Micellar Flooding The Propagation of the Polymer Mobility Buffer Bank

1978 ◽  
Vol 18 (01) ◽  
pp. 5-12 ◽  
Author(s):  
S.P. Gupta

Abstract This study shows the factors that affect the polymer mobility buffer bank, that is, slug size and polymer mobility buffer bank, that is, slug size and concentration. The slug size is a function of polymer/chase-water mixing, polymer inaccessible polymer/chase-water mixing, polymer inaccessible pore volume (IPV), and polymer retention. The pore volume (IPV), and polymer retention. The designed polymer concentration depends on polymer apparent viscosity and, to varying degrees, on shear degradation. The polymer/chase-water mixing-zone volume at a given mobility ratio is the same for glycerine (classical miscible fluid), biopolymer, and polyacrylamide. However, the propagation rate of the polyacrylamide. However, the propagation rate of the mining zone is much higher for polymer than for glycerine because of IPV. Therefore, a larger polymer bank is required to protect the micellar polymer bank is required to protect the micellar slug than would be indicated by mixing-zone volume alone. IPV increased as polymer concentration decreased over the investigated range. A micellar fluid ahead of the polymer bank increased IPV. When polyacrylamides are used in the mobility buffer bank, their concentration should be increased to compensate for the effect of shear degradation. For each field application, shear-degradation tests should be conducted in field cores using field brine and at anticipated sand-face velocities. The loss of polyacrylamide effectiveness because of shear degradation should be determined from apparent viscosity measurement of the sheared polymer, not from polymer concentration, Brookfield viscosity, or screen factor. Introduction In a micellar flood, water-soluble polymers are used as a mobility buffer to protect the micellar slug from invasion by high-mobility chase water. In addition, polymer may be added to the micellar fluid to adjust viscosity, to improve sweep in a waterflood, as a preflush in micellar flood to improve the sweep, to control water production in producers, and for selective partial plugging of high-permeability thief zones. Biopolymers (Xanthan gum) and polyacrylamides are two classes of polymers most commonly used in oil recovery processes. processes. When designing a polymer slug for field application, proper sizing and chemical concentration are critical variables. In a micellar flood, the polymer-mobility buffer-bank size depends on polymer inaccessible pore volume (IPV), mixing, polymer inaccessible pore volume (IPV), mixing, and polymer retention. Because the primary purpose of the polymer bank is to provide adequate mobility control, a sufficient polymer concentration must be selected. However, the concentration for polyacrylamides often must be increased to account polyacrylamides often must be increased to account for losses resulting from shear degradation. This study was undertakento determine the magnitude of and variables affecting polymer inaccessible pore volume (IPV),to characterize the effect of IPV on polymer/chase-water mixing behavior, andto examine polyacrylamide shear degradation. In these IPV and mixing studies, the biopolymer is Kelzan MF TM (Xanflood); and the polyacrylamide is Dow Pusher 500. In shear polyacrylamide is Dow Pusher 500. In shear degradation studies, the polyacrylamides are Dow Pusher 500, Pusher 700, and Amoco Chemicals Pusher 500, Pusher 700, and Amoco Chemicals Sweepaid 105 (an experimental polymer). POLYMER INACCESSIBLE PORE VOLUME POLYMER INACCESSIBLE PORE VOLUME Polymers propagate through porous media more rapidly than through their carrier water. The pore space volume available for polymer flow is pore space volume available for polymer flow is less than the volume available to water. The volume in which polymer cannot flow commonly is called polymer inaccessible pore volume (IPV). The polymer inaccessible pore volume (IPV). The exact mechanism of IPV is not clear. However, it has been estimated that the polymer molecule size is of the same order as pore sizes in rock. In many cases, the smaller rock pores are not capable of transporting polymer molecules, but can transport water. Another phenomenon possibly contributing to IPV is the inability of the polymer molecule center to get near the pore wall. As a result, the average velocity of the polymer molecules is greater than that of water molecules. SPEJ p. 5

1975 ◽  
Vol 15 (04) ◽  
pp. 323-337 ◽  
Author(s):  
M.T. Szabo

Abstract Numerous single-phase flow and oil-recovery tests were carried out in unconsolidated sands and Berea sandstone cores using C14-tagged, hydrolyzed polyacrylamide solutions. The polymer-retention polyacrylamide solutions. The polymer-retention data from these flow tests are compared with data obtained from static adsorption tests. Polymer concentrations in produced water in Polymer-flooding tests were studied using various Polymer-flooding tests were studied using various polymer concentrations, slug sizes, salt polymer concentrations, slug sizes, salt concentrations, and different permeability sands. Results show that polymer retention by mechanical entrapment had a dominant role in determining the total polymer retention in short sand packs. However, the role of mechanical entrapment was less in the large-surface-area Berea cores. In oil-recovery tests, high polymer concentrations were noted at water breakthrough in sand-pack experiments, an indication that the irreducible water was not displaced effectively ahead of the polymer slug. However, in similar tests with Berea cores, a denuded zone developed at the leading edge of the polymer slug. polymer slug. The existence of inaccessible pore volume to polymer flow is shown both in sand packs and in polymer flow is shown both in sand packs and in sandstone cores. Absolute polymer-retention values show an almost linear dependency on polymer concentration. The effect of polymer slug size on absolute polymer retention is also discussed. Distribution of retained polymer in sand packs showed an exponential decline with distance. The "dynamic polymer-retention" values in short sand packs showed much higher vales than the ‘static packs showed much higher vales than the’ static polymer-adsorption" values caused by mechanical polymer-adsorption" values caused by mechanical entrapment. The mechanism of polymer retention in silica sands and sandstones is described, based on the observed phenomenon. Introduction It is widely recognized that, as polymer solution flows in a porous medium, a portion of the polymer is retained. It is evident that both physical adsorption and mechanical entrapment contribute to polymer retention. The question of the relative importance of these retention mechanisms has not been studied adequately. The effect of residual oil saturation on polymer retention and the polymer retention during the displacement of oil from porous media has also been studied inadequately. Mungen et al. have reported a few data on polymer concentration in produced water in oil-recovery tests. However, no produced water in oil-recovery tests. However, no comparison was made between polymer retention at 100-percent water saturation and at partial oil saturation. It has been shown that the actual size of the flowing polymer molecules, with the associated water, can approach the dimensions of certain smaller pores found in porous media. Therefore, an inaccessible pore volume exists in which no polymer flow occurs. In this study, the existence polymer flow occurs. In this study, the existence of inaccessible pore volume is shown clearly, both in sand and sandstone. Although polymer-retention values have been reported for various conditions, correlation is difficult because of the differing conditions of measurements. The effect of slug size, polymer concentration, salinity, and type of porous media on polymer retention has not been systematically studied. The purpose of this study was to develop answers to these questions, rather than to provide adsorption data for actual field core samples. For this reason, unconsolidated silica sands were used in most of the experiments reported. This permitted identical, uniform single-layer and multilayer porous media to be constructed for repeated experiments under varying test conditions. Some experiments were also carried out in Berea sandstone cores to determine whether sand-pack results can be extrapolated to consolidated sandstones. Using a C 14-tagged polymer provided a very rapid, simple, and accurate polymer-concentration determination technique. SPEJ P. 323


2014 ◽  
Vol 17 (03) ◽  
pp. 314-325 ◽  
Author(s):  
R.N.. N. Manichand ◽  
R.S.. S. Seright

Summary During a polymer flood, polymer retention can have a major impact on the rate of polymer propagation through a reservoir, and consequently on oil recovery. A review of the polymer-retention literature revealed that iron and high-surface-area minerals (e.g., clays) dominate polymer-retention measurements in permeable rock and sand (>100 md). A review of the literature on inaccessible pore volume (IAPV) revealed inconsistent and unexplained behavior. A conservative approach to design of a polymer flood in high-permeability (>1 darcy) sands would assume that IAPV is zero. Laboratory measurements using fluids and sands associated with the Sarah Maria polymer flood in Suriname suggested polymer retention and IAPV values near zero [0±20 μg/g for retention and 0±10% pore volume (PV) for IAPV]. A procedure was developed using salinity-tracer and polymer concentrations from production wells to estimate polymer retention during the Sarah Maria polymer flood in the Tambaredjo reservoir. Field calculations indicated much higher polymer-retention values than those from laboratory tests, typically ranging from approximately 50 to 250 μg/g. Field cores necessarily represent an extremely small fraction of the reservoir. Because of the importance of polymer retention, there is considerable value in deriving polymer retention from field results, so that information can be used in the design of project expansions.


1992 ◽  
Vol 7 (1-2) ◽  
pp. 25-32 ◽  
Author(s):  
T. Lund ◽  
E.Ø. Bjørnestad ◽  
A. Stavland ◽  
N.B. Gjøvikli ◽  
A.J.P. Fletcher ◽  
...  

2021 ◽  
Author(s):  
Konstantin Mikhailovich Fedorov ◽  
Tatyana Anatolyevna Pospelova ◽  
Aleksandr Vyacheslavovich Kobyashev ◽  
Aleksandr Yanovich Gilmanov ◽  
Tatyana Nikolaevna Kovalchuk ◽  
...  

Abstract The application of chemical enhanced oil recovery methods is based mainly on data from experiments. Determining the adsorption constants without destroying the sample remains a relevant problem. It is necessary for accurate data. The determination of filtration parameters of high-molecular polymers in a porous medium using special model is considered in this paper. The aim of the investigation is the solution of inverse problem of polymer transport with adsorption. The key data for this are the characteristic times of the polymer front propagation, water and rock densities, porosity, and initial polymer concentration. The solutions of the direct problem and the inverse problem from the characteristic form of equations are obtained. The algorithm of interpretation of adsorption-retention parameters and inaccessible pore volume form non-destructive experimental studies is developed. Comparison of the calculated values of the inaccessible pore volume with the results of laboratory studies leads to an error within 10%. The practical application of the algorithm was carried out using the data obtained in previously conducted experiments.


2013 ◽  
Vol 807-809 ◽  
pp. 2607-2611
Author(s):  
Byung In Choi ◽  
Moon Sik Jeong ◽  
Kun Sang Lee

Water salinity and hardness have been regarded as main limitation for field application of polymer floods. It causes not only reduction of polymer concentration, but also injectivity loss in the near wellbore. Based on the mathematical and chemical theory, extensive numerical simulations were conducted to investigate performance of polymer floods in the high-salinity reservoirs. According to results from simulations, the high salinity reduces the viscosity of polymer in contacting area. That causes a poor sweep efficiency of polymer flooding. Moreover, the presence of divalent cations makes the project of polymer flooding worse. That is because of excessively increased bottom-hole pressure in injection well by the precipitation of polymer. The quantitative assessment of polymer floods needs to be required before field application. Therefore, the results in this paper are helpful for optimal polymer flooding design under harsh reservoir conditions.


Author(s):  
John H. Doveton

The primary objective of porosity estimations based on measurements made either from petrophysical logs or core is the volume of pore space within the rock, given simply by the equation: . . . Φ = Vp/Vb . . . The Greek letter, phi, is the standard symbol for porosity and is expressed in this equation as the ratio of the volume of void space (Vp) to the bulk volume of the rock (Vb). The simplest concepts of porosity are generally explained in terms of the packing of spheres as the sum of the pore volume of the space between the spheres. There are five basic arrangements of uniform-sized spheres that can be constructed: simple cubic, orthorhombic, double-nested, face-centered cubic, and rhombohedral packing (Hook, 2003). Each has a geometrically defined pore volume that represents an upper limit for granular rocks whose constituent grains have a variety of sizes and shapes and whose pore volumes have been reduced by compaction and diagenetic cements. This intergranular model is a useful starting point for the characterization of pores in clastic rocks and will be considered first, before reviewing the additional complexities of pore geometry introduced by dissolution in carbonate rocks. The solid framework of a sandstone consists of a nonconductive “matrix” dominated by quartz, but commonly with accessory nonconductive minerals, and conductive clay minerals, whose electrical properties are caused by cation exchange with ions in saline formation water. It is important to distinguish between connected and unconnected pores, as well as larger pores that sustain fluid movement in contrast to smaller pores filled with capillary-bound water. A graphic presentation of these components is widely used in the petrophysical literature as a reference basis to disentangle terminology that can be confusing and contradictory. In particular, the term “effective porosity” has different meanings that vary from one technical discipline to another. In their review of porosity terms, Wu and Berg (2003) concluded that many core analysts considered all porosity to be effective, log analysts excluded clay-bound water, while petroleum engineers excluded both clay-bound and capillary-bound from porosity consideration, thereby restricting effective porosity to pores occupied by mobile fluids.


Author(s):  
T. Lund ◽  
E. Ø. Bjørnestad ◽  
A. Stavland ◽  
N. B. Gjøvilki ◽  
A. J. P. Fletcher ◽  
...  

SPE Journal ◽  
2019 ◽  
Vol 25 (01) ◽  
pp. 497-514 ◽  
Author(s):  
Vitor H. S. Ferreira ◽  
Rosangela B. Z. L. Moreno

Summary The term polymer retention describes all mechanisms that remove the polymer from the flowing solution, with adsorption being its primary cause. This phenomenon can lead to detrimental effects during polymer enhanced oil recovery (EOR). In this paper, we present an investigation of dynamic polymer adsorption in sandstone-outcrop cores using polymer solutions. We study the effects of permeability and polymer concentration on the adsorption under two conditions: on virgin cores (adsorption) and a previously polymer-flooded core (readsorption). According to the results, two concentration plateaus and two regions of concentration-dependent adsorption characterize the polymer adsorption in a virgin porous medium, following a proposed Type IV isotherm. The transition between the first plateau and the second adsorption region occurs near to the overlapping concentration from dilute to semidilute regimes (cp*). Polymer readsorption increases slightly with the successive injection of banks with a higher polymer concentration, following a Type I (Langmuir) isotherm. For that case, we propose a readsorption mechanism on the basis of the desorption of a polymer molecule section and the adsorption of a new free polymer molecule. The adsorption and readsorption isotherms are similar until cp*, while the adsorption is much higher than readsorption for concentrations higher than cp*. Therefore, if the polymer concentration of the mobility control bank is greater than cp*, the total polymer loss during field applications can be reduced by preinjecting a polymer bank of lower concentration.


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