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Simultaneous Measurement of Volumetric Flowrates of Gas–Liquid Bubbly Flow Using a Turbine Flowmeter

The flowrate measurement of the gas–liquid two-phase flow frequently observed in industrial equipment, such as in heat exchangers and reactors, is critical to enable the precise monitoring and operation of the equipment. Furthermore, certain applications, such as oil and natural gas processing plant...

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Autores principales: Uchiyama, Tomomi, Miyamoto, Shogo, Horie, Kosuke, Takamure, Kotaro
Formato: Online Artículo Texto
Lenguaje:English
Publicado: MDPI 2023
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC10181500/
https://www.ncbi.nlm.nih.gov/pubmed/37177473
http://dx.doi.org/10.3390/s23094270
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author Uchiyama, Tomomi
Miyamoto, Shogo
Horie, Kosuke
Takamure, Kotaro
author_facet Uchiyama, Tomomi
Miyamoto, Shogo
Horie, Kosuke
Takamure, Kotaro
author_sort Uchiyama, Tomomi
collection PubMed
description The flowrate measurement of the gas–liquid two-phase flow frequently observed in industrial equipment, such as in heat exchangers and reactors, is critical to enable the precise monitoring and operation of the equipment. Furthermore, certain applications, such as oil and natural gas processing plants, require the accurate measurements of the flowrates of each phase simultaneously. This study presents a method that can simultaneously measure the volumetric flowrates of each phase of gas and liquid two-phase mixtures, Q(g) and Q(l), respectively, without separating the phases. The method employs a turbine flowmeter and two pressure sensors connected to the pipes upstream and downstream of the turbine flowmeter. By measuring the rotational speed of the rotor and the pressure loss across the flowmeter, the flowrate of the two-phase mixtures Q(tp) = (Q(g) + Q(l)) and the gas volumetric flowrate ratio β = (Q(g)/Q(tp)) are determined. The values of Q(g) and Q(l) are calculated as βQ(tp) and (1 − β)Q(tp). This study also investigates the measurement accuracies for air–water two-phase flows at 0.67 × 10(−3) ≤ Q(tp) ≤ 1.67 × 10(−3) m(3)/s and β ≤ 0.1, concluding that the full-scale accuracies of Q(tp), β, Q(g), and Q(l) are 3.1%, 4.8%, 3.9%, and 3%, respectively. These accuracies either match or improve the accuracies of similar methods reported in the literature, indicating that the proposed method is a viable solution for the determination of phase-specific flowrates in gas–liquid two-phase mixtures.
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spelling pubmed-101815002023-05-13 Simultaneous Measurement of Volumetric Flowrates of Gas–Liquid Bubbly Flow Using a Turbine Flowmeter Uchiyama, Tomomi Miyamoto, Shogo Horie, Kosuke Takamure, Kotaro Sensors (Basel) Article The flowrate measurement of the gas–liquid two-phase flow frequently observed in industrial equipment, such as in heat exchangers and reactors, is critical to enable the precise monitoring and operation of the equipment. Furthermore, certain applications, such as oil and natural gas processing plants, require the accurate measurements of the flowrates of each phase simultaneously. This study presents a method that can simultaneously measure the volumetric flowrates of each phase of gas and liquid two-phase mixtures, Q(g) and Q(l), respectively, without separating the phases. The method employs a turbine flowmeter and two pressure sensors connected to the pipes upstream and downstream of the turbine flowmeter. By measuring the rotational speed of the rotor and the pressure loss across the flowmeter, the flowrate of the two-phase mixtures Q(tp) = (Q(g) + Q(l)) and the gas volumetric flowrate ratio β = (Q(g)/Q(tp)) are determined. The values of Q(g) and Q(l) are calculated as βQ(tp) and (1 − β)Q(tp). This study also investigates the measurement accuracies for air–water two-phase flows at 0.67 × 10(−3) ≤ Q(tp) ≤ 1.67 × 10(−3) m(3)/s and β ≤ 0.1, concluding that the full-scale accuracies of Q(tp), β, Q(g), and Q(l) are 3.1%, 4.8%, 3.9%, and 3%, respectively. These accuracies either match or improve the accuracies of similar methods reported in the literature, indicating that the proposed method is a viable solution for the determination of phase-specific flowrates in gas–liquid two-phase mixtures. MDPI 2023-04-25 /pmc/articles/PMC10181500/ /pubmed/37177473 http://dx.doi.org/10.3390/s23094270 Text en © 2023 by the authors. https://creativecommons.org/licenses/by/4.0/Licensee MDPI, Basel, Switzerland. This article is an open access article distributed under the terms and conditions of the Creative Commons Attribution (CC BY) license (https://creativecommons.org/licenses/by/4.0/).
spellingShingle Article
Uchiyama, Tomomi
Miyamoto, Shogo
Horie, Kosuke
Takamure, Kotaro
Simultaneous Measurement of Volumetric Flowrates of Gas–Liquid Bubbly Flow Using a Turbine Flowmeter
title Simultaneous Measurement of Volumetric Flowrates of Gas–Liquid Bubbly Flow Using a Turbine Flowmeter
title_full Simultaneous Measurement of Volumetric Flowrates of Gas–Liquid Bubbly Flow Using a Turbine Flowmeter
title_fullStr Simultaneous Measurement of Volumetric Flowrates of Gas–Liquid Bubbly Flow Using a Turbine Flowmeter
title_full_unstemmed Simultaneous Measurement of Volumetric Flowrates of Gas–Liquid Bubbly Flow Using a Turbine Flowmeter
title_short Simultaneous Measurement of Volumetric Flowrates of Gas–Liquid Bubbly Flow Using a Turbine Flowmeter
title_sort simultaneous measurement of volumetric flowrates of gas–liquid bubbly flow using a turbine flowmeter
topic Article
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC10181500/
https://www.ncbi.nlm.nih.gov/pubmed/37177473
http://dx.doi.org/10.3390/s23094270
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