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Artificially drying lucerne immediately after cutting eliminates quality losses during field drying and minimizes the number of field operations. The average potential saving, calculated over a 20-year period for southeast Queensland, is about $40 (Australian)/t of hay, minus drying costs. The optimum technique of hay drying (immediately after cutting) in a solar-supplemented, step-flow dryer was investigated. A computer model was developed to minimize the cost of drying and to define the optimum drying parameters. Sensitivity analyses were carried out for drying air temperatures in tiie range of 30 to 70° C. The results show that there is an optimum number of hours of operation per day (8 h/d) for any combination of the other variables. The most critical factors affecting annual savings are the temperature of drying air, the length of the drying season, the cost of fuel, and the specific cost of the collector. An economic analysis showed that an average annual increase in profit of about $16/t of dried hay (at 12% w.b.) could be attained under optimum sets of operating conditions.

The benefits of using solar tracking mechanisms, particularly where photovoltaic arrays are used to power a water pumping system, are discussed. The principles of designing and constructing a simple automatic solar tracking mechanism are shown. A single-axis tracking system is used, involving the rotation of the solar receiver at the rate of 15 deg per hour around a north-south axis. A water clock device, with a system of valves controlling the flow of water and so the tracking and reversing rotation mode, is used to track the sun. One hundred and forty to 320 litres of water were used in each cycle. The results of the tests shown that the maximum error of tracking was 15 deg during a 4-week period. After that period, resetting of the mechanism was necessary. The total cost of the materials used for construction of the tracking mechanism was approximately US$50, excluding the frame supporting the photovoltaic array.

Field losses of wheat grain and sprouting can be reduced by harvesting at higher moisture content than is currently practised. When drying from high moisture content the throughput of continuous flow driers can be increased by preheating the grain at the inlet into the drier, using a microwave heating system. A simulation model was developed to establish the performance and the cost of drying for such a system. The effect of the specific costs of the microwave source, electricity and fuel on the overall cost of drying were investigated. Sensitivity analyses were carried out for drying air temperatures in the range 50 to 90°C and for initial grain moisture contents of 16% to 24% w.b. (wet basis). The most critical factors affecting the cost of drying were the specific costs of the microwave source, electricity and fossil fuel. With the present costs of fuel and electricity of around 0·05 Australian dollars per kWh, the maximum economically viable cost of the microwave component of the drying system is 480 $/kW. The highest saving on the cost of drying was achieved when a microwave-supplemented drier operated at an air temperature of about 75°C and dired 150 t/d, reducing grain moisture from 18% w.b. to 12% w.b.