scholarly journals Wellbore flow model for carbon dioxide and brine

2009 ◽  
Vol 1 (1) ◽  
pp. 71-78 ◽  
Author(s):  
Lehua Pan ◽  
Curtis M. Oldenburg ◽  
Yu-Shu Wu ◽  
Karsten Pruess
2011 ◽  
Vol 2011 ◽  
pp. 1-15 ◽  
Author(s):  
Georg Janicki ◽  
Stefan Schlüter ◽  
Torsten Hennig ◽  
Hildegard Lyko ◽  
Görge Deerberg

In the medium term, gas hydrate reservoirs in the subsea sediment are intended as deposits for carbon dioxide (CO2) from fossil fuel consumption. This idea is supported by the thermodynamics of CO2 and methane (CH4) hydrates and the fact that CO2 hydrates are more stable than CH4 hydrates in a certain P-T range. The potential of producing methane by depressurization and/or by injecting CO2 is numerically studied in the frame of the SUGAR project. Simulations are performed with the commercial code STARS from CMG and the newly developed code HyReS (hydrate reservoir simulator) especially designed for hydrate processing in the subsea sediment. HyReS is a nonisothermal multiphase Darcy flow model combined with thermodynamics and rate kinetics suitable for gas hydrate calculations. Two scenarios are considered: the depressurization of an area 1,000 m in diameter and a one/two-well scenario with CO2 injection. Realistic rates for injection and production are estimated, and limitations of these processes are discussed.


2017 ◽  
Vol 7 (4) ◽  
pp. 745-755 ◽  
Author(s):  
Weiqiang Song ◽  
Hongjian Ni ◽  
Ruihe Wang ◽  
Mengyun Zhao

Author(s):  
Farshid Zabihian ◽  
Alan S. Fung

This paper investigates the impacts of carbon dioxide concentration in the inlet fuel on the performance of a hybrid tubular solid oxide fuel cell (SOFC) and gas turbine (GT) cycle with two configurations: system with and without anode exhaust recirculation. The reference case is introduced when the system is fueled by pure methane. Then, the performance of the hybrid SOFC-GT system is investigated when methane is partially replaced by CO2 from concentration of 0% to 90% with an increment of 5% at each step. The steady-state macro level model of the SOFC-GT hybrid system was developed in Aspen Plus® using built in and user-defined modules. The performance of the system was monitored by estimating and recording performance parameters, such as SOFC and system thermal efficiency; net and specific work of SOFC, GT, and cycle as a whole; air to fuel ratio; and mass and molar flow rate and temperature of various streams. The results demonstrate that the CO2 fraction in the inlet fuel has remarkable influences on the system’s operating parameters, such as efficiency and specific work.


2008 ◽  
Author(s):  
Silviu Livescu ◽  
Louis J. Durlofsky ◽  
Khalid Aziz ◽  
Jean-Charles Ginestra

SPE Journal ◽  
1998 ◽  
Vol 3 (02) ◽  
pp. 124-133 ◽  
Author(s):  
Liang-Biao Ouyang ◽  
Sepehr Arbabi ◽  
Khalid Aziz

2015 ◽  
Vol 752-753 ◽  
pp. 1210-1213
Author(s):  
Shuang Cindy Cao ◽  
Jong Won Jung ◽  
Jong Wan Hu

Geological CO2 sequestration is a promising method to reduce atmospheric CO2. Deep saline aquifers are one of the most important sites due to their capacity for CO2 storage. Thus, a better understanding of immiscible brine-CO2 mobility and their saturations including invading patterns in deep saline aquifers as CO2 storage sites is required. Microfluidic model provides the opportunity to discover unrecognized processes and to explore existing theories in fluid flow through porous media. In this study, the microfluidic model is used to explore the effects of both the supercritical carbon dioxide (scCO2) injecting velocity and ionic strength in saline aquifers on scCO2 invading patterns in geological CO2 sequestration. The results show that scCO2-brine displacement ratio increases with (1) increased scCO2 injecting velocity up to 40 μL/min, and (2) decreased ionic strength in the range of 1M~5M NaCl.


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