Mathematical modeling and simulation of an industrial rotary dryer: A case study of ammonium nitrate plant

被引:31
作者
Abbasfard, Hamed [1 ]
Rafsanjani, Hasan Hashemipour [1 ]
Ghader, Sattar [1 ,2 ]
Ghanbari, Mehdi [3 ]
机构
[1] Shahid Bahonar Univ Kerman, Sch Engn, Dept Chem Engn, Kerman 7618891167, Iran
[2] Shahid Bahonar Univ Kerman, Mineral Ind Res Ctr, Kerman 7618891167, Iran
[3] Shiraz Univ, Sch Chem & Petr Engn, Dept Chem Engn, Shiraz 71345, Iran
关键词
Ammonium nitrate plant; Rotary dryer; Mathematical modeling; Equilibrium moisture; Drying kinetics; RESIDENCE TIME; SOLIDS TRANSPORT;
D O I
10.1016/j.powtec.2013.02.037
中图分类号
TQ [化学工业];
学科分类号
081705 [工业催化];
摘要
Drying of solids is of great significance in fertilizer industry as the quality of final product should meet the commercial required standards. A rotary dryer which has been investigated in the present study is used in ammonium nitrate (AN) plant located at Shiraz Petrochemical Complex (SPC). This plant is designed to produce 650 metric tons of final products in a day. In this work, mathematical modeling of the concurrent rotary dryer for AN including heat and mass transfer equations between solid and air was developed. New correlations were proposed for AN equilibrium moisture and drying rate which were used in the modeling. The model was checked against the industrial data which showed a good agreement. The model predicts air and product moisture and temperature depending on working conditions of the rotary dryer. Regardless of the slope and speed of the dryer, inlet AN moisture and air temperature have been shown to be the variables that have the greatest effect, on the outlet moisture content of the product. (C) 2013 Elsevier B.V. All rights reserved.
引用
收藏
页码:499 / 505
页数:7
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