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Добірка наукової літератури з теми "Fluid measurements"

Автор: Grafiati
Опубліковано: 10 грудня 2022
Оновлено: 29 січня 2023

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Статті в журналах з теми "Fluid measurements"

1

Rockwell, D. "Fluid mechanics measurements." International Journal of Heat and Fluid Flow 8, no. 1 (March 1987): 78. http://dx.doi.org/10.1016/0142-727x(87)90058-0.

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2

Roodhart, L. P. "Fracturing Fluids: Fluid-Loss Measurements Under Dynamic Conditions." Society of Petroleum Engineers Journal 25, no. 05 (October 1, 1985): 629–36. http://dx.doi.org/10.2118/11900-pa.

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Abstract When filter-cake-building additives are used in fracturing fluids, the commonly applied static, 30-minute API filtration test is unsatisfactory, because in a dynamic situation (like fracturing) the formation of a thick filter cake will be inhibited by the shearing forces of the fracturing fluid. A dynamic, filter-cake-controlled, leakoff coefficient that is dependent on the shear rate and shear stress at the fracture face is, therefore, introduced. A test apparatus has been constructed in which the fluid leakoff is measured under conditions of temperature, rate of shear, duration of shear, and fluid-flow pattern as encountered under fracturing conditions. The effects of rock permeability, shear rate, and differential pressure on the permeability, shear rate, and differential pressure on the dynamic leakoff coefficient are presented for various, commonly used fracturing-fluid/fluid-loss-additive combinations. Introduction An important parameter in hydraulic fracturing design is the rate at which the fracturing fluid leaks into the formation. This parameter, known as fluid loss, not only determines the development of fracture length and width, but also governs the time required for a fracture to heal after the stimulation treatment has been terminated. The standard leakoff test is a static test, in which the effect of shear rate in the fracture on the viscosity of the fracturing fluid and on the filter-cake buildup is ignored. Dynamic vs. Static Tests The three stages in filter-cake buildup arespurt loss during initiation of the filter cake,buildup of filtercake thickness, during which time leakoff is proportional to the square root of time, andlimitation of filter-cake growth by erosion. In the standard API leakoff test, 1 the fracturing fluid, with or without leakoff additives, is forced through a disk of core material under a pressure differential of 1000 psi [7 MPa), and the flow rate of the filtrate is determined. In such a static test, the third stage-erosion of the filter cake-is absent. In a dynamic situation there is an equilibrium whereby flow along the filter cake limits the filter-cake thickness, and the leakoff rate becomes constant. The duration of each of these stages depends on the type of fluid, the type of additive, the rock permeability, and the test conditions. The differences between dynamic and static filtration tests are shown in Fig. 1, where the cumulative filtrate volume (measured in some experiments with the dynamic fluid-loss apparatus described below) is expressed as a function of time (Fig. la) and as a function of the square root of time (Fig. ]b), The shear rate at the surface of the disk is either static (O s -1 ), or 109 s -1 or 611 s -1. The curves indicate that the dynamic filtration velocities are higher than those measured in a static test and increase rapidly with increasing shear rate. This is in agreement with the observations made by Hall, who used an axially transfixed cylindrical core sample along which fracturing fluid was pumped, while the filtrate was collected from a bore through the center. Fig. la shows how the lines were drawn to fit the data: Vc = Vsp + A t + Bt, .........................(1) where Vc = cumulative volume per unit area, t = filtration time, Vsp= spurt loss, A = static leakoff component, andB = dynamic leakoff component. In static leakoff theory, B =0 and then A =2Cw, twice the static leakoff coefficient.-3 Each of the terms in Eq. 1 represents one of the stages in the leakoff process-spurt loss, buildup of filter cake, and erosion of filter cake. Analysis of the experimental data shows that the spurt loss, Vsp, and the static leakoff component, A, are independent of the shear rate, but the dynamic component, B, varies strongly with the shear rate (see Table 1). This means that, the higher the shear rate, the more the leakoff process is controlled by the third stage. process is controlled by the third stage. One model commonly used is based solely on square-root-of-time behavior with a constant spurt loss. Fig. 1 shows that little accuracy is lost by describing the leakoff with a single square-root-of-time equation: Vc = VsP + m t,...........................(2) where the dynamic leakoff coefficient. Cw = 1/2m, depends heavily on shear. and the spurt loss remains the same as in Eq. 1 and independent of the shear rate Table 2 shows that the error in C, that arises as a result of measuring under static conditions can be more than 100%. SPEJ P. 629
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3

Espenhahn, Björn, Lukas Schumski, Christoph Vanselow, Dirk Stöbener, Daniel Meyer, and Andreas Fischer. "Feasibility of Optical Flow Field Measurements of the Coolant in a Grinding Machine." Applied Sciences 11, no. 24 (December 7, 2021): 11615. http://dx.doi.org/10.3390/app112411615.

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For industrial grinding processes, the workpiece cooling by metalworking fluids, which strongly influences the workpiece surface layer quality, is not yet fully understood. This leads to high efforts for the empirical determination of suitable cooling parameters, increasing the part manufacturing costs. To close the knowledge gap, a measurement method for the metalworking fluid flow field near the grinding wheel is desired. However, the varying curved surfaces of the liquid phase result in unpredictable light deflections and reflections, which impede optical flow measurements. In order to investigate the yet unknown optical measurement capabilities achievable under these conditions, shadowgraphy in combination with a pattern correlation technique and particle image velocimetry (PIV) are applied in a grinding machine. The results show that particle image velocimetry enables flow field measurements inside the laminar metalworking fluid jet, whereby the shadowgraph imaging velocimetry complements these measurements since it is in particular suitable for regions with spray-like flow regimes. As a conclusion, optical flow field measurements of the metalworking fluid flow in a running grinding machine are shown to be feasible.
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4

Jasmita, Murda, and Ardian Putra. "Identifikasi Karakteristik Mata Air Panas Bumi di Sibanggor Tonga Kabupaten Mandailing Natal Menggunakan Diagram Segitiga Fluida." Jurnal Fisika Unand 9, no. 4 (January 25, 2021): 428–35. http://dx.doi.org/10.25077/jfu.9.4.428-435.2020.

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Telah dilakukan penelitian tentang identifikasi karakteristik fluida mata air panas tipe fluida, kesetimbangan, asal usul sumber fluida dan pengenceran mata air panas bumi di Sibanggor Tonga Kabupaten Mandailing Natal. Sampel penelitian diambil dari lima sumber mata air dengan volume sampel di setiap lokasi sebanyak 500 ml. Nilai pH dari 5 titik mata air panas berkisar dari 0,6 sampai 6,3 dan pengukuran temperatur permukaan diperoleh mulai dari 37,6 oC hingga 95,3 oC. Konsentrasi unsur Na, K, Mg, K, B dan Li diukur menggunakan Inductively Coupled Plasma-Atomic Emission Spectroscopy (ICP-AES). Pengukuran konsentrasi unsur Cl diperoleh dari persamaan konduktivitas yang didapatkan dari alat conductivity meter dan pengukuran konsentrasi SO4 dengan metode visible spectroscopy. Pengukuran konsentrasi HCO3 diukur dengan metode titrasi asam basa. Diagram Cl-HCO3-SO4 menunjukkan semua fluida bertipe sulfat-klorida dan diagram Na-K-Mg menunjukkan semua fluida berada pada immature water yang mengindikasikan fluida telah mengalami reaksi dengan unsur lain saat menuju permukaan. Asal sumber fluida berada jauh dari reservoir atau aliran fluida bergerak secara lateral saat menuju permukaan, yang terlihat dari diagram Cl-B-Li. Research has been carried out on the identification of the characteristics of the hot spring fluid type, equilibrium, the origin of the fluid source and the dilution of the geothermal springs in Sibanggor Tonga, Mandailing Natal Regency. The research sample was taken from five springs with a sample volume of 500 ml at each location. The pH values of the 5 hot springs ranged from 0.6 to 6.3 and surface temperature measurements were obtained from 37.6°C to 95.3°C. The concentrations of Na, K, Mg, K, B and Li were measured using Inductively Coupled Plasma-Atomic Emission Spectroscopy (ICP-AES). Measurement of the element concentration of Cl is obtained from the conductivity equation obtained from a conductivity meter and measurement of SO4 concentrations using the visible spectroscopy method. HCO3 concentration measurements were measured by the acid-base titration method. The Cl-HCO3-SO4 diagram shows all sulfate-chloride type fluids and the Na-K-Mg diagram shows all fluids are in immature water which indicates that the fluid has undergone a reaction with other elements when it reaches the surface. As long as the fluid source is far from the reservoir or the fluid flow moves laterally towards the surface, as seen from the Cl-B-Li diagram.
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5

Carpenter, Chris. "Automated Drilling-Fluids-Measurement Technique Improves Fluid Control, Quality." Journal of Petroleum Technology 73, no. 11 (November 1, 2021): 53–54. http://dx.doi.org/10.2118/1121-0053-jpt.

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This article, written by JPT Technology Editor Chris Carpenter, contains highlights of paper SPE 204041, “Automatic Drilling-Fluids Monitoring,” by Knut Taugbøl, SPE, Equinor, and Bengt Sola and Matthew Forshaw, SPE, Baker Hughes, et al., prepared for the 2021 SPE/IADC International Drilling Conference and Exhibition, originally scheduled to be held in Stavanger, 9–11 March. The paper has not been peer reviewed. The complete paper presents new units for automatic drilling-fluids measurements with emphasis on offshore drilling applications. The surveillance of fluid properties and the use of data in an onshore operations center is discussed. The authors present experiences from use of these data in enabling real-time hydraulic measurements and models for automatic drilling control and explain how these advances can improve safety in drilling operations and drilling efficiency. Introduction An operator has worked with different suppliers for several years to find and develop technology for automatic measurements of drilling-fluid properties. In the described study, methods for measuring parameters such as viscosity, fluid loss control, pH, electrical stability, particle-size distribution, and cuttings morphology and mineralogy were all fitted into a flow loop in an onshore test center. These tests, however, were all performed with prototype equipment. Since then, work has continued to optimize equipment for offshore installations, made for operating in harsh environments and requiring limited maintenance to provide continuous and reliable data quality. The fluid-measuring technique presented in this paper is based on rheology measurement through a pipe rheometer and density measurements through a Coriolis meter. This rheometer measures at ambient temperature. Dual DP is the terminology that refers to pressure measurements between two differential pressure sensors. The dual-DP pipe rheometer is set up with high-accuracy pressure transducers to measure pressure loss inside the straight section of the pipe rheometer. By varying the flow rate through pipes of different dimensions, a rheology profile at varying shear rates can be calculated. Field Implementation Installation of a unit begins with a rig survey conducted in concert with the drilling contractor to find the best location and sampling point. Fluid normally is taken from the charge manifold for the mud pumps, ensuring measurement of the fluid going into the well. The first installation in the North Sea of an automatic fluid-monitoring (AFM) unit was in 2017. This unit is still operational, sending data to an onshore support center. Fig. 1 shows such a unit installed offshore. The AFM unit has only one movable part, the monopump supplying drilling fluid through the unit. Once the dual-DP rheometer was factory-acceptance-tested in the yard, it was sent offshore to be commissioned and verified on a fixed installation in the North Sea. The related data presented in the complete paper were acquired in the field while drilling the 355-m, 8½-in. section with 1.35-SG low-equivalent-circulating-density oil-based drilling fluid, with drilling conducted at approximately 4000 m measured depth. The mud engineer onboard was requested to perform rheology checks on a viscometer at equal ambient temperature to the AFM so that the results could be compared; the AFM also measures rheology at ambient temperature.
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Huang, Jinrui, Frederic Cegla, Andy Wickenden, and Mike Coomber. "Simultaneous Measurements of Temperature and Viscosity for Viscous Fluids Using an Ultrasonic Waveguide." Sensors 21, no. 16 (August 18, 2021): 5543. http://dx.doi.org/10.3390/s21165543.

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The characterisation and monitoring of viscous fluids have many important applications. This paper reports a refined ‘dipstick’ method for ultrasonic measurement of the properties of viscous fluids. The presented method is based on the comparison of measurements of the ultrasonic properties of a waveguide that is immersed in a viscous liquid with the properties when it is immersed in a reference liquid. We can simultaneously determine the temperature and viscosity of a fluid based on the changes in the velocity and attenuation of the elastic shear waves in the waveguide. Attenuation is mainly dependent on the viscosity of the fluid that the waveguide is immersed in and the speed of the wave mainly depends on the surrounding fluid temperature. However, there is a small interdependency since the mass of the entrained viscous liquid adds to the inertia of the system and slows down the wave. The presented measurements have unprecedented precision so that the change due to the added viscous fluid mass becomes important and we propose a method to model such a ‘viscous effect’ on the wave propagation velocity. Furthermore, an algorithm to correct the velocity measurements is presented. With the proposed correction algorithm, the experimental results for kinematic viscosity and temperature show excellent agreement with measurements from a highly precise in-lab viscometer and a commercial resistance temperature detector (RTD) respectively. The measurement repeatability of the presented method is better than 2.0% in viscosity and 0.5% in temperature in the range from 8 to 300 cSt viscosity and 40 to 90 °C temperature.
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7

Alipour, Fariborz. "Fluid dynamics measurements during phonation." Journal of the Acoustical Society of America 121, no. 5 (May 2007): 3121. http://dx.doi.org/10.1121/1.4782097.

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8

Deng, Feng, Lizhi Xiao, Mengying Wang, Ye Tao, Lulin Kong, Xiaoning Zhang, Xinyun Liu, and Dongshi Geng. "Online NMR Flowing Fluid Measurements." Applied Magnetic Resonance 47, no. 11 (October 6, 2016): 1239–53. http://dx.doi.org/10.1007/s00723-016-0832-2.

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MATSUO, Shigenobu. "Measurements of Fluid Transport Properties." Review of High Pressure Science and Technology 11, no. 2 (2001): 113–20. http://dx.doi.org/10.4131/jshpreview.11.113.

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10

Zuo, Julian Y., Dan Zhang, Francois Dubost, Chengli Dong, Oliver C. Mullins, Michael O’Keefe, and Soraya S. Betancourt. "Equation-of-State-Based Downhole Fluid Characterization." SPE Journal 16, no. 01 (October 27, 2010): 115–24. http://dx.doi.org/10.2118/114702-pa.

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Summary Downhole fluid analysis (DFA), together with focused-sampling techniques and wireline-formation-tester (WFT) tools, provides real-time measurements of reservoir-fluid properties such as the compositions of four or five hydrocarbon components/groups and gas/oil ratio (GOR). With the introduction of a new generation of DFA tools that analyze fluids at downhole conditions, the accuracy and reliability of the DFA measurements are improved significantly. Furthermore, downhole measurements of live-fluid densities are integrated into the new tools. Direct pressure and temperature measurements of the flowline ensure capture of accurate fluid conditions. To enhance these advanced features further, a new method of downhole fluid characterization based on the equation-of-state (EOS) approach is proposed in this work. The motivation for this work is to develop a new approach to maximize the value of DFA data, perform quality assurance or quality control of DFA data, and establish a fluid model for DFA log predictions along with DFA fluid profiling. The basic inputs from DFA measurements are weight percentages of CO2, C1, C2, C3–C5 and C6+, along with live-fluid density and viscosity. A new method was developed in this work to delump and characterize the DFA measurements of C3–C5 (or C2–C5) and C6+ into full-length compositional data. The full-length compositional data predicted by the new method were compared with the laboratory-measured gas chromatograph data up to C30+ for more than 1,000 fluids, including heavy oil, conventional black oil, volatile oil, rich gas condensate, lean gas condensate, and wet gas. These fluids have a GOR range of 8–140,000 scf/STB and a gravity range from 9 to 50°API. A good agreement was achieved between the delumped and gas-chromatograph compositions. In addition, on the basis of the delumped and characterized full-length compositional data, EOS models were established that can be applied to predict fluid-phase behavior and physical properties by virtue of DFA data as inputs. The EOS predictions were validated and compared with the laboratory-measured pressure/volume/temperature (PVT) properties for more than 1,000 fluids. The GOR, formation-volume factor, density, and viscosity predictions were in good agreement with the laboratory measurements. The established EOS model then was able to predict other PVT properties, and the results were compared with the laboratory measurements in good agreement. Consequently, the established EOS models have laid a solid foundation for DFA log predictions in DFA fluid profiling, which has been integrated successfully with DFA measurements in real time to delineate compositional and asphaltene gradients in oil columns and to determine reservoir connectivity. The latter results are beyond the scope of this work and have been given in separate technical papers.
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Дисертації з теми "Fluid measurements"

1

Ernst, Herbert. "High resolution thermal measurements in fluids." [S.l. : s.n.], 2001. http://deposit.ddb.de/cgi-bin/dokserv?idn=963763555.

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2

Liu, Ying. "Measurements of jet velocity in unstratified and stratified fluids." Thesis, Georgia Institute of Technology, 2000. http://hdl.handle.net/1853/19474.

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3

Khahledi, Morakane Charlotte. "Non-Newtonian fluid flow measurement using sharp crested notches." Thesis, Cape Peninsula University of Technology, 2014. http://hdl.handle.net/20.500.11838/1038.

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Master of Technology: Civil Engineering In the Faculty of Engineering At the Cape Peninsula University of Technology 2014
Notches, particularly rectangular and V shaped are the cheapest and most common devices used to measure the flow rate of water in open channels. However, they have not been used to measure the flow rate of non-Newtonian fluids. These viscous fluids behave differently from water. It is difficult to predict the flow rate of such fluids during transportation in open channels due to their complex viscous properties. The aim of this work was to explore the possibility of extending the application of especially rectangular and V-shaped notches to non-Newtonian fluids. The tests reported in this document were carried out in the Flow Process and Rheology Centre laboratory. Notches fitted to the entrance of a 10 m flume and an in-line tube viscometer were calibrated using water. The in-line tube viscometer with 13 and 28 mm diameter tubes was used to determine the fluid rheology. Flow depth was determined using digital depth gauges and flow rate measurements using magnetic flow meters. Three different non-Newtonian fluids, namely, aqueous solutions of Carboxymethyl Cellulose (CMC) and water-based suspensions of kaolin and bentonite were used as model non-Newtonian test fluids. From these the coefficient of discharge (Cd) values and appropriate non-Newtonian Reynolds numbers for each fluid and concentration were calculated. The experimental values of the coefficient of discharge (Cd) were plotted against three different definitions of the Reynolds number. Under laminar flow conditions, the discharge coefficient exhibited a typical dependence on the Reynolds number with slopes of ~0.43-0.44 for rectangular and V notches respectively. The discharge coefficient was nearly constant in the turbulent flow regime. Single composite power-law functions were used to correlate the Cd-Re relationship for each of the two notch shapes used. Using these correlations, the Cd values could be predicted to within ±5% for the rectangular and V notches. This is the first time that such a prediction has been done for a range of non-Newtonian fluids through sharp crested notches. The research will benefit the mining and food processing industries where high concentrations of non-Newtonian fluids are transported to either disposal sites or during processing.
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4

Handford, Peter Mark. "Measurements and calculations in three dimensional separated flow." Thesis, Imperial College London, 1986. http://hdl.handle.net/10044/1/8504.

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5

Zhang, Junfang. "Computer simulation of nanorheology for inhomogenous fluids." Australasian Digital Thesis Program, 2005. http://adt.lib.swin.edu.au/public/adt-VSWT20050620.095154.

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Thesis (PhD) - Swinburne University of Technology, School of Information Technology, Centre for Molecular Simulation - 2005.
A thesis submitted in fulfilment of requirements for the degree of Doctor of Philosophy, Centre for Molecular Simulation, School of Information Technology, Swinburne University of Technology - 2005. Typescript. Bibliography: p. 164-170.
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6

Weber, Amanda Clare. "Visualization and quantitative measurements of flow within a perfused bioreactor." Thesis, Georgia Institute of Technology, 2000. http://hdl.handle.net/1853/16907.

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7

Or, Chun-ming, and 柯雋銘. "Flow development in the initial region of a submerged round jet in a moving environment." Thesis, The University of Hong Kong (Pokfulam, Hong Kong), 2009. http://hub.hku.hk/bib/B42664512.

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8

Pickles, K. "Velocity measurements in a thermally convecting high prandtl number fluid." Thesis, University of Newcastle Upon Tyne, 1985. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.354406.

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9

Zhao, Xiaomin. "Effects of heterogeneities on fluid flow and borehold permeability measurements." Thesis, Massachusetts Institute of Technology, 1994. http://hdl.handle.net/1721.1/11933.

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Thesis (Ph. D.)--Massachusetts Institute of Technology, Dept. of Earth, Atmospheric, and Planetary Sciences, 1994.
Includes bibliographical references (leaves 216-221).
by Xiaomin Zhao.
Ph.D.
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10

Blasch, Kyle William. "Streamflow timing and estimation of infiltration rates in an ephemeral stream channel using variably saturated heat and fluid transport methods." Diss., The University of Arizona, 2003. http://etd.library.arizona.edu/etd/GetFileServlet?file=file:///data1/pdf/etd/azu_e9791_2003_253_sip1_w.pdf&type=application/pdf.

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Книги з теми "Fluid measurements"

1

J, Goldstein Richard, ed. Fluid mechanics measurements. 2nd ed. Washington, DC: Taylor & Francis, 1996.

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2

Furness, R. A. Fluid flow measurement. Burnt Mill, England: Longman, 1989.

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3

Baker, R. C. An introductory guide to flow measurement. London: Professional Engineering, 1989.

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4

Gad-el-Hak, Mohamed. Advances in Fluid Mechanics Measurements. Berlin, Heidelberg: Springer Berlin Heidelberg, 1989.

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5

Gad-el-Hak, Mohamed, ed. Advances in Fluid Mechanics Measurements. Berlin, Heidelberg: Springer Berlin Heidelberg, 1989. http://dx.doi.org/10.1007/978-3-642-83787-6.

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6

Fomin, Nikita A. Speckle Photography for Fluid Mechanics Measurements. Berlin, Heidelberg: Springer Berlin Heidelberg, 1998. http://dx.doi.org/10.1007/978-3-662-03707-2.

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7

Fomin, N. A. Speckle photography for fluid mechanics measurements. Berlin: Springer, 1998.

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Fomin, Nikita A. Speckle Photography for Fluid Mechanics Measurements. Berlin, Heidelberg: Springer Berlin Heidelberg, 1998.

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9

Optical rheometry of complex fluids. New York: Oxford University Press, 1995.

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10

P, Cheremisinoff Nicholas, ed. Encyclopedia of fluid mechanics. Houston: Gulf Pub. Co., Book Division, 1986.

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Частини книг з теми "Fluid measurements"

1

Polak, T. A., and C. Pande. "Fluid Flow Measurement." In Engineering Measurements, 71–95. Chichester, UK: John Wiley & Sons, Ltd, 2014. http://dx.doi.org/10.1002/9781118903148.ch6.

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2

Venkateshan, S. P. "Measurement of Fluid Velocity." In Mechanical Measurements, 281–314. Chichester, UK: John Wiley & Sons, Ltd, 2015. http://dx.doi.org/10.1002/9781119115571.ch8.

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3

Venkateshan, S. P. "Measurement of Fluid Velocity." In Mechanical Measurements, 303–41. Cham: Springer International Publishing, 2021. http://dx.doi.org/10.1007/978-3-030-73620-0_8.

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4

Nandagopal, PE, Nuggenhalli S. "Fluid Flow Measurements." In Fluid and Thermal Sciences, 137–47. Cham: Springer International Publishing, 2022. http://dx.doi.org/10.1007/978-3-030-93940-3_5.

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5

Fernando, Harindra, Marko Princevac, and Ronald Calhoun. "Atmospheric Measurements." In Springer Handbook of Experimental Fluid Mechanics, 1157–78. Berlin, Heidelberg: Springer Berlin Heidelberg, 2007. http://dx.doi.org/10.1007/978-3-540-30299-5_17.

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6

Chereskin, Teresa, and Bruce Howe. "Oceanographic Measurements." In Springer Handbook of Experimental Fluid Mechanics, 1179–217. Berlin, Heidelberg: Springer Berlin Heidelberg, 2007. http://dx.doi.org/10.1007/978-3-540-30299-5_18.

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7

Fomin, Nikita A. "Velocity Measurements." In Speckle Photography for Fluid Mechanics Measurements, 129–47. Berlin, Heidelberg: Springer Berlin Heidelberg, 1998. http://dx.doi.org/10.1007/978-3-662-03707-2_8.

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8

Leehey, Patrick. "Dynamic Wall Pressure Measurements." In Advances in Fluid Mechanics Measurements, 201–27. Berlin, Heidelberg: Springer Berlin Heidelberg, 1989. http://dx.doi.org/10.1007/978-3-642-83787-6_5.

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9

Romano, Giovanni, Nicholas Ouellette, Haitao Xu, Eberhard Bodenschatz, Victor Steinberg, Charles Meneveau, and Joseph Katz. "Measurements of Turbulent Flows." In Springer Handbook of Experimental Fluid Mechanics, 745–855. Berlin, Heidelberg: Springer Berlin Heidelberg, 2007. http://dx.doi.org/10.1007/978-3-540-30299-5_10.

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Sundén, Bengt. "Convective Heat Transfer and Fluid Dynamics in Heat Exchanger Applications." In Applied Optical Measurements, 159–70. Berlin, Heidelberg: Springer Berlin Heidelberg, 1999. http://dx.doi.org/10.1007/978-3-642-58496-1_10.

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Тези доповідей конференцій з теми "Fluid measurements"

1

Taugbøl, Knut, Jan Ove Brevik, and Bjørn Rudshaug. "Automatic Drilling Fluid Measurements." In SPE Russian Petroleum Technology Conference. Society of Petroleum Engineers, 2019. http://dx.doi.org/10.2118/196793-ms.

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2

Webb, A., and D. Maynes. "Velocity profile measurements in microtubes." In 30th Fluid Dynamics Conference. Reston, Virigina: American Institute of Aeronautics and Astronautics, 1999. http://dx.doi.org/10.2514/6.1999-3803.

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3

Sree, Dave. "Estimation of turbulence scales from LDV measurements." In Fluid Dynamics Conference. Reston, Virigina: American Institute of Aeronautics and Astronautics, 1996. http://dx.doi.org/10.2514/6.1996-2040.

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4

Taugbøl, Knut, Jan Ove Brevik, and Bjørn Rudshaug. "Automatic Drilling Fluid Measurements (Russian)." In SPE Russian Petroleum Technology Conference. Society of Petroleum Engineers, 2019. http://dx.doi.org/10.2118/196793-ru.

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5

Bridges, James. "'Measurements' of jet acoustic source density." In 30th Fluid Dynamics Conference. Reston, Virigina: American Institute of Aeronautics and Astronautics, 1999. http://dx.doi.org/10.2514/6.1999-3787.

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6

Harris, Scott, Richard Miles, and Walter Lempert. "PHANTOMM flow tagging measurements in complex 3D flows." In Fluid Dynamics Conference. Reston, Virigina: American Institute of Aeronautics and Astronautics, 1996. http://dx.doi.org/10.2514/6.1996-1966.

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7

McMillan, Madeline N., Alexandre R. Berger, and Edward B. White. "Measurements of Distributed Roughness Receptivity." In 47th AIAA Fluid Dynamics Conference. Reston, Virginia: American Institute of Aeronautics and Astronautics, 2017. http://dx.doi.org/10.2514/6.2017-4416.

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McGinley, C., E. Spina, and M. Sheplak. "Turbulence measurements in a Mach 11 helium boundary layer." In Fluid Dynamics Conference. Reston, Virigina: American Institute of Aeronautics and Astronautics, 1994. http://dx.doi.org/10.2514/6.1994-2364.

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Cattafesta, I, L., and Jay IIMoore. "Uncertainty estimates for luminescent temperature-sensitive paint intensity measurements." In Fluid Dynamics Conference. Reston, Virigina: American Institute of Aeronautics and Astronautics, 1995. http://dx.doi.org/10.2514/6.1995-2193.

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McAlister, Kenneth. "Measurements in the near wake of a hovering rotor." In Fluid Dynamics Conference. Reston, Virigina: American Institute of Aeronautics and Astronautics, 1996. http://dx.doi.org/10.2514/6.1996-1958.

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Звіти організацій з теми "Fluid measurements"

1

Mopsik, Frederick I. Two-fluid measurements on thin films. Gaithersburg, MD: National Bureau of Standards, 1992. http://dx.doi.org/10.6028/nist.tn.1294.

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2

Condie, Keith Glenn, Glenn Ernest Mc Creery, and Donald Marinus McEligot. Measurements of Fundamental Fluid Physics of SNF Storage Canisters. Office of Scientific and Technical Information (OSTI), September 2001. http://dx.doi.org/10.2172/910677.

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3

Lee, E. Automated Electric Charge Measurements of Fluid Microdrops Using the Millikan Method. Office of Scientific and Technical Information (OSTI), December 2004. http://dx.doi.org/10.2172/839780.

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4

Delisi, Donald P., George C. Greene, Donald B. Altman, Lee E. Piper, and Raminder Singh. Laboratory Measurements of the Evolution of a Vortex Pair in a Nonstratified Fluid. Fort Belvoir, VA: Defense Technical Information Center, April 1992. http://dx.doi.org/10.21236/ada268419.

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5

Liu, D., and T. de Bruin. New technology for fluid dynamic measurements in gas-liquid-solid three-phase flow reactors. Natural Resources Canada/ESS/Scientific and Technical Publishing Services, 1991. http://dx.doi.org/10.4095/304508.

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6

Peterson, E. W., P. L. Lagus, and K. Lie. Fluid flow measurements of Test Series A and B for the Small Scale Seal Performance Tests. Office of Scientific and Technical Information (OSTI), December 1987. http://dx.doi.org/10.2172/5697691.

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Marboe, R. C., A. A. Fontaine, and T. Cawley. Instrumentation and Equipment Upgrades to Improve Acoustical and Fluid Dynamic Measurements in the Garfield Thomas Water Tunnel. Fort Belvoir, VA: Defense Technical Information Center, October 2003. http://dx.doi.org/10.21236/ada418897.

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8

Kedzierski, Mark A., and Lingnan Lin. Update of Legacy NIST Horizontal Micro-Fin Tube Convective Boiling Measurements and Model with Current Fluid Property Values. National Institute of Standards and Technology, November 2021. http://dx.doi.org/10.6028/nist.tn.2179.

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9

Harmut Spetzler. Seismic Absorption and Modulus Measurements in Porous Rocks Under Fluid and Gas Flow-Physical and Chemical Effects: a Laboratory Study. Office of Scientific and Technical Information (OSTI), November 2005. http://dx.doi.org/10.2172/860985.

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Hoffman, Jeffrey A., Eric Eberhardt, and Jay K. Martin. Comparison Between Air-Assisted and Single-Fluid Pressure Atomizers for Direct-Injection SI Engines Via Spatial and Temporal Mass Flux Measurements,. Fort Belvoir, VA: Defense Technical Information Center, February 1997. http://dx.doi.org/10.21236/ada324774.

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