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1

DHIWAR, AARTI. "Study About Venturi Meter." INTERANTIONAL JOURNAL OF SCIENTIFIC RESEARCH IN ENGINEERING AND MANAGEMENT 09, no. 02 (2025): 1–9. https://doi.org/10.55041/ijsrem41495.

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Venturi meters are indispensable flow measurement devices used across a range of industries because of their accuracy and reliability. This paper comprehensively explores venturi meters, encompassing their working principle based on Bernoulli's theorem, distinct components, various types categorized by orientation and design, potential defects affecting performance, diverse applications ranging from water management to industrial processes, and a balanced discussion of their advantages and disadvantages. Proper selection, installation, and maintenance ensure the proper working of a venturi met
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2

Pham, T. M., J. M. Michel, and Y. Lecoffre. "Dynamical Nuclei Measurement: On the Development and the Performance Evaluation of an Optimized Center-Body Meter." Journal of Fluids Engineering 119, no. 4 (1997): 744–51. http://dx.doi.org/10.1115/1.2819493.

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This work is concerned with the development of a center-body venturi for nuclei measurements of novel design, the Venturix. Our project aims to: 1. Define a specially tailored geometry for cavitation nuclei measurement. This design study takes into consideration the following main aspects: the venturi mean flow in subcavitating regime, the viscous effects, the bubble dynamics. 2. Evaluate the performance of the meter: After testing the proposed design concepts, the venturi operating characteristics, in particular its operational limits, are assessed. Finally, the performance of the acoustic me
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3

Ighalo, Joshua O., and Queendarlyn A. Nwabueze. "An Analysis of Flow Measuring Mechanisms to Arbitrate Losses in Bends and Fittings for Analogous Operations." Petroleum Technology Development Journal 10, no. 1 (2020): 4–13. https://doi.org/10.5281/zenodo.3870453.

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Measurement, monitoring and analysis of fluid flow are important procedures in the process industry. The focus of this study was to analyse the flow measuring mechanism officiated to arbitrate shrinkages in bends and fittings owing to analogous operations. The results were computed by a flow analysis of the system based on the head loss of each respective equipment. The bends and fittings considered were the venturi meter, orifice meter, rotameter, diffuser, and right-hand bend. It was observed that the venturi meter is the most defined estimating equipment for the measurement of flow owing to
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4

Bober, W., and W. L. Chow. "Nonideal Gas Effects for the Venturi Meter." Journal of Fluids Engineering 113, no. 2 (1991): 301–4. http://dx.doi.org/10.1115/1.2909496.

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A method for treating nonideal gas flows through a venturi meter is described. The method is an extension of a previous study reported in an earlier paper. The method involves the determination of the expansion factor which may then be used to determine the mass flow rate through the venturi meter. The method also provides the means for determining the critical pressure ratio as well as the maximum flow rate per unit throat area. The Redlich-Kwong equation of state is used, which allows for closed form expressions for the specific heat at constant volume and the change in entropy. The Newton-R
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5

J. A. Replogle and B. Wahlin. "Venturi Meter Constructions for Plastic Irrigation Pipelines." Applied Engineering in Agriculture 10, no. 1 (1994): 21–26. http://dx.doi.org/10.13031/2013.25822.

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6

Yanagihara, S. "Variable area venturi-type exhaust gas flow meter." JSAE Review 20, no. 2 (1999): 265–67. http://dx.doi.org/10.1016/s0389-4304(99)00003-x.

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7

Huang, Si, Peng Wang, and Yu Hui Guan. "Theoretical and Experimental Study on Oil-Water Two-Phase Flow in a Downhole Venturi Meter." Applied Mechanics and Materials 232 (November 2012): 284–87. http://dx.doi.org/10.4028/www.scientific.net/amm.232.284.

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This paper presents a study on an oil-water two-phase flow model in a downhole Venturi meter by theoretical calculation, numerical simulation and experimental testing. The flow field and pressure characteristics with different flow and oil-water ratios in Venturi tube are investigated. It is found that the flow is stratified in the Venturi tube, the water phase accumulates in the tube center and the oil phase concentrates on the wall; the pressure drop is increased with flow; theoretical and numerical results are verified by experimental data.
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8

d’Agostino, L., and A. J. Acosta. "A Cavitation Susceptibility Meter With Optical Cavitation Monitoring—Part One: Design Concepts." Journal of Fluids Engineering 113, no. 2 (1991): 261–69. http://dx.doi.org/10.1115/1.2909490.

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This work is concerned with the design of a Cavitation Susceptibility Meter based on the use of a venturi tube for the measurement of the active cavitation nuclei concentration in water samples as a function of the applied tension. The operation of the Cavitation Susceptibility Meter is analyzed and the main considerations leading to the proposed design are illustrated and critically discussed. The results of this analysis indicate that the operational range is mainly limited by nuclei interference, flow separation and saturation (choking), and suggest to develop a Cavitation Susceptibility Me
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9

Dindorf, Ryszard. "Measurement of Pneumatic Valve Flow Parameters on the Test Bench with Interchangeable Venturi Tubes and Their Practical Use." Sensors 23, no. 13 (2023): 6042. http://dx.doi.org/10.3390/s23136042.

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A test bench with interchangeable venturi tubes was built to automatically measure the flow parameters of pneumatic valves of a wide range of sizes. This measuring stand contained components recommended by the ISO 6358 standard, an individually configured flow meter circuit, and HMI measurement and control panels. The flow meter circuit, individually configured with interchangeable venturi tubes, bypass loops, and Setaram thermal microflow meter, was calibrated using Molbloc/Molbox equipment. The tuning curve and theoretical flow rate characteristics of the tested valve were fitted to the flow
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10

Rosa, Euge^nio S., and Rigoberto E. M. Morales. "Experimental and Numerical Development of a Two-Phase Venturi Flow Meter." Journal of Fluids Engineering 126, no. 3 (2004): 457–67. http://dx.doi.org/10.1115/1.1758267.

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An algebraic model is developed access the gas and the liquid flow rates of a two-phase mixture through a Venturi tube. The flow meter operates with upward bubbly flows with low gas content, i.e., volumetric void fraction bellow 12%. The algebraic model parameters stem from numerical modeling and its output is checked against the experimental values. An indoor test facility operating with air-water and air-glycerin mixtures in a broad range of gas and liquid flow rates reproduces the upward bubbly flow through the Venturi tube. Measurements of gas and liquid flow rates plus the static pressure
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11

Steven, R. N. "Wet gas metering with a horizontally mounted Venturi meter." Flow Measurement and Instrumentation 12, no. 5-6 (2002): 361–72. http://dx.doi.org/10.1016/s0955-5986(02)00003-1.

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12

He, Denghui, and Bofeng Bai. "Numerical investigation of wet gas flow in Venturi meter." Flow Measurement and Instrumentation 28 (December 2012): 1–6. http://dx.doi.org/10.1016/j.flowmeasinst.2012.07.008.

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13

d’Agostino, L., T. Pham, and S. Green. "Comparison of a Cavitation Susceptibility Meter and Holography for Nuclei Detection in Liquids." Journal of Fluids Engineering 111, no. 2 (1989): 197–203. http://dx.doi.org/10.1115/1.3243623.

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This work compares the results obtained from a Cavitation Susceptibility Meter (CSM) and from direct holographic observations for the detection of cavitation nuclei in tap water samples. The CSM uses a cavitating venturi tube to measure the concentration of active cavitation nuclei as a function of the pressure at the venturi throat, while the holographic system measures the nuclei concentration size distribution. Microbubbles are used as the dominant type of cavitation nuclei. The data from the two nuclei detection methods are then compared and interpreted in view of the expected dynamic beha
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14

K.V., Santhosh. "FUSION OF VENTURI AND ULTRASONIC FLOW METER FOR ENHANCED FLOW METER CHARACTERISTICS USING FUZZY LOGIC." ICTACT Journal on Soft Computing 05, no. 03 (2015): 936–41. http://dx.doi.org/10.21917/ijsc.2015.0131.

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15

d’Agostino, Luca, and S. I. Green. "Simultaneous Cavitation Susceptibility Meter and Holographic Measurements of Nuclei in Liquids." Journal of Fluids Engineering 114, no. 2 (1992): 261–67. http://dx.doi.org/10.1115/1.2910025.

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Cavitation Susceptibility Meter (CSM) and holographic measurements of cavitation nuclei distributions are compared in this paper. The CSM optically detects cavitation in water samples flowing through a venturi and relates the unstable nuclei concentration to the applied tension in the fluid. A ruby laser holographic system measures the nuclei size distribution directly. Microbubbles have been used as the dominant nuclei source. The data from the two detection schemes are correlated by accounting for the dynamic response of the cavities in the venturi throat. The active nuclei distributions pre
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16

Xu, Lijun, Wanlu Zhou, and Xiaomin Li. "Wet gas flow modeling for a vertically mounted Venturi meter." Measurement Science and Technology 23, no. 4 (2012): 045301. http://dx.doi.org/10.1088/0957-0233/23/4/045301.

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17

Feng, Ding, Si Huang, Yu Hui Guan, and Wei Guo Ma. "CFD Simulation of Two-Phase Flow in a Downhole Venturi Meter." Applied Mechanics and Materials 130-134 (October 2011): 3644–47. http://dx.doi.org/10.4028/www.scientific.net/amm.130-134.3644.

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This work performs an oil-water two-phase flow simulation in a downhole Venturi meter to investigate the flow field and pressure characteristics with different flow and oil-water ratios. The relation between the pressure drop and the feed flow rate in the flowmeter is investigated for its optimal design.
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18

Adamski, Krzysztof, Bartosz Kawa, and Rafał Walczak. "3D Printed Flowmeter Based on Venturi Effect with Integrated Pressure Sensors." Proceedings 2, no. 13 (2018): 1509. http://dx.doi.org/10.3390/proceedings2131509.

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In this paper we present a 3D printed flow meter based on venturri effect. Dimensions of the microchannels are 800 µm for wider and 400 µm for thinker channel. Application of different type of sensors was investigated: differential, absolute and digital barometer. Results of measurement of differential pressure and calculation of liquid flow are shown. Presented microfluidics device can be also easy adapted for modular systems. Presented flow meter is the first integration of commercial available sensors and 3D printed microfluidics structure in a single chip.
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19

Oliveira, Natalia M. B., Luiz Gustavo Martins Vieira, and João Jorge Ribeiro Damasceno. "Numerical Methodology for Orifice Meter Calibration." Materials Science Forum 660-661 (October 2010): 531–36. http://dx.doi.org/10.4028/www.scientific.net/msf.660-661.531.

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Orifice Meters are mechanical devices used to measure gases and liquids flows. Due to manufacturing, installation and operation simplicity, the orifice meters are widely used in the industrial processes in which there is flow of gases or liquids. Moreover, their acquisition and operation costs are smaller than the ones verified for other flow meters (Venturi, flowmeter). However, before the utilization of any calibration orifice meters, they demand an experimental calibration procedure. Thus, in order to suppress this laborious experimental procedure, this work objectified to apply computation
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20

Li, Xia, Zhiyao Huang, Zhenzhen Meng, Baoliang Wang, and Haiqing Li. "OIL-WATER TWO-PHASE FLOW MEASUREMENT USING A VENTURI METER AND AN OVAL GEAR FLOW METER." Chemical Engineering Communications 197, no. 2 (2009): 223–31. http://dx.doi.org/10.1080/00986440902938469.

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21

Chahine, G. L., and Y. T. Shen. "Bubble Dynamics and Cavitation Inception in Cavitation Susceptibility Meters." Journal of Fluids Engineering 108, no. 4 (1986): 444–52. http://dx.doi.org/10.1115/1.3242602.

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To improve the understanding of the scaling effects of nuclei on cavitation inception, bubble dynamics, multibubble interaction effects, and bubble-mean flow interaction in a venturi Cavitation Susceptibility Meter are considered theoretically. The results are compared with classical bubble static equilibrium predictions. In a parallel effort, cavitation susceptibility measurements of ocean and laboratory water were carried out using a venturi device. The measured cavitation inception indices were found to relate to the measured microbubble concentration. The relationship between the measured
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22

Huang, X., and S. W. Van Sciver. "Performance of a venturi flow meter in two-phase helium flow." Cryogenics 36, no. 4 (1996): 303–9. http://dx.doi.org/10.1016/0011-2275(96)88790-x.

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23

d’Agostino, L., and A. J. Acosta. "A Cavitation Susceptibility Meter With Optical Cavitation Monitoring—Part Two: Experimental Apparatus and Results." Journal of Fluids Engineering 113, no. 2 (1991): 270–77. http://dx.doi.org/10.1115/1.2909491.

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This work is concerned with the development and operation of a Cavitation Susceptibility Meter based on the use of a venturi tube for the measurement of the active cavitation nuclei concentration in water samples as a function of the applied tension. The pressure at the venturi throat is determined from the upstream pressure and the local flow velocity without corrections for viscous effects because the flow possesses a laminar potential core in all operational conditions. The detection of cavitation and the measurement of the flow velocity are carried out optically by means of a Laser Doppler
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24

Carpenter, Chris. "Adjustable Cone Meter Adapts Automatically to Wet-Gas Conditions." Journal of Petroleum Technology 74, no. 12 (2022): 61–63. http://dx.doi.org/10.2118/1222-0061-jpt.

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_ This article, written by JPT Technology Editor Chris Carpenter, contains highlights of paper SPE 207505, “Using an Adjustable Cone Meter To Measure Wet Gas,” by Sakethraman Mahalingam, SPE, Saudi Aramco; Gavin Munro, SPE, GM Flow Measurement; and Muhammad Arsalan, SPE, Saudi Aramco, et al. The paper has not been peer reviewed. _ A traditional fixed-size Venturi meter has a turndown of approximately 8:1 under dry-gas conditions that may drop to as low as 3:1 under wet-gas flow. When the well conditions change, a replacement of the original Venturi meter with one of a different size is needed.
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25

Karimi, Muhammad Akram, Muhammad Arsalan, and Atif Shamim. "Extended Throat Venturi Based Flow Meter for Optimization of Oil Production Process." IEEE Sensors Journal 21, no. 16 (2021): 17808–16. http://dx.doi.org/10.1109/jsen.2021.3083532.

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26

Monni, Grazia, Mario De Salve, and Bruno Panella. "Two-phase flow measurements at high void fraction by a Venturi meter." Progress in Nuclear Energy 77 (November 2014): 167–75. http://dx.doi.org/10.1016/j.pnucene.2014.06.006.

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27

Ghassemi, Hojat, and Hamidreza Farshi Fasih. "Application of small size cavitating venturi as flow controller and flow meter." Flow Measurement and Instrumentation 22, no. 5 (2011): 406–12. http://dx.doi.org/10.1016/j.flowmeasinst.2011.05.001.

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28

Syed Mutheeulla Shaahid, Luai Muhammad Alhems, Aftab Ahmad, et al. "Parametric Study on Venturi Pressure Drop for Two Phase Oil (D130)-Water Flow for Different Operating Conditions – An Experimental Investigation." Journal of Advanced Research in Fluid Mechanics and Thermal Sciences 121, no. 2 (2024): 27–36. http://dx.doi.org/10.37934/arfmts.121.2.2736.

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The governing parameters which affect pressure drop of two-phase oil-water flow across the venturi meter are water cut and angle of inclination. The study investigates experimentally the effect of inclination and water cut on pressure drop measurements across different venturi meters with beta ratios (β) = 0.4, and 0.6 for oil–water two-phase flow experiments in a 3-inch pipe for different operating conditions. Two-phase inclinable flow loop has been employed for conducting the experiments for different fluid mixture flow rates and water cuts. The working fluids utilized are Exxsol mineral oil
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29

Xu, Lijun, Wanlu Zhou, Xiaomin Li, and Shaliang Tang. "Wet Gas Metering Using a Revised Venturi Meter and Soft-Computing Approximation Techniques." IEEE Transactions on Instrumentation and Measurement 60, no. 3 (2011): 947–56. http://dx.doi.org/10.1109/tim.2010.2045934.

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Lijun Xu, Wanlu Zhou, Xiaomin Li, and Minghao Wang. "Wet-Gas Flow Modeling for the Straight Section of Throat-Extended Venturi Meter." IEEE Transactions on Instrumentation and Measurement 60, no. 6 (2011): 2080–87. http://dx.doi.org/10.1109/tim.2011.2117190.

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31

Monni, G., M. Caramello, M. De Salve, and B. Panella. "Venturi flow meter and Electrical Capacitance Probe in a horizontal two-phase flow." Journal of Physics: Conference Series 655 (November 16, 2015): 012033. http://dx.doi.org/10.1088/1742-6596/655/1/012033.

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32

Carter, Michael, William Johansen, and Charles Britton. "Performance of a gas flow meter calibration system utilizing critical flow venturi standards." MAPAN 26, no. 3 (2011): 247–54. http://dx.doi.org/10.1007/s12647-011-0023-4.

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33

Pambudiarto, Benny Arif, Ilham Arifin Pahlawan, Yuni Fatmawati, and Muhammad Shobichul Mirbath. "Analysis of The Performance of Microbubble Generators as Aerators in Tilapia Cultivation with High Density Fishery Systems." Bioscientist : Jurnal Ilmiah Biologi 12, no. 2 (2024): 2343. https://doi.org/10.33394/bioscientist.v12i2.13064.

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Fish farmers in Gresik Regency face significant challenges in developing aquaculture, including land conversion and extended dry seasons that lead to pond drought. Microbubble generators (MBGs) present a potential solution to these issues. This study evaluates the effectiveness of different MBG types in tilapia farming. Weekly measurements of fish mass and length were conducted to determine growth rates using direct methods. Water quality was assessed by testing COD and ammonia levels at the Gresik Regency DLH Laboratory and measuring dissolved oxygen levels directly with a DO meter. The distr
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34

Zhen, Yang. "Research on the Coaxial Connection between Gas Flowmeter and Critical Flow Venturi Nozzle Gas Flow Standard Device." Key Engineering Materials 693 (May 2016): 194–99. http://dx.doi.org/10.4028/www.scientific.net/kem.693.194.

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As an important measurement instruments of trade metering, gas flowmeter has been more and more widely used, and the quantity value transfer of the flow meter is becoming increasingly significant. In order to realize the accurate measurement, the method of the coaxial connection between gas flowmeter and critical flow Venturi nozzle gas flow standard device is studied in this paper, and the coaxial error between this gas flowmeter and standard device within ±1mm is achieved.
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35

G, Kavin, Vignesh S, Subhasan R, and Shanmugavalli M. "Fluid Dynamics Analysis of Flow through T-junctions and Venturi Meters Using Computational Methods." International Journal of Multidisciplinary Research Transactions 6, no. 3 (2024): 70–82. https://doi.org/10.5281/zenodo.11050097.

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In this study, we're examining how water flows through a T-junction and into a Venturi tube via a pipe. We're using a computer program called ANSYS FLUENT 2018.1   to help us understand what's going on. We're interested in how things like the speed of the water and the pressure change as it moves through this system. To do this, we're looking at a few different factors. We're considering the size of the pipe (which is 25 mm in diameter) and how far it is from the T-junction to the outlet of the  Venturi  tube (which is 350 mm). We're also looking at something called the Rey
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36

Xu, Ying, Chao Yuan, Zheng Hai Long, Qiang Zhang, Zhen Lin Li, and Tao Zhang. "Experimental Investigation of the Wet Gas Measurement Based on Triple Differential Pressures Method." Applied Mechanics and Materials 220-223 (November 2012): 781–84. http://dx.doi.org/10.4028/www.scientific.net/amm.220-223.781.

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In order to meter the wet gas without separation online, a novel measurement device composed of a long throat Venturi tube and a V-cone is proposed and a new metering method based on triple differential pressures. In this method, the ratios of the differential pressures are vital parameters used to establish the measurement correlations. The comparison of these correlations is also presented. In laboratory test, the measurement accuracy of the gas and liquid are 2.13% and 6.68% respectively.
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Sakr, Ismail, Wageeh ElAskary, Mohamed Sheha, and Tarek ghonim. "Experimental Study of the Performance of a Venturi-Meter with Suspended Gas-Solid Flow." ERJ. Engineering Research Journal 43, no. 3 (2020): 195–97. http://dx.doi.org/10.21608/erjm.2020.95142.

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38

Steven, Richard. "A dimensional analysis of two phase flow through a horizontally installed Venturi flow meter." Flow Measurement and Instrumentation 19, no. 6 (2008): 342–49. http://dx.doi.org/10.1016/j.flowmeasinst.2008.05.004.

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39

Gajan, P., Q. Decaudin, and J. P. Couput. "Analysis of high pressure tests on wet gas flow metering with a Venturi meter." Flow Measurement and Instrumentation 44 (August 2015): 126–31. http://dx.doi.org/10.1016/j.flowmeasinst.2014.12.004.

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40

Lathifa Putri Afisna and Wibawa Endra Juwana. "APLIKASI MICROBUBBLE GENERATOR POROUS-VENTURI PADA PENGOLAHAN AIR LIMBAH BUATAN." KURVATEK 5, no. 1 (2020): 11–18. http://dx.doi.org/10.33579/krvtk.v5i1.1818.

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Abstrak
 Keterbatasan air bersih akibat terjadinya pencemaran air dari limbah rumah tangga dan industri maka perlu mengembangkan sebuah alat teknologi pengolahan air limbah yang ramah lingkungan dan instalasi yang mudah. Microbubble generator (MBG) digunakan untuk menghasilkan oksigen yang diperlukan oleh bakteri untuk melakukan dekomposisi air limbah. Pada penelitian ini didesain MBG porous-venturi dipasang pada kolam air limbah buatan. Parameter yang akan diukur koefisien perpindahan massa (KLa), kadar dissolved oxygen (DO) dan chemical oxygen demand (COD). Nilai KLa diukur dengan mengg
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41

Mwinyi, Vitalis. "Wet gas metering performance using conventional flow measurement devices." Tanzania Journal of Engineering and Technology 44, no. 2 (2025): 449–70. https://doi.org/10.52339/tjet.v44i2.1318.

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The demand for and production of natural wet gas from wells has significantly risen in recent years. Although natural gas liquids hold substantial value in the oil and gas market, their presence in wet gas adversely affects gas metering, leading to overreading during measurement. A comprehensive study has been undertaken to formulate and enhance correlations for rectifying overreading in wet gas metering. Nevertheless, most current correlations are designed for horizontal configurations of traditional meters. Mitigating this constraint is crucial to consider the impact of gravity on pressure l
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42

Gribok, Andrei V., Ibrahim K. Attieh, J. Wesley Hines, and Robert E. Uhrig. "Regularization of Feedwater Flow Rate Evaluation for Venturi Meter Fouling Problem in Nuclear Power Plants." Nuclear Technology 134, no. 1 (2001): 3–14. http://dx.doi.org/10.13182/nt01-a3181.

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43

Elperin, T., A. Fominykh, and M. Klochko. "Performance of a Venturi meter in gas–liquid flow in the presence of dissolved gases." Flow Measurement and Instrumentation 13, no. 1-2 (2002): 13–16. http://dx.doi.org/10.1016/s0955-5986(02)00013-4.

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44

Xu, Lijun, Jian Xu, Feng Dong, and Tao Zhang. "On fluctuation of the dynamic differential pressure signal of Venturi meter for wet gas metering." Flow Measurement and Instrumentation 14, no. 4-5 (2003): 211–17. http://dx.doi.org/10.1016/s0955-5986(03)00027-x.

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45

Panchal, R., N. C. Gupta, A. Garg, et al. "Design and engineering validation of venturi flow meter for current feeder system of SST 1." Indian Journal of Cryogenics 39, no. 1 (2014): 53. http://dx.doi.org/10.5958/2349-2120.2014.00800.0.

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46

Wrasse, Aluisio Do N., Dalton Bertoldi, Eduardo N. Dos Santos, Rigoberto E. M. Morales, and Marco J. Da Silva. "Gas–Liquid Flow Rate Measurement Using a Twin-Plane Capacitive Sensor and a Venturi Meter." IEEE Access 7 (2019): 135933–41. http://dx.doi.org/10.1109/access.2019.2942772.

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47

d’Agostino, L., and A. J. Acosta. "Separation and Surface Nuclei Effects in a Cavitation Susceptibility Meter." Journal of Fluids Engineering 113, no. 4 (1991): 695–98. http://dx.doi.org/10.1115/1.2926536.

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This work is concerned with the effects of flow separation and surface nuclei on the operation of a fixed geometry Cavitation Susceptibility Meter (CSM) with laminar flow. Cavitation is induced under controlled conditions at the throat of a glass venturi tube for the measurement of the active nuclei concentration in water samples as a function of the applied tension. Both cavitation and flow velocity are monitored optically by a Laser Doppler Velocimeter. The throat pressure is determined indirectly from the upstream pressure and the local flow velocity. The results show that laminar flow sepa
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48

Chen, Desheng, Haibin Cao, and Baoling Cui. "Study on flow field and measurement characteristics of a small-bore ultrasonic gas flow meter." Measurement and Control 54, no. 5-6 (2021): 554–64. http://dx.doi.org/10.1177/00202940211007515.

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A new structure is proposed for a DN25-type ultrasonic gas flow meter with a V-shape double sound channel arrangement. The flow field characteristics are analyzed including velocity curves for the four channel lines, velocity profiles for different cross-sections of the flow meter, and streamlines of the transducer channel sections. The metering characteristics of the flowmeter are measured using a Venturi nozzle device. When the pipeline flow rate is less than 2.26 m/s, the pipe installation does not have a significant effect on the velocity profile and the velocity in the channel lines. Howe
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Perdana, Rendi Hadi, Nur Aji Wibowo, and Made R. S. S. N. Ayub. "Design of measuring flow velocity device for liquid fluid with venturi meter principles based on Arduino." Journal of Science and Science Education 2, no. 1 (2018): 13–20. http://dx.doi.org/10.24246/josse.v2i1p13-20.

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Abstract:
Fluid flow velocity in physics can be found on the principle of venturi meter. The Fluid flow concept is easy to understand if visualized. We need a learning media of fluid velocity, so the concept can understanding. Design of this tool aims to help students understand the fluid flow velocity. Data is taken automatically by Arduino-based water flow sensor, with speed change at the speed knop. Based on the design result of the tool which can be obtained by measuring the fluid flow velocity at a speed greater than 0.36 m/s, and proved by graph analysis logarithmic between velocity values of magn
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50

Huang, Zhiyao, Dailiang Xie, Hongjian Zhang, and Haiqing Li. "Gas–oil two-phase flow measurement using an electrical capacitance tomography system and a Venturi meter." Flow Measurement and Instrumentation 16, no. 2-3 (2005): 177–82. http://dx.doi.org/10.1016/j.flowmeasinst.2005.02.007.

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