Journal
APPLIED ENERGY
Volume 88, Issue 9, Pages 2934-2939Publisher
ELSEVIER SCI LTD
DOI: 10.1016/j.apenergy.2011.02.035
Keywords
Oxygen-bearing coal-bed methane; Liquefaction; Rectification; Flammability limit; Safety measure
Categories
Funding
- Science and Technology Research Project of Harbin [RC2008QN007002]
- Ministry of Education [NCET-07-0544]
Ask authors/readers for more resources
A novel liquefaction and distillation process has been proposed and designed for the typical oxygen-bearing coal-bed methane (CBM), in which the impurities of the oxygen and nitrogen components are removed in the distillation column. The flammability limit theory combining with HYSYS simulation results are employed to analyze and calculate the flammability limits and the results indicate that no flammability hazard exists in the stages of compression, liquefaction and throttling. However, flammability hazard exists at the top the distillation column because the methane mole fraction decreases to the value below the upper flammability limit (UFL). The safety measures of initially removing oxygen content from the feed gas combining with the control of the bottom flowrate (flowrate of the liquid product at column bottom) are proposed to ensure the operation safety of the liquefaction process. The results reveal that the operation safety of the whole process can be guaranteed, together with high methane recovery rate and high purity of the liquid product. The applicability of the liquefaction process has also been analyzed in this paper. The simulation results can offer references for the separation of oxygen from CBM, the analysis of flammability limits and the safety measures for the whole process. (C) 2011 Elsevier Ltd. All rights reserved.
Authors
I am an author on this paper
Click your name to claim this paper and add it to your profile.
Reviews
Recommended
No Data Available