scholarly journals Estimates for the local permeability of the Cobourg limestone

2018 ◽  
Vol 10 (6) ◽  
pp. 1009-1019 ◽  
Author(s):  
A.P.S. Selvadurai ◽  
A. Głowacki
Keyword(s):  
2012 ◽  
Vol 560-561 ◽  
pp. 1103-1113
Author(s):  
Zheng Gang Xiao ◽  
Wei Dong He ◽  
San Jiu Ying ◽  
Fu Ming Xu

To acquire better understanding of the early ignition phenomena in 100mm ignition simulator loaded with packed propellant bed, a theoretical model of ignition gas flow through rigid porous media is developed. Three pressure gauges are installed in the lateral side of ignition simulator for chamber pressure measurements after ignition. The pseupropellant loaded in the chamber is similar to the standard 13/19 single-base cylindrical propellant in size. It is composed of rigid ceramic composite with low thermo conductivity. It is assumed that the pseupropellant bed is rigid in contrast to the previous elastic porous media assumption. The calculated pressure values can be verified by the experimental data well at the low loading density of pseupropellant bed of 0.18 g/cm3. However, there is still error between the experimental and calculated results in the early pressure peak position close to the ignition primer when the loading density of pseupropellant bed increases to 0.73 and 1.06g/cm3, due to the change of local permeability of pseupropellant bed at high loading density, which is assumed a constant in the model for the modeling easily. The calculations can enable better understanding of physical processes of ignition gas flow in the ignition simulator loaded with the pseupropellant bed.


2005 ◽  
Vol 39 (10) ◽  
pp. 929-947 ◽  
Author(s):  
Markus Nordlund ◽  
T. Staffan Lundstrom

1988 ◽  
Vol 27 (9) ◽  
pp. 715-716
Author(s):  
P. A. Vityaz' ◽  
V. M. Kaptsevich ◽  
V. K. Sheleg ◽  
V. V. Savich ◽  
A. G. Kostornov ◽  
...  

2020 ◽  
Vol 54 (20) ◽  
pp. 2739-2751
Author(s):  
Zhaofei Xiao ◽  
Xiaoling Liu ◽  
Lee T Harper ◽  
Andreas Endruweit ◽  
Nicholas A Warrior

A force-directed algorithm was developed to create representative geometrical models of fibre distributions in directed carbon fibre preforms. Local permeability values were calculated for the preform models depending on the local fibre orientation, distribution and volume fraction. The effect of binder content was incorporated by adjusting the principal permeability values of the meso-scale discontinuous fibre bundles, using corresponding experimental data obtained for unidirectional non-crimp fabrics. The model provides an upper boundary for the permeability of directed carbon fibre preform architectures, where predictions are within one standard deviation of the experimental mean for all architectures studied.


2003 ◽  
Vol 388-389 ◽  
pp. 761-762 ◽  
Author(s):  
Takashi Murata ◽  
Masashi Tokunaga ◽  
Tsuyoshi Tamegai

2020 ◽  
Author(s):  
Philip Meredith ◽  
Nicolas Brantut ◽  
Patrick Baud

<p>Compaction of porous sandstones is generally associated with a reduction in permeability. Depending on porosity and other microstructural characteristics, compaction may be diffuse or localised in bands. Compaction bands have been shown to act as barriers to fluid flow and therefore reduce permeability perpendicular to the band orentiation, and thus also introduce permeability anisotropy. Additionally, the localised nature of compaction bands should also introduce strong permeability heterogeneity. We present new experimental data on sandstone compaction combining acoustic emission monitoring and spatially distributed pore fluid pressure measurements, allowing us to establish how permeability heterogeneity develops during progressive compaction. Three sandstones were tested in the compactant regime: Locharbriggs sandstone, which is microstructurally heterogeneous with beds of higher and lower initial permeability; a low porosity (21%) Bleurville sandstone, which is microstructurally homogeneous and produces localised compaction bands; and a high porosity (24%) Bleurville sandstone, which is also homogeneous but produces compaction in a more diffuse pattern. At regular intervals during compactive deformation, a constant pore pressure difference was imposed at the upper and lower boundaries of the cylindrical samples, and steady-state flow allowed to become established. Following this, local pore pressure measurements were made at four locations, allowing us to derive estimates of the local permeability. In all samples, progressive compaction produced overall reductions in permeability. In addition, localised compaction also produced internal reorganisation of the permeability structure. Localised compaction bands caused local decreases in permeability, while more diffuse compaction produced a more homogeneous overall reduction in permeability.</p><p> </p>


1984 ◽  
Vol 24 (03) ◽  
pp. 351-360 ◽  
Author(s):  
D.P. Schmidt ◽  
H. Soo ◽  
C.J. Radke

Abstract Lack of mobility control is a major impediment to successful EOR, especially for high-viscosity oils. This paper presents experimental and theoretical results for continuous, linear, secondary oil displacement using dilute, stable suspensions of oil drops. The major hypothesis is that the oil/water (O/W) emulsion provides microscopic mobility control through entrapment or local permeability reduction not through viscosity-ratio improvement. To describe the displacement process, previous emulsion filtration theory is extended to longer cores and to two-phase flow. Agreement between theory and experiment is satisfactory for continuous secondary oil displacement with 1- to 2-µm [1- to 2-micron] diameter drops of volume concentrations up to 5% in unconsolidated sand packs with permeabilities ranging from 1 to 3 µm2 [1 to 3 darcies]. Dilute suspensions of stable oil drops in water also are successful in diverting flow in parallel-core flooding to the lower-permeability core; therefore, they provide macroscopic mobility control. Introduction To date, two alkaline displacement processes employing stable emulsions have been suggested to improve oil recovery.1 In one process, emulsification with entrainment, oil drops are generated in situ upon reaction of alkali with acidic crude oil. Oil production occurs as an O/W emulsion. In emulsification with entrapment, the other process, oil drops that are generated in situ, or which are externally injected, aid in oil recovery by providing mobility control. These two processes are based on opposing views of how emulsions behave in porous media. According to the entrainment view, oil drops do not interact with the reservoir medium, and recovery of tertiary oil is a possibility.1 Conversely, according to the entrapment view, oil drops interact strongly with the reservoir medium, and improvement only in secondary recovery is sought. Recent work by Soo2 on silute emulsion flow in unconsolidated porous media shows that oil drops clog in pore constrictions and on pore walls, thereby restricting flow. Once captured, there is negligible particle reentrainment. Even drops smaller than the pore throats have a significant capture probability. Soo's study supports the entrapment picture as a more viable description of emulsion flow. However, in spit of field applications of the entrapment technique,3,4 no current methodology exists to predict quantitatively possible mobility-control improvement. This paper presents a theoretical framework for calculation of secondary oil displacement in linear systems with injection of dilute, stable O/W emulsions. Although we focus mainly on microscopic mobility control with dilute emulsions, some attention is given to macroscopic flow redistribution or sweep improvement in parallel cores. The basic premise is that dilute emulsions lower the mobility of the displacing phase through local permeability reduction, not through increasing the viscosity of the displacing phase. We rely heavily on filtration theory, which is successful in describing transient emulsion flow in water-saturated cores.2 The significance of the mathematical treatment is not restricted to the emulsion entrapment technique. It is well known that certain polymers, notably polyacrylamides, establish more mobility control than can be accounted for by bulk rheology.5–11 Large permeability reductions sometimes are observed following polymer injection. Adsorption does not appear to be the main cause of this flow restriction but rather mechanical entrapment - i.e., trapping of high-molecular-weight polymer molecules or, as likely, gels in pore constrictions. Willhite and Dominguez11 recognized the analogy between polymer mechanical entrapment and deep-bed filtration of liquid or solid particulate suspensions. However, they did not explore this analogy quantitatively. Polymer, solid particulate, and emulsion droplet entrapment are directly analogous. Hence, any theory devised for one phenomenon should, in principle, be applicable to the other. Moreover, macroemulsions, as distinguished from microemulsions, sometimes form in surfactant/polymer flooding. Larson et al.12 outline how such emulsion formation might be modeled in displacement calculations. They consider the emulsified oil drops to be retarded in percolating through the porous medium. Permanent capture is not envisioned. This study focused on the filtration and mobility-control aspects of emulsified oil flow. It, therefore, provides an alternative treatment to that of Larson et al. To model EOR with dilute emulsions requires extension of the filtration theory of Soo2 to long cores and to two-phase flow. Combination with classical Buckley-Leverett water flooding theory then permits transient displacement calculations. Before outlining the theory, we present the experimental procedures.


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