TY - GEN
T1 - Microwave-convective drying characteristics of okra
AU - Kumar, Deepak
AU - Prasad, Suresh
PY - 2010
Y1 - 2010
N2 - Okra (Abelmoschus esculentus), also known as ladyfinger, is an important vegetable of subtropical Asia. Because of its high moisture content, okra is susceptible to rapid deterioration. The present study was conducted to investigate the potential of microwaves (MW) combined with hot air for drying of okra. Okra was dried from initial moisture content of about 89% (wet basis) to a safe level of about 0.1 g water/ g dry matter under different combinations of air velocity (1, 2 m/s), hot air temperature (40, 50, 60 and 70°C) and microwave power levels (0.5, 1, 1.5, 2 and 2.5 W/g). Drying time in microwave-convective drying decreased by many folds as compare to that of hot-air drying. Drying time was found decreasing with increase in either air temperature or microwave power level. However, effect of air temperature was more significant at lower microwave power levels. High air velocities prolonged the drying process due to its cooling effect on surface of the product. Most of the drying took place in falling rate period. The values of average effective moisture diffusivity ranged from 17.594×10-10 to 89.837 × 10-10 m2/s for microwave-convective drying. Empirical Page model gave the excellent fit for the drying data under all drying conditions with R2 (correlation coefficient) values in the range of 0.988-0.999.
AB - Okra (Abelmoschus esculentus), also known as ladyfinger, is an important vegetable of subtropical Asia. Because of its high moisture content, okra is susceptible to rapid deterioration. The present study was conducted to investigate the potential of microwaves (MW) combined with hot air for drying of okra. Okra was dried from initial moisture content of about 89% (wet basis) to a safe level of about 0.1 g water/ g dry matter under different combinations of air velocity (1, 2 m/s), hot air temperature (40, 50, 60 and 70°C) and microwave power levels (0.5, 1, 1.5, 2 and 2.5 W/g). Drying time in microwave-convective drying decreased by many folds as compare to that of hot-air drying. Drying time was found decreasing with increase in either air temperature or microwave power level. However, effect of air temperature was more significant at lower microwave power levels. High air velocities prolonged the drying process due to its cooling effect on surface of the product. Most of the drying took place in falling rate period. The values of average effective moisture diffusivity ranged from 17.594×10-10 to 89.837 × 10-10 m2/s for microwave-convective drying. Empirical Page model gave the excellent fit for the drying data under all drying conditions with R2 (correlation coefficient) values in the range of 0.988-0.999.
KW - Drying rate
KW - Effective moisture diffusivity
KW - Microwave convective drying
KW - Okra
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M3 - Conference contribution
AN - SCOPUS:78649703467
SN - 9781617388354
T3 - American Society of Agricultural and Biological Engineers Annual International Meeting 2010, ASABE 2010
SP - 1715
EP - 1725
BT - American Society of Agricultural and Biological Engineers Annual International Meeting 2010, ASABE 2010
PB - American Society of Agricultural and Biological Engineers
ER -