Analytical Modeling of Oil Recovery by Steam Injection: Part 2-Asymptotic and Approximate Solutions (include associated papers 10943 and 10951 )

1981 ◽  
Vol 21 (02) ◽  
pp. 179-190 ◽  
Author(s):  
Y.C. Yortsos ◽  
G.R. Gavalas

Abstract This article studies the development of asymptotic and approximate solutions for the growth of the steam zone in steam injection processes in one-dimensional reservoirs at constant injection rates. These solutions generally are derived by using integral balances which include heat losses to the surroundings and the hot liquid zone. In this way, the effects of preheating caused by heat transport in the hot liquid zone ahead of the steam front are accounted for completely. At the beginning of injection, the advance of the front is well described by the Marx-Langenheim (ML) model, provided that the injection rates are sufficiently high. At longer times, deviations occur and a criterion is developed in terms of a single heat transfer dimensionless parameter, R, that defines the time interval of applicability of the ML model. The asymptotic behavior at large times depends solely on a dimensionless parameter, F, defined as the ratio of the latent to the total heat injected. It is shown that the final dimensionless expression does not depend on R (i.e., on the injection rates) although the time taken to reach the asymptotic state is influenced significantly by R. An approximate analytical solution that reduces to the respective asymptotic expressions at small and large times is obtained under conditions of high injection rates (R »1). The solution is shown to give a better approximation to the steam-zone growth rate for intermediate and large times than the approximate expressions developed by Marx and Langenheim, Mandl and Volek (MV), and Myhill and Stegemeier (MS). For a wider range of operating conditions, including low injection rates (i.e., for R between 1 and), an approximate numerical solution based on a quasisteady state approximation is presented. The proposed solution requiring very modest computation is expected to give reliable results under a variety of operating conditions. Introduction In a previous paper we dealt with the derivation of upper bounds for the volume of the steam zone in one-, two-, or three-dimensional reservoirs. The resulting expressions incorporate minimal information regarding heat transfer in the hot liquid zone and find applications in setting an upper estimate to oil recovery at constant or variable injection rates. To obtain more precise results concerning the steam zone growth, an alternative approach is initiated involving a detailed description of heat transfer in the hot liquid zone. The subject of heat transfer by convection, conduction, and lateral heat losses in the region ahead of a moving condensation front has been discussed separately in another paper. Here we make use of the results obtained in that paper to derive approximate solutions to the volume of the steam zone as a function of time. The relative importance of including preheating effects in the hot liquid zone and the surroundings when calculating the performance of a steam drive is demonstrated by comparing the solutions obtained against simple approximate expressions developed by Marx and Langenheim, and subsequently revised by Mandl and Volek, and Myhill and Stegemeier. From the comparison with exact results, the range of validity of the previous approximations can be delineated. SPEJ P. 179^

1981 ◽  
Vol 21 (02) ◽  
pp. 162-178 ◽  
Author(s):  
Y.C. Yortsos ◽  
G.R. Gavalas

Abstract This paper deals with the derivation of upper bounds for the growth of the steam zone in steam injection processes for one- or multidimensional reservoirs at constant or variable injection rates. The bounds are derived from the integral balances describing a reservoir of arbitrary geometry by introducing lower bounds for the heat losses to the surrounding area and the hot liquid zone. In this way, the effect of preheating in the hot liquid zone is estimated to determine the recovery efficiency of a steam drive. The growth rate of a one-dimensional steam zone at variable injection rates is subject to two upper bounds resulting from the total thermal energy and the latent heat balances, respectively. Each of the bounds controls the rate of growth of the steam zone in a certain time interval, depending on the dominant mode of heat transfer in the hot liquid zone. At constant injection rates, the steam zone growth at large times is controlled by the bound based on the latent heat balance. This balance depends on a dimensionless parameter, F, defined as the ratio of the latent heat to the total heat injected. Based on the relative magnitude of F with respect to the critical value F= 2/pi, the region of validity of the Marx-Langenheim solution is delineated on a Ts vs. fs diagram. The Marx-Langenheim solution is satisfactory at large times when F greater than 2/pi and becomes less satisfactory as F assumes smaller values. Similar upper bounds are obtained for a two-dimensional steam drive (thin reservoirs). In three-dimensional reservoirs, on the other hand, bounds are derived only for a special form of displacement (separable front). These bounds depend on the models for the steam front shape, K can be determined in terms of the physical variables of the process. Introduction Injection of steam (steamflood or steam drive) is an important thermal recovery method that is applied on a commercial scale in many parts of the world. The main elements of continuous steam injection, as a displacement process, were analyzed thoroughly by experimental studies under both laboratory and field conditions. Along with laboratory and field tests, mathematical models are sought to aid in understanding and designing the process. The engineering evaluation of a steam drive often is based on a simplified mathematical description of reservoir heating by hot fluid injection presented by Marx and Langenheim and subsequently modified by Mandl and Volek. This theory was combined further with simple fluid flow considerations to determine the oil recovery rates in one-dimensional reservoirs. To account for the important effects of gravity override in three-dimensional geometries, Neuman and van Lookeren (following different approaches) derived simple analytical formulas for the calculation of the performance of a steamflood in three-dimensional reservoirs. An increasing number of investigators also have concentrated on the development of reliable numerical models. Three-phase numerical simulators were derived by Shutter for one- and two-dimensional flow; by Abdalla and Coats for two-dimensional flow; and by Coats et al., Coats, and Weinstein et al. for three-dimensional flow. The last two models also account for steam distillation of oil. SPEJ P. 162^


1997 ◽  
Vol 119 (2) ◽  
pp. 265-271 ◽  
Author(s):  
I. Etsion ◽  
M. D. Pascovici ◽  
L. Burstein

The boiling interface in a misaligned two-phase mechanical seal is analyzed using a complete thermohydrodynamic approach that requires complex simultaneous iterative solutions of the nonaxisymmetric heat transfer and phase-change problems. It is shown that under certain operating conditions, characterized by a modified Sommerfeld number, several approximate solutions with various levels of simplification can be utilized to calculate the boiling radius.


2011 ◽  
Vol 133 (7) ◽  
Author(s):  
Mark Aaron Chan ◽  
Christopher R. Yap ◽  
Kim Choon Ng

Abstract This study presents a generalized confined boiling correlation applicable for various working fluids and operating conditions. A dimensionless parameter, Bond number, has been incorporated into the correlation to include the effects of confinement in the ebullition process of boiling. The proposed correlation is compared with an existing correlation based on their capability in predicting confined boiling data from the literature. A phenomenon of heat transfer coefficient stagnation is found for boiling in narrow spaces despite an increase in heat flux. Results show that the proposed correlation entails an excellent agreement with experimental data, and the predictions have a reasonably low mean absolute error of 17.3% for the entire database.


2021 ◽  
pp. 1-20
Author(s):  
Mohammad Izadi ◽  
Phuc H. Nguyen ◽  
Hazem Fleifel ◽  
Doris Ortiz Maestre ◽  
Seung I. Kam

Summary While there are a number of mechanistic foam models available in the literature, it still is not clear how such models can be used to guide actual field development planning in enhanced oil recovery (EOR) applications. This study aims to develop the framework to determine the optimum injection condition during foam EOR processes by using a mechanistic foam model. The end product of this study is presented in a graphical manner, based on the sweep-efficiency contours (from reservoir simulations) and the reduction in gas mobility (from mechanistic modeling of foams with bubble population balance). The main outcome of this study can be summarized as follows: First, compared to gas/water injection with no foams, injection of foams can improve cumulative oil recovery and sweep efficiency significantly. Such a tendency is observed consistently in a range of total injection rates tested (low, intermediate, and high total injection rates Qt). Second, the sweep efficiency is more sensitive to the injection foam quality fg for dry foams, compared to wet foams. This proves how important bubble-population-balance modeling is to predict gas mobility reduction as a function of Qt and fg. Third, the graphical approach demonstrates how to determine the optimum injection condition and how such an optimum condition changes at different field operating conditions and limitations (i.e., communication through shale layers, limited carbon dioxide (CO2) supply, cost advantage of CO2 compared to surfactant chemicals, etc.). For example, the scenario with noncommunicating shale layers predicts the maximum sweep of 49% at fg = 55% at high Qt, while the scenarios with communicating shale layers (with 0.1-md permeability) predicts the maximum sweep of only 40% at fg = 70% at the same Qt. The use of this graphical method for economic and business decisions is also shown, as an example, to prove the versatility and robustness of this new technique.


1971 ◽  
Vol 11 (02) ◽  
pp. 185-197 ◽  
Author(s):  
Satter Abdus ◽  
David R. Parrish

Abstract The widely used Marx and Langenheim solution for reservoir heating by steam injection fails to account for the growth of the hot liquid zone ahead of the steam zone. Furthermore, that solution does not consider radial heat conduction both within and outside the reservoir and vertical conduction within the reservoir. In the present paper, a more realistic and generalized solution is provided by eliminating several restrictive assumptions of the ‘old theory'. However, fluid flow is not considered in this model. The partial-difference equations that describe the condensation within the steam zone and temperature distribution within the system have been solved by finite-difference schemes. Calculated results are presented to show the effects of steam injection pressures ranging from 500 to 2,500 psia and rates, 120 and 240 lb/hr-ft, on the growth of the steam and hot liquid zones. A 50-ft thick reservoir with fixed thermal and physical characteristics was considered. Results show that heat losses from the reservoir into the surrounding rocks are not greatly different from those predicted by Marx and Langenheim. However, the heat distribution is markedly different. A sizable portion of the reservoir heat was contained in the hot liquid zone which grows indefinitely. This means that heat (warm water) could arrive at the producing wells sooner than predicted by the old theory. This is particularly true for low injection rate or high injection pressure. Curiously, for a given injection rate and pressure, the heat content of the hot liquid zone remains (except for early times) essentially a constant percentage of the cumulative heat injected. INTRODUCTION In 1959. Marx and Langenheim1 made a theoretical study of reservoir heating by hot fluid injection. Their solution has been widely used in the industry for the evaluation of the steam-drive process. This solution, however, is based upon an unrealistic assumption that the growth of the hot liquid zone ahead of the steam zone is negligible. Therefore, it cannot predict the arrival of warm water at the producing wells earlier than steam. Furthermore, in the so-called ‘old theory', radial heat conduction both within and outside the reservoir was neglected. Willman et al.2 presented another analytical solution of the same problem. Their solution is comparable to the Marx-Langenheim solution and suffers from the same disadvantages. Wilson and Root3 presented a numerical solution for reservoir heating by steam injection. While radial and vertical heat conduction both within and outside the reservoir were considered, their solution was provided essentially for the injection of a noncondensable fictitious hot fluid. The specific heat of the injected fluid was assumed to be equal to the difference between the enthalpy of steam and the enthalpy of water at the reservoir temperature divided by the difference in the two temperatures. Baker4 carried out an experimental study of heat flow in steam flooding using a sand pack. 4 in. thick and 6 ft in diameter. The steam injection pressure was 2 to 5 psig and rates ranged from 22 to 299 lb/hr-ft. He showed that a significant portion of the injected heat was contained in the hot water zone. The theoretical steamed or heated volume, as calculated by the Marx and Langenheim method, fell between the experimental steamed and heated (including hot water) volumes. Spillette5 made a critical review of the known analytical solutions dealing with heat transfer during hot water injection into a reservoir. These solutions are based upon many restrictive assumptions similar to the simplified solutions of the steam heating process. Spillette also presented a numerical solution for multidimensional heat transfer problems associated with hot water injection and demonstrated the utility and accuracy of the method. Most mathematical models of steam and hot water recovery processes neglect fluid flow considerations.


Author(s):  
Sulaman Pashah

The use of extended surfaces or fins is very common for enhancing the heat transfer between a prime surfaces and surrounding environment. The applications cover both scenarios where the prime surface is either at a higher or at a lower temperature than the surrounding environment. In the first case, only sensible heat transfer occurs whereas the latter is typical for refrigeration and air conditioning applications where both sensible and latent heat transfer occur. The performance of a fin is well described through a dimensionless parameter called fin efficiency. The efficiency is represented graphically in form of charts as a function of another dimensionless parameter called the fin parameter. The objective of the dimensionless presentation is that it provides the solution to a class of problems. However, this is true only for the dry fins because such charts for wet fins are for a set of particular operating conditions (i.e. temperature and psychrometric data). Thus, a separate chart is required if operating conditions are changed. The objective of present study is to investigate the possibility of developing the fin efficiency charts in the form which are independent of the operating conditions, thus a single chart covering all possible operating conditions. The finite element formulation is used to account for the actual nonlinear psychrometric relationships.


Author(s):  
Giuseppe Starace ◽  
Lorenzo Falcicchia ◽  
Pierpaolo Panico ◽  
Maria Fiorentino ◽  
Gianpiero Colangelo

AbstractIn refrigeration systems, evaporative condensers have two main advantages compared to other condensation heat exchangers: They operate at lower condensation temperature than traditional air-cooled condensers and require a lower quantity of water and pumping power compared to evaporative towers. The heat and mass transfer that occur on tube batteries are difficult to study. The aim of this work is to apply an experimental approach to investigate the performance of an evaporative condenser on a reduced scale by means of a test bench, consisting of a transparent duct with a rectangular test section in which electric heaters, inside elliptical pipes (major axis 32 mm, minor axis 23 mm), simulate the presence of the refrigerant during condensation. By keeping the water conditions fixed and constant, the operating conditions of the air and the inclination of the heat transfer geometry were varied, and this allowed to carry out a sensitivity analysis, depending on some of the main parameters that influence the thermo-fluid dynamic phenomena, as well as a performance comparison. The results showed that the heat transfer increases with the tube surface exposed directly to the air as a result of the increase in their inclination, that has been varied in the range 0–20°. For the investigated conditions, the average increase, resulting by the inclination, is 28%.


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