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

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176 6 Diffusion <strong>of</strong> Non-Electrolytes<br />

6.3 Diffusion with Changing Donor Concentrations:<br />

The Transient State<br />

Permeance (P) is a composite property (2.18). It is proportional to solubility (K)<br />

<strong>and</strong> mobility (D) <strong>of</strong> water <strong>and</strong> solutes in membrane, <strong>and</strong> inversely proportional<br />

to thickness <strong>of</strong> the membrane (ℓ). In homogeneous membranes, solute permeability<br />

is characterised using D <strong>and</strong> K because they are easily measured. <strong>Cuticles</strong> are<br />

highly asymmetrical (Sect. 1.4), <strong>and</strong> both water concentration <strong>and</strong> mobility vary<br />

with position (Chap. 4). <strong>Water</strong> transport occurs in aqueous pores, cutin <strong>and</strong> waxes,<br />

<strong>and</strong> their mutual arrangements determine water permeability. The question arises<br />

whether this also applies to solutes. In Sect. 6.2 we used permeances to characterise<br />

solute permeability, which can be measured easily in the steady state using various<br />

methods. Unfortunately, since P is a mixed quantity it is not possible to explain why<br />

permeances differ among cuticles from different species. In an attempt to obtain a<br />

better underst<strong>and</strong>ing <strong>of</strong> solute permeability in cuticles, we have developed methods<br />

to estimate solute mobility in CM, MX <strong>and</strong> in waxes.<br />

6.3.1 Simultaneous Bilateral Desorption<br />

Diffusion coefficients can be estimated from sorption <strong>and</strong> desorption experiments<br />

(Sect. 2.6). We have used this approach to measure mobility <strong>of</strong> lipophilic 2,4-D<br />

in CM <strong>and</strong> MX membranes. Astomatous CM <strong>and</strong> MX membranes obtained from<br />

leaves <strong>and</strong> fruits were submerged in aqueous buffer (pH 3) containing 14 C-labelled<br />

2,4-D. After equilibration they were removed from the buffer, blotted dry, flattened<br />

on a piece <strong>of</strong> Teflon <strong>and</strong> air-dried. Dry membranes were inserted between the two<br />

half-cells <strong>of</strong> a transport apparatus made <strong>of</strong> stainless steel (Fig. 9.4). This made it possible<br />

to desorb 2,4-D separately from the outer <strong>and</strong> inner surfaces <strong>of</strong> the membranes.<br />

Borax buffer (pH 9.18), in which 2,4-D is fully ionised, was used as desorption<br />

medium. By changing desorption media quickly <strong>and</strong> repeatedly, the amounts <strong>of</strong><br />

2,4-D desorbed at various times (Mt) were studied.<br />

Desorption was very rapid, <strong>and</strong> 90% <strong>of</strong> the 2,4-D initially contained in the CM<br />

<strong>and</strong> MX membranes were desorbed in 4 h (Fig. 6.15a). With a homogeneous membrane,<br />

50% <strong>of</strong> solute should be desorbed from either side <strong>and</strong> the two desorption<br />

plots should be symmetrical. This was clearly not the case, neither with CM <strong>and</strong><br />

MX. Only very small amounts (5%) were desorbed from the morphological outer<br />

surfaces <strong>of</strong> the Citrus CM, while 17% could be desorbed from the outer surface<br />

<strong>of</strong> the MX membranes. The largest fraction <strong>of</strong> 2,4-D was desorbed from the inner<br />

surface, as in 240 min 86% (CM) <strong>and</strong> 71% (MX) left the membranes through the<br />

morphological inner surfaces. Clearly, these membranes are highly asymmetrical,<br />

<strong>and</strong> this asymmetry can be characterised by comparing the initial rates <strong>of</strong> desorption<br />

from the inner <strong>and</strong> outer surfaces respectively. During the first 3 min, 163 times<br />

more 2,4-D was desorbed from the inner surface <strong>of</strong> the CM than from the outer. With

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