Article ID | Journal | Published Year | Pages | File Type |
---|---|---|---|---|
6656367 | Fuel Processing Technology | 2018 | 8 Pages |
Abstract
A Chinese raw lignite with total water (RC) and molecular water (MWC) were prepared. Those samples were dewatered by a microwave drying equipment using constant power selected from 450-600â¯W. The first order reaction kinetic equation and ten thin-layer drying models were used to analyze the dewatering processes of MWC and RC respectively. Moreover, the effective diffusion coefficient of water, the activation energy of the water removal and the drying rate constant (k) were calculated. The first order reaction kinetic equation and the Two-term exponential model provided a better fit for the drying processes of MWC and RC respectively. The effective diffusion coefficient of water obtained by Fick's second law varies from 0.3708â¯Ãâ¯10â8 to 1.6715â¯Ãâ¯10â8â¯m2·minâ1 for MWC and from 0.5099â¯Ãâ¯10â8 to 3.3169â¯Ãâ¯10â8â¯m2·minâ1 for RC. The activation energy for the removal of the molecular water is 28.59â¯kJ·molâ1, and that for the total water is 24.25â¯kJ·molâ1. The k of MWC and RC are in the range of 0.0894-0.4364â¯minâ1 and 0.2737-1.4740â¯minâ1 respectively. From the energy consumption aspects, it is suggested the microwave power higher than 550â¯W should be used to remove the free water and capillary water, and 525â¯W used to remove the molecular water.
Related Topics
Physical Sciences and Engineering
Chemical Engineering
Chemical Engineering (General)
Authors
Chao Li, Jun-Jie Liao, Yang Yin, Qiong Mo, Li-Ping Chang, Wei-Ren Bao,