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Simultaneous application of microwave energy and hot air to whole drying process of apple slices: drying kinetics, modeling, temperature profile and energy aspect

机译:微波能量和热风同时应用于苹果切片的整个干燥过程:干燥动力学,建模,温度曲线和能量方面

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摘要

Drying kinetics, modeling, temperature profile and energy indices were investigated in apple slices during drying by a specially designed microwave-hot air domestic hybrid oven at the following conditions: 120, 150 and 180 W microwave powers coupled with 50, 60 and 70 ℃ air temperatures. Both sources of energy were applied simultaneously during the whole drying processes. The drying process continued until the moisture content of apple slices reached to 20% from 86.3% (wet basis, w.b). Drying times ranged from 330 to 800 min and decreased with increasing microwave power and air temperatures. The constant rate period was only observed at low microwave powers and air temperatures. Two falling rate periods were observed. Temperature of apple slices sharply increased within the first 60 min, then reached equilibrium with drying medium and finally increased at the end of the drying process. In order to describe drying behavior of apple slices nine empirical models were applied. The Modified Logistic Model fitted the best our experimental data (R~2 = 0.9955-0.9998; Χ~2 = 3.46 ×10~(-5)-7.85 × 10~(-4) and RMSE = 0.0052-0.0221). The effective moisture and thermal diffusivities were calculated by Fick's second law and ranged from 1.42 × 10~(-9) to 3.31 × 10~(-9) m~2/s and 7.70 × 10~(-9) to 12.54 × 10~(-9) m~2/s, respectively. The activation energy (Ea) values were calculated from effective moisture diffusivity (Deff), thermal diffusivity (a) and the rate constant of the best model (k). The Ea values found from these three terms were similar and varied from 13.04 to 33.52 kJ/mol. Energy consumption and specific energy requirement of the hybrid drying of apple slices decreased and energy efficiency of the drying system increased with increasing microwave power and air temperature. Apples can be dried rapidly and effectively by use of the hybrid technique.
机译:通过特殊设计的微波-热空气家用混合烤箱在以下条件下,研究了苹果片干燥过程中的干燥动力学,模型,温度分布和能量指数:120、150和180 W微波功率以及50、60和70℃的空气温度。在整个干燥过程中,两种能源都同时使用。干燥过程一直持续到苹果切片的水分含量从86.3%(湿基,w.b)达到20%。干燥时间从330到800分钟不等,并且随着微波功率和空气温度的升高而缩短。仅在低微波功率和空气温度下才能观察到恒定速率周期。观察到两个下降速率周期。在开始的60分钟内,苹果片的温度急剧上升,然后与干燥介质达到平衡,最后在干燥过程结束时升高。为了描述苹果片的干燥行为,应用了九个经验模型。修改后的逻辑模型最适合我们的实验数据(R〜2 = 0.9955-0.9998;Χ〜2 = 3.46×10〜(-5)-7.85×10〜(-4)和RMSE = 0.0052-0.0221)。有效水分和热扩散率是根据菲克第二定律计算的,范围为1.42×10〜(-9)至3.31×10〜(-9)m〜2 / s和7.70×10〜(-9)至12.54×10 〜(-9)m〜2 / s。活化能(Ea)值是根据有效水分扩散率(Deff),热扩散率(a)和最佳模型的速率常数(k)计算得出的。从这三个术语中发现的Ea值相似,从13.04到33.52 kJ / mol。随着微波功率和空气温度的升高,苹果片混合干燥的能耗和比能量需求降低,干燥系统的能量效率提高。使用混合技术可以快速有效地干燥苹果。

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  • 来源
    《Heat and mass transfer》 |2018年第2期|425-436|共12页
  • 作者单位

    Food Engineering Department, Engineering Faculty, Gaziantep University, 27310 Gaziantep, Turkey;

    Food Engineering Department, Engineering Faculty, Gaziantep University, 27310 Gaziantep, Turkey;

    Arcelik A.S, Research and Development Department, Tuzla, Istanbul, Turkey;

    Food Engineering Department, Engineering Faculty, Gaziantep University, 27310 Gaziantep, Turkey;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);
  • 原文格式 PDF
  • 正文语种 eng
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