Investigation of the Effect of Duct Geometry on Drying Air Flow in Conventional Grain Dryers by Porous Media Approach

Yıl 2024, Cilt: 36 Sayı: 1, 61 - 71, 28.03.2024

Merdin Danışmaz

https://doi.org/10.35234/fumbd.1338087

Öz

It is a traditional practice to store many agricultural products after drying, ensuring that they are used all year round. Mixed counter flow air drying is one of the most common and traditional methods in the bulk drying process. In this application, the air flow produced by the air channels placed in the dryer bed is forced to flow through the grains in the opposite direction to the grain flow. The moisture contained in the grains is thrown out of the dryer through forced convection. However, it is expected that the air ducts installed in the dryers should not obstruct the flow of grain and provide the best possible drying performance. In this study, computational fluid dynamics (CFD) modeling for a counter-flow grain dryer was performed and the effect of the geometry of the drying channels on the process was investigated. Fluent 2020 R2 commercial software was used for 2-D flow modeling through the dryer. The airflow in the grain zone, modeled as porous media, was included in the calculation for three different geometries of the dryer air ducts (circular, angular, and straight). A constant temperature boundary condition (37°C) was applied for the air ducts in which the drying air circulated without mixing with the grain. As an output of the analysis, the dryer outlet temperature and differential pressure variation along the flow were calculated for 5 different inlet velocities (between 0.005-0.25) to determine the behavior of different air flow rates in the drying process. The increase in the inlet velocity increased the pressure difference and consequently the stability of the flow for all models. The outlet temperature decreased by about 2.5 °C with a 5-fold increase in velocity. The results showed that the sufficient outlet air for moisture removal depends on the structure of the porous medium and the flow geometry. For this analysis, the best flow was found to be for the circular cross-section model and the outlet temperature could be at acceptable levels.

Anahtar Kelimeler

Grain dryer, drying, pressure drop, porous media

Geleneksel Tahıl Kurutuculardaki Kanal Geometrisinin Kurutma Havası Akışına Etkisinin Gözenekli Ortam Yaklaşımıyla İncelenmesi

Öz

Pek çok tarım ürünün kurutulduktan sonra depolanması geleneksel bir uygulamadır ve bu şekilde yıl boyu kullanılması sağlanır. Hasadı yapılan tahılın depolama ömrünün artırılması için nem içeriğinin kabul edilebilir seviyelere (genellikle <%15) indirilmesi gerekir. Yığın kurutma prosesinde karışan karşıt akışlı havayla kurutma, en yaygın ve geleneksel yöntemlerden biridir. Bu uygulamada, kurutucu yatağına yerleştirilen hava kanalları sayesinde üretilen hava akışı, tahılların içerisinden tahıl akışına ters yönde akmaya zorlanır. Tahılların içerdiği nem zorlanmış taşınım yoluyla kurutucudan dışarıya atılır. Ancak, kurutuculara yerleştirilen hava kanallarının hem tahıl akışını engellememesi hem de mümkün olan en iyi kurutma performansını sağlaması beklenir. Bu çalışmada, karşıt akışlı bir tahıl kurutucu için hesaplamalı akışkanlar dinamiği (HAD) modellemesi yapıldı ve kurutma kanalları geometrisinin prosese etkisi incelendi. Kurutucu içerisindeki 2-boyutlu akış modellemesi için Fluent 2020 R2 ticari yazılımı kullanıldı. Gözenekli ortam olarak modellenen tahıl bölgesindeki hava akışı, kurutucu hava kanallarının üç farklı geometrisi (dairesel, açısal ve düz) için hesaplamaya dâhil edildi. Tahıla karışmayan kurutma havasının havanın dolaştığı hava kanalları için sabit sıcaklık sınır koşulu (37 °C) uygulandı. Analiz sonucunda, farklı hava akış hızlarının kurutma prosesindeki davranışını belirlemek için 5 farklı giriş hızının (0,005-0,25 arası) kurutucu çıkış sıcaklığı ve akış boyunca fark basınç değişimi hesaplandı. Giriş hızındaki artış, tüm modeller için basınç farkını ve buna bağlı olarak akışın kararlılığını artırdı. Çıkış sıcaklığı ise hızın 5 kat artmasıyla yaklaşık 2,5 °C düşüşe sebep oldu. Elde edilen sonuçlar, nem atma için yeterli çıkış havasının gözenekli ortamın yapısına ve akış geometrisine bağlı olduğunu gösterdi. Bu analiz için en iyi akışın dairesel kesitli model için olduğu ve çıkış sıcaklığının kabul edilebilir seviyelerde olabileceğini ortaya koydu.

Anahtar Kelimeler

Tahıl kurutucu, kurutma, basınç düşüşü, gözenekli ortam

Kaynakça

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