SPE Members Abstract An integrated reservoir, well tubing string, and surface pipeline network model of the Prudhoe Bay oil field has been constructed. The integrated model incorporates a new procedure for the simultaneous solution of the reservoir and surface pipeline network flow equations. It also includes an optimization technique to allocate well production rates. As a result of the effectiveness of the developed procedures, the new technology for integrated reservoir and surface facility modeling has been successfully applied to a facility optimization study of the giant Prudhoe Bay oil field. Introduction Business Motivation. Production from the Prudhoe Bay oil field is on decline. For this reason, optimal usage of the surface facilities is a major factor in reducing production costs. Along with other measures, production costs for Prudhoe Bay can be reduced by–defining the optimum surface facility structure and operating conditions (optimum number of separator stages and their connections, optimum separator pressure, etc.);–using any excess capacity in the Prudhoe Bay surface facilities to process third party fluid production from satellite oil fields. However, changes to the surface facility system will impact production from Prudhoe Bay wells. For example, tubinghead pressures for some Prudhoe Bay wells will increase if production from the satellite fields is conveyed to the separators via the existing surface pipeline network system. In this case, production rates for these wells would be reduced. Tools. Integrated compositional models of–the reservoir,–well tubing strings,–the surface pipeline network system,–separator banks, and central gas facility are constructed to evaluate the impact of facility modifications on well production profiles. The compositional reservoir model and its history matching will be described in a separate paper. The integration of the central gas facility and reservoir models is presented in Reference 1. In this paper, we describe the well tubing string and surface pipeline network models and their integration with the reservoir model. Model Objectives. The integrated reservoir and surface pipeline network model provides the capability to–allocate production well rates in a reservoir simulation from pressure constraints at the separator banks and from surface facility limits,–define optimum well assignments to high or low pressure flowline and separation systems–determine the impact of surface facility changes on a production profile. Normally, tubinghead pressure or bottomhole pressure is used for the well rate allocation in reservoir simulations. However, well tubinghead (or bottomhole) pressures change in time as a result of well gas-oil ratio and water cut variations, and these changes are difficult to predict. Challenges. Construction of an integrated model of the reservoir and surface pipeline network system for the Prudhoe Bay oil field is a very challenging and difficult problem for the following reasons: P. 435^
Waterflood residual oil saturation, in mixed wettability reservoirs, is often a strong function of pore volumes (PV) injected. The Endicott Field, Alaska displays typical mixed wettability behavior with coreflood remaining oil saturation varying from 40% at 1 PV to 12% at infinite PVs. Although only about 1 PV will be injected in the reservoir, surface film drainage may act to reduce oil saturation making determination of the correct effective residual oil saturation difficult.Accurate determination of waterflood residual oil saturation is essential for assessment of waterflood performance and evaluation of enhanced recovery processes. To minimize uncertainty in predicting effective residual oil saturation in mixed wettability reservoirs it is necessary to consider the competing effects of relative permeability, graVity forces, and imbibition capillary pressure. A mechanistic simulation approach is presented for scaling up laboratory results, that considers all active forces.References and Illustrations at end of paper.
Original SPE manuscript received for review Oct. 7, 1993. Revised manuscript received July 19, 1994. Paper accepted for publication Aug. 12, 1994. Paper first presented at the 1993 SPE Western Regional Meeting in Anchorage, May 26-28. Journal of Petroleum Technology, November 1994. Summary This paper presents a general method for forecasting oilfield economic performance that integrates cost data with operational, reservoir, and financial information. Practices are developed for determining economic limits for an oil field and its components. The economic limits of marginal wells and the role of underground competition receive special attention. Also examined is the influence of oil prices on operating costs. Examples illustrate application of these concepts. Categorization of costs for historical tracking and projections is recommended. Introduction Ultimate recoverable oil and gas volumes (" reserves") are estimated for many purposes, including internal company planning, external asset valuation, and government and financial reporting. A key element of field performance forecasting is quantification of hydrocarbons that are both "technically" and "economically" recoverable. In the U.S., a number of regulatory agency and industry guidelines have evolved over the years to reduce subjectivity, but reserves estimation and reporting continue to be debated. Technical reserves are usually calculated by estimating original oil in place (OOIP) and recovery factor. OOIP is a measure of reservoir size and is mainly a function of rock and fluid properties. Recovery factor is an engineering estimate based on geology, reservoir development, and reservoir management strategies. A wide variety of methods to estimate recovery factors are used, including analytical calculations, performance-based correlations, and numerical simulations. Estimation of technical reserves is better understood by the industry than determination of economic producibility. Technical and economic components of reserves often are calculated independently by different professionals. Sometimes technical recovery is predicted in more detail than is commensurate with the economics. Campbell noted that the advent of the computer in performance analysis has "enhanced precision and detail without a necessary increase in accuracy." He called for a "new paradigm" in evaluation methods in which petroleum professionals are not only technically competent but also possess a "higher degree of economic literacy." Recommended Approach Oil fields, like other businesses, should be operated to maximize returns to shareholders (subject to legal and health, safety, and environmental quality constraints). Performance forecasting should reflect this philosophy. Projections of field activities, costs, and production must be integrated to predict economic performance. Field operations/activities that are and will likely remain uneconomical should be identified and shut down. Although it may reduce fieldwide oil rate, the shutdown or consolidation of large portions of the field may be necessary to maximize cash flow in mature fields. Such an operation, which we call "de-development," might involve groups of wells, projects, or surface processing facilities. Field production will be maintained until continued negative net cash flows are expected and further operational reductions would reduce revenues faster than expenses. (This paper does not consider the distinction between shutdown and abandonment decisions.) Company and industry analysts speculate about future oil prices, but generally do not have control of this parameter. Maximizing the value of an oil field will depend on understanding and controlling operating costs. Published Cost Models Three basic methods are discussed within the published literature for prediction of future operating costs: constant lifting cost per barrel, constant lifting cost per well per year, and constant lifting cost per platform (or field) per year. Cost per well per unit time is the most commonly used. Next is the total field/platform basis with or without adjustments for real cost or oil price inflation rates. All three methods have limitations. Use of constant cost per barrel is optimistic for fields with declining production because fixed costs are ignored. By contrast, the other two methods incorrectly assume all costs are independent of fluid rates and time. Techniques with fixed and oil-rate dependent components of operating costs have been presented. These methods, however, do not include the influence of associated gas and water production on costs. Also volumes, prices, and costs are assumed independent. Cost Relationships Cash profit is maximized by producing to the point where the marginal cost (MC), defined as the change in total costs to supply an additional unit, for each activity is equal to its marginal revenue (MR), defined as the change in total revenues received after selling one more unit. For a competitive industry (no single producer can affect market price), MR is average realized price per unit. MC, however, is rarely the same as average cost (total costs/total produced units), as the example in Fig. 1 illustrates. Use of average unit costs instead of MC will rarely maximize profits (defined as total revenues minus total costs). Accurate prediction of future operating expenses requires a good understanding of cost relationships and the factors that influence them. The shape and magnitude of the MC curve will vary with short-term changes in activities and long-term economic forces. Activities that determine costs over a relatively short period of time are called cost drivers. Internal or external forces acting to change the cost-driver relationships over time (and thus shift the MC curve) are called cost accelerators. Cost Drivers Short-term operating costs are estimated at a given time by determining cost drivers. We believe that, for a producing property, three categories of cost drivers exist.Costs related to production. Usually fuel/power and chemicals, but could include some maintenance.Costs that vary with well count.Costs that are "fixed" over the short-term but are subject to upward or downward pressure in the long-term. This may be expressed as (CT)t=f(fluid rates, well count, field fixed costs)t (1) where (2) and (3) The equations in this paper are based on oil production. Similar relations can be developed for gas fields and sales. P. 965^
This paper was prepared for presentation at the 1999 SPE Annual Technical Conference and Exhibition held in Houston, Texas, 3–6 October 1999.
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