In the modern fuel mix, the leading positions are occupied by hard coal and crude oil, both accounting for around 35% of annual mined energy content (Andruleit et al., 2012). With a 2% share, lignite does not compete with the former two in the global perspective. However, easy accessibility and low production costs ensure its important role in the energy policies of particular countries worldwide. Utilization of this energy carrier is limited, though, due to the water content often exceeding 50% of raw mass. High moisture content negatively affects calorific value and precludes transportation and storage. So, lignite is less advantageous than hard coal in terms of utilization in the power generation industry. On the other hand, the usage of lignite is also considered for a wide range of applications, including coking or briquetting, and considerable volatile matter content makes it a prospective fuel for gasification purposes. Thus, the efforts made to upgrade its quality seem justified.The removal of water, contributing to increase in thermal efficiency of lignite-fired power plants, can be performed by a variety of methods, separated into evaporative thermal drying, non-evaporative thermal drying and other Marcin ZAKRZEWSKI* , **, Yosuke KOMATSU***, Anna SCIAZKO*, Taro AKIYAMA***, Akira HASHIMOTO***, Naoki SHIKAZONO***, Shozo KANEKO***, Shinji KIMIJIMA** , ***, Janusz S. SZMYD* and Yoshinori KOBAYASHI***
AbstractLow calorific value of lignite, mostly attributed to high moisture content, undermines usability of this low rank coal. Upgrading the quality of this energy carrier, which benefits coal-fired power plant's thermal efficiency, can be effectively realized by means of drying. The kinetics of superheated steam drying was studied for 30 mm spherical samples from Belchatow lignite mine in Poland. The experiment featured simultaneous and continuous measurements of weight and temperature. The drying kinetics, described by curves of moisture content, drying rate and temperature profile, were evaluated using the data acquired. The appearance of the sample throughout the process was video-recorded. Widespread cracking and shrinkage, which differ depending on the conditions, along with series of droplets typical for larger sample, were observed. The examined particles were suitable for predictions of thermodynamically derived drying rate and time, as proposed in the previous study for 5 and 10 mm particles from the same coal deposit. However, in comparison they exhibited more uniform density distribution. On the basis of experimental results and material properties, the numerical model of drying process was applied. Simulated drying behavior was consistent with empirical observations. Extensive investigation, revealing features of variously-sized samples as well as diameter dependence on drying process, is required for purposes of designing industrial drying system dedicated to specific type of coal.