Comparative evaluation of performance and energy consumption of hot air and superheated steam impinging stream dryers for high-moisture particulate materials

被引:38
作者
Choicharoen, Kwanchai [2 ]
Devahastin, Sakamon [1 ]
Soponronnarit, Somchart [2 ]
机构
[1] King Mongkuts Univ Technol Thonburi, Fac Engn, Dept Food Engn, Bangkok 10140, Thailand
[2] King Mongkuts Univ Technol Thonburi, Sch Energy Environm & Mat, Bangkok 10140, Thailand
关键词
Cyclone; Flash drying; Soy residue; Specific energy consumption; Steam recycle; Unhindered drying rate period; Volumetric water evaporation rate; Volumetric heat transfer coefficient; HEAT-TRANSFER; PADDY;
D O I
10.1016/j.applthermaleng.2011.06.030
中图分类号
O414.1 [热力学];
学科分类号
摘要
Impinging stream dryer (ISD) is a novel alternative to flash dryer for drying high-moisture particulate materials. A number of studies have been conducted on various aspects of an ISD; however, in almost all of the previous studies hot air was used as the drying medium. Since it is well recognized that use of superheated steam as the drying medium could lead to much reduced net energy consumption of the drying process, it was the aim of the present study to investigate the use of superheated steam as the drying medium in an ISD. Okara (soy residue) was used as a test high-moisture particulate material. The performance of the drying system, in terms of the volumetric heat transfer coefficient and volumetric water evaporation rate, as affected by the superheated steam temperature, steam velocity, material feed flow rate and the dryer geometric parameter viz. impinging distance was assessed. In addition, the ability to reuse the exhausted steam as well as the specific energy consumption of the system were evaluated. Comparison was made with the hot air drying results. The maximum volumetric water evaporation rate was found to be around 807 kg(water)/m(3)h, while the maximum volumetric heat transfer coefficient was around 7950 W/m(3)K at the steam recycle ratios of 46-63%. The lowest total specific energy consumption of the system was around 3.1 MJ/kg(water) at an inlet steam temperature of 190 degrees C, inlet steam velocity of 20 m/s, material feed flow rate of 20 kg(dry solid)/h, impinging distance of 5 cm and steam recycle ratio of 63%. Compared with the hot air drying results at the same corresponding conditions, savings of the total specific energy consumption in the range of 9-46% were noted. (C) 2011 Elsevier Ltd. All rights reserved.
引用
收藏
页码:3444 / 3452
页数:9
相关论文
共 17 条
[1]  
[Anonymous], OFF METH AN
[2]  
[Anonymous], DRYING TECHNOLOGY
[3]   Performance and Energy Consumption of an Impinging Stream Dryer for High-Moisture Particulate Materials [J].
Choicharoen, Kwanchai ;
Devahastin, Sakamon ;
Soponronnarit, Somchart .
DRYING TECHNOLOGY, 2010, 28 (01) :20-29
[4]   EVAPORATION OF LIQUIDS INTO THEIR SUPERHEATED VAPORS [J].
CHU, JC ;
LANE, AM ;
CONKLIN, D .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1953, 45 (07) :1586-1591
[5]  
Felder R.M., 2005, Elementary principles of chemical processes
[6]  
Hosseinalipour S.M., 1997, Mathematical Modeling and Numerical Techniques in Drying Technology, P537
[7]   SUPERHEATED STEAM DRYING OF A SINGLE-PARTICLE IN AN IMPINGING STREAM DRYER [J].
HOSSEINALIPOUR, SM ;
MUJUMDAR, AS .
DRYING TECHNOLOGY, 1995, 13 (5-7) :1279-1303
[8]  
Hu XG, 1999, DRY TECHNOL, V17, P1879, DOI 10.1080/07373939908917658
[9]   PERFORMANCE OF A COAXIAL GAS SOLID 2-IMPINGING-STREAMS (TIS) REACTOR - HYDRODYNAMICS, RESIDENCE TIME DISTRIBUTION, AND DRYING HEAT-TRANSFER [J].
KITRON, Y ;
TAMIR, A .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1988, 27 (10) :1760-1767
[10]  
Kudra T., 2009, Advanced Drying Technologies