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Page 175 of 977 Results 1741 - 1750 of 9762

G. Kok, N. Pelevic, A. Chiribiri, X. Milidonis, M. Nazir, M. Capstick, S. Drost, C. Poelma, T. Schaeffter
A calibrated physical flow standard for medical perfusion imaging

In the medical sector, various imaging methodologies or modalities (e.g. MRI, PET, CT) are used to assess the health of various parts of the bodies of patients. One such investigation is the blood flow or perfusion of the heart muscle, expressed as the (blood) flow rate normalized by the mass of the volume of interest, with unit mL/min/g. Currently there is no physical flow standard for the assessment and validation of myocardial perfusion imaging methodologies, resulting in a large proportion of medical diagnoses being inaccurate and highly dependent on the scanner type, software used and the clinical operator. In the EMPIR 15HLT05 PerfusImaging project a phantom simulating myocardial perfusion has recently been developed with which imaging modalities can be tested. In this paper the construction and validation of the phantom is described which involved several iterations with design updates, computational fluid dynamics simulations, 3D printing of the phantom, ultrasound imaging velocimetry and magnetic resonance imaging (MRI). Dynamic contrastenhanced MRI was performed to image the passage of a tracer through the phantom and estimate perfusion. Two flow models and associated data analysis methods to relate the measurement data with the reference flow rates are presented and discussed.

S. Wada, N. Furuichi, H. Hamada, T. Akama, T. Yamaguchi, S. Suzuki, S. Takatsuka
Experimental Study on Flow Rate Measurement Downstream of an Elbow Pipe using the Clamp-on ultrasonic Flowmeter

This paper presents experimental measurements using the clamp-on ultrasonic flowmeter. To obtain an uncertainty of flow rate measurement using the clamp-on ultrasonic flowmeter, experiments are carried out at the national standard calibration facility of water flow rate in Japan (the National Institute of Advanced Industrial Science and Technology, National Metrology Institute of Japan). Flow rate given by the clamp-on ultrasonic flowmeter is compared with the static gravimetric method using a tank system weighing 50 t. The uncertainty of the reference flow rate given by the 50 t weighing tank system is 0.060% (k = 2). The transducers of clamp-on ultrasonic flowmeter are mounted downstream of an elbow pipe. The length from the elbow to the transducers is five times of the pipe diameter and ten times of the pipe diameter, respectively. The curvature radius of the elbow is equal to the pipe diameter. Flow rate measurement is based on a time of flight of pulsed ultrasound. The multi-pass mode of the clamp-on ultrasonic flowmeter is used to measure the disturbed flow condition, and the number of ultrasound pass is up to four. The pipe is made of stainless steel with the outer diameter of 216.3 mm and the thickness is 6.5mm. The flow rate condition is from 100 m³/h to 700 m³/h. The results show that the clamp-on ultrasonic flowmeter using the multi-pass mode can measure the flow rate accurately, even if the velocity profiles are disturbed by the upstream elbow pipe.

I. B. S. Bispo, L. C. Pacifico, W. O. Chaves, N. M. Taira, P. J. S. Jabardo
Comparison of two different methods for calibration of Cole type Pitot tubes

The Cole type Pitot tubes (Pitot-Cole tubes) are widely used by water utility companies to map fluid flow velocity profile and thus measure the flow rate in pipelines. This technique is mainly used for on-site calibration of other kind of flow meters, such as electromagnetic or ultrasonic, particularly when removing the meter from the pipeline is somehow not feasible. Therefore, when using Pitot-Cole tubes for those purposes, the determination of the calibration coefficient (Cd) and its associated uncertainty contributes significantly to the results of such measurements.
This paper presents the description and comparison between the results of two different methodologies for calibration of Pitot-Cole tubes: in a wind-tunnel and in a towing tank. Comparisons were also performed for two configurations of the Pitot-Cole tube, with and without a central pin between the two pressure tips, in which the inclusion of this feature increases the measured differential pressure, leading to a set of more reliable measurements.
The obtained results demonstrate coherence and feasibility of the wind-tunnel calibration for normalized Reynolds numbers (RE/L) greater than 7×105. These results also show that a more precise value can be applied along distinct velocity ranges, individually for each Pitot-Cole tube, instead of employing the usual value of Cd = 0.869, used since Cole proposed this form of Pitot tube in 1896. Another major result shows that, for lower values of Re/L, a correction of the calibration coefficient is needed, in order to reduce the uncertainty associated to the measurement. This second result is especially important since the corresponding velocities are related to lower flow rates, in which their measurements are usually followed by larger uncertainty estimates.

A. N. Johnson, I. I. Shinder, J. B. Filla, J. T. Boyd, R. Bryant, M. R. Moldover, T. D. Martz
Non-Nulling Measurements of Flue Gas Flows in a Coal-Fired Power Plant Stack

Exhaust flows from coal-fired stacks are determined by measuring the flue gas velocity at prescribed points in the stack cross section. During the last 30+ years these velocity measurements have been made predominantly using Stype pitot probes. These probes are robust and inexpensive; however, S-probes measure only two components of the velocity vector and can give biased results if the stack flow has significant yaw and pitch angles. Furthermore, Sprobe measurements are time intensive, requiring probe rotation (or nulling) at each traverse point to find the yaw angle. The only EPA-sanctioned alternatives to the S-probe are 5-hole probes (i.e., the prism probe and spherical probe) that also require yaw-nulling. We developed a non-nulling technique applicable to the spherical probe and two custom designed 5-hole probes that reduce testing time and may improve measurement accuracy. The non-nulling technique measures all 3 components of velocity without rotating the probe. We assessed the performance of these 5-hole probes in a coal-fired stack at the high-load (16 m/s) and the low-load (7 m/s). For the spherical probes, the non-nulling results and the nulling results were in excellent mutual agreement (< 0.1 %). For the custom probes, the non-nulling and nulling results were inconsistent: the differences were 5% at the high load and 10 % at the low load. We speculate that the nulling data for the custom probes were flawed because the non-nulling data for all the probes accurately determined the yaw and pitch angles at high and low loads. Our results demonstrate that the non-nulling technique can accurately measure flue gas flows in a coal-fired stack.

N. Pedisius, A. Bertasiene
Reproduction of air velocity in the entrance region of the pipe

Information about the airflow development in pipes in the entrance region is still not thoroughly investigated due to the complexity and restricted access for experiments. However, the reproduction of air velocity values, as well as calibration of the devices, is usually made in free streams from the nozzles or in the entrance region of the channels (pipes). In this study, different flow regimes have been investigated using different air velocity measurement methods for mean velocity to define. Experimental and numerical results in the entrance region of the pipe and in the test chamber of higher dimensions give a broad spectrum of information about the developing flow. Ultrasonic anemometer (UA) installed into the entrance region of the aerodynamic test facility shows reliable and highly comparable results in a wide range of velocities with another non-intrusive method – laser Doppler velocimetry (LDA). Due to the fast response, it enabled to analyse fluctuations in the flow. The mean air velocity values were determined from the singe path sound propagation time in the pipe with a defined distance between the transducers placed at an angle of 45 degrees with the main axis. Local vortices identified in the flow might have influenced the low-frequency fluctuations and the scatter of measurement results. Moreover, high-frequency fluctuations found in the flow originated from the flow turbulence and the electronic or acoustic noise. The stabilisation of the entrance region and the boundary layer of the pipe influenced mean velocity value, velocity distribution and axial velocity development in different test sections of the pipe. Along with the recirculation zones in cavities of ultrasonic transducers they are the essential impact factors on velocity value defined.

Arnthor Gunnarsson, Jos van der Grinten, Mijndert van der Beek, Bodo Mickan
Primary Piston Prover Intercomparison Between PTB, VSL and FORCE Technology

The EuReGa members that use a Piston Prover as a primary calibration device (PTB, VSL and FORCE Technology) performed an intercomparison in 2018-2019. This paper will describe the Piston Provers used in the intercomparison after which the intercomparison results and their implication will be presented.
Degree of equivalence has been determined on multiple occasions in the past between the participants. What distinguishes this intercomparison from others is that it is performed with Piston Provers, which is the starting point in the respective participants traceability systems. This means that the CMC reported in the intercomparison is lower compared to previous intercomparisons between the participants, with reported CMC uncertainty between 0.07% and 0.086%. The traceability of the participants is independent from each other, since the results are directly traceable to the participants respective Piston Provers, the Piston Provers being primary calibration systems traceable to length.
EuReGa consists of four members with established traceability chains, LNE-LADG, PTB, FORCE Technology and VSL. LNE-LADG did not participate in the intercomparison because they use a PVTt system to establish their traceability.
The results support the CMC claims of the participants, showing that also at the starting point in the traceability, and therefore at the low end of the uncertainty spectre of the participants, there are acceptable differences between the members of EuReGa. The intercomparison report for this project has been submitted under EURAMET project no. 1301 which forms a basis for this report.

J. D. Wright, S. D. Sheckels, J. T. Boyd
Automated Substitution Weighing Apparatus for Liquid Volume Measurement

The custody transfer of petroleum worth $1 x 1012 / year is traced to the volume delivered from provers and liquid test measures. Mistakes as small as 0.02 % in a custody meter calibration can lead to multi-million dollar corrections in bills. NIST presently uses the direct weighing method to measure the volume delivered from a test measure, by weighing (on a calibrated balance) the test measure when it is full of pure water and again after it has been drained. Recently, NIST reduced the uncertainty of its calibrations of volumes between 3.8 L and 40 L by constructing an automated substitution-weighing standard. The new standard reduces the mass measurement uncertainty by alternately placing 1) the test measure (unknown mass) and 2) approximately equal reference masses on the balance. Automated, pneumatically-driven hardware moves heavy liquid-filled volumes and reference masses on and off the weigh scale, thereby protecting the operator’s safety and comfort. We describe the system’s design, operation, uncertainty, and repeatability. The new standard was validated by comparison to NIST’s well established direct weighing approach and by repeated calibration of a 38 L pipette during more than 2 years. The results are fully consistent with the 95 % confidence level uncertainty estimate of 0.007 % for the substitution weighing standard. Correlation between temperature and the volume of the 38 L pipette shows the need for improved environmental temperature control in the laboratory. We also describe the design of a set of four pipettes with an overflow filling system that can be used as references in an automated volume transfer standard.

J. D. Wright, J. W. Schmidt
Reproducibility of Liquid Micro-Flow Measurements

New applications in biology, medicine, and manufacturing require reliable measurements of liquid flows smaller than 100 μL/min. NIST addressed this requirement by improving the reliability and ease of use of NIST’s Dynamic Gravimetric Micro-Flow Standard. The meter under test is now connected to the weighing beaker by a liquid bridge that reduces variations in parasitic surface tension forces as the level of liquid in the collection beaker rises. We describe other improvements to NIST’s standard (e.g. pipette positioning and evaporation reduction) and provide an uncertainty analysis for the present system. The gravimetric standard measures liquid flow between 0.1 μL/min and 100 μL/min with uncertainty ranging from 4.5 % to 0.04 %. Repeated calibrations of five commercially available micro-flow meters (one for nearly 2 years) show that their calibrations are reproducible within 1.5 % for many months.

Chuanbo Zheng, Xingchuan Chen, Yiwen Liu, Wei Han, Zhe Liu
Study on Data Collection Methods of Natural Gas Flow Verification

Based on the different ways of data collection which adopted by the current domestic natural gas flow metering station, this paper first analyzes the theoretically applicability and limitations for two kinds of data collection methods: instantaneous flow and cumulative flow, and obtains the relation and distinction between these two ways. Then, the flow-meters with different diameters are actual tested in two data acquisition ways, instantaneous flow and cumulative flow, which performed by the work level standard device of substation in Guangzhou. The results show that the different methods of data collection have no evident impact on indication error but high effect on the repeatability of indication error.

Qingqiang Hou, Meng Yang, W. Han, J. H. Niu, K. C. Wu
The Discussion of Influence of the Inlet Temperature Measurement on the CFVN Calibration

When the CFVN calibration is carried out, the inlet temperature measurement of the CFVN is detailed described in both “ISO 9300:2005 Measurement of gas flow by means of critical flow Venturi nozzles” and “JJG 620-2008 Critical Flow Venturi Nozzle”. But in some cases, the sensing element can not be strictly confirmed to the requirement for some reasons. To explore the influence of the inlet temperature measurement, two different kinds of installation are presented in this paper. Differences between the two installations are the diameter of the sensing element and the location of the sensing element. As the results shown, the inlet temperature measurement has non-negligible influence on the CFVN calibration. According to the comparison, to ensure the accuracy and reliability of traceability, the CFVN should be calibrated under the same installation conditions as that on site. And both the interlaboratory measurement comparison and proficiency testing of CFVN should take the installation impact as an important factor if there are some differences.

Page 175 of 977 Results 1741 - 1750 of 9762