Production Practices and Quality Assessment of Food Crops. Vol. 1
Production Practices and Quality Assessment of Food Crops. Vol. 1
Production Practices and Quality Assessment of Food Crops. Vol. 1
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With centrifugal energy systems droplet sizes with optimum target collection efficiency<br />
can be produced (Harden, 1992), meaning that less volume <strong>of</strong> total liquid<br />
is needed as large drops are not produced. Drift can also be minimised, as there<br />
are no droplets at the small end <strong>of</strong> the spectrum. However, CDA equipment requires<br />
constant careful maintenance for optimal efficiency, <strong>and</strong> the system needs to be<br />
understood to be used effectively as flow rate, liquid viscosity <strong>and</strong> rotational speed<br />
are critical for droplet formation.<br />
3.3. Airshear<br />
The airshear principle involves the shattering <strong>of</strong> a liquid stream with a fast moving<br />
column <strong>of</strong> air. The liquid is sheared into small droplets, with droplet size controlled<br />
by the liquid/air ratio. Smaller droplets are produced with reduced liquid flow<br />
<strong>and</strong> higher air velocities. In order to obtain maximum liquid shatter <strong>and</strong> correct<br />
droplet formation, it is necessary to generate air speeds <strong>of</strong> 65–90 m/sec at the nozzle<br />
(Alcorn, 1993). The energy <strong>of</strong> the motor is used primarily to drive the fan producing<br />
the air flow <strong>and</strong> the ducting is designed to provide maximum air speed at the point<br />
<strong>of</strong> droplet formation. Advantages <strong>of</strong> this system are the ability to use reduced carrier<br />
volumes <strong>and</strong> the air movement created by the equipment moves droplets to the target<br />
<strong>and</strong> provides energy for impaction/capture. The liquid/air flow ratio must be correctly<br />
adjusted <strong>and</strong> maintained if a narrow droplet spectrum is to be produced.<br />
Airshear can also be used for secondary break up <strong>of</strong> larger droplets produced<br />
initially by hydraulic nozzles (e.g. orchard air-blast sprayers). The orientation <strong>of</strong><br />
the hydraulic nozzles in relation to the air stream affects the degree <strong>of</strong> secondary<br />
airshear <strong>and</strong> therefore the droplet spectrum (Harden, 1992).<br />
3.4. Kinetic<br />
Droplets can be formed in either low-energy vibrators or ultrasonic atomisers. The<br />
former tends to produce relatively large droplets <strong>and</strong> are not widely used in<br />
pesticide application except where large volumes <strong>of</strong> pesticide per unit area <strong>and</strong><br />
minimum drift are required. Liquid is gravity fed through a series <strong>of</strong> orifices which<br />
are vibrated to break up the liquid stream into droplets (Banks et al., 1990).<br />
Ultrasonic atomisers use electric <strong>and</strong> magnetic transducers <strong>and</strong> can produce uniform<br />
droplets as small as 50 micron (µm) in diameter.<br />
3.5. Thermal<br />
Droplets can be produced by vaporising the pesticide in a stream <strong>of</strong> hot gas which<br />
is then cooled by rapid expansion. Condensation produces a dense fog <strong>of</strong> very<br />
small droplets. Such droplets are very susceptible to drift. This system is not suited<br />
to the orchard situation.<br />
3.6. Electrodynamic methods<br />
Spray Technology in Perennial Tree <strong>Crops</strong> 87<br />
No mechanical energy is required for droplet formation in this system. The liquid<br />
stream is fed between two charged plates which subject it to an intensely diver-