2010
DOI: 10.1111/j.1745-4549.2009.00377.x
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Determination of Suitable Thin Layer Model for Air Drying of Coroba Slices (Attalea Maripa) at Different Air Temperatures and Velocities

Abstract: An air dryer was used for thin layer drying process of coroba, and moisture ratio at any drying time was compared by eight models (Newton, Page, Henderson and Pabis, logarithmic, two‐term, two‐term exponential, Verma et al., and Midilli and Kucuk). The effect of drying air temperature (71, 82 and 93C) and velocity (0.82, 1.00 and 1.18 m/s) on the coefficients of the best suited moisture ratio model was determined by multiple regression method. Coefficient of determination (R2) and reduced chi‐square (χ2) were … Show more

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Cited by 8 publications
(9 citation statements)
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“…In a similar work by [13], maize cobs dried in a biomass natural convection dryer had its moisture content reduced to 14% between 5 and 6 hours of drying. Similar results were also obtained for the drying of beans as reported by [19], and coroba slices by [20]. The final moisture content of the dried maize grains was close to…”
Section: Effect Of Drying Temperature On Moisture Loss Kernel Damagesupporting
confidence: 88%
“…In a similar work by [13], maize cobs dried in a biomass natural convection dryer had its moisture content reduced to 14% between 5 and 6 hours of drying. Similar results were also obtained for the drying of beans as reported by [19], and coroba slices by [20]. The final moisture content of the dried maize grains was close to…”
Section: Effect Of Drying Temperature On Moisture Loss Kernel Damagesupporting
confidence: 88%
“…As the drying temperature increased in the above range, the drying time and dynamic equilibrium moisture content (EMC) decreased from 480 to 270 min and from 7.70 to 1.70% (db), respectively (Table 2). Similar results were obtained for the drying of eggplant (Ertekin and Yaldiz, 2004), potato (Aghbashlo et al, 2009a), and coroba slices (Corzo et al, 2010).…”
Section: Drying Time and Equilibrium Moisture Of Cassava Starch In Trsupporting
confidence: 78%
“…Many empirical and semi-theoretical models have been proposed and applied by investigators to the estimation of the moisture ratios and drying times of several agricultural and food products. These include eggplant (Ertekin and Yaldiz, 2004), apple , Menges and Ertekin, 2006, Kaya et al, 2007and Meisami-asl et al, 2010, apricot (Togrul andPehlivan, 2002, Bozkir, 2006), potato (Aghbashlo et al, 2009a), carrot (Domaz, 2004, Aghbashlo et al, 2009b, coroba (Corzo et al, 2010), grape (Yaldiz et al, 2001, Zomorodian andDadashzadeh, 2009), kiwifruit (Mohammadi et al, 2008), leek (Dadali and Ozbek, 2008), red chili pepper (Alibas, 2012), pepper, pumpkin, green bean and onion , pumpkin (Doymaz, 2007, Perez andSchmalko, 2009), spinach leaves (Doymaz, 2009), wheat (Mohapatra and Rao, 2005), cocoa (Hii et al, 2008), pretreated sour cherry (Gazor and Roustapour, 2015), and potato starch (Dixit et al, 2012). Aviara (2010) and Aviara et al (2010aAviara et al ( , 2010b reported that drying techniques and conditions significantly affect the physicochemical and functional properties of starch, and suggested that the drying techniques and conditions should be carefully chosen or modeled to avoid the adverse modification of the product characteristics that can occur when wet starch is subjected to heating.…”
Section: Figure 1 Laboratory-model Tray Dryer (1) Drying Chamber (2mentioning
confidence: 99%
“…In this method, heated air comes into contact with the wet samples to promote heat and mass transfer. Different types of dryers can be used in this methodology, for example, fixed bed, cabinet, kiln, tunnel, belt‐trough, sliding bed, pneumatic and conveyor dryers, among others …”
Section: Introductionmentioning
confidence: 99%