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DALIAN UNIVERSITY OF TECHNOLOGY Login 中文
Yongchen Song

Professor
Supervisor of Doctorate Candidates
Supervisor of Master's Candidates


Gender:Male
Alma Mater:大连理工大学
Degree:Doctoral Degree
School/Department:能源与动力学院
Discipline:Energy and Environmental Engineering
Business Address:能动大楼810
Contact Information:songyc@dlut.edu.cn
E-Mail:songyc@dlut.edu.cn
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Current position: Home >> Scientific Research >> Paper Publications

Competitive adsorption/desorption of CH4/CO2/N-2 mixture on anthracite from China for ECBM operation

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Indexed by:会议论文

Date of Publication:2016-10-08

Included Journals:EI、CPCI-S

Volume:105

Page Number:4289-4294

Key Words:CH4/CO2/N-2 mixture; adsorption/desorption; volumetric method; ECBM

Abstract:The adsorption/desorption of CH4/CO2/N-2 mixture was investigated at 294 K, 311 K, 333 K, and 353 K with a wide pressure range (0 similar to 70 Bar) on anthracite from China using a High Pressure Volumetric Analyzer (HPVAII-200). When the temperature is relatively low (293 K and 311 K), as the pressure rises, the excess adsorbed amount increases and peaks before experiencing a decrease. However, when the temperature is relatively high (353 K), the excess adsorbed amount increases and plateaus among the entire pressure range in this study. The pressure corresponding to the maximum adsorbed amount is lower in the process of desorption compared with adsorption, because there exists a hysteresis between adsorption and desorption. With the increasing temperature, the excess adsorbed amount is on the decline, which is the same as pure gas. While the pressure corresponding to the maximum adsorbed amount ascends as the temperature rises, even beyond the pressure range in this study. Moreover, the excess adsorbed amount have a good linear relationship with the temperature. Furthermore, the CO2 shows the best adsorption capacity and the adsorption capacity of CH4 is greater slightly than N-2. In addition, with the increasing temperature, the competitive adsorption among CO2, CH4 and N-2 is weaker. (C) 2016 The Authors. Published by Elsevier Ltd.