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Materials used for seed storage containers: response to Gómez-Campo [Seed Science Research16, 291–294 (2006)]†

Published online by Cambridge University Press:  01 December 2007

Christina Walters*
Affiliation:
USDA-ARS National Center for Genetic Resources Preservation, 1111 South Mason Street, Fort Collins, Colorado, USA
*
*Correspondence Fax: 1-970-221-1427 Email: christina.walters@ars.usda.gov
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Abstract

Efficient seed storage is a shared concern among the growing number of seed banks established for crop improvement or ex situ conservation. Container properties greatly affect seed interactions with the environment and the overall cost and success of seed banking operations. Several material properties contribute to their suitability as seed containers. This paper provides a consolidated list of water vapour permeability properties of thermal plastics commonly used for packaging. Composite packages with layers of film with different properties provide distinct advantages to seed banks. Different seed banks must rank the importance of the various factors depending on their mission and resources. Once the risks, costs and benefits are weighed, an appropriate strategy can be developed that addresses a seed bank's specific needs. Because there are many problems and several solutions, it is likely that strategies will vary among seed banks. This response details variables to consider when selecting seed storage packages, and focuses on water diffusion rates of packages with different compositions. A ‘moisture audit’ will help seed bank operators make informed decisions about packaging.

Information

Type
Research Article
Copyright
Copyright © Cambridge University Press 2007
Figure 0

Table 1 Properties of seed storage containers that affect overall operating efficiency

Figure 1

Table 2 Saturation water vapour pressure (VPsat) at sea-level and different temperatures from a psychrometric chart (Harriman, 1990; Parsons, 1997; Wikipedia, 2007c, e). Values are given in mmHg or kPa for air over liquid water or ice. The relationships are also calculated using the Goff–Gratch and Clausius–Clapeyron equations using standard values for constants (Atkins, 1982; Parsons, 1997; Wikipedia, 2007b, d). The Clausius–Clapeyron model assumes constant heat of vaporization (over liquid water) or sublimation (over ice) and so is less accurate

Figure 2

Table 3 Water vapour permeability (WVP) of thermal plastics and other materials used for protective coatings or packaging. WVP is calculated based on material properties obtained from an Internet search ending on 26 February 2007. Units for WVP for all studies were converted to g·cm m−2 h−1 kPa−1, which expresses the mass of water (g) that diffuses through a barrier thickness (cm) over a specified surface area (m2) in a specified time (h) as a result of a specified water pressure difference (kPa). The conversions required to assemble Table 3 made assumptions to calculate g water (using STP if water flux was expressed in volume, and T and P were not specified) and ΔVP (use of equation (2) and Table 2; conversion of mmHg used 750 mmHg to 1 bar), temperature was assumed to be 25°C if not reported, and atmospheric pressure at sea-level. Materials are listed in order of decreasing permeability, and classified by comparison to air (essentially no barrier)

Figure 3

Table 4 Calculated permeance of composite packaging materials

Figure 4

Table 5 ‘Functional’ permeance values for thin aluminium and silica glass layers, based on the total surface area of pinholes and fractures produced during layer deposition. Permeance values will change during handling, as these materials are fragile

Figure 5

Figure 1 (a) The initial rate of water vapour diffusion into 14 × 16 cm packet made of high-density polyethylene with 0.004 cm thick walls, as a function of the quality of the seal. Seal opening was assumed as twice the thickness of the material (0.008 cm) × the width of the package opening (14 cm). Flux rates at 25°C are calculated for inside RH = 25% and surrounding RH = 90% and 50% (indicated), and elevation = 0 (solid) and 1645 m (dashed lines). (b) The initial rate of water vapour diffusion into a glass jar (7.6 cm diameter, 13.2 cm height, 0.01 cm thick) with a polytetrafluoroethylene (PTFE) lid (0.01 cm thick) as a function of the thickness of the air layer between jar and lid. Inside RH is 25%. Scenarios are given for 25°C, 0 m elevation, surrounding RH = 90% (solid line); and for 5°C, 1645 m elevation and surrounding RH = 50% (dashed line). The perfectly sealed polyethylene packet allows a flux of 0.172 g H2O d− 1 (WVP÷thickness × SA × ΔVP) for 25°C, 0 m, 90% RH [circle on vertical axis in (a)], and is comparable to a 0.003 cm gap between jar and lid [dashed box and arrow in (b)].

Figure 6

Figure 2 Rate of water vapour diffusion (WVTR) through 0.004 cm thick, high-density polyethylene (HDPE), as a function of the surrounding relative humidity and temperature. Inside RH is 25% and elevation = 0 m. Units used in Fig. 1a can be obtained by multiplying the ordinate by package surface area (SA). In Fig. 1a, the package SA is 0.0448 m2.

Figure 7

Figure 3 Time, (a) temperature and (b) relative humidity recorded by a data logger within a 400 ml glass jar containing 200 g of pea seeds, sealed with a screw cap metal lid wrapped with Teflon tape. The jar was moved from the laboratory bench (arrows 1) to the freezer ( − 18°C) (arrow 2) to an oven (45°C) (arrow 3).