Water and Solute Permeability of Plant Cuticles: Measurement and ...
Water and Solute Permeability of Plant Cuticles: Measurement and ...
Water and Solute Permeability of Plant Cuticles: Measurement and ...
You also want an ePaper? Increase the reach of your titles
YUMPU automatically turns print PDFs into web optimized ePapers that Google loves.
112 4 <strong>Water</strong> <strong>Permeability</strong><br />
a Pwv <strong>of</strong> 4.23×10 −11 m 2 s −1 . This is nearly identical to polyethylene. Polyethylene<br />
<strong>and</strong> parafilm <strong>of</strong> 333 nm thickness would have a permeance (Pwv = Pwv/ℓ) <strong>of</strong><br />
1–1.27 × 10 −4 ms −1 , <strong>and</strong> for a 1.1µm thick membrane permeance would be 3.0–<br />
3.84 × 10 −5 ms −1 . Comparing these values with those shown in Table 4.9 leaves no<br />
doubt that a hydrophobic membrane having Pwv similar to PE or parafilm cannot<br />
account for most <strong>of</strong> the permeances observed especially not for those <strong>of</strong> leaf CM.<br />
Pwv measured for a liquid paraffin (hexamethyl tetracosane) is even 100 times<br />
higher (3.3 × 10 −9 m 2 s −1 ) (Schatzberg 1965), <strong>and</strong> it can be ruled out that liquid<br />
cuticular waxes might contribute to barrier properties. Citrus wax is in the fluid state<br />
when T > 70 ◦ C (Reynhardt <strong>and</strong> Riederer 1991). At 25 ◦ C Pw was 5.9 × 10 −10 ms −1 ,<br />
<strong>and</strong> at 55 ◦ C it had dropped to 2×10 −8 ms −1 (Haas <strong>and</strong> Schönherr 1979). This is not<br />
too far from Pw measured for the polymer matrix, which is 2.5×10 −7 ms −1 . Clearly,<br />
we need a solid wax to account for water permeability <strong>of</strong> cuticular membranes.<br />
Fox (1958) studied water vapour transmission <strong>of</strong> thin cellophane films coated<br />
with paraffin waxes. Waxes were applied at temperatures above the melting point,<br />
<strong>and</strong> solidified at various temperatures. The composite membranes were stored at<br />
23 ◦ C or 35 ◦ C before vapour transmission rates were determined at 23 ◦ C <strong>and</strong> 50%<br />
humidity using a cup method (Sect. 9.7). Data obtained with a paraffin wax having<br />
a melting point <strong>of</strong> 62 ◦ C are shown in Table 4.11.<br />
In the original paper, wax load was given as lb/ream. These figures were converted<br />
to gm −2 using 453.6 g per pound <strong>and</strong> 278.71m 2 per ream. Depending on<br />
type <strong>of</strong> paper the ream can have variable size. The ream <strong>of</strong> glassine paper consists<br />
<strong>of</strong> 500 sheets <strong>of</strong> 24 × 36 inches (Scott et al. 1995). <strong>Water</strong> vapour transmission rates<br />
reflect permeability <strong>of</strong> the wax films because cellophane has very high water permeability.<br />
WVTR depended on temperature <strong>of</strong> water used for cooling the melt <strong>and</strong><br />
on duration <strong>of</strong> storage <strong>of</strong> solidified wax. Rapid cooling at 1.7 ◦ C resulted in high initial<br />
WVTR, which decreased to about one half during 4–5 days storage. At higher<br />
cooling temperatures initial WVTR were lower, <strong>and</strong> decreased to 0.02gm −2 day −1 .<br />
Longer storage (38 days) had little effect, but with some waxes WVTR dropped to<br />
0.01gm −2 day −1 . After 4–5 days storage at 35 ◦ C, permeance (Pwv) ranged from<br />
2.2 × 10 −8 to 8.9 × 10 −8 ms −1 . This is lower by at least one order <strong>of</strong> magnitude<br />
than Pwv for CM (Table 4.9).<br />
Table 4.11 <strong>Water</strong> vapour transmission rate (WVTR) <strong>of</strong> cellophane membranes coated with molten<br />
paraffin wax <strong>and</strong> cooled at various temperatures either in water or air. WVTR rates measured at<br />
23 ◦ C <strong>and</strong> 50% humidity<br />
Cooling T( ◦ C) Wax ℓ <strong>of</strong> WVTR WVTR Pwv (ms −1 )<br />
load wax (first day) (after 4–5 days)<br />
(gm −2 ) (µm) (gm −2 day −1 ) (gm −2 day −1 )<br />
1.7 (water) 11.7 12.9 0.15 0.08 8.9 × 10 −8<br />
7.2 (water) 10.9 12.0 0.12 0.03 3.3 × 10 −8<br />
12.8 (water) 9.6 10.6 0.05 0.03 3.3 × 10 −8<br />
18.3 (water) 9.8 10.8 0.07 0.02 2.2 × 10 −8<br />
23.0 (air) 10.7 11.8 0.09 0.02 2.2 × 10 −8