with solutes dissolved in water. With<br />

water vapour, partial pressure or activity <strong>of</strong> water can be used as an alternative. At<br />

this point we decide to use partial pressure as driving force, but we shall deal with

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