Microwave assisted air drying of osmotically treated pineapple with variable power programmes

Abstract Variable power programmes for microwave assisted air drying of pineapple were studied. The pineapple pieces were pre-treated by osmotic dehydration in a 55° Brix sucrose solution at 40 °C for 90 min. Variable power output programmes were designed and ran with different inlet air temperatures between 30 and 70 °C. Results indicated that the use of variable microwave power combined with low air temperatures can result in a fast drying process without significant charring of pineapple pieces. High microwave powers need to be reduced quickly, faster than the decrease in water content would suggest, to minimize charring. In this study an inlet air temperatures of 70 °C was found to be excessive when combined with microwave energy (5 W/g – after compensating for the moisture loss), resulting in fast temperature increase. Microwave power was found to be most effective in the first hour to 1.5 h of processing. It should then be reduced to 0.1 W/g (initial product weight) in the final stages of drying to avoid charring of the fruit pieces. The best microwave programme tested lead to 20% water content with just 1% losses due to charring, but the results allow to conclude that charring could be completely reduced by switching off microwave energy altogether after 1.5 h and then finish off drying with higher air temperatures. The use of low air temperatures (30–50 °C) is advantageous with microwave energy in the first stages of drying as it limits the peaks of specific energy absorption, but it slows down drying towards the end probably because of a too low point of equilibrium (saturation humidity of air). Microwave energy did not significantly influence the drying process towards the end, although drying rates showed a “memory effect”, that is, drying rates in processes with the same conditions after a given time depended on the conditions up to that point.

[1]  Medeni Maskan,et al.  Kinetics of colour change of kiwifruits during hot air and microwave drying , 2001 .

[2]  Valérie Orsat,et al.  Microwave-Assisted Drying of Biomaterials , 2007 .

[3]  Jun Wang,et al.  Drying characteristics and drying quality of carrot using a two-stage microwave process , 2005 .

[4]  C. Clary,et al.  Improving grape quality using microwave vacuum drying associated with temperature control. , 2007, Journal of food science.

[5]  Shaojin Wang,et al.  Fixed and Incremental Levels of Microwave Power Application on Drying Grapes under Vacuum , 2005 .

[6]  Hao Feng,et al.  Microwave Finish Drying of Diced Apples in a Spouted Bed , 2006 .

[7]  Suresh Prasad,et al.  Drying of garlic (Allium sativum) cloves by microwave-hot air combination , 2001 .

[8]  Arun S. Mujumdar,et al.  Trends in microwave- related drying of fruits and vegetables , 2006 .

[9]  Arun S. Mujumdar,et al.  Microwave Drying of Corn III. Constant Power, Intermittent Operation , 1992 .

[10]  Jorge C. Oliveira,et al.  Osmotic dehydration of pineapple as a pre-treatment for further drying , 2008 .

[11]  R. G. Bosisio,et al.  Microwave Drying of Corn II. Constant Power, Continuous Operation , 1992 .

[12]  Lilia Ahrné,et al.  Microwave Convective Drying of Plant Foods at Constant and Variable Microwave Power , 2007 .

[13]  H. S. Ramaswamy,et al.  Microwave-assisted convective air drying of thin layer carrots , 1995 .

[14]  P. V. Bartels,et al.  Osmotic dehydration as a pre-treatment before combined microwave-hot-air drying of mushrooms , 2001 .

[15]  L. Ahrné,et al.  Quality optimisation of combined osmotic dehydration and microwave assisted air drying of pineapple using constant power emission , 2012 .

[16]  Antonio Marsaioli,et al.  Effect of microwave power, air velocity and temperature on the final drying of osmotically dehydrated bananas , 2007 .

[17]  Lilia Ahrné,et al.  Effects of Combined Osmotic and Microwave Dehydration of Apple on Texture, Microstructure and Rehydration Characteristics , 2001 .

[18]  G.S.V. Raghavan,et al.  Drying of Corn Using Variable Microwave Power with a Surface Wave Applicator , 1991 .