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2004, Petroleum review
A recent study carried out by members of the HM-L-4B Oil Transportation Measurement Committee - supported by the Energy Institute (El) and the API - has confirmed the general accuracy of the existing IP/API/ASTM Petroleum Measurement Tables (1980). The tables are used to convert densities and volumes measured at ambient conditions to standard conditions. In addition, new, simple equations have been developed based on velocity of sound, which can provide improved precision over the existing tables. Paul Harrison*, Melverley Consultants, and Denis Fitzgerald**, H&D Fitzgerald, report.
Proceedings of the National Academy of Sciences, 2012
SEG Technical Program Expanded Abstracts 2010, 2010
Measurement is the basis of commerce between producers, royalty owners, transporters, process plants, marketers, state and federal government authorities, and the general public. In fact, accurate measurement of hydrocarbon fluids and materials has a significant impact on the Gross National Product of exporting and importing countries, the financial performance and asset base of global companies, and the perceived efficiency of operating facilities. The need for accurate fiscal measurement is obvious. Given the present or future levels of the cost of natural gas, one can quickly quantify the material and economic value unaccounted for that is associated with each kO.Ol% of systematic uncertainty that might unknowingly exist in the measurement systems. Measurement errors can have both immediate and long-term impacts on profits. Inaccurate measurement may result in loss of customers, adverse publicity, potential penalties, and legal liabilities. In short, equitable and accurate measurement is essential to business. It affects the validity of financial and operating reports as well as the corporate reputation (cash flow, profit and loss, balance sheet, royalties and taxes). For reasons such as these, it is essential that material quantity measurements be precise and accurate with minimal bias errors. Furthermore, it is incumbent on those involved in custody transfer to establish and maintain the traceability chains that link their measurements to appropriate domestic and international standards. xix xx Preface In this manner, fiscal transfers can be done equitably with the confidence of both seller and buyer alike. The capital and operating resources (CAPEX, OPEX) applied for fiscal transfers must be commensurate with the total cost of measurement: the capital cost of technology, the operating cost of technology, industry practice or standards, regulatory compliance and the total fiscal exposure or risk (commodity value times throughput), the strategic and tactical business direction, and competitors' strategy, The amount of uncertainty is governed by the investment of resources (CAPEX and OPEX) combined with the inherent uncertainty associated with the method of measurement (primary, secondary, and tertiary devices) and the fiscal exposure or risk Measurement is a technically demanding, complex, state-ofthe-art field with a significant impact on the profitability of any business. As such, the field of measurement demands a highly technical language of definitions, acronyms, and symbols that must be fully understood and embraced by managers, supervisors, engineers, technicians, and operating personnel. The combination of the "roadmaps" (sources of uncertainty) for each flowmeter technology, the uncertainty estimations (USs), and the statistical weighting method are tools that can Identify error types and magnitude for the primary, secondary, Identify areas of improvement for existing facilities (upgrade Set achievable loss performance based on the invested resources Identify OPEX requirements for each flowmeter technology. Set priorities on OPEX resource allocation for each location. Set priorities on the loss investigation process. and tertiary devices. or replacement). (CAPEX). The author's desire is that the information contained in this handbook provides a clear presentation of the measurement principles, state-of-the-art technology, and its applications in the real world.
2017
Seismic methods play an important role in the exploration for hydrocarbon reservoirs. However, the success of the method depends strongly on the reliability of the measured or predicted information regarding the velocity of sound in the media. Speed of sound has been used to study the thermodynamic properties of fluids. In this study, experimental data are reported and analyzed on the speed of sound in toluene and octane binary mixture. Three-factor three-level Box-Benhkam design is used to determine the significance of each factor, the synergetic effects of the factors, and the most significant factors on speed of sound. The developed mathematical model and statistical analysis provided a critical analysis of the simultaneous interactive effects of the independent variables indicating that the developed quadratic models were highly accurate and predictive.
Spe Journal, 2007
Investigating the properties of live heavy oil, as pressure declines from the original reservoir pressure to ambient pressure, can aid in interpreting and simulating the response of heavy-oil reservoirs undergoing primary production. Foamy oil has a distinctly different and more complex behavior compared to conventional oil as the reservoir pressure depletes and the gas leaves solution from the oil. Solution gas separates very slowly from the oil; thus, conventional pressure/volume/temperature (PVT) measurements are not trivial to perform. In this paper, we present novel experiments that utilize X-ray computerized assisted technology (CT) scanning and low field nuclear magnetic resonance (NMR) techniques. These nondestructive tomographic methods are capable of providing unique in-situ measurements of how oil properties change as pressure depletes in a PVT cell. Specifically, this paper details measurements of oil density, oil and gas formation volume factor, solution gas/oil ratio, (GOR), and oil viscosity as a function of pressure. Experiments were initially performed at a slow rate, as in conventional PVT tests, allowing equilibrium to be reached at each pressure step. These results are compared to non-equilibrium tests, whereby pressure declines linearly with time, as in coreflood experiments. The incremental benefit of the proposed techniques is that they provide more detailed information about the oil, which improves our understanding of foamy-oil properties.
2013
Ultrasonic flow meters, as all velocity or inference type devices, require an adequate flow stream conditioning in order to assure an accurate performance. Typical flow conditioning consists of straightening the upstream and downstream of the measuring section. The upstream section usually contains a tube bundle, which allows the upstream section to be reduced in length. This tube bundle serves to eliminate any swirl in the flow stream before reaching the meter, presenting a symmetrical velocity profile to the turbine rotor. Some ultrasonic flow meters may produce a non-uniform pulse output, which can prove a wide span of repeatability. For such cases where is a need to correct the velocity flow profiles which affect the robustness of the integration method, this research work tries to develop a mathematical modeling and simulation in MATLAB and Microsoft Excel, with the purpose to combine the individual acoustic path measurements into a full volumetric flow rate measurement procedu...
In recent years, Colorado has seen ozone levels that exceed national ambient air quality standards with levels increasing at several sites. It is thought that volatile organic compound (VOC) emissions from the prevalent upstream oil and gas operations may contribute in part to these exceedances. In 2008, EPA Region 8 requested OAQPS assistance in quantifying VOC emissions from upstream oil and gas facilities as currently there is limited data, particularly regarding fugitive emissions, from this these operations. Oil and gas fields provide very challenging emission testing issues due to the large number and variety of emissions points including separators, dehydrators, generators, gas-powered pneumatics, injection wells, heaters, compressors/engines, storage tanks, and produced water ponds along with activities such as well drilling, well completion, well work over, and loading/unloading of oil/produced water into trucks. Though interested in VOC data for all these emission points, Region 8 wanted to first focus on quantifying VOC emissions from the produced water ponds. Our project team (EPA OAQPS, EPA ORD and their contractors, Region 8, Colorado, and Wyoming) chose to use EPA Other Test Method 10 (OTM 10), an optical remote sensing-based technique, with two open-path Fourier transform infrared (OP-FTIR) instruments in a four corners configuration to provide mass emission flux estimates for a representative alkane mixture. To supplement the alkane mixture flux assessment, FTIR spectra for select VOC compounds that were individually quantifiable were analyzed for concentration and reported as flux estimates using a ratio approach. VOC concentrations were determined at a point along two of the FTIR beam paths using summa canisters with EPA Method TO-14A and TO-15 analysis to provide additional information on the overall VOC emissions from the ponds. The data from this study is currently under internal review by EPA.
Ultrasonic flow meters, as all velocity or inference type devices, require an adequate flow stream conditioning in order to assure an accurate performance. Typical flow conditioning consists of straightening the upstream and downstream of the measuring section. The upstream section usually contains a tube bundle, which allows for the upstream section to be reduced in length. This tube bundle serves to eliminate any swirl in the flow stream before reaching the meter, presenting a symmetrical velocity profile to the turbine rotor. Some ultrasonic flow meters may produce a non-uniform pulse output, which can prove a wide span of repeatability. For such cases where is a need to correct the velocity flow profiles which affect the robustness of the integration method, this research work tries to develop a mathematical modeling and simulation in MATLAB and Microsoft Excel, with the purpose to combine the individual acoustic path measurements into a full volumetric flow rate measurement procedure. The relation between velocity and viscosity, using Reynolds Number, was calculated in Microsoft Excel. The Nusselt Number was then used to plot fluid mean temperature and wall temperature diagrams in Microsoft Excel.
This paper describes an 8-path ultrasonic flow meter, with emphasis on how this meter can be used as a master meter with traceability to appropriate standards. In particular the paper describes the methodology whereby transit time measurements and calibration factors can be established in factory and laboratory tests and then verified in the field. Simulations of distorted and swirling flows, and supporting test results are used to demonstrate the insensitivity of the 8-path configuration to installation effects.
This publication is a new entry in this catalog.
This standard is issued under the fixed designation D 1298; the number immediately following the designation indicates the year of original adoption or, in the case of revision, the year of last revision. A number in parentheses indicates the year of last reapproval. A superscript epsilon (e) indicates an editorial change since the last revision or reapproval.
2002
A "Handbook of uncertainty calculations-Ultrasonic fiscal gas metering stations" [1] has been developed in a cooperation between NFOGM, NPD and CMR, addressing fiscal metering of gas using multipath ultrasonic transit time flow meters (USM). The many different approaches to calculating the uncertainty of ultrasonic gas metering stations have been a source of confusion;-varying practice in this respect has definitely been experienced. The intention of the present initiative has been that a handbook together with a spreadsheet program EMU-USM Fiscal Gas Metering Station, based upon the principles laid down in the "Guide to the expression of uncertainty in measurement (GUM)" [2] and ISO/DIS 5168 [3], would satisfy the need for a modern method of uncertainty evaluation in the field of ultrasonic fiscal gas measurement. In the present work, calculation of the expanded uncertainty of the following four metering station measurands is addressed: the actual volume flow rate, the standard volume flow rate, the mass flow rate, and the energy flow rate. The analytical uncertainty model accounts for metering station instrumentation such as pressure transmitter, temperature element and transmitter, compressibility factor calculation (from gas chromatograph analysis), density measurement (vibrating element densitometer), calorific value measurement, and a flow calibrated multipath ultrasonic gas flow meter (USM). The expanded uncertainty of each of these measurands and instruments can be calculated and analyzed, isolated and combined (for the metering station). The basis for the Handbook and the program is described, together with an example of a metering station uncertainty evaluation.
This study investigated the relationship between velocity of sound and properties of natural gases under different equations of state and the operational implications on acoustic gas metering. The velocity of sound was related to the thermodynamic properties of natural gas using both the Soave-Redlich-Kwong (SRK) and Peng-Robinson (PR) equations of state and applied to 5 wet and 5 dry natural gas samples from the Niger Delta at different conditions of temperature and pressure. Predicted results were statistically analyzed and compared with experimental data. For wet gas, SRK and PR equations gave average absolute deviation (AAD) of 9.50% and 1.15% for velocity of sound respectively; while AAD of 0.943% and 7.021% were obtained for dry gas, using the SRK and PR equations respectively. Predictions of sonic velocity and gas properties using both SRK and PR tend to give higher accuracy at high pressures than at ambient pressures and temperatures suggesting that correction factors must b...
Journal of Fluids Engineering, 2014
Controlled flow rate tests using mixtures of crude oil and water at different mass fractions were carried out in a flow loop at the University of Tulsa. A noninvasive acoustic method developed at the Los Alamos National Laboratory (LANL) was applied to calculate the mass and volume fractions of oil and water in the mixed two-phase flow by measuring the speed of sound through the composite fluid mixture along with the instantaneous temperature. The densities and sound speeds in each fluid component were obtained in advance for calibration at various temperatures, and the fitting coefficients were used in the final algorithm. In this paper, we present composition measurement results using the acoustic technique from LANL for different mixture ratios of crude oil and water and at varying flow rates and a comparison of the results from the acoustics-based method with those from Coriolis meters that measured individual mass flow rates prior to mixing. The mean difference between the two metering techniques was observed to be less than 1.4% by weight and is dependent on the total flow rates. A Monte Carlo analysis of the error due to calibration uncertainty has also been included. Downloaded From: http://fluidsengineering.asmedigitalcollection.asme.org/ on 01/30/2014 Terms of Use: http://asme.org/terms
Flow Measurement and Instrumentation, 2020
The oil and gas markets are of fundamental importance to the world's scenario dealing with high value products. Several rules and regulations define the various operating procedures due to environmental, social, political, and financial impacts. Liquid and gaseous hydrocarbon measurement stations are inside this context, either in the transfer of ownership of the product (custody transfer) or for values calculation for tax purposes (fiscal measurement). This is a conservative application in the industry but one that cannot fail to introduce the new features provided by the advances of the fourth industrial revolution. Thus, this article, based on a broad bibliographic research based on a qualitative analysis, addresses the concepts of some technologies already available in the automation market and how they can be applied to these stations to provide a greater reliability through risk reduction.
Oil viscosity assessed from core samples can increase dramatically during core storage and the process of oil extraction from core. Accurate measurement of bitumen viscosity from core is crucial for targeting sweet spots, locating production wells, and developing an appropriate recovery strategy. Here we show that viscosity error may be due sample storage conditions, storage duration, bitumen extraction method, sample composition and contamination, type of viscometer and laboratory practices. The effects of oil evaporation are also discussed along with a method to normalize viscosity data collected over a number of years by using a storage time viscosity correction (STVC) for incorporation into a geological model for oil mobility mapping.
Geostandards and Geoanalytical Research, 2017
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2012
This paper presents a method of determining the volume fractions of two liquid components in a two-phase flow by measuring the speed of sound through the composite fluid and the instantaneous temperature. Two separate algorithms are developed, based on earlier modeling work by Urick , "A Sound Velocity Method for Determining the Compressibility of Finely Divided Substances," J. Appl. Phys., 18(11), pp. 983-987) and , "Velocity and Attenuation of Seismic Waves in Two-Phase Media: Part 1. Theoretical Formulations," Geophysics, 39(5), pp. 587-606). The main difference between these two models is the representation of the composite density as a function of the individual densities; the former uses a linear ruleof-mixtures approach, while the latter uses a nonlinear fractional formulation. Both approaches lead to a quadratic equation, the root of which yields the volume fraction (/) of one component, subject to the condition 0 / 1. We present results of a study with mixtures of crude oil and process water, and a comparison of our results with a Coriolis meter. The liquid densities and sound speeds are calibrated at various temperatures for each fluid component, and the coefficients are used in the final algorithm. Numerical studies of sensitivity of the calculated volume fraction to temperature changes are also presented.
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