Dissertations / Theses on the topic 'Open channel'
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Hopton, Stephen. "Modelling open channel flow." Thesis, University of Nottingham, 2010. http://eprints.nottingham.ac.uk/11594/.
Full textDelis, Anargiros. "Computational modelling of open channel flow." Thesis, University of the West of England, Bristol, 1998. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.244309.
Full textMoores, Andrew. "Solute mixing in open channel flow." Thesis, Heriot-Watt University, 1996. http://hdl.handle.net/10399/686.
Full textShrestha, Purushottam. "Steady flow in steep open channel systems." Thesis, National Library of Canada = Bibliothèque nationale du Canada, 1998. http://www.collectionscanada.ca/obj/s4/f2/dsk2/tape17/PQDD_0026/MQ31403.pdf.
Full textDickman, Brian Daniel. "Large scale roughness in open channel flow." Thesis, Georgia Institute of Technology, 1990. http://hdl.handle.net/1853/22953.
Full textLegono, D. "Behaviour of flow in open channel bends." Thesis, City University London, 1986. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.375820.
Full textDaish, N. C. "Shear dispersion problems in open-channel flows." Thesis, University of Cambridge, 1985. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.372648.
Full textBayat, David, and Fabian Grönvik. "Demonstration station for open water channel flow." Thesis, KTH, Skolan för teknikvetenskap (SCI), 2020. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-276582.
Full textArshad, Arslan. "Flow characteristics of narrow vegetated open channels." Thesis, Edith Cowan University, Research Online, Perth, Western Australia, 2023. https://ro.ecu.edu.au/theses/2649.
Full textMcClymont, David W. "Exploring open channel block of the NMDA receptor." Thesis, University of Nottingham, 2011. http://eprints.nottingham.ac.uk/12996/.
Full textRoberts, Matthew Vincent Taylor. "Flow dynamics at open channel confluent-meander bends." Thesis, University of Leeds, 2004. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.414170.
Full textMacDonald, Ian. "Analysis and computation of steady open channel flow." Thesis, University of Reading, 1996. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.336664.
Full textStewart, Mark Thomas. "Turbulence structure of rough-bed open-channel flow." Thesis, University of Aberdeen, 2014. http://digitool.abdn.ac.uk:80/webclient/DeliveryManager?pid=210848.
Full textBoxall, Joseph B. "Dispersion of solutes in sinuous open channel flows." Thesis, University of Sheffield, 2000. http://etheses.whiterose.ac.uk/14803/.
Full textAya, Shirou. "Longitudinal and Transverse Mixing in Open-Channel Flows." Kyoto University, 1991. http://hdl.handle.net/2433/74583.
Full textBurger, Johannes Hendrik. "Non-Newtonian open channel flow: the effect of shape." Thesis, Cape Peninsula University of Technology, 2014. http://hdl.handle.net/20.500.11838/1296.
Full textOpen channels, flumes or launders are used in the mining industry to transport slurries during processing and to disposal sites. Water plays a major part in the makeup of these slurries, its usage and availability is critical in countries where there are strict water usage management programs. The optimisation of flume design involves the maximisation of solids transport efficiency whilst, at the same time reduces water usage. The design of open channels is complex as it is dependent on both the slurry rheology and the channel shape. Very little has been reported in the literature for predicting non-Newtonian laminar flow in open channels of arbitrary cross-section. The only method available was that proposed by Kozicki and Tiu (1967, 1986). The shape factors they used were those evaluated from analytical solutions for flow of Newtonian fluids in open channels of the same cross-section. However, they carried out no experimental work to validate their model. Few experimental studies have been made on the effect of shape on non-Newtonian flow in open channels. Naik (1983) tested kaolin in water suspensions in a rectangular channel. Coussot (1994) provided some data for the flow of a Herschel-Bulkley fluid in rectangular and trapezoidal channels. Fitton (2007; 2008) obtained data for flow of three different non-Newtonian fluids (carboxymethylcellulose, carbopol and thickened tailings) in a semi-circular channel. A large experimental database for non-Newtonian flow in rectangular open channels was published by Haldenwang (2003) at the Flow Process Research Centre, Cape Peninsula University of Technology. Guang et al. (2011) performed Direct Numerical Simulations of turbulent flow of a yield- pseudoplastic fluid in a semi-circular channel. They compared their simulations with actual field measurements and found them to over-predict the flow velocity by approximately 40%. The source for this discrepancy was difficult to ascertain. A comprehensive database was compiled during this research of the flow of three non–Newtonian fluids in rectangular, trapezoidal, semi-circular and triangular channels. The flow of carboxymethylcellulose solutions and aqueous kaolin and bentonite suspensions was investigated in a 10 meter long flume at angles ranging from 1° to 5° from the horizontal plane. The effect of channel shape on the friction factor-Reynolds number relationship for laminar and turbulent open channel flow of these three fluids was investigated. New models for the prediction of laminar and turbulent flow of non-Newtonian fluids in open channels of different cross-sectional shapes are proposed. The new laminar and turbulent velocity models are compared with three previously-published velocity models for laminar flow and five previously-published velocity models for turbulent flow using average velocity as comparison criteria. For each channel shape, the laminar flow data can be described by a general relationship, f = K/Re where f is the Fanning friction factor and Re is the appropriate Haldenwang et al. (2002) Reynolds number. The K values were found to be 14.6 for triangular channels with a vertex angle of 90°, 16.2 for semi-circular channels, 16.4 for rectangular channels and 17.6 for trapezoidal channels with 60 degree sides. These K values were found to be in line with those reported by Straub et al. (1958) and Chow (1969) for open channel laminar flow of Newtonian fluids as opposed to the assumption made by Haldenwang et al. (2002; 2004) of using a constant value of 16 based on the pipe flow paradigm for all channel shapes. This new laminar model gave a closer fit to the laminar flow data than those from the three previously-published models. However, the presence of the yield stress still presents a problem, which makes the flow prediction in laminar flow for such fluids not very accurate. The investigation on non-Newtonian turbulent flow of the three fluids in the four different shaped open channels revealed that the data was described by the modified Blasius equation f = a Re b where a and b are constant values determined for each channel shape and Re is the Haldenwang et al. (2002) Reynolds number. Values of a and b for a rectangular channel were found to be 0.12 and -0.330, for a semi- circular channel 0.048 and -0.205, for a trapezoidal channel with 60° sides, 0.085 and -0.266 and for a triangular channel with vertex angle of 90°, 0.042 and -0.202. New laminar and turbulent velocity models were derived from using the new laminar f = K/Re and turbulent f = a Re b, friction factor-Reynolds number relationship. The laminar velocity model did not always give the best result, but the majority of the time it did, compared to the three previously published models. The new turbulent velocity model yielded the best results when compared to the five previously published models using average velocity as comparison criteria. The composite power law modelling procedure of Garcia et al. (2003) used for pipe flow predictions was extended to the present work on non-Newtonian flow in open channels of various cross-sections. The results show that the modelling technique used by Garcia et al. (2003) for pipe flow can be used to adequately predict flow in an open channel of a given cross-sectional shape provided that an appropriate Reynolds number is used to take into account the non-Newtonian behaviour of the test fluid. It was found that the results using the Haldenwang et al. (2002) Reynolds number yielded better results than those based on the adapted Metzner-Reed Reynolds number. The correlations and models developed and experimentally validated during this research can be used to further improve the design of rectangular, semi-circular, trapezoidal and triangular open channels to transport non-Newtonian fluids.
Hunt, Alan Ernest. "The behaviour of turbulence in unsteady open channel flow." Thesis, University of Canterbury. Civil Engineering, 1997. http://hdl.handle.net/10092/7722.
Full textBelcher, Brian James. "VORTEX MODEL OF OPEN CHANNEL FLOWS WITH GRAVEL BEDS." UKnowledge, 2009. http://uknowledge.uky.edu/gradschool_diss/702.
Full textSharifi, Soroosh. "Application of evolutionary computation to open channel flow modelling." Thesis, University of Birmingham, 2009. http://etheses.bham.ac.uk//id/eprint/478/.
Full textWitz, Matthew J. "Mechanics of particle entrainment in turbulent open-channel flows." Thesis, University of Aberdeen, 2015. http://digitool.abdn.ac.uk:80/webclient/DeliveryManager?pid=225690.
Full textDvorak, Joseph Scot. "An optical water velocity sensor for open channel flows." Diss., Kansas State University, 2012. http://hdl.handle.net/2097/13979.
Full textDepartment of Biological and Agricultural Engineering
Naiqian Zhang
An optical sensor for determining water velocity in natural open channels like creeks and rivers has been designed and tested. The sensor consists of a plastic body which is shaped so that water flows through a U-shaped channel into which are mounted LEDs and matching phototransistors at various angles. A small amount of dye is injected into the water just upstream of two sets of LEDs and phototransistors which are spaced 4 cm apart. The time delay between the dye’s effects on these signals depends on water velocity and is determined using a biased cross correlation calculation. In addition to providing velocity, the LEDs and phototransistors can also be used to estimate soil sediment concentration. A previous version of the sensor was tested in enclosed flow to confirm that the general design of the sensor, including LEDs, phototransistors, dye and electronics, would indeed work to detect the velocity of water flowing through the sensor. Although the conditions for the test were unlike those experienced in natural open channels, the ability to catch all the fluid flowing through the sensor provided a simple confirmation of the velocity estimate that was not available in field settings. Further testing in the field then confirmed that the sensor worked in the field but also identified several areas needing improvement. Computational fluid dynamics was used to improve the sensor body. The electronics and program running the sensor were also redesigned. After making these improvements, a new version of the sensor was produced. The testing of the new version of the sensor confirmed its ability to accurately detect velocity in natural open channels. The velocity measurements from this sensor were compared to the commercially available Flowtracker velocity sensor. A regression analysis on the measurements from the two sensors found that the velocity measurements from each sensor were nearly identical across a range of velocities. Other tests established that the electronics and programming running the sensor performed as designed. The development and testing of this sensor has resulted in a system which works in natural open channels like creeks and rivers.
Valyrakis, Manousos. "Initiation of Particle Movement in Turbulent Open Channel Flow." Diss., Virginia Tech, 2011. http://hdl.handle.net/10919/27289.
Full textPh. D.
Campbell, Lorna J. "Double-averaged open-channel flow over regular rough beds." Thesis, University of Aberdeen, 2005. http://digitool.abdn.ac.uk/R?func=search-advanced-go&find_code1=WSN&request1=AAIU214372.
Full textShumate, Eric Dean. "Experimental Description of Flow at an Open-Channel Junction." Thesis, University of Iowa, 1998. https://ir.uiowa.edu/etd/5368.
Full textWAI, THWE AUNG. "DEVELOPMENT OF FUNDAMENTAL THEORY ON UNSTEADY OPEN CHANNEL FLOWS." Kyoto University, 2019. http://hdl.handle.net/2433/244536.
Full textSavio, Mario. "Turbulent structure and transport processes in open-channel flows with patchy-vegetated beds." Thesis, University of Aberdeen, 2017. http://digitool.abdn.ac.uk:80/webclient/DeliveryManager?pid=237016.
Full textKim, Su Jin. "3D numerical simulation of turbulent open-channel flow through vegetation." Diss., Georgia Institute of Technology, 2011. http://hdl.handle.net/1853/42892.
Full textOsawe, Maxwell Osayande. "Open channel turbulence modelling using layer-averaged large eddy simulation." Thesis, Queen Mary, University of London, 2001. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.392113.
Full textBeaman, Faye. "Large eddy simulation of open channel flows for conveyance estimation." Thesis, University of Nottingham, 2010. http://eprints.nottingham.ac.uk/11130/.
Full textLagoa, Sérgio Miguel Chilra. "Open economy New Keynesian macroeconomic models and the cost channel." Thesis, University of Leicester, 2010. http://hdl.handle.net/2381/8596.
Full textLu, Zhihua. "Stochastic modelling of unsteady open channel flow and reliability analysis /." View abstract or full-text, 2008. http://library.ust.hk/cgi/db/thesis.pl?CIVL%202008%20LU.
Full textOelerich, Jerry J. "Open-channel capillary flow in micro-scale helical support structures." Pullman, Wash. : Washington State University, 2009. http://www.dissertations.wsu.edu/Thesis/Spring2009/J_Oelerich_042709.pdf.
Full textTitle from PDF title page (viewed on June 8, 2009). "Department of Chemical Engineering." Includes bibliographical references (p. 70-71).
Kawamoto, Hideko. "Summer rain part 1, Summer rain - dawn, for two channel tape ; part 2, After the summer rain, for piano and two channel tape /." connect to online resource. Access restricted to the University of North Texas campus, 2001. http://www.library.unt.edu/theses/open/20013/kawamoto%5Fhideko/index.htm.
Full textWelch, Chapman. "Tele using vernacular performance practices in an eight channel environment /." Thesis, connect to online resource, 2003. http://www.library.unt.edu/theses/open/20032/welch%5Fchapman/index.htm.
Full textPapadopoulou, Symela. "Velocity distribution in shallow open channel flow over square bar roughness." Available from the University of Aberdeen Library and Historic Collections Digital Resources, 2009. http://digitool.abdn.ac.uk:80/webclient/DeliveryManager?application=DIGITOOL-3&owner=resourcediscovery&custom_att_2=simple_viewer&pid=58994.
Full textHurther, David. "3-D acoustic Doppler velocimetry and turbulence in open-channel flow /." Lausanne, 2001. http://library.epfl.ch/theses/?nr=2395.
Full textKironoto, Bambang Agus. "Turbulence characteristics of uniform and non-uniform, rough open-channel flow /." [S.l.] : [s.n.], 1993. http://library.epfl.ch/theses/?nr=1094.
Full textYulistiyanto, Bambang. "Flow around a cylinder installed in a fixed-bed open channel /." [S.l.] : [s.n.], 1997. http://library.epfl.ch/theses/?nr=1631.
Full textAfzalimehr, Hossein. "Contribution to non-uniform open channel flows over gravel and cobble." Thesis, National Library of Canada = Bibliothèque nationale du Canada, 1998. http://www.collectionscanada.ca/obj/s4/f2/dsk2/tape17/PQDD_0013/NQ36222.pdf.
Full textTachie, Mark Francis. "Open channel turbulent boundary layers and wall jets on rough surfaces." Thesis, National Library of Canada = Bibliothèque nationale du Canada, 2001. http://www.collectionscanada.ca/obj/s4/f2/dsk3/ftp04/NQ63927.pdf.
Full textWang, Kun-Pao, and 王昆保. "Open-Channel Chute Flow Analysis." Thesis, 1997. http://ndltd.ncl.edu.tw/handle/22950202375055464346.
Full text淡江大學
水資源及環境工程學系
85
This study presents experimental analysis for open-channel chute flow at channel bed with 30, 35, 38, and 41 degrees. The channel bed was coated by plastic blankets with rough surface to simulate the Manning''s roughness coefficients. The Manning''s roughness coefficients were equal 0.020, 0.022, and 0.025. The location of white water inception point was found to be proportional to bed slope and inversely proportional to Reynolds number and Manning''s roughness coefficient. The Manning''s roughness coefficients were further modified by the experimental data. Relationships between the effective depth or the depth with air concentration being 95% and the depth calculated by the standard step without air concentration were found which enable the depth-averaged air concentration to be calculated.
Yang, Ching-Hsu, and 楊景旭. "90 degree Dividing Open-Channel Flow." Thesis, 1997. http://ndltd.ncl.edu.tw/handle/85394637105908981463.
Full text淡江大學
水資源及環境工程學系
85
Dividing flow are of considerable importance in study of open-channel. An experimental investigation of the flow structure at a right angles dividing open-channel flow is presented. The most comprehensive studies were concerned with backwater characteristic and energy losses. Most of the investigators have studied the problem depending on the control condition in the main channel and the branch channel. At present, the study of dividing flow problem restricted the width ration of the branch channel to the main channel 1.0 and 0.5. At the downstream of the branch channel, using a pump of 5 hp to pump. Result of this study indicates that the section U4 and the section LO and the section L4 has about equal depth. In the branch channel, the width of circulation zone is larger at the surface than at the surface than at the bottom. The energy loss is large in the branch channel.
FAN, YUNN-CHERNG, and 樊運成. "90 degree Dividing Open-channel Flow." Thesis, 1998. http://ndltd.ncl.edu.tw/handle/01088593417882090150.
Full text淡江大學
水資源及環境工程學系
86
Dividing flow are of considerable importance in study of open- channel. An experimental investigation of the flow structure at a right angles dividing open-channel flow is presented. The most comprehensive studies were concerned with backwater characteristic and energy losses. Most of the investigators have studied the problem depending on the control condition in the main channel and thebranch channel. At present , the study of dividing flow problem restricted thewidth ration of the branch channel to the main channel 1.0 and 0.5. At thedownstream of the branch channel, using a pump of 5 hp to pump. Result of this study indicates that the section L0 and the section L4 has about equal depth. In the branch channel, the width of circulation zone is larger at the surface than at the bottom. The energy loss is large in the branch channel due to circulation.
WU, YING-BIN, and 吳慶彬. "Wave deformation in open channel of abrupt transitions of channel width." Thesis, 1989. http://ndltd.ncl.edu.tw/handle/13400964832284106807.
Full textHaque, AKM Enamul. "Some characteristics of open channel transition flow." Thesis, 2009. http://spectrum.library.concordia.ca/976403/1/MR63268.pdf.
Full textLi, Cheng-Pu, and 李政璞. "A Study of Open-Channel Chute Flow." Thesis, 2001. http://ndltd.ncl.edu.tw/handle/43530004196557697508.
Full text淡江大學
水資源及環境工程學系
89
This study talks about the chute flow of open-channel at channel bed with 41 degrees .The channel bed was covered with plastic blankets to simulate the Manning’s roughness coefficients .The study lets the Manning’s roughness coefficients equal to 0.020. In the study , use hot-film anemometer and conical hot-film probe and water probe calibration to get a calibration value about voltage and velocity of water .After computing , produce a critical voltage value and get an air concentration value . Use the both values to abtain the air concentration distribution normal to the bed . And get a perturbation range value .The depth calculated and the depth with air concentration being 95% and the effective depth were found in the study.
Li, Wei-Yi, and 李威毅. "Design of Non-contactive Open-channel Flowmeter." Thesis, 1999. http://ndltd.ncl.edu.tw/handle/00994582701707992505.
Full text國立中央大學
電機工程研究所
87
In industry, flow velocities and volumes are both very important parameters, but it is not easy to be measured accurately. Traditional flowmeters have some limitations, such as high temperature, erosive, poison, inflammable environment. Hence, they are only used in certain types of fluid and may cause great inaccuracy or inconvenience. Moreover, highly accurate flowmeters are expensive in both price and maintenance. Consequently the motive of this dissertation is coming out. The aim of this project is to measure flow velocity in open channel. The measurement theory is based on the Cross-Correlation Technique ,which calculates the relationship between two groups of signal. Two optical sensors are placed in line above the open channel and along the direction of flow. Because of the continuity of the flow, the time delay between the two received signals can be calculated by the cross-correlation function. The flow velocity can then be calculated by dividing distance by the time laterly. The non-contative flowmeter using the cross-correlation technique can avoid the complexity caused by different fluid properties. A 8052 single chip is used in the circuit. This makes the other merits of the circuit. Programmable softwares in the chip are designed to replace complex hardware circuit, to minimize the size of the flowmeter, and to reduce the cost of the development and maintenance. Moreover, it can achieve real-time measurement and display of the velocity of the flow. The data can be transmited to the PC, the curves of cross-correlation function, flow velocity and volume are displayed on screen. It is very helpful in verifying the correction of calculation process and the results of measurement.
Kuo, Po-Wen, and 郭博文. "A Study for Unsteady Open Channel Flow." Thesis, 2002. http://ndltd.ncl.edu.tw/handle/43664883488092232446.
Full text淡江大學
水資源及環境工程學系
90
The objective of this study is to develop a linearized analytical solution for unsteady open channel flow. The method is applied to rectangular trapezoidal cross sections and natural stream flow. In the process, I neglected the inertia terms in the Saint-Venant moment equation. And obtained the linearized Saint-Venant equation by small perturbation method. Compare the analytical solutions with the numerical solutions, the linearized analytical solution can obtain a good approximation efficiently if we choose an appropriate reference discharge.
Subrahmanya, Praveena Alangar, and 蘇邁亞. "Pool boiling on open trapezoidal channel surface." Thesis, 2015. http://ndltd.ncl.edu.tw/handle/82191724169102979509.
Full text國立中央大學
能源工程研究所
103
In this thesis pool boiling experiment is carried out on open trapezoidal channel surface to study the effect of channel top width (0.4mm, 0.8mm, 1.4mm and 2.0mm) and fin pitch using saturated methanol as working fluid at one atmospheric pressure along with bubble dynamic visualisation. The channel were cut using wire electro-discharge machining technique and results are compared with corresponding plane surfaces. Plain boiling surface with comparatively high roughness value (manufactured by wire electro-discharge machining) consistently showed higher heat transfer performance than emery surface with lower roughness value. All channel surfaces performed better than plain surface prepared by emery paper. For all the tested trapezoidal channel surfaces, bubbles only generated from the channel surface because of high roughness on channel surface. There was no bubble generation from fin top surface. Therefore overall channel surface area played major role along with the effect of channel geometry on HTC & CHF and the results are meant to compare with plain surface made by EDM process. Two distinctive bubble dynamics are observed as the channel top width increased. For channel having top width 0.4mm, single bubble generated across the channel and it attached to channel side surface and grew on top of channel till the departure. Therefore the heat transfer performance increased as the fin pitch reduced. But in comparison with Plain EDM surface, its nucleate boiling HTC found to be lower because overall available boiling surface area (ie channel surface area) is lower. From channel having top width 0.8mm to 2.0mm, number of nucleation sites across channel surface increased accordingly with the channel cross section area. Therefore multiple bubble nucleation sites were observed. On these channel top width surfaces, a heat transfer enhancement mechanism observed. Therefore even though the channel surface area was lower than that of plain EDM surface, nucleate boiling HTC were either equal or more than plain EDM surface observed. Reduction in fin pitch had no major effect on HTC. For channel made by EDM process having different roughness value in comparison with fin top surface has different liquid and vapor flow path ways. Majority of the liquid supply to rewet the boiling surface (i.e channel surface) were from fin top surface. As the fin pitch decreases, CHF found to increase for all tested channel top widths because of increases in channel surface area as well as enhancement in heat transfer mechanism over channel surface.
Yu, Wen-Pu, and 游文圃. "Energy Loss for series Cylinders along channel bank in Open-Channel Flow." Thesis, 2012. http://ndltd.ncl.edu.tw/handle/22786350800670770832.
Full text淡江大學
水資源及環境工程學系碩士班
100
This study uses the model and simulation to analyze the Energy Loss for series cylinders along channel bank in Open-Channel Flow. The test model to placed on straight channel. The experiment was conducted in flume 10.50m long, 0.39m wide and 0.19m high with bed slope=0.003. Placed in the channel one to nine cylindrical,cylinder width of 3.4cm and 4.0cm,cylindrical center distance is 4.0cm The test set Different boundary conditions up to Energy loss of series cylinder under various Froude numbers. This study uses the FLUENT to establish the unsteady flow numerical model. Simulate with turbulence model based on three-dimensional model. The simulation conditions and model conditions are the same. Compare and analyze simulation and experimental results.