determination of suitable thin layer drying curve model

Impact of different drying methods on the drying kinetics

2019-1-22The moisture ratio data were adapted to the nine thin-layer models that are typically used to model drying curves (Table 1) The moisture ratio (MR) values were calculated using Equations (1) and (2): MR M t M e M o M e (1) where M t corresponds to the moisture content at a given time (g water g dry matter-1) M o corresponds to the initial

‪Ebru Kavak Akpinar‬

Determination of suitable thin layer drying curve model for some vegetables and fruits EK Akpinar Mathematical modelling of thin layer drying process of long green pepper in solar dryer and under open sun EK Akpinar Y Bicer Energy Conversion and Management 49 (6) 1367-1375 2008 146: 2008: Determination of the wind energy potential

Mathematical and Kinetic Modelling for Convective

2019-7-1The kinetic modelling of thin layer drying is performed with various agricultural products such as seeds grains fruits and some plant species with economic importance Sweet Potato ( Ipomoea batatas L ) is a widely consumed and its industrialization is on the increase The thin layer drying kinetics of sweet potato were experimentally investigated in a convective hot air dryer

Drying kinetics of dill leaves in a convective dryer

Thin layer drying characteristics of dill leaves under fixed semi-fluidized and fluidized bed conditions were studied at air temperatures of 30 40 50 and 60C In order to find a suitable drying curve 12 thin layer-drying models were fitted to the experimental data of the moisture ratio Among the applied mathematical models the Midilli et al model was the best for drying behavior

Mathematical Modeling of Kinetics of Thin

In mathematical modeling the thin layer drying equations in table 2 were tested to select the best model for describing the drying curve of the apple slices Table 2 Mathematical models applied to drying curves Model no Model name Model References 1 Newton MR = exp(-kt) (Westerman et al 1973) 2 Page MR = exp(-ktn) (Page 1949)

Effect of air

Within the drying oven the pellets were placed as a thin-layer on a stainless steel bin connected to a scale (Ohaus SP402 NJ USA) of accuracy 0 01 g The data on the variation in the mass of the pellets were recorded and stored in a PC through an interface system ( Ohaus RS232 NJ USA ) using Microsoft HyperTerminal software

Effects of microwave power on the drying characteristics

2017-6-19the drying characteristics drying time color properties phenolic content and specific energy consumption of dried Spirogyra sp undergoing laboratory-scale of the microwave drying In addition to this a proper mathematical model for thin-layer drying which can describe the drying characteristics of Spirogyra sp was investigated

Determination of suitable thin layer drying curve

2006-3-1This study presents a mathematical modeling of thin layer drying of potato apple and pumpkin slices in a convective cyclone dryer In order to estimate and select the appropriate drying curve equation 13 different models which are semi-theoretical and/or empirical were applied to the experimental data and compared according to their coefficients of determination (r χ 2) which were

DETERMINATION OF SUITABLE THIN

2018-7-4DETERMINATION OF SUITABLE THIN-LAYER DRYING MODELS FOR BREWER'S YEAST (Saccharomyces cerevisiae)Rolando Mendieta1 Masoud Haerinejad2 Apolinar Picado1 2 * 1Facultad de Ingeniera Qumica Universidad Nacional de Ingeniera (UNI) Av Universitaria Managua 11127 Nicaragua 2Department of Chemical Enginering and Technology KTH Royal Institute of Technology

Hot Air Drying and Quality of Red and White Varieties

2020-8-1This study was undertaken to investigate the drying characteristics of red and white varieties of onion (Allium cepa) in a convective dryer The drying characteristics of onion slices were examined at air temperatures of 50℃ 60℃ and 70℃ and sample thicknesses of 2 mm During the drying experiments air velocity was held stable at 0 9 m/s

REVIEW OF MATHEMATICAL MODELLING OF THIN LAYER

2015-11-16fitted to 13 thin layer drying models Midilli [4] model gave the lowest RMSE and the highest regression coefficient values Hence the Midilli model was chosen to represent the thin layer drying of soybeans Akpinar [5] investigated suitable thin layer drying curve model for some vegetables and fruits This study presents a mathematical

The Mathematical Modelling of the Effects of Thin Layer

2018-7-28the drying curve 5 different thin layer semi-theor A research was done on the effects of mathematical modelling of the thin layer drying of groundnuts (Kerstigiella geocarpa harms) at 67% Moisture Content (% dry basis ) and varying air temperatures of 45

Mathematical modelling of thin

This paper presents a new mathematical model for thin-layer drying process which was verified with experimental data A laboratory scale static-tray dryer was used to obtain the experimental data Carrot cubes were used for drying experiments Experiments were performed at air temperatures of

Influence of Different Drying and Aging Conditions on

2019-5-26Determination of a suitable thin layer drying curve model for saffron (Crocus sativus L) stigmas in an infrared dryer Scientia Iranica 2011 18 (6) 1397-1401 DOI: 10 1016/j scient 2011 08 014 Luana Maggi Manuel Carmona Simon D

THIN LAYER SOLAR DRYING OF SOME VEGETABLES

Drying time changed between 30 29 and 90 43 hours for different vegetables by the solar drying This drying time was between 48 59 and 121 81 hours for the natural sun drying Drying curves could be explained by determined thin layer drying models satisfactorily with very high determination coeffcients

Evaluation and Selection of Thin

2018-12-11In order to select a suitable form of the drying curve 12 different thin layer drying models were fitted to experimental data Fick's second law was used as a major equation to calculate the moisture diffusivity with some simplification The high values of coefficient of determination and the low values of reduced

PAPER OPEN ACCESS Mathematical modelling of paddy

crops and one of them is thin-layer modelling However there are still limited information about mathematical modelling in paddy drying In this paper thin layer modelling of paddy drying curve on drying using fluidized bed dryer is presented The drying paddy was done with drying temperature variations of 50 60 70 80 and 90 o C

Determination of a suitable thin layer drying curve

2011-12-1The main objective of this study is to determine and test the most appropriate thin layer drying model from between four thin-layer drying models namely Lewis Handerson and Pabis Page and Midilli and Kucuk for understanding the drying behavior of saffron stigmas in an infrared dryer 2 Materials and methods 2 1

Mathematical model on thin layer drying of of olive fruit

2014-1-23Journal of Agricultural Technology 2013 Vol 9(5): 1097-1110 1097 Mathematical model on thin layer drying of of olive fruit (Olea europeae L ) Belgacem Mahdhaoui1 Ridha Fethi Mechlouch1 Ammar Mahjoubi1 Karim Zahafi2 and Ammar Ben Brahim1 1Applied Thermodynamic Research Unit (UR11ES80) National School of Engineering of Gabes Gabes University Avenue of Omar Ibn

Modeling of thin

Natural drying characteristics of sesame seeds (SS) were investigated under indoor conditions with both forced convection (FC) and natural convection (NC) of air The drying kinetics of SS was characterized in terms of effective diffusion coefficient and resistance to diffusion For the FC

Mathematical modeling of convective air drying of

Experimental determination of drying curves The drying experiments were carried out using a convective dryer designed and built in the Department of Food Engineering of Universidad de La Serena Akpinar E K (2006) Determination of suitable thin layer drying curve model for some vegetables and fruits J

Model Pengeringan Lapisan Tipis Rebung Bambu "Tabah

Therefore the aim of this research was to study the characteristics of bamboo shoots Tabah drying by applying thin layer drying models Bamboo shoots split into two and four pieces were dried under drying air temperatures 50 o C 60 o C and 70 o C Instantaneous moisture content of the shoots are modeled by Newton and Page model

Drying characteristics of walnut (Juglans regia L ) during

2009-5-18variety on drying kinetics of walnut b) to select a suitable thin-layer drying model and c) to calculate drying constants Int Agrophysics 2009 23 129-135 Drying characteristics of walnut (Juglans regia L ) during convection drying** S R Hassan-Beygi M Aghbashlo* M H Kianmehr and J Massah

Modelling the Drying of Normal and Blanched Unripe

2018-1-6Modelling of olive cake thin-layer drying process J Food Eng 68: 455-461 CrossRef | Direct Link | Akpinar E K 2006 Determination of suitable thin layer drying curve model for some vegetables and fruits J Food Eng 73: 75-84 Y S 2006 Second-order kinetic model for the sorption of cadmium onto tree fern: A comparison of linear

Modeling the Thin‐Layer Drying of Fruits and

Incorrect collection of experimental data from the thin‐layer drying experiments will affect the drying process and subsequently the selection of appropriate thin‐layer models Thus the selection of the most suitable thin‐layer drying model is also a very important tool in describing the drying