click here for permission to reuse the content of this articlePipeline & Gas Journal July issue 1999:

 

Moving Toward Real Time

Natural Gas Flow 
Measurement In The 21st Century


by Edgar C. Bowles, Jr.
Section Manager,
Metering Research Facility At Southwest Research Institute
San Antonio, Texas

The traditional business arrangement between natural gas producers and transporters experienced a fundamental change in the 1990s due to government deregulation of the industry. Long-term agreements between gas producers and transporters were superceded by a commodity-based, supply-and-demand business. This paradigm shift placed greater importance on accurate, timely, and cost-effective gas measurement by gas transporters.

Accurate gas measurement by gas transmission pipeline operators has always been important to ensure fair and equitable transactions at custody transfer points, to allow efficient management of gas supplies and deliveries, to control inventory, to minimize unaccounted-for gas volumes, to avoid custody transfer disputes, and to provide customer satisfaction. Now, there is also a growing emphasis on the timeliness and cost-effectiveness of this measurement information. It is becoming necessary for gas measurement data to be provided instantaneously (or in “real time”) so that gas transporters can optimize pipeline operations, maximize system throughput and respond to rapidly changing market opportunities. Availability of this information to all departments of a company is also critical because nearly all aspects of a transporter’s business are affected, in some way, by gas measurement.

The cost of acquiring gas measurement data is a significant issue because capital costs associated with the installation of measurement systems and operating costs associated with the maintenance and upkeep of these systems can be quite high. For instance, a new, large-volume gas meter station may cost a million dollars or more to install. Today’s market pressures demand that capital and operating expenses be kept to a minimum. This includes gas measurement costs. One way gas transportation companies are trying to control costs is by applying new or improved gas measurement technology that offers the prospect of reduced capital or operating costs.

As the competitive market for natural gas continues to develop, what changes or improvements in measurement technology can we expect? It is apparent that the gas transportation companies that are quickest to acquire, process, and analyze gas measurement data in a cost-effective way will gain a distinct business advantage. What gas measurement technology will be available in the coming years to help companies gain this business advantage? Following is a brief preview of what we can expect.

Orifice Flow Meters
The number of orifice flow meters installed in the gas transmission pipeline network in the United States is in the tens of thousands and accounts for approximately 80 percent of the total. Therefore, we cannot ignore the importance of this measurement method as we look toward the future. Although this is a mature technology, advancements and improvements are still needed and are being made.

The primary focus of recent advancements has been the identification and elimination of measurement bias errors. There has been substantial research at the Gas Research Institute (GRI) Metering Research Facility (and elsewhere) on the effect of upstream piping configuration on orifice meter accuracy. The effects of flow conditioners have also been studied extensively. A flow conditioner is a device placed upstream of a flow meter that mitigates any adverse effects created by the upstream piping configuration. Some example flow conditioners are pictured in Photo 1.

Recent research has given us a better understanding of how measurement bias errors can be caused by the meter station installation configuration. We also have a better understanding of how different types of flow conditioners affect meter performance. This work has led to the pending revision of the American standard for orifice flow meters — the American Petroleum Institute (API) Manual of Petroleum Measurement Standards (MPMS), Chapter 14.3, Part 2. The revised standard[1] will provide more comprehensive guidance on orifice meter installation configuration. The revised standard is currently out for ballot by the API and is expected to be published later this year.

Future improvements in orifice metering will probably come via the secondary instrumentation systems — the pressure and temperature sensors and the data acquisition and storage system. With micro-sensor and microcomputer technology becoming more advanced, the pressure and temperature transducers and the data acquisition, storage, and transmission systems will become smaller, more capable, and less expensive. Integrated systems in which the measurement sensors and the data acquisition, storage, and transmission electronics are all contained in a single module may become the norm in the next few years. One example of how improvements in sensor technology may affect orifice meter configuration and performance is a new design developed under the auspices of the Gas Machinery Research Council. With this new meter design, differential pressure across the orifice is measured using small sensors embedded in the face of the orifice plate. Compared to conventional orifice meters, this new design provides superior responsiveness to fluctuations in gas flow rate. In addition, there are no gage line pressure effects to deal with, since the gage lines to an outboard pressure transducer have been eliminated.

Several other orifice meter designs have been proposed recently, although they have not yet gained broad acceptance. These alternate designs[2],[3] are all similar in that the orifice plate has multiple holes or slots, rather than a single hole in the center of the plate. The multiple-hole patterns are designed to make the flow element much less susceptible to errors caused by the upstream installation configuration.

Turbine Flow Meters
As with orifice meters, there are many turbine meters installed in gas transmission pipelines in the United States and this technology is relatively mature. Turbine meters account for approximately 5 percent to 10 percent of the total. However, there have been some recent developments in turbine flow meter technology. Meter manufacturers have recently expanded meter flow range, improved meter self-diagnostic capability, and improved wear life and durability of the rotating components.[4],[5] Changes in rotor geometry have resulted in extended flow range. Features such as onboard microprocessors and modems now allow meters to monitor their functionality and indicate when a problem develops. Sealed bearings and improved bearing materials have helped extend the useful life of the rotating components that are susceptible to wear failures. Further refinements in meter performance, self-diagnostics, and wear life may be forthcoming in the next few years.

New Flow Meter Technologies
Several new gas metering technologies have either recently come into the marketplace or are expected to come into the marketplace in the next few years. The most commercially successful new technology is the ultrasonic gas flow meter. An example of a multi-path ultrasonic meter is shown in Photo 2. The conventional ultrasonic meter design utilizes a time-of-flight measurement technique. It has only been within the past five years that ultrasonic meters have gained acceptance by gas transmission pipeline operators in the United States. Pipeline operators first used ultrasonic meters only as check meters. Ultrasonic meters are now being used in some custody transfer applications. The first reference document for ultrasonic gas flow meters[6] was a recommended practice published by the American Gas Association (A.G.A.) in June 1998.

Although ultrasonic gas metering technology continues to experience a growth in popularity, it is still a maturing technology. Meter manufacturers and researchers are working to better define the performance envelope of these meters. As manufacturers learn more about the operational characteristics of these meters and accumulate more field experience, they update component designs and improve manufacturing processes. The result is usually a meter with better performance characteristics and improved reliability. It is expected that this development trend will continue for several more years. Additional improvements are anticipated in the design and performance of the ultrasonic transducers, the self-diagnostic capabilities of the meter, and the manufacturing precision of the meter body and transducer mounting points. Consideration is also being given to designing ultrasonic meters with integral flow conditioners. The flow conditioner would properly shape the flow profile at the meter and minimize the number of ultrasonic transducers required to produce an accurate measurement. This approach could produce a meter that is less costly than conventional designs.

Currently, most ultrasonic meter users prefer to flow calibrate their meters before installation. Flow calibration helps correct for any measurement bias error not accounted for by dimensional measurements and static calibration. These errors may be introduced by the meter fabrication process (i.e., dimensional tolerance issues) or by the electronic timing circuitry in the meter (i.e., timing circuit tolerance issues). In the future, tighter control of manufacturing tolerances and better understanding of the interaction between the flow and the ultrasonic pulses may minimize the need for flow calibration.

Coriolis gas flow meters are just beginning to generate some interest as an alternative metering technology. Coriolis flow meters have a long and successful history in liquid flow measurement, but there is less experience in gas transmission pipeline flow measurement. There are two basic meter configurations—straight tube and curved tube.

The most likely niche for Coriolis flow meters in transmission pipelines appears to be high-pressure, low-volume applications. At present, there are few field meter installations in transmission pipelines in the United States. However, Coriolis meter manufacturers are conducting laboratory tests in the United States and Canada. Some field tests are also ongoing, primarily in other countries, such as Australia. In May 1999, the A.G.A. Transmission Measurement Committee agreed to initiate development of a gas industry standard for Coriolis gas flow meters.

Several other alternative gas flow measurement techniques are in various stages of development. Some of these techniques are proprietary and details cannot be divulged at this time, while others are so early in the development process that their future is uncertain. One measurement approach that deserves at least some mention is the laser-based optical method. Two different techniques that utilize this technology have been proposed to date. One proposal is to use a holographic approach to map the flow field in the pipeline. The other proposal is to use an array of micro-laser-Doppler velocimeters (configured in back-scatter mode) to measure gas velocity at many discrete points throughout the pipe cross-section.

The second approach is a byproduct of technology being developed by NASA’s Jet Propulsion Laboratory.[7] Both techniques are non-intrusive (only requiring optical access to the gas flow inside the pipe) and are made from low-cost components (e.g., laser-diodes or distributed feedback micro-lasers). The significance of this approach is that the flow field can be measured in greater detail than with other methods. This means there is potential for better measurement accuracy, even if significant distortions in the flow field (e.g., velocity profile asymmetry or swirl) exist.

One other pending development that may be significant in the not too distant future is the possible emergence of technologies that provide lower cost alternatives to gas chromatography for determining gas composition and heating value. Natural gas is bought and sold based on energy delivered per unit time (e.g., Btus per hour). Historically, energy flow rate has been determined by combining independent measurements of flow rate and heating value. A composition assay by gas chromatography is often performed to calculate heating value and gas properties (required to determine flow rate). A recent study funded by the U.S. Department of Energy[8] reviewed a number of energy rate measurement concepts and concluded that it may be possible to accurately characterize natural gas composition by the measurement of a small number of inferential variables (e.g., gas sound speed, carbon dioxide concentration, nitrogen concentration, etc.). This conclusion was based, in part, on previous GRI-funded research on the development of a new equation-of-state model for natural gas mixtures [9]. This approach, if successful, could be much less costly than conventional gas chromatography.

Other Considerations
Now that we have highlighted some of the recent or pending improvements in gas flow meters, let’s look at the bigger picture. The flow meter is only part of a system that provides gas measurement data. In addition to the flow meter, there is secondary instrumentation (e.g., pressure sensors, temperature sensors, gas densitometers, gas chromatographs, etc.) that provides supplemental measurements; a computerized data acquisition and transmission system that typically records, stores, and transmits the measured data; and a computer network that distributes the data throughout the company. Expect future system improvements to allow more gas measurement information to be delivered more quickly. Also, expect greater use of embedded microprocessors in measurement systems to help improve measurement accuracy, to speed the transfer/distribution of the measured data, and to expand self-diagnostic capability of the measurement equipment.

A potential benefit of improved information availability is that measurement data could be made available to both the gas transporter and the transporter’s customers. This scenario could reduce the likelihood of custody transfer disputes and eliminate the requirement for redundant measurement systems (i.e., check metering) at custody transfer points. Significant cost savings to transporters and their customers would result.

One limiting aspect of pipeline gas measurement is that the measurements are made at relatively few points on a gas transmission pipeline network. Measurements are typically made at custody transfer stations and other selected locations, such as near compressor stations. Measurement sites can be many miles apart. To better understand what is occurring in the pipeline between measurement sites, gas transmission companies are beginning to rely on computer modeling to supplement field measurement data. These computer models simulate the gas flow in pipelines by using numerical modeling techniques.

Measurement data acquired from the field are input as boundary conditions to the model. These predictive models can provide a more thorough understanding of system status. This additional information provided by the computer model can help pipeline operators increase operational efficiency, maximize system throughput, reduce operating costs, and ensure safe operation. Pipeline simulation codes continue to improve over time. It is anticipated that pipeline simulation modeling will become more commonplace as the computer codes become more powerful and easier to use.

Another critical aspect of gas measurement is industry standardization. Standardization of measurement equipment helps minimize equipment costs, provides improved interchangeability and commonality of hardware and software, and allows sharing of information between gas suppliers, transporters, and consumers. Standardization can also help new technology establish itself in the marketplace, as exemplified by ultrasonic flow meters and the recent publication of A.G.A. Report No. 9. Expect increased emphasis on gas measurement equipment standardization in the future.

Economic Impact Of New Or Improved Technology
The economic impact of new or improved gas measurement technology is difficult to quantify because there are not only direct benefits, but also many indirect benefits derived from good gas measurement. However, a 1999 GRI survey[10] of 10 interstate gas transmission pipeline companies operating in the United States reported that the companies expected to derive a tangible economic benefit of at least $14 million per year over the time period from 1997-2005 from GRI-supported research and development in gas measurement technology. Although the results of this survey do not represent the benefits to the industry as a whole, the findings do indicate that the value of technological advancement will be substantial.

Conclusions
In summary, as natural gas transmission pipelines continue to improve their operations, we can expect improvements in existing gas measurement technologies and the introduction of new measurement technologies. The focus will be on more cost-effective, accurate, and reliable measurement systems. Real-time measurement data will also be a goal of most gas transportation companies. Greater reliance on computer technology will be seen. Expanded use of embedded microprocessors in measurement systems should improve measurement accuracy, speed the transfer/distribution of the measured data, and enhance the self-diagnostic capabilities of the measurement equipment. Computer modeling of gas flow through transportation networks will supplement field measurement data and provide a more accurate view of system status/performance/safety.

All of these improvements should increase operational efficiency, maximize system throughput, reduce operating costs, and help ensure safe operation. Also, expect greater emphasis on industry standardization. This will help minimize equipment costs, provide improved interchangeability and commonality of hardware and software, and allow sharing of information between gas transporters and their consumers.

We have given a general preview of the changes that are expected in gas measurement technology in the coming years. Upcoming editions of P&GJ will present a series of articles featuring detailed information on specific technological advancements and new gas measurement devices. P&GJ

References

  1. Manual of Petroleum Measurement Standards, Chapter 14.3, Part 2 - “Specification and Installation Requirements for Concentric, Square-Edged Orifice Meters,” American Petroleum Institute, 1996.

  2. Morrison, G.L., et al., “Comparison of Orifice and Slotted Plate Flowmeters,” Flow Measurement Instrumentation, Vol. 5, No. 2, 1994.

  3. Laws, Elizabeth M., and Abdel K. Ouazzane, “Integrated Flow Conditioning and Flow Metering,” American Society of Mechanical Engineers, Fluids Engineering Division, Fluid Measurement and Instrumentation, Vol. 211, 1996.

  4. Peace, Daniel W., “Turbine Meters in Dirty Gas Applications,” Proceedings from the American Gas Association Operations Conference, Cleveland, OH, May 1999.

  5. Schieber, William M., “The Accutest, A Self-Proving Gas Turbine Meter,” Proceedings from the American Gas Association Operations Conference, Cleveland, OH, May 1999.

  6.  “Measurement of Gas by Multipath Ultrasonic Meters,” Transmission Measurement Committee Report No. 9, American Gas Association, June 1998

  7. Hoenk, Michael E., et al., “Microlaser Doppler Anemometers,” NASA Tech Briefs, August 1997.

  8. Behring, Kendricks A., et al., “A Technology Assessment and Feasibility Evaluation of Natural Gas Energy Flow Measurement Alternatives,” Final Report, Tasks A and B, U.S. Department of Energy Cooperative Agreement No. DE-FC21-96MC33033, January 1999.

  9. Savidge, Jeffrey L., “GRI Extended Thermodynamic Properties Computer Program,” Gas Research Institute, Chicago, IL, March 1989.

  10. “Impact Derived from GRI Technologies by Ten Interstate Gas Pipeline Companies,” Radian International LLC, Gas Research Institute Report No. GRI-99/0021, 1999.

 

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   Originally Posted  July 9,1999