Novel mass air flow meter for automobile industry based on thermal flow microsensor. II. Flow meter,test procedures and results

A prototype of mass air flow meter for automobile industry was developed on the basis of thermal flow microsensor. Design and manufacturing technology of the flow meter are described. Test procedure and results are presented. Developed prototype of flow meter can diagnose gas flow rates in a wide range.     

基于三轴加速度探头的涡街湿气分相流量测量

针对涡街湿气测量过读问题,提出了基于加速度检测的涡街过读校正和分相流量测量方法。设计了高频响三轴加速度探头,分别对敏感元件、探头尺寸和封装进行了优化设计。干气标定结果表明,在4.43×10⁴～1.81×10⁵雷诺数范围内,测量精度为±1.0%,线性度为1.06%。然后,在不同湿气工况(载气压力和流量、液相流量)下测试了输出频率和加速度幅值特性,以气、液相韦伯数为参数,分别建立了涡街过读和两相加速度幅值模型。最后,联立两方程建立了湿气测量模型,并利用牛顿迭代算法进行求解。预测结果表明,气相测量误差在±1.0%以内,不确定度0.46%,液相全量程误差在±15%以内,不确定度10.04%。与未过读校正时最大8%的测量误差相比,气相测量精度大大提升,同时实现了湿气中分相流的在线测量。     

The Coriolis mass flow meter as a volume meter for the custody transfer in liquid hydrocarbons logistics

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.     

Development, modeling and certain investigations on thermal mass flow meters

This paper discusses a thermal mass bypass flow meter giving details of its design, principle of operation, calibration, and testing of effects of ambient temperature and orientation. Results of a computer model of the meter are also given.     

Performance evaluation of Coriolis mass flow meter in laminar flow regime

In many fluid flow applications, mass flow rate is preferred over volume flow rate, as it is more beneficial in terms of cost and material balance calculations. Coriolis mass flow meter (CMFM) is accepted widely for mass flow measurement owing to its accuracy and reliability. However, it has been found to under-read the mass flow rate in laminar flow region [1], thus limiting its application in this region. The secondary flow in the curved tube section influences the generated Coriolis force and leads to a deviation in meter readings. Commercial CMFMs are available with various curved tube configurations and need to be analyzed for their application in laminar region. This paper presents comprehensive experimental and numerical investigations performed to evaluate the influence of tube configuration and other meter parameters, such as drive frequency, amplitude of vibration, and sensor position, on the performance of the CMFM in laminar region. The findings of this study have put forth a suitable combination of tube configuration, drive frequency, and sensor position while using the CMFM in laminar flow regime.     

Horizontally installed cone differential pressure meter wet gas flow performance

Differential pressure (DP) meters which utilise a cone as the system’s primary element are increasingly being used to measure wet natural gas flows (i.e. mixtures of natural gas, light hydrocarbon liquids and water). It is therefore important to understand this meter’s response to wet natural gas flows. Research into the wet gas response of the horizontally installed cone DP meter is discussed in this paper. Consideration is given to the significant influence of the liquid properties on wet gas flow patterns and the corresponding influence of the flow pattern on the cone DP meter’s liquid phase induced gas flow rate prediction error. A wet natural gas flow correlation for 4 in. 0.75 beta ratio cone DP meters with natural gas, hydrocarbon liquid and water flow has been developed from multiple data sets from three different wet gas flow test facilities. This corrects the liquid induced gas flow rate prediction error of a wet gas flow up to a Lockhart–Martinelli parameter of 0.3, for a known liquid flow rate of any hydrocarbon liquid/water ratio, to ±4% at a 95% confidence level.     

逆流冷凝塔热泵系统热质交换过程数值模拟研究

冷凝塔作为冷凝式热泵系统的重要组成部分,其热质交换过程对于降低能耗及热泵系统设计具有重要意义.以逆流冷凝塔热泵系统形式为基础,通过建立冷凝塔内热质交换过程的数学模型,推导出热质交换过程的通用计算方程组,并以贵阳地区的气象参数为参考,对不同工况下塔内热质交换情况进行模拟计算及具体分析.研究结果表明,不同入口空气参数对溶液...     

差压式流量传感器测量一般气体流量时的温度压力补偿方法

简要介绍使用差压式流量传感器进行一般气体流量测量时的温压补偿方法;指出了差压方式流量传感器测量一般气体的通用流量温压补偿公式,并写出了公式的推导过程;与线性流量传感器温压补偿方法进行对比,强调指出了采用差压式流量传感器时进行温压补偿的注意要点.对公用工程中的一般气体的流量计量工作有一定的指导作用.     

A V-Cone meter measurement correlation in low pressure wet gas based on Chisholm model

To gain a deeper understanding of the performance of V-Cone meter in low pressure wet gas measurement, the over-reading of the V-Cone meter was experimentally investigated in the present study. The equivalent diameter ratio of the V-Cone meter is 0.55. The experimental fluids were air and tap water. The operating pressure and the gas volume fraction ranged from 0.1 MPa to 0.4 MPa and 97.52%–100%, respectively. The results showed that the existing V-Cone wet gas correlation, which was developed for the medium and high pressure wet gas cannot be well extended to the low pressure conditions. The Chisholm exponent monotonically decreased with the ratio of liquid-to-gas mass flow rate increasing, and was almost not affected by the gas to liquid density ratio and the gas densiometric Froude number in the present test ranges. A measurement correlation dedicated for the low pressure wet gas was developed. In the present cases, the relative deviation of the gas mass flow rate predicted by the new correlation was within ±4.0% and ±3.0% under the 95% and 90% confidence level, respectively; the average relative deviation was 0.046%. Our results provide insights into the measurement performance of V-Cone meter in low pressure wet gas and may help to develop a more comprehensive wet gas correlation.     

Coriolis mass flow measurement of gas under normal conditions

This paper presents a new method of directly measuring the mass flow of gas using the well-known Coriolis principle, which has proved successful for mass flow measurement of liquids. The prototype consists of two U-shaped tubes, forming a device resembling very much a tuning fork, which is stimulated by electromagnetic actuators to perform autonomous bending oscillations. By this means the fluid is subjected to a radial velocity that, in combination with the axial velocity of the flow, induces harmonic Coriolis forces of the same frequency. This causes the U-shaped tube to perform torsional oscillations that superimpose on the bending oscillations. Both oscillations can be detected via electromagnetic transducers.

The amplitude of the torsional oscillation induced by the Coriolis forces is very small as the density of gas is very low. It can be amplified by tuning the eigenfrequencies of torsion and bending in a control loop. This results in an amplification of the torsional amplitude by a factor of 10², allowing the mass flow of gas to be measured under normal conditions.     

Burnett simulations of gas flow and heat transfer in microchannels

In micro- and nanoscale gas flows, the flow falls into the transition flow regime. There are not enough molecule collisions and the gas deviates from the equilibrium. The Navier-Stokes equations fail to describe the gas flow in this regime. The direct simulation Monte Carlo method converges slowly and requires lots of computational time. As a result, the high-order Burnett equations are used to study the gas flow and heat transfer characteristics in micro- and nanoscale gas flows in this paper. The Burnett equations are first reviewed, and the augmented Burnett equations with high-order slip boundary conditions are then used to model the gas flow and heat transfer in Couette and Poiseuille flows in the transition regime.     

Calibration procedures and uncertainty analysis for a thermal mass gas flowmeter of a new generation

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.     

Model analysis for differential pressure two-phase flow rate meter in intermittent flow

Multiphase flow rate metering is a challenging problem, specially for flow patterns other than wet-gas. This paper brings forward a new comparative analysis of three differential pressure calibration models suited for liquid dominated two-phase flows, in a total of seven model configurations. First, the models are compared theoretically and classified in terms of the type of input data required. Then, experimental data of over 300 horizontal air–water experiments, for $1$” and $2$” pipe diameters, supports quantitative analyses of the prediction accuracies and sensitivity of the superficial velocities of gas and liquid to measurement errors in the model input variables. Finally, a method for assessing the decoupled measurement errors for the void fraction and gas velocity is shown, as these variables are typically subject to higher uncertainties. It results that, though the void fraction is shown to be systematically under evaluated in more than 10%, the total mass flow rate is estimated through the Paz et al. (2010) model with an overall root mean squared deviation (RMSD) of 5.75% for the $2$” data. Also, the use of gas velocity measurements, even if subject to considerable errors, decreased the RMSD for the gas superficial velocity by more than half for the $1$” data.     

Analysis of conjugate heat transfer and turbulent flow in mechanical seals

A numerical investigation of conjugate heat transfer of turbulent flow within a mechanical seal chamber is presented. The computational model takes into account the heat generation at the contact interface between the rotating ring and the stationary ring, heat conduction into the rings, and heat convection into the surrounding fluid in the chamber. Correlations are developed for predicting the average heat transfer coefficient on the wetted outer surfaces of the seal rings assuming that the flow in the seal chamber is turbulent.     

新型脉冲式热流计分析研究

现有热流计都需要流量计来计量流量.流量计很容易损坏并产生计量误差.为了解决这一问题,依据能量守恒提出了一种新型热量计,并对该装置的测量原理进行了理论分析和数值模拟,从而实现了只测量温差的情况下测出用户消耗的热量,摆脱了流量对测量结果的影响,从模拟和理论分析证明本方法能够较准确的计量热量值.     

Wet gas metering with a horizontally mounted Venturi meter

Wet gas metering is becoming an increasingly important problem to the Oil and Gas Industry. The Venturi meter is a favoured device for the metering of the unprocessed wet natural gas production flows. Wet gas is defined here as a two-phase flow with up to 50% of the mass flowing being in the liquid phase. Metering the gas flowrate in a wet gas flow with use of a Venturi meter requires a correction of the meter reading to account for the liquids effect. Currently, most correlations in existence were created for Orifice Plate Meters and are for general two-phase flow. However, due to no Venturi meter correlation being published before 1997 industry was traditionally forced to use these Orifice Plate Meter correlations when faced with a Venturi metering wet gas flows. This paper lists seven correlations, two recent wet gas Venturi correlations and five older Orifice Plate general two-phase flow correlations and compares their performance with new independent data from the NEL Wet Gas Loop with an ISA Controls Ltd. Standard specification six inch Venturi meter of 0.55 beta ratio installed. Finally, a new correlation is offered.     

基于多尺度加权形态网络的燃气流量计健康状态评估

燃气流量计是天然气贸易计量的重要仪器,而其健康状态的改变会造成计量偏差。为了减少燃气企业的经济损失,本文提出了一种基于多模态数据扩充、形态学特征学习和多尺度自适应加权形态学网络的燃气流量计健康状态评估方法。首先,采用基于Wasserstein距离和谱归一化的ACGAN算法进行数据扩充。其次,针对燃气流量计振动信号数据的复杂性和噪声影响,提出了一种基于平均帽变换的形态学方法提取信号的正负脉冲信息。最后,针对非平稳、变工况的工业条件,引入多尺度自适应加权形态学网络,采用具有不同结构元素尺度的多个分量来分别提取脉冲信息,并利用自适应加权融合来增强提供强脉冲分量的尺度。通过实验结果表明,所提出的方法对燃气流量计健康状态评估的准确度超过94%。该方法对实际燃气贸易计量有重要的应用价值。     

新型正弦行星齿轮流量计的三维实现及流量脉动分析

根据正弦函数曲线类比推导出了正弦齿轮的直角坐标方程,利用CAXA电子图板2007的公式曲线功能和Pro/E软件建立了正弦齿轮和流量计的三维模型。为了探究正弦行星齿轮流量计的测量精确性,进行了流量脉动分析,分析结果表明:该流量计比渐开线齿轮流量计具有更小的流量脉动率。     

微小缝隙式层流流量计设计及测量特性研究

为解决层流流量计(LFM)线性度不佳的问题,提出了一种微小缝隙式LFM,并介绍了层流流量计的测量原理、结构设计及参数计算。对一台设计流量范围约为0～280 mL/min的试验件进行了试验,试验中使用的标准装置为活塞标准装置,合成不确定度为0.12%,扩展不确定度为0.24%(k=2)。试验结果显示,在未使用任何修正系数的前提下,试验件最大引用误差为-0.90%。试验件基本达到准确度1.0级的设计指标,量程比10∶1。此外试验件线性度优良,其Re_(max)d_e/l值为3.42,大于传统要求的2～2.5,说明此结构设计可有效克服突扩突缩带来的非线性影响。     

Analysis of high pressure tests on wet gas flow metering with a Venturi meter

This work deals with the flow metering of wet gas issued from high pressure natural reservoirs. Some recent results obtained from tests performed on the CEESI facilities are presented. They are performed at 75 bar with 0.6 beta ratio Venturi meter installed in horizontal pipe configuration. Correction factors obtained are compared to predictions deduced from the flow modelling inside of the meter. These results are analysed in order to explain the agreements or disagreements obtained between the experiments and the flow modelling.