Abstract

As well as most agricultural products, some medicinal plants need to go through a drying process to ensure quality maintenance, however each product behaves differently. Therefore, the present study aimed to evaluate the drying kinetics of spiked pepper (Piper aduncum L.) leaves and determine their thermodynamic properties at different drying temperatures in laboratory scale. Leaves with initial moisture content of 78% w.b. (wet basis) were subjected to drying at temperatures of 40, 50, 60 and 70 ºC and air speed of 0.85 m s-1 in an experimental fixed bed dryer. The drying kinetics of the leaves was described by statistical fitting of mathematical models and determination of effective diffusion coefficient and activation energy. Enthalpy, entropy and Gibbs free energy were also evaluated for all drying conditions. It was concluded that, among the models evaluated, only Midilli and Valcam can be used to represent the drying of Piper aduncum leaves; the first for the two highest temperatures (60 and 70 ºC) and the second for 40 and 50 ºC. The activation energy was approximately 55.64 kJ mol-1, and the effective diffusion coefficient increase with the elevation of temperature. The same occurs with the values of Gibbs free energy, whereas the specific enthalpy and entropy decrease.

Highlights

  • The species Piper aduncum L., popularly known as spiked pepper, has organic compounds with antifungal action which act on the elimination of skin and hair diseases (Monzote, Scull, Cos, & Setzer, 2017)

  • The present study aimed to describe the drying kinetics of Piper aduncum leaves, selecting the mathematical model that best represents the phenomenon, and determine the diffusion coefficient and thermodynamic properties of the product

  • Piper aduncum L. leaves were collected at the Federal University of Grande Dourados (UFGD), in the garden of the Faculty of Agrarian Sciences (FCA)

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Summary

Introduction

The species Piper aduncum L., popularly known as spiked pepper, has organic compounds with antifungal action which act on the elimination of skin and hair diseases (Monzote, Scull, Cos, & Setzer, 2017). There are several advantages in using drying, such as product preservation, stability of aromatic components at room temperature for long periods of time, protection against enzymatic degradation and oxidation, mass reduction, energy saving for not requiring refrigeration, and it contributes with more adequate conditions of storage, making the product available during any period of the year Since it is a complex process, which involves heat and mass transfers (Yilbas, Hussain, & Dincer, 2003; Delgado & Lima, 2016; Haghi & Amanifard, 2008), several studies have been conducted in the attempt to describe drying, especially at laboratory scale, by fitting mathematical models, using statistical parameters. Modeling allows describing the drying kinetics (Al-Ali & Parthasarathy, 2019) and predicting the behavior of the product during the process, as well as optimizing the operation parameters in the dryer project (Nadi, 2016)

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