DOI: 10.1016/j.jcou.2019.02.018
Scopus记录号: 2-s2.0-85062725997
论文题名: An enthalpy model of CO 2 -CH 4 -H 2 S-N 2 -brine systems applied in simulation of non-isothermal multiphase and multicomponent flow with high pressure, temperature and salinity
作者: Guo Y. ; Li J. ; Ahmed R. ; Shen N. ; Li X.
刊名: Journal of CO2 Utilization
ISSN: 22129820
出版年: 2019
卷: 31 起始页码: 85
结束页码: 97
语种: 英语
英文关键词: Carbon geological utilization and storage (CGUS)
; CO 2 -CH 4 -H 2 S-N 2 -brine
; Enthalpy model
; Multiphase and multicomponent flow
; Non-isothermal effect
; Numerical simulation
Scopus关键词: Carbon dioxide
; Computer simulation
; Digital storage
; Isotherms
; Multiphase flow
; Pressure effects
; Multicomponent flow
; Nonisothermal
; Peng-Robinson EOS
; Phase equilibriums
; Pressure ranges
; Salinity effects
; Saturation state
; Temperature range
; Enthalpy
英文摘要: An accurate enthalpy model for CO 2 -CH 4 -H 2 S-N 2 -brine fluid system is proposed in this work. For the gas system (CO 2 -CH 4 -H 2 S-N 2 ), the model is based on Peng-Robinson EOS enthalpy deviation to calculate real gas system specific enthalpy. For the brine system, the model extends conventional saturation state enthalpy model considering pressure effect along with the temperature and salinity effects. For the dissolution heat, the model combines phase equilibrium parameters to describe the gas dissolved enthalpy. The model can predict CO 2 -CH 4 -H 2 S-N 2 -brine fluid system enthalpy well with temperature range from 0 to 300, pressure range from 0 to 1000 bar and salinity range from 0 to 6 mol/kg water. The model performs favorable with respect to existing experimental data and other models and reproduces reliable data for pure water, various salinity of brine and gas systems. © 2019 Elsevier Ltd. All rights reserved.
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资源类型: 期刊论文
标识符: http://119.78.100.158/handle/2HF3EXSE/117277
Appears in Collections: 气候变化与战略
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Recommended Citation:
Guo Y.,Li J.,Ahmed R.,et al. An enthalpy model of CO 2 -CH 4 -H 2 S-N 2 -brine systems applied in simulation of non-isothermal multiphase and multicomponent flow with high pressure, temperature and salinity[J]. Journal of CO2 Utilization,2019-01-01,31