Javascript must be enabled to continue!
Microwave Assisted Convective Air Drying of Sugarloaf Pineapples (Ananas Comosus)
View through CrossRef
HighlightsMicrowave pretreatment before drying reduced drying time significantly.Microwave-assisted drying increased the effective moisture diffusivity coefficient.Microwave pretreatment before convective hot-air drying improved quality parameters.The Middili et al. (2002) model best fitted the microwave-assisted drying of sugarloaf pineapples.Abstract. This study’s objective was to provide the optimum drying conditions to produce quality dried sugarloaf pineapples using microwave pretreatments before the conventional hot air drying. For this, the effect of microwave power (385 to 697 W), microwave time (2 to 4 min), and air temperature (50°C to 70°C) on the drying kinetics and quality of sugarloaf pineapple were evaluated using the Box Behnken response surface methodology. To reach a 17.44±0.09% kg/kg dry matter moisture content, we found the optimum drying conditions for sugarloaf pineapples to be 697 W microwave power for 2.26 min before convective hot air drying at a temperature of 64.75°C. The predicted drying time, ascorbic acid content, and browning index were 13.68 h, 20.89 mg/100 g, and 0.099 Abs unit at this optimum condition, respectively. The pineapple slices’ effective moisture removal rate pretreated with microwave before drying was higher than the control and was between 6.42 × 10-10 m2/s and 11.82 × 10-10 m2/s while ones without a microwave were between 3.54 × 10-10 m2/s and 8.78 × 10-10 m2/s for drying at air temperature between 50°C and 70°C. It was discovered that the Midilli et al. (2002) model was the most appropriate thin layer model for microwave-assisted drying of sugarloaf pineapples. The pineapple slices’ drying rate potential generally increased with microwave power and pretreatments time but not the corresponding increase in the air temperature. Drying time for microwave-assisted drying was in the range of 11 to 20 h, while the ones without microwaves were between 18 and 24 h. Therefore, microwaves should be considered a pretreatment step to the industrial production of sugarloaf pineapple to reduce drying time and produce better quality products. Keywords: Drying, Hot air, Microwave, Moisture diffusivity, Sugarloaf pineapple.
American Society of Agricultural and Biological Engineers (ASABE)
Title: Microwave Assisted Convective Air Drying of Sugarloaf Pineapples (Ananas Comosus)
Description:
HighlightsMicrowave pretreatment before drying reduced drying time significantly.
Microwave-assisted drying increased the effective moisture diffusivity coefficient.
Microwave pretreatment before convective hot-air drying improved quality parameters.
The Middili et al.
(2002) model best fitted the microwave-assisted drying of sugarloaf pineapples.
Abstract.
This study’s objective was to provide the optimum drying conditions to produce quality dried sugarloaf pineapples using microwave pretreatments before the conventional hot air drying.
For this, the effect of microwave power (385 to 697 W), microwave time (2 to 4 min), and air temperature (50°C to 70°C) on the drying kinetics and quality of sugarloaf pineapple were evaluated using the Box Behnken response surface methodology.
To reach a 17.
44±0.
09% kg/kg dry matter moisture content, we found the optimum drying conditions for sugarloaf pineapples to be 697 W microwave power for 2.
26 min before convective hot air drying at a temperature of 64.
75°C.
The predicted drying time, ascorbic acid content, and browning index were 13.
68 h, 20.
89 mg/100 g, and 0.
099 Abs unit at this optimum condition, respectively.
The pineapple slices’ effective moisture removal rate pretreated with microwave before drying was higher than the control and was between 6.
42 × 10-10 m2/s and 11.
82 × 10-10 m2/s while ones without a microwave were between 3.
54 × 10-10 m2/s and 8.
78 × 10-10 m2/s for drying at air temperature between 50°C and 70°C.
It was discovered that the Midilli et al.
(2002) model was the most appropriate thin layer model for microwave-assisted drying of sugarloaf pineapples.
The pineapple slices’ drying rate potential generally increased with microwave power and pretreatments time but not the corresponding increase in the air temperature.
Drying time for microwave-assisted drying was in the range of 11 to 20 h, while the ones without microwaves were between 18 and 24 h.
Therefore, microwaves should be considered a pretreatment step to the industrial production of sugarloaf pineapple to reduce drying time and produce better quality products.
Keywords: Drying, Hot air, Microwave, Moisture diffusivity, Sugarloaf pineapple.
Related Results
Combining desiccant dehumidification with Hot Air and Microwave food drying: a sustainable and economical method to produce dried snacks
Combining desiccant dehumidification with Hot Air and Microwave food drying: a sustainable and economical method to produce dried snacks
Abstract
Solar hot air drying is a food dehydration method that is quickly gaining traction in South Asia due to its very low capital and operational cost. The long drying ...
Effect of microwave and conventional drying process on the drying kinetics and physico-chemical quality of brown shrimp (Metapenaeus dobsonii)
Effect of microwave and conventional drying process on the drying kinetics and physico-chemical quality of brown shrimp (Metapenaeus dobsonii)
The aim of this study was to compare the drying kinetics, proximate composition, instrumental texture and colour profiling of dried shrimp (Metapenaeus dobsonii) under open sun dry...
Recent developments in tomato drying techniques: A comprehensive review
Recent developments in tomato drying techniques: A comprehensive review
AbstractTomatoes, a highly perishable agricultural product, are commonly dried to extend their shelf life. They serve as raw materials in various domains, including direct consumpt...
Fluidised and Convective Drying Kinetics of Onion Slices
Fluidised and Convective Drying Kinetics of Onion Slices
Onion (Alium cepa L.) is an important tuber crop widely used for culinary purposes and pharmaceutical industries. Dried onion powder has gained commercial importance in food indust...
THE INFLUENCE OF MICROWAVE DRYING ON PHYSICOCHEMICAL PROPERTIES OF LIUSHUHE OIL SHALE; pp. 29–41
THE INFLUENCE OF MICROWAVE DRYING ON PHYSICOCHEMICAL PROPERTIES OF LIUSHUHE OIL SHALE; pp. 29–41
In this paper, microwave drying of Liushuhe oil shale was studied and compared with conventional drying process. Oil shale was treated in a microwave oven at four different microwa...
Association between low drying temperature and ozonation process to control pest and preserve the maize quality
Association between low drying temperature and ozonation process to control pest and preserve the maize quality
Maize is one of the cereals major produced for its nutritional and energy characteristics and that has become one of the most cultivated crop in the world. To maintain high quality...
Optimizing solar drying efficiency: Effects of PCM, and IR on energy and exergy performance
Optimizing solar drying efficiency: Effects of PCM, and IR on energy and exergy performance
This study investigates the drying behavior of potatoes using a hybrid solar dryer equipped with a Compound Parabolic Concentrator (CPC) collector, Phase Change Materials (PCM), an...
KARAKTERISTIK PENGERINGAN BIJI PINANG MENGGUNAKAN EXPERIMENTAL DRYER
KARAKTERISTIK PENGERINGAN BIJI PINANG MENGGUNAKAN EXPERIMENTAL DRYER
Abstract
Areca nut seeds at harvest generally have a high water content, so to reduce the water content of betel nuts, namely drying or drying the betel nuts, they must be dr...

