Numerical study and evaluation of solid-liquid extraction of Montan wax in stirred tanks on different scales

被引:9
作者
Wang, Yan [1 ,2 ,3 ]
Herdegen, Volker [3 ]
Li, Xiang [4 ]
Repke, Jens-Uwe [3 ,5 ]
机构
[1] Cent S Univ, State Key Lab High Performance Complex Mfg, Changsha 410083, Hunan, Peoples R China
[2] Cent S Univ, Sch Mech & Elect Engn, Changsha 410083, Hunan, Peoples R China
[3] TU Bergakad Freiberg, Inst Thermal Environm & Nat Prod Proc Engn, Leipziger Str 28, D-09596 Freiberg, Germany
[4] Cent S Univ, Sch Resources & Safety Engn, Changsha 410083, Hunan, Peoples R China
[5] TU Berlin, Proc Dynam & Operat Grp, D-10623 Berlin, Germany
关键词
Brown coal extraction; Montan wax; Solid-liquid extraction; Stirred tank; Mathematical model; MASS-TRANSFER; KINETICS; MODEL;
D O I
10.1016/j.seppur.2018.04.044
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In this paper, mathematical models for the solid-liquid extraction of Montan wax from brown coal are formulated, considering the external mass transfer in liquid phase and the diffusion inside the brown coal particles (effective diffusion) in terms of mass conservation. For parameter identification and evaluation purposes, the Montan wax extraction from brown coal is conducted with small-scale and scaled-up immersion apparatuses. The effective diffusion coefficient D-e for the solute transport of Montan wax from brown coal in toluene is obtained with the proposed correlation D-e = D-AB.epsilon(n epsilon)(P) (n(epsilon) = 2.9) where epsilon(p), denotes the particle porosity. The effects of the important conditions such as temperature, solvent-solid ratio, the stirring speed and the particle size in terms of extraction rate are investigated by simulation. A sensitivity analysis is performed for the extraction yield with respect of mass transfer coefficient k(f) and effective diffusion coefficient D-e.
引用
收藏
页码:90 / 97
页数:8
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