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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-

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