1. Introduction
Water shortages throughout the world, exacerbated by climate change, are accelerating the adoption of technologies to help crop production use less water [
1,
2]. One little-used technology is the retardation of water vapour loss from stomata on the leaves of crop plants by the application of polymers, referred to as film antitranspirants in this context. These polymers are used on high-value ornamental plants, but are not yet widely-used on lower-value major food crops [
3].
Recent research has revealed the potential for these polymers to reduce food crop yield loss from drought if application is timed to drought-sensitive stages of development in wheat [
4,
5] and in rapeseed [
6]. Appropriately-timed film antitranspirant applications under drought have been previously associated with enhanced water saving strategies, lowered abscisic acid accumulation and an increase in leaf intrinsic water use efficiency leading to sustained key yield components under distinct reduced water availability patterns [
4,
5,
6]. A further use of film antitranspirants is to reduce photosynthesis and, thus, excessive sugar accumulation in grapes resulting from rising temperature as the climate changes [
7,
8]. However, the problem with current commercially-available film antitranspirant products is that they are expensive, and this inhibits their use in crop production. A cheaper film antitranspirant would facilitate their use in crop production. One possibility for producing a cheaper product may be to use waste material as a source of antitranspirant, and in our study we use waste leaves trimmed from brassica produce after harvesting. Currently, fresh produce processors in the UK send waste brassica leaves for either anaerobic digestion or livestock feed. Brassica species have a substantial layer of leaf wax, e.g., [
9], which in all plants has evolved as a natural barrier covering the majority of the leaf surface to reduce water vapour loss from the leaf cuticle [
10]. If this wax could be extracted cheaply, it may act as an antitranspirant if appropriately formulated and sprayed onto plants at risk of water stress. Thus, the hypothesis tested in our study was that leaf wax extracted from cauliflower trimming waste may have the potential to reduce transpiration when applied to rapeseed plants.
The objectives of the studies described in this paper were:
To extract wax using supercritical CO2 from cauliflower (Brassica oleracea L.) leaf waste and to formulate the wax for spraying as a film antitranspirant.
To evaluate the efficacy of this wax formulation in comparison with a current commercial film antitranspirant (di-1-p-menthene) for reducing stomatal conductance and water use of young glasshouse-grown plants of rapeseed (Brassica napus L.) in three experiments.
To compare the cost of the extracted wax with the cost of di-1-p-menthene.
2. Materials and Methods
An outline of the main steps in the research methodology is shown in
Figure 1.
2.1. Supercritical CO2 Extraction of Wax and Its Characterization
Air-dried cauliflower leaves were extracted using a Thar SFC-1000 laboratory system fitted with a 2000 mL extractor and a 500 mL separator operating at 350 bar, 50 °C, 40 g minute−1 CO2 for 4 h. The leaf wax deposited in the separator was recovered using dichloromethane and the dichloromethane was subsequently removed in vacuo. The yield of the leaf wax was measured and the wax compounds were analysed with an Agilent 6890 gas chromatograph coupled to an Agilent 5973 mass spectrometer (EI detector).
A 6% (m/m) cauliflower leaf wax formulation was prepared for in vivo plant assessments by adding wax and glycerol monostearate into hot water at a ratio of 1:2 along with 1.0% (m/m) of Tween 20. This mixture was homogenised at 4000 rpm using an IKA T18 basic Ultra-Turrax until an emulsion was formed.
2.2. Plant Material and Experimental Design
Three seeds per pot were sown of rapeseed (cv. Excalibur) in 1 L pots (13 cm top diameter) filled with ~600 g of John Innes #2 compost [
11] at 22 ± 1% volumetric water content (VWC) analysed with a soil moisture probe (ML2X theta probe, Delta-T Devices, Cambridge, UK). The pots were placed on a bench in a glasshouse at Harper Adams University (52.8° N 2.4° W) and the pots were thinned to one plant at the 2nd leaf stage. The solar radiation in the glasshouse was supplemented from sodium vapour lamps (Osram Ltd., Reading, UK, model: Vialox NAV-T 400) set to 16 hrs per day. The glasshouse heating minimum temperature was set to 15 °C during the day and 5 °C during the night, and because the experiments were conducted in winter, higher temperatures would have occurred only infrequently. The pots were manually watered approximately to saturation on the day that the seeds were sown and no water was applied until the seedlings appeared. After the seedlings appeared, until the application of the treatments, the pots were manually watered approximately to saturation every other day.
All three experiments had three spray treatments (water, di-1-p-menthene and wax) in six (Experiment 1) or eight (Experiments 2 and 3) randomised blocks.
2.3. Water Management and Treatment Application
The available water content (AWC) in mL of the pots was calculated by plotting a volumetric water content (VWC)—pot weight curve: three pots (filled with ~600 g of compost at 22 ± 1% VWC) were water-saturated and then dried over ten days at 30 °C. The VWC by soil moisture probe (ML2X theta probe 120, Delta-T Devices, Cambridge, UK) and the weight by balance (0.1 g resolution, PCB 2500-2, Kern and Sohn GmbH, Balingen, Germany) were recorded daily. For John Innes #2 compost the permanent wilting point and the pot capacity were ~7% VWC and ~45% VWC, respectively [
12]. The total AWC in mL was then calculated as the difference between the weight of the pot at pot capacity (~1000 g) and the weight of the pot at 7% VWC (~650 g) measured by moisture probe. Before the spray treatments were imposed, the surface of each pot was covered by 100 g of plastic beads, so that the water evaporation from the soil surface was minimised.
The spray treatments were applied 14 November 2016, 31 January 2017 and 20 February 2017 for the three experiments, respectively, at the 4th leaf stage. The 4th leaf stage was chosen because by this stage the leaf area and water transpired should be large enough to enable measurement of water use by weight. Spraying occurred just after the pots were watered to pot capacity (45% VWC) for the last time. After this date, the pots were not watered until the experiments ended at 10 days after spraying, which was also 10 days after the imposition of drought.
The three treatments were as follows: water (for control); 1%
v/
v Vapor Gard (di-1-
p-menthene 96% [volumetric or gravimetric not stated], Miller Chemical and Fertilizer LLC, Hanover, USA) in water with no adjuvant; 1%
v/
v wax in water + adjuvant 0.5%
v/
v Wetcit (alcohol ethoxylate 9%, ORO_AGRI Inc, Trophy Club, TX, USA). For Experiments 1 and 2, the adaxial surface of the leaves was uniformly sprayed using a 0.5 L hand-held trigger sprayer at a distance of a few cm until the surface was fully covered. This technique was chosen to ensure complete coverage of the adaxial leaf surface. The assessment of coverage of each plant during spraying is, however, subjective and, therefore, to reduce variation between plants in the quantity of spray applied in Experiment 3, the plants were sprayed using a custom-built automatic pot sprayer in an enclosed chamber that simulates a field crop sprayer more-closely (
Figure 1). The twin nozzle spray boom had nozzles at 50 cm height from the plants, and delivered the spray at 3 bar pressure at 1 m/s speed using Flat Fan 015 nozzles (Teejet, Rockford, MI, USA) delivering the equivalent of 200 L/ha.
2.4. Physiological Assessments
Stomatal conductance (gs) was measured on several days after spraying with a transient state diffusion porometer (AP4, Delta-T Devices, Cambridge, UK) calibrated before every use. Three readings for adaxial gs and abaxial gs were taken from the 3rd leaf of each plant, and the mean calculated. Data were collected between 11.00 am to 2.00 pm, in a blockwise manner to minimise any diurnal effect on gs.
Plant water use was quantified every day from the date of the spray application to 10 days after spraying by weighing each pot between 8.30 am to 9.30 am. It was assumed that the beads completely blocked evaporation of water from soil. Daily water use of each pot was calculated as the difference between the weight of the pot on the day and the weight of the pot after 24 h. Cumulative water use of each plant for the period of experimentation was calculated by summing up daily water use.
2.5. Statistical Analysis
All the data were analysed using Genstat (18th and 20th Editions, VSNi, Hemel Hempstead, UK). Adaxial and abaxial gs were analysed with a two factor (Time × Treatment) randomised complete block repeated measures ANOVA. Cumulative water use was analysed by a single factor (Treatment) randomised complete block ANOVA.
3. Results
The principal components of the wax were nonacosane, 15-nonacosanone, triacontane and γ-sitosterol (
Figure 2), and we obtained a wax yield from dried leaves of 1.31% (m/m).
Figure 3 shows that abaxial
gs was higher than adaxial
gs at the start of all three experiments and the
gs on both leaf surfaces was higher at the start of the measurement period in Experiment 1 than in Experiments 2 and 3. In Experiments 1 and 2, both di-1-
p-menthene and wax reduced adaxial
gs initially, but this effect diminished as the plants became more stressed after water was withheld and
gs declined (
p < 0.001 for Time × Treatment interactions). There was an indication that adaxial
gs responded similarly in Experiment 3 but this was not significant (
p = 0.473 for Time × Treatment interaction). Abaxial
gs also responded to di-1-
p-menthene and wax in Experiment 2 (
p = 0.005 for Treatment) but not in Experiments 1 and 3.
Water use of control plants was greatest in Experiment 1 (
Figure 4), similar to stomatal conductance, and in this experiment di-1-
p-menthene gave only a small (non-significant) reduction, whereas wax significantly reduced water use by 14%. Water use was not affected by either di-1-
p-menthene or wax in Experiments 2 and 3.
4. Discussion
The composition and concentration of wax we obtained are consistent with previous work on
B. Oleracea [
13,
14]. Laila et al. [
14] give wax concentration values of 0.15% (m/m) on a fresh weight basis, and re-calculating our wax yield on a fresh weight basis gives a similar value of 0.18% (m/m).
Both low stomatal conductance at the last measurement date and cumulative water use close to the AWC indicate that the plants in all experiments were highly stressed by the end of the experiments. Higher abaxial
gs may be because rapeseed usually has greater stomatal density on the abaxial than on the adaxial leaf surface, e.g., [
15,
16], as most dicotyledonous species [
17]. The difference in
gs between experiments may be because the leaves in Experiment 1 developed in higher light intensity during leaf development, which is well-known to give greater stomatal density, e.g., [
17], and thus higher
gs. Leaves in Experiment 1 developed mostly in October when solar radiation was higher (monthly total 196 MJ/m
2) compared with leaf development for Experiment 2 mostly in January (57 MJ/m
2) and for Experiment 3 mostly in February (107 MJ/m
2). In addition to the higher solar radiation for Experiment 1 indirectly giving greater
gs through affecting stomatal density as the leaves developed, the higher solar radiation at the time of measurement would be expected to increase
gs in Experiment 1 [
18].
The differences in
gs response between experiments may be a consequence of differences in spraying. Experiments 1 and 2 were both sprayed with hand-held sprayers until the adaxial surface was covered, and this may have delivered a greater volume, thus giving a significant reduction in
gs compared with the automatic pot sprayer used in Experiment 3. Different operators sprayed Experiments 1 and 2, and the abaxial response in Experiment 2, but not in Experiment 1, may result from a difference in hand-spraying technique between operators. In future experiments, the spraying conditions may need further investigation since leaf coverage with antitranspirants is important for blocking stomata to reduce transpiration, and coverage varies with spray parameters, e.g., dose rate [
19].
The lack of response of water use in Experiments 2 and 3 may possibly be because the water use and gs of control plants were lower in these experiments compared with in Experiment 1.
The experiments show that wax formulated with glycerol monostearate is generally as effective as di-1-p-menthene in reducing stomatal conductance when sprayed at 1% (v/v). This is a much lower concentration of active substance (a.s.) for wax since the wax before dilution was 6% (m/m) a.s. whereas di-1-p-menthene before dilution was 96% (volumetric or gravimetric not stated) a.s., possibly implying a much lower optimum concentration of wax than of di-1-p-menthene. Further experiments are needed to confirm this implied difference in activity, and, if it is confirmed, three possible reasons could be:
Wax may be more effective than di-1-
p-menthene at blocking stomata, as shown previously for petroleum-derived wax products [
20,
21].
The glycerol monostearate used to formulate the wax for spraying may have also acted as an antitranspirant since both the alcohol and acid parts of this ester are known to have antitranspirant properties [
22,
23].
Another plant component co-extracted with the wax may have had antitranspirant activity, e.g., if abscisic acid was co-extracted, as this hormone is a metabolic antitranspirant [
3].
The third objective of the study was to compare the cost of the wax with the cost of di-1-p-menthene. The cost of extracting the wax is estimated at GBP 167/kg (equivalent to USD 225/kg). This calculation assumes: a wax concentration of 1.5% in the waste biomass (similar to the concentration found in this study); a 1000 kg batch of wax is extracted; a currency conversion of 1.35 USD/GBP. An approximate cost of production for a formulated wax AT (based on the wax cost only) at 6% (m/m) as used in this research, would be GBP 10.02/l or USD 13.53/L). The retail price of a biostimulant with this cost of production may possibly have to be in the region of USD 130/L to be cost effective for commercial sale (S. Adams, Plant Impact, Personal communication). In comparison, the di-1-
p-menthene product (Vapor Gard) retail price per US gallon (3.79 L) is USD 69.9 [
24] or a unit price of USD 18.44/L, indicating that a wax AT would need a much lower cost of production than USD 13.53/L to be a viable commercial proposition. It is possible that the cost of production of a formulated wax antitranspirant can be kept low if: a lower wax concentration can be used in the formulated antitranspirant as implied from the greater efficacy; larger batch sizes of wax can be extracted; waste biomass with greater wax concentration can be sourced; the wax can be a co-product from biomass utilization in an integrated biorefinery.
Further work is necessary to investigate: optimal spraying conditions; dose-response characteristics of the wax compared with di-1-p-menthene (to confirm the greater activity of the wax); activity of the formulation component glycerol monostearate applied separately; leaf photosynthesis before and after spraying; ways to lower the cost of production; performance of the wax in the field in a range of countries with different climatic conditions.
In conclusion, we have shown that leaf wax can be extracted from cauliflower leaf waste using supercritical CO2 and can be formulated as a film antitranspirant for spraying; this wax formulation had similar efficacy to a current commercial film antitranspirant (di-1-p-menthene) for reducing stomatal conductance and water use of young glasshouse-grown plants of rapeseed. A lower cost of production of the wax is needed for commercial exploitation.