Effect of Drying Air Velocity on Drying Kinetics of Tomato Slices in a Forced-Convective Solar Tunnel Dryer

Mamouda Moussa Na Abou, S. Madougou, Makinta Boukar
{"title":"Effect of Drying Air Velocity on Drying Kinetics of Tomato Slices in a Forced-Convective Solar Tunnel Dryer","authors":"Mamouda Moussa Na Abou, S. Madougou, Makinta Boukar","doi":"10.4236/JSBS.2019.92005","DOIUrl":null,"url":null,"abstract":"The objective of this work is to analyse the extent to which a change in the drying air velocity may affect the drying kinetics of tomato in a forced-convective solar tunnel dryer. 2 m⋅s−1 (V1) and 3 m⋅s−1 (V2) air speeds were applied in similar drying air temperature and humidity conditions. Main drying constants calculated included the drying rate, the drying time and the effective water diffusivity based on the derivative form of the Fick’s second law of diffusion. Henderson and Pabis Model and Page Model were used to describe the drying kinetics of tomato. We found that solar drying of tomato occurred in both constant and falling-rate phases. The Page Model appeared to give a better description of tomato drying in a forced-convective solar tunnel dryer. At t = 800 min, the drying rate was approximately 0.0023 kg of water/kg dry matter when drying air velocity was at 2 m/s. At the same moment, the drying rate was higher than 0.0032 kg of water/kg dry matter when the drying air velocity was 3 m/s. As per the effective water diffusivity, its values changed from 2.918E−09 m2⋅s−1 to 3.921E−09 m2⋅s−1 when drying air velocity was at 2 and 3 m⋅s−1 respectively, which is equivalent to a 25% increase. The experimentations were conducted in Niamey, on the 1st and 5th of January 2019 for V2 and V1 respectively. For both two experiments, the starting time was 9:30 local time.","PeriodicalId":71705,"journal":{"name":"可持续生物质能源系统(英文)","volume":" ","pages":""},"PeriodicalIF":0.0000,"publicationDate":"2019-04-15","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"6","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"可持续生物质能源系统(英文)","FirstCategoryId":"1087","ListUrlMain":"https://doi.org/10.4236/JSBS.2019.92005","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 6

Abstract

The objective of this work is to analyse the extent to which a change in the drying air velocity may affect the drying kinetics of tomato in a forced-convective solar tunnel dryer. 2 m⋅s−1 (V1) and 3 m⋅s−1 (V2) air speeds were applied in similar drying air temperature and humidity conditions. Main drying constants calculated included the drying rate, the drying time and the effective water diffusivity based on the derivative form of the Fick’s second law of diffusion. Henderson and Pabis Model and Page Model were used to describe the drying kinetics of tomato. We found that solar drying of tomato occurred in both constant and falling-rate phases. The Page Model appeared to give a better description of tomato drying in a forced-convective solar tunnel dryer. At t = 800 min, the drying rate was approximately 0.0023 kg of water/kg dry matter when drying air velocity was at 2 m/s. At the same moment, the drying rate was higher than 0.0032 kg of water/kg dry matter when the drying air velocity was 3 m/s. As per the effective water diffusivity, its values changed from 2.918E−09 m2⋅s−1 to 3.921E−09 m2⋅s−1 when drying air velocity was at 2 and 3 m⋅s−1 respectively, which is equivalent to a 25% increase. The experimentations were conducted in Niamey, on the 1st and 5th of January 2019 for V2 and V1 respectively. For both two experiments, the starting time was 9:30 local time.
干燥空气速度对强制对流式太阳能隧道干燥机中番茄切片干燥动力学的影响
这项工作的目的是分析在强制对流太阳能隧道干燥器中,干燥空气速度的变化可能在多大程度上影响番茄的干燥动力学。在类似的干燥空气温度和湿度条件下,采用2 m·s−1(V1)和3 m·s–1(V2)的空气速度。根据Fick第二扩散定律的导数形式计算出的主要干燥常数包括干燥速率、干燥时间和有效水扩散率。采用Henderson和Pabis模型以及Page模型对番茄的干燥动力学进行了描述。我们发现,番茄的太阳能干燥分为恒速和降速两个阶段。佩奇模型似乎更好地描述了番茄在强制对流太阳能隧道干燥机中的干燥。在t=800分钟时,当干燥空气速度为2m/s时,干燥速率约为0.0023kg水/kg干物质。同时,当干燥空气速度为3m/s时,干燥速率高于0.0032kg水/kg干物质。根据有效水扩散率,当干燥空气速度分别为2和3 m·s−1时,其值从2.918E−09 m2·s−-1变为3.921E−09 m2·s−1.相当于增加了25%。实验分别于2019年1月1日和5日在尼亚美对V2和V1进行。两个实验的开始时间均为当地时间9:30。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
求助全文
约1分钟内获得全文 求助全文
来源期刊
自引率
0.00%
发文量
117
×
引用
GB/T 7714-2015
复制
MLA
复制
APA
复制
导出至
BibTeX EndNote RefMan NoteFirst NoteExpress
×
提示
您的信息不完整,为了账户安全,请先补充。
现在去补充
×
提示
您因"违规操作"
具体请查看互助需知
我知道了
×
提示
确定
请完成安全验证×
copy
已复制链接
快去分享给好友吧!
我知道了
右上角分享
点击右上角分享
0
联系我们:info@booksci.cn Book学术提供免费学术资源搜索服务,方便国内外学者检索中英文文献。致力于提供最便捷和优质的服务体验。 Copyright © 2023 布克学术 All rights reserved.
京ICP备2023020795号-1
ghs 京公网安备 11010802042870号
Book学术文献互助
Book学术文献互助群
群 号:604180095
Book学术官方微信
小红书