FIGURE 2. Drying efficiency with drying time for various crops. Performance Tables 1 and 2 show the changes in moisture cc crops with the time of day, drying time sunshine ( average temperature in the dryer, and the drying e The drying efficiency (qr) was calculated from the YI = Q,ffx 100 Qi, = 27.777 x W, x L AxIxt where: Qeff Qi, W, L A I t = quantity of heat used in the drying pr = quantity of heat entering the dryer = crop weight loss (kg) = latent heat of vaporisation (KJ/kg) = dryer cover area (m2) = solar radiation level (W/m2) = drying time (h). Solar radiation intensity, I, was estimated from the mean daily solar radiation data of Smith (1967), for Trinidad. An average daily value for the dry months ofJanuary to May was estimated at 18.5 MJ/m2 day or 428 W/m2 for 12 hours of the day. The changes in drying efficiency during the drying cycle and the drying times for the four crops are shown in Figure 2. As dry- ing progresses, and as the rate of drying of the crop decreases in the dryer, drying efficiency also falls. Lawand (1966) and Umarov and Tairov (1982) have reported similar changes in drying effi- ciency with drying time. Based upon the results given in Tables 1 and 2, average, weighted drying efficiencies for the entire drying cycles can be calculated. These are 25 %, 44%, 28% and 37% for mango slices, diced sweet potatoes, de-seeded sorrel and cut hot peppers respectively. It should be noted that the hot peppers were dried to a moisture content of 31%, and with further drying necessary for safe storage, a lower drying efficiency can be ex- pected. The sweet potatoes dried rapidly, principally due to the size reduction, and hence showed the highest drying efficiency. Pande et al. (1981) have reported average drying efficiencies in a solar cabinet dryer for cluster bean pods, chilies and dates, of 19%, 20% and 18% respectively. VOL. XX-PROCEEDINGS of the CARIBBEAN FOOD CROPS SOCIETY TECHNICAL AND ECONOMIC CONSIDERATIONS )ntent of the Based on Equation [1], a moisture removal rate M (kg/m2 h), e hours), the for a solar cabinet dryer may be described and is given by, efficiency M = We/At relationship, = 36 rI x 10-3/L [EQUATION 2] For many perishable crops, drying in a solar cabinet dryer can be completed in two full days, as seen in Tables 1 and 2. The dryer installed capacity Co (kg/batch), can therefore be mini- mised for the small farmer, and the dryer used throughout the [EQUATION 1 crop duration, if Co = 2N D [EQUATION 3] where ocess N = quantity of crop to be dried per year (kg) D = duration of crop harvest (days). Under these conditions and assuming negligible sensible heating, the transparent cover area S (m2) required for the cabinet dryer can be evaluated, S = Co x (M,- M) M x t x (1- My) [EQUATION 4] = (2N) (M, -My) x (DMt) (1 My) [EQUATION 5] where M, = initial moisture content of the crop, decimal wet basis My = final moisture content of the crop, decimal wet basis t = drying time of 2 days, (24 h). The initial cost of the dryer X ($) can be given through a linear relationship and is, X = KS [EQUATION 6] where K = cost of dryer per m2 of cover area ($/m2). DISCUSSION Sorrel, with a yield of 12,000 kg/ha and a harvesting period of 12 weeks, may be used as an example of a crop with potential for solar drying by small farmers. The crop could be dried from an in- itial moisture content of 90%, to a final moisture content of 15 % in 2 days with a cabinet dryer. It can be assumed that 50% of the annual crop will be sold on the fresh market, with the remainder 265 g/ass metal base 92 screened opening 100 I 8o sweet potato \. -----* pepper . ..........o sorrel 60 60 ."*. ---. mango 40 - 40 ^S' ... 0 4 8 12 16 20 24 Drying time- hours FIGURE 1. The solar cabinet dryer. I