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1.
In recent years, the Coriolis mass flow meters (CMF), devices based on the Coriolis effect over a vibrating pipe, have developed better metrological performance and they are now a reasonable alternative for the custody transfer measurements. Nowadays, many custody transfer operations require measurement of the net volume (volume measured at a certain reference temperature) and, therefore, it is not feasible to use the CMF as a mass flow meter. However, the actual CMF can be used as net volume meters because they have special equipment to measure density and temperature, and a flow computer. In this work, firstly a mathematical simplification of the physical model is proposed for the CMF. We part from the dimensional analysis of the flow-phase relationship produced by the Coriolis force, the main physical principle behind these devices. A simplified formula is obtained and it permits identifying the magnitudes of influence of the CMF as a mass meter. Secondly, its metrological properties are characterized. For such purpose, a 4” straight tube commercial meter has been calibrated in volume, in the 50 to 165 m3/h range against a standard container and a bidirectional prover, employing gas oil and kerosene (JET-A1). These calibrations have turned out to be compatible with the ones performed by the manufacturer in mass and using water. Then it is verified that the CMF fulfills the requisites of the legal metrology: maximum error allowed, linearity and repeatability. Skewness is observed in the relative error (expressed in %) of the CMF and it has been researched to be due to systematic effects related to constructive parameters of the meter. Lineal correlation is verified between relative error and temperature, and between relative error and flow rate, with negative slopes of −0.03% °C−1 and −0.001% h/m3 respectively. 相似文献
2.
本文介绍弯管流量计确定标定数据的实验方法,尝试新的计算方法,得到较精确的标定数据. 相似文献
3.
Determining and reducing the measurement uncertainty of LNG energy transfer in custody transfer operations is considered extremely important and challenging for industry. The European Metrology Research Programme (EMRP) for Liquefied Natural Gas (LNG) has been focused on reducing the uncertainty in the evaluation of LNG energy transfers by improving existing measurement methods, validating new measurement methods and development of new traceable calibration systems. Part of this project was to produce realistic measurement uncertainty budgets and to determine the sensitivity of the overall LNG energy transfer uncertainty to changes in the composition and temperature of different LNG cargoes.This paper provides details on the development of an uncertainty budget and the results from the sensitivity study. It was found that the uncertainty in the LNG energy transfer ranged from 0.56% to 0.77% when using the uncertainty budget for 461 LNG cargoes. The variation was mainly due to the difference in the LNG composition and its associated uncertainty. 相似文献
4.
Increasing trade of liquefied natural gas (LNG) imposes stringent requirements for accurate flow rate measurement of this high energy content fluid. To satisfy this demand, a flow meter has been developed by CEASAME Exadebit which is based on velocity measurement behind a contraction nozzle using Laser Doppler Velocimetry technique (LDV). For this instrument, a calibration factor is defined relating the measured velocity to the flow rate. This calibration factor depends on the Reynolds number and it can be sensitive to the velocity profile behind the nozzle outlet and to presence of upstream flow disturbances such as bends, valves, etc. when the meter is installed on-site. In this paper, CFD modelling, using OpenFoam software, was employed to analyse the sensitivity of the calibration factor to flow disturbances for two types of disturbing elements; a U-bend and half-plate orifice. The CFD model was validated by comparison with experimental data for the calibration factor and velocity profiles obtained from preliminary LDV measurements with air. Two measurement setups were considered where the velocity is measured either in one point at the nozzle axis or integrated along a line across the nozzle diameter. The results show that the considered disturbing elements cause deviations in the calibration factor in the order of tenths of percent and that the maximal sensitivity of the line-setup to these disturbances is approximately half of the maximal sensitivity of the point-setup. On the other hand, it was shown that the line-setup is more sensitive to the LDV positioning than the point-setup. 相似文献
5.
A static weighing system for a liquid microflow calibration rig, whose minimum flow rate is 1 mg/min (equivalent to 1 μL/min for water), was designed and evaluated. The developed weighing system, which can collect over 10 g of water, has two features: (i) an automatic detachable device with a sealing and wiper mechanism in contact with a needle and (ii) a flexible air bag to contain the air from the weighing vessel. Having these two features, the weighing system succeeds in reducing the evaporation effect as well as preventing tension on the weighing scale. However, uncertainty due to the mass difference of adhering liquid on the outside surface of needle before needle insertion and after needle extraction should be considered. Theoretical and experimental analysis were conducted. The mass difference due to the adhering liquid on the needle was estimated to be smaller than 1/3 of the target standard uncertainty of mass measurement set at 0.1 mg, indicating that the detachable procedure was not a dominant uncertainty source for mass measurement. The evaporation rate during collection was experimentally estimated to be less than 0.001 mg/min, which corresponds to less than 0.1% for the lowest flow rate of 1 mg/min. 相似文献
6.
对微通道中液氮流动沸腾换热特性进行试验研究和分析。给出典型的沸腾曲线,分析壁温、干度和换热系数沿微通道管程的变化规律,考察热流密度、质量流量和压力对流动沸腾换热的影响。将126个试验数据点与四个换热关联式比较,并对微通道中流动沸腾换热机理进行分析。结果表明,在多数情况下干度和热流密度对沸腾换热系数的影响较小,换热系数主要决定于质量流量和压力,随两者增加而增加,换热以对流蒸发为主导机理。KLIMENKO关联式预测效果最好,TRAN微通道关联式次之,对常规管道得到广泛使用的CHEN关联式和SHAH关联式都远远高估了试验值。基于两相流压降和换热特性分析,推知微通道中的两相流流型不同于常规管道:在低干度情况下,流型以弥散泡状流为主;而在高干度情况下,流型以由雾状汽芯和不规则液膜组成的环状流为主。 相似文献
7.
微细通道内液氮流动沸腾的流型特性 总被引:1,自引:0,他引:1
采用高速摄像,得到内径为1.931 mm、1.042 mm、0.531 mm的竖直上升圆管内液氮流动沸腾的主要流型为泡状流、弹状流、搅拌流和环状流;并且在1.042 mm、0.531 mm管内发现受限气泡流。并绘制流型图,分析表面张力,压力和管径对流型转变的影响。表面张力是影响流型转变的重要物性参数,相对于空气—水的流型图,对应的弹状流/搅拌流,搅拌流/环状流流型转变线向较低的气体表观速度方向移动;而泡状流/弹状流的转变线向较高的气体表观速度方向移动。压力越高,相应的流型转变曲线向较低的气体表观速度方向移动。管径对流型转变有重要影响,随着管径的减小,相应的流型转变线向较低的气体表观速度方向移动。试验结果与通用的流型转变理论模型作比较,发现理论模型的预测结果与试验结果相差较大。 相似文献
8.
The calibration facility with the multi-nozzle calibrator was developed for the calibration of flow meters to be used with high-pressure, high-flow-rate hydrogen gas. The critical nozzles installed in the multi-nozzle calibrator were calibrated with traceability to the national standard. The relative standard uncertainty of the mass flow rates produced from the calibration facility is 0.09% when the flow rate is between 150 g/min and 550 g/min. In this study, the Coriolis flow meter was calibrated for a pressure range of 15–35 MPa. The relative standard uncertainty of the flow rates obtained from the Coriolis flow meter was 0.44% for the case of the worst fluctuations in the output of the flow meter; based on the calibration curve, this is 0.91%. The present result shows that there is a maximum 3% difference between the output of the Coriolis flow meter and the mass flow rates of the multi-nozzle calibrator, even though the Coriolis flow meter was calibrated using water. Therefore, for the development of a calibration facility that can calibrate a flow meter under the same conditions as those encountered in actual use, it will be important to develop a new flow meter. 相似文献
9.
Chris Y. Yuan Hong C. Zhang Gregory McKenna Carol Korzeniewski Jianzhi Li 《The International Journal of Advanced Manufacturing Technology》2007,34(7-8):657-666
Printed circuit board (PCB) recycling is an important challenge for today’s industry. This paper presents results from a study
of cryogenic decomposition as a potential alternative recycling method for obsolete printed circuit board scraps. In this
method liquid nitrogen is employed as a cryogen to form an environment as low as 77 K for PCB treatment. In order to test
the effect of thermal stress set-up during the rapid cryogenic treatment, impact tests were used to simulate the current shredding
process. The treated PCB scraps were investigated under a monocular microscope with a 200X magnitude for micro-crack effect
observation. Fatigue behavior of the boards was also examined by repeating the cryogenic treatment. The experimental results,
as analyzed, demonstrated no obvious support to this alternative PCB recycling method. The energy absorbed during the impact
tests for the cryogenically treated boards is insignificantly different from those without the treatment. 相似文献
10.
微通道中液氮的流动沸腾——两相流动压降分析 总被引:3,自引:0,他引:3
对液氮在直径为0.531 mm,加热长度为250mm的圆管中的流动沸腾压降和传热特性进行研究.作为第一部分,主要对微通道中液氮的两相流动压降进行试验研究与分析.结果表明:在核态沸腾起始时,质量流量迅速降低,而压降突然增大,并伴随着明显的温度滞后,幅度约为4.0~5.0 K.由于压降很大,在微通道内液氮的两相流动中会出现闪蒸,从而对质量干度产生重要影响.最后,利用均相模型和三个两相流动模型(L-M模型,Chisholm B系数模型和Friedel模型)对微通道沿程压降进行分析和比较.不同于常规通道的是,均相模型可以很好地预测压降试验结果,而三个两相流动模型的预测偏差较大,这是由于在微小通道中的高速流动情况下,汽相和液相混合比较均匀;同时液氮的液汽密度比很小,这也有利于均相模型的预测. 相似文献
11.
Kenichi Tezuka Michitsugu Mori Takeshi Suzuki Toshimasa Kanamine 《Flow Measurement and Instrumentation》2008,19(3-4):155-162
At hydraulic power stations, Pitot tubes have commonly been used to measure flow rates in steel penstocks for performance testing of hydraulic turbines. Due to the difficulties of Pitot tube installation, transit-time ultrasonic flow meters are becoming a popular replacement, but their accuracy is sensitive to velocity profiles that depend on Reynolds numbers and pipe surface roughness. Ultrasonic pulse Doppler flow meters have recently gained favor as suitable tools to measure flow rates in steel penstocks because they can measure instantaneous velocity profiles directly. Field tests were conducted at an actual hydraulic power plant using an ultrasonic pulse Doppler flow meter, and it was found capable of measuring velocity profiles in a large steel penstock with a diameter of over one meter and Reynolds number of more than five million. Furthermore, two ultrasonic transducers were placed on the pipe surface to validate the multi-line measurement of asymmetric flow. Each transducer recorded the velocity profile simultaneously from the pipe centerline to its far wall during plant operation. Velocity profiles were obtained from three-minute measurements to improve the accuracy of flow rate measurements. 相似文献
12.
In the early nineties a hot water test facility was planned and constructed for calibration and testing of volume and flow meters at the National Volume Measurement Laboratory at RISE (formerly SP Technical Research Institute of Sweden). The main feature of the test facility is the capability to measure flow in a wide temperature and flow range with very high accuracy. The objective of the project, which was initiated in 1989, was to design equipment for calibration of flow meters with stable flow and temperature conditions.After many years of international debate whether static testing is adequate to represent the later more dynamic application of domestic water meters, the EMPIR project 17IND13 Metrology for real-world domestic water metering (“Metrowamet”) was launched in 2018. The project investigates the influence of dynamic flow testing on the measurement accuracy of different types of domestic flow meters. One of the main objectives of the project is the development of infrastructure to carry out dynamic flow measurements. The existing test facility at RISE was at the time of construction one of the best hot and cold-water test facilities in the world. Due to the Metrowamet project the test facility has been upgraded to meet the needs of an infrastructure for dynamic flow investigations. The first findings from dynamic consumption profile measurements are reported in this paper. 相似文献
13.
14.
Calibration procedures and uncertainty analysis for a thermal mass gas flowmeter of a new generation
《Measurement》2016
This paper deals with the differences between traditional and new technology gas meters, and focuses specifically on the calibration procedure and uncertainty evaluation of CTTMFs (Capillary Type Thermal Mass Flow Meter). In particular, measurements performed on a sample set of commercial CTTMFs for natural gas in domestic/residential (G4) applications allowed to evaluate the modifications to calibration procedures required by the new generation, digital, gas flow meters. Indeed, traditionally natural gas is metered by means of volumetric measurement techniques, while the modern, static gas flow meters (thermal and ultrasonic ones) are based on electronic flow sensors. This implies that the gas volume through the meter is measured by sampling the flow rate at selected time points and integrating the flow rate in time. The measurement time becomes therefore an important parameter, thus requiring a thorough rethinking of the calibration procedure. In order to analyse the effects of the various parameters, a series of ad-hoc calibrations were performed. Specifically, one set of calibrations was performed with constant totalized volume, while the other required a constant measurement time. In order to highlight the novelties that will have to be implemented in ordinary calibration procedures to get the best of the new technologies, the two procedures as performed on a sample set CTTMFs will be compared; the theoretical (generic) evaluation of the associated uncertainty will also be presented. Measurements were carried out at the test facility of INRIM, the Italian National Metrology Institute. 相似文献
15.
This paper investigates the current challenges and practices of quality measurement in the oil & gas industry. It particularly focuses on automatic pipeline sampling of petroleum liquids according to ISO 3171. The problem is tackled using innovative diagnostic techniques, advanced design optimisation tools and a new mixing system that uses a Liquid Jet In Cross Flow (LJICF) configuration. First, a 2.5″ diameter small multiphase flow loop (SMPFL) was developed and magnetic resonance (MR) was utilised to characterise the mechanistic behaviour of mixing and the mixing efficiency of various nozzles. Second, a computational fluid dynamics (CFD) model was developed and validated using MR measurements on the SMPFL. The CFD model was then used to optimise the nozzle design as well as the design of a 10” nominal diameter large multiphase flow loop (LMPFL). The LMPFL is a well instrumented facility and was used to conduct mixing experiments on low velocity, low density and low viscosity fluids flowing in a horizontal pipe, which constitute challenging conditions for a mixing device to create homogeneous mixture. To quantify the homogeneity of the mixture created by the new mixing system on the LMPFL, a multiport profile proving (MPP) technique was developed and used to conduct water injection testing in compliance with ISO 3171 and API 8.2 standards. The water volume fraction (WVF) determined by the MPP had low relative error when compared to the mean WVF measured by the water cut meters and samples analysed using Coulometric Karl-Fischer (KF). Additionally, in an earlier study [1], the MPP measurement was able to detect a density gradient across the diameter of the pipe, making it an appropriate method to judge the homogeneity of the mixture. Therefore, the new mixing system together with the MPP technology shows real promise as an effective sampling and proving system for the petrochemical industry. 相似文献
16.
17.
Flow instability in LRE (liquid rocket engine) occurs due to various reasons such as flow interactions with valve, orifice
and venturi, etc. The inception of cavitation, especially in the propellant feeding system, is the primary cause of mass and
pressure oscillations because of the cyclic formation and depletion of cavitation. Meanwhile, the main propellant in a liquid
rocket engine is the cryogenic fluid, which properties are very sensitive to temperature variation. And the change of propellant
properties to temperature variation by thermodynamic effect needs to be properly taken into account in the flow analysis in
order to understand basic mechanisms for cryogenic cavitation. The present study focuses on the formation of cryogenic cavitation
by using the IDM model suggested by Shyy and coworkers. The flow instability was also numerically investigated in the downstream
of orifice with a developed numerical code. Calculation results show that cryogenic cavitation can be a primary source of
flow instability, leading to mass fluctuations accompanied by pressure oscillations. The prediction of cavitation in cryogenic
fluid is of vital importance in designing a feeding system of an LRE.
This paper was recommended for publication in revised form by Associate Editor Jun Sang Park
Changjin Lee received his B.S. and M.S. degrees in Aeronautical Engineering from Seoul National University in 1983 and 1985. He then went
on to receive his Ph.D. degree from University of Illinois at Urbana- Champaign in 1992. Dr. Lee is currently a Professor
at the department of Aerospace Engineering at Konkuk University in SEOUL, Korea. His research interests are in the area of
combustion instabilities of hybrid, liquid rocket and jet propulsions.
Tae-Seong Roh received his B.S. and M.S. degrees in Aeronautical Engineering from Seoul National University in 1984 and 1986. He then went
on to receive his Ph.D. degree from Pennsylvania State University in 1995. Dr. Roh is currently a Professor at the department
of Aerospace Engineering at Inha University in Incheon, Korea. His research interests are in the area of combustion instabilities,
rocket and jet propulsions, interior ballistics, and gas turbine engine defect diagnostics. 相似文献
18.
Within the framework of a research project regarding investigations on a high-pressure Coriolis mass flow meter (CMF) a portable flow test rig for traceable calibration measurements of the flow rate (mass - and volume flow) in a range of 5 g min−1 to 500 g min−1 and in a pressure range of 0.1 MPa to 85 MPa was developed. The measurement principle of the flow test rig is based on the gravimetrical measuring procedure with flying-start-and-stop operating mode. Particular attention has been paid to the challenges of temperature stability during the measurements since the temperature has a direct influence on the viscosity and flow rate of the test medium. For that reason the pipes on the high-pressure side are double-walled and insulated and the device under test (DUT) has an enclosure with a separate temperature control. From the analysis of the first measurement with tap water at a temperature of 20 °C and a pressure of 82.7 MPa an extensive uncertainty analysis has been carried out. It was found that the diverter (mainly due to its asymmetric behaviour) is the largest influence factor on the total uncertainty budget. After a number of improvements, especially concerning the diverter, the flow test rig has currently an expanded measurement uncertainty of around 1.0% in the lower flow rate range (25 g min−1) and 0.25% in the higher flow rate range (400 g min−1) for the measurement of mass flow. Additional calibration measurements with the new, redesigned flow test rig and highly viscous base oils also indicated a good agreement with the theoretical behaviour of the flow meter according to the manufacturers׳ specifications with water as test medium. Further improvements are envisaged in the future in order to focus also on other areas of interest. 相似文献
19.
Coriolis mass flowmeters are used for many applications, including as transfer standards for proficiency testing and liquified natural gas (LNG) custody transfer. We developed a model to explain the temperature dependence of a Coriolis meter down to cryogenic temperatures. As a first step, we tested our model over the narrow temperature range of 285 K to 318 K in this work. The temperature dependence predicted by the model agrees with experimental data within ± 0.08 %; the model uncertainty is 0.16 % (95 % confidence level) over the temperature range of this work.Here, basic concepts of Coriolis flowmeters will be presented, and correction coefficients will be proposed that are valid down to 5 K based on literature values of material properties. 相似文献
20.
Shane Y. Hong 《Machining Science and Technology》2013,17(1):133-155
ABSTRACT Cryogenic machining is considered an environmentally safe alternative to conventional machining where cutting fluid is used. In cryogenic machining, liquid nitrogen (LN2) is well recognized as an effective coolant due to its low temperature, however, its lubrication effect is less well known. Our previous studies of the change in cutting forces, tool wear, chip microstructure, and friction coefficient indicate a possible lubrication effect of LN2. This paper proposes two mechanisms on how LN2 can provide lubrication in the cutting process. To verify these proposed LN2 mechanisms and distinguish them, idealized disk-flat contact tests were performed. A low temperature can alter the material properties and change the friction coefficient between the specimens. However, from the test results, this lubrication mechanism was dependent on the material pairs. An uncoated carbide insert with a low carbon steel or titanium alloy disk test showed reduction of friction under LN2 cooling, but a coated insert increased the friction force. LN2 injection to form a physical barrier or hydrodynamic effect between two bodies is always effective in reducing the friction force. 相似文献