Calculation on the phase equilibrium and critical temperature of CH4/CO2

被引:4
作者
Guo, Gang [1 ]
Wang, Fei [1 ]
Liu, Guo-Qiang [2 ]
Luo, Sheng-Jun [1 ]
Guo, Rong-Bo [1 ]
机构
[1] Chinese Acad Sci, Qingdao Inst Bioenergy & Bioproc Technol, Shandong Ind Engn Lab Biogas Prod & Utilizat, Shandong Prov Key Lab Synthet Biol,Key Lab Biofue, Qingdao 266101, Shandong, Peoples R China
[2] Qingdao Univ Sci & Technol, Coll Chem Engn, Qingdao 266042, Peoples R China
基金
中国博士后科学基金;
关键词
CH4/CO2; Phase equilibrium; Critical temperature; Rapid estimation; Equations of state; Peng-Robinson EOS; EQUATION-OF-STATE; VAPOR-LIQUID-EQUILIBRIUM; CARBON-DIOXIDE; MULTICOMPONENT MIXTURES; HYDROCARBON SYSTEMS; VOLUME TRANSLATION; CHAIN MOLECULES; CUBIC EQUATIONS; BINARY-MIXTURES; FLUID MIXTURES;
D O I
10.1016/j.psep.2017.11.007
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The phase equilibrium and critical temperature are the pivotal parameters for the application of biogas, especially the liquefied biogas. In this work, rapid estimation methods for the phase equilibrium (e.g. SRK, PR and PC-SAFT equations of state (EOS)) and critical temperature (e.g. MF, CVF, CP, GT, RK, MW and GC methods) of synthetic biogas (CH4/CO2) were summarized based on previous studies and the accuracy was then verified according to the experimental data. The results showed that PR EOS gave more accurate results when estimating the phase equilibrium of CH4/CO2. For the estimation of critical temperature of CH4/CO2, in the region with low CH4 composition (<50%), all the estimation methods except GC method gave the results close to the experimental data, while GC method produced obviously lower values. While in the region with high CH4 composition (>60%), only MF and CP methods gave the most accurate results. (C) 2017 Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:369 / 377
页数:9
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