Investigation of thermochemical process of coal particle packed bed reactions for the development of UCG
Investigation of thermochemical process of coal particle packed bed reactions for the development of UCG
In this study, a packed bed reactor was developed to investigate the gasification process of coal particles. The effects of coal particle size and heater temperature of reactor were examined to identify the thermochemical processes through the packed bed. Three different coal samples with varying size, named as A, B, and C, are used, and the experimental results show that the packed bed with smaller coal size has higher temperature, reaching 624 °C, 582 °C, and 569 °C for coal A, B, and C, respectively. In the case of CO formation, the smaller particle size has greater products in the unit of mole fraction over the area of generation. However, the variation in the porosity of the packed bed due to different coal particle sizes affects the reactions through the oxygen access. Consequently, the CO formation is least from the coal packed bed formed by the smallest particle size A. A second test with the temperature variations shows that the higher heater temperature promotes the chemical reactions, resulting in the increased gas products. The findings indicate the important role of coal seam porosity in underground coal gasification application, as well as temperature to promote the syngas productions.
476-492
Sutardi, Tata
0bb997f9-265e-4491-a9b2-9ac09940688a
Wang, Linwei
d85a25dd-ce87-4ce8-b9f3-156d3bf9d82f
Karimi, Nader
620646d6-27c9-4e1e-948f-f23e4a1e773a
Paul, Manosh C.
e1054c74-4d6c-41b7-b384-9935b956dfd5
3 September 2020
Sutardi, Tata
0bb997f9-265e-4491-a9b2-9ac09940688a
Wang, Linwei
d85a25dd-ce87-4ce8-b9f3-156d3bf9d82f
Karimi, Nader
620646d6-27c9-4e1e-948f-f23e4a1e773a
Paul, Manosh C.
e1054c74-4d6c-41b7-b384-9935b956dfd5
Sutardi, Tata, Wang, Linwei, Karimi, Nader and Paul, Manosh C.
(2020)
Investigation of thermochemical process of coal particle packed bed reactions for the development of UCG.
International Journal of Coal Science & Technology, 7 (3), .
(doi:10.1007/s40789-020-00360-x).
Abstract
In this study, a packed bed reactor was developed to investigate the gasification process of coal particles. The effects of coal particle size and heater temperature of reactor were examined to identify the thermochemical processes through the packed bed. Three different coal samples with varying size, named as A, B, and C, are used, and the experimental results show that the packed bed with smaller coal size has higher temperature, reaching 624 °C, 582 °C, and 569 °C for coal A, B, and C, respectively. In the case of CO formation, the smaller particle size has greater products in the unit of mole fraction over the area of generation. However, the variation in the porosity of the packed bed due to different coal particle sizes affects the reactions through the oxygen access. Consequently, the CO formation is least from the coal packed bed formed by the smallest particle size A. A second test with the temperature variations shows that the higher heater temperature promotes the chemical reactions, resulting in the increased gas products. The findings indicate the important role of coal seam porosity in underground coal gasification application, as well as temperature to promote the syngas productions.
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Published date: 3 September 2020
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Local EPrints ID: 509131
URI: http://eprints.soton.ac.uk/id/eprint/509131
ISSN: 2095-8293
PURE UUID: 19c380a7-316b-4c73-9831-062812ace62f
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Date deposited: 11 Feb 2026 17:55
Last modified: 12 Feb 2026 03:31
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Contributors
Author:
Tata Sutardi
Author:
Linwei Wang
Author:
Nader Karimi
Author:
Manosh C. Paul
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