Dissertations / Theses on the topic 'Microchannel'
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Price, Gareth James. "Microchannel plates in astronomy." Thesis, University of Leicester, 2001. http://hdl.handle.net/2381/8638.
Full textChecketts, Gus Thomas. "Microchannel Radiator: an Investigation of Microchannel Technology with Applications in Automotive Radiator Heat Exchangers." Thesis, University of North Texas, 2014. https://digital.library.unt.edu/ark:/67531/metadc700005/.
Full textBenoit, Vincent. "Flow-through microchannel DNA chips." Thesis, University of Glasgow, 2001. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.368731.
Full textMartin, Adrian Peter. "Exploitation of microchannel plate optics." Thesis, University of Leicester, 2000. http://hdl.handle.net/2381/30635.
Full textSiu, Billy Chin Pang. "Condensation heat transfer in microchannel /." View abstract or full-text, 2004. http://library.ust.hk/cgi/db/thesis.pl?MECH%202004%20SIU.
Full textIncludes bibliographical references (leaves 43-46). Also available in electronic version. Access restricted to campus users.
Mehrotra, Rajat. "Monodispersed polygonal water droplets in microchannel." [College Station, Tex. : Texas A&M University, 2008. http://hdl.handle.net/1969.1/ETD-TAMU-2726.
Full textBurg, Thomas P. (Thomas Peter). "Suspended microchannel resonators for biomolecular detection." Thesis, Massachusetts Institute of Technology, 2005. http://hdl.handle.net/1721.1/34471.
Full textIncludes bibliographical references (leaves 115-124).
Microfabricated transducers enable the label-free detection of biological molecules in nanoliter sized samples. Integrating microfluidic detection and sample-preparation can greatly leverage experimental efforts in systems biology and pharmaceutical research by increasing analysis throughput while dramatically reducing reagent cost. Microfabricated resonant mass sensors are among the most sensitive devices for chemical detection, but degradation of the sensitivity in liquid has so far hindered their successful application in biology. This thesis introduces a type of resonant transducer that overcomes this limitation by a new device design: Adsorption of molecules to the inside walls of a suspended microfluidic channel is detected by measuring the change in mechanical resonance frequency of the channel. In contrast to resonant mass sensors submersed in water, the sensitivity and frequency resolution of the suspended microchannel resonator is not degraded by the presence of the fluid. Our device differs from a vibrating tube densitometer in that the channel is very thin, and only molecules that bind to the walls can build up enough mass to be detected; this provides a path to specificity via molecular recognition by immobilized receptors.
(cont.) Suspended silicon nitride channels have been fabricated through a sacrificial polysilicon process and bulk micromachining, and the packaging and microfluidic interfacing of the resonant sensors has been addressed. Device characterization at 30 mTorr ambient pressure reveals a quality factor of more than 10,000 for water filled resonators; this is two orders of magnitude higher than previously demonstrated Q-values of resonant mass sensors for biological measurements. Calculation of the noise and the sensitivity of suspended microchannel resonators indicate a physical limit for mass resolution of approximately 0.01 ng/cm2 (1 Hz bandwidth). A resolution of -0.1 ng/cm2 has been experimentally demonstrated in this work. This resolution constitutes a tenfold improvement over commercial quartz crystal microbalance based instruments. The ability to detect adsorbing biomolecules by resonance frequency has been validated through binding experiments with avidin and various biotinylated proteins.
by Thomas P. Burg.
Ph.D.
Parak, Muhammad. "Development of a microchannel reactor model." Master's thesis, University of Cape Town, 2011. http://hdl.handle.net/11427/11615.
Full textIncludes bibliographical references (p. 151-157).
The development and future wide-spread use of hydrogen fuel cells is inhibited by problems associated with hydrogen storage. A possible alternative is to store and then reform hydrocarbons to yield hydrogen in an on-board fuel processing system. Microchannel reactors have reduced mass and heat transfer limitations and are able to exploit fast intrinsic kinetics. Also, their high surface area to volume ratio reduces their size for a constant throughput, increasing their potential for miniaturised deployment. Current microchannel reactor models are either over simplified and neglect important subtleties, or too complex and are not usable for optimisation or sensitivity studies. The objective of this project is to develop a comprehensive model that obeys the phenomenological laws and is fast enough to be used for optimisation.
Fogg, David W. "Bubble dynamics in microchannel flow boiling /." May be available electronically:, 2007. http://proquest.umi.com/login?COPT=REJTPTU1MTUmSU5UPTAmVkVSPTI=&clientId=12498.
Full textDagle, Robert Alexander. "Fuel processing catalysis for microchannel applications." Online access for everyone, 2005. http://www.dissertations.wsu.edu/Thesis/Spring2005/r%5Fdagle%5F050305.pdf.
Full textPettersen, Jostein. "Flow vaporization of CO2 in Microchannel Tubes." Doctoral thesis, Norwegian University of Science and Technology, Faculty of Engineering Science and Technology, 2002. http://urn.kb.se/resolve?urn=urn:nbn:no:ntnu:diva-87.
Full textLee, Hyun Ho. "A thin film transistor driven microchannel device." Texas A&M University, 2004. http://hdl.handle.net/1969.1/1439.
Full textGao, Yanfeng. "Inertial migration of particles in microchannel flows." Thesis, Toulouse, INSA, 2017. http://www.theses.fr/2017ISAT0010/document.
Full textThis thesis aims to better understand the physical mechanism controlling the trajectories of particles in confined flows in order to improve predictive models. In the first step we have developed experimental tools based on microscopy and image analysis in order to identify the particles positions in confined flows in square section microchannels. These tools have then permitted to obtain original results on the lateral migration of spherical particles in flows at low inertia. In particular we have shown that neutrally buoyant particles in square channels are focused at channel center at low Reynolds number and at four channel faces at high Reynolds, and that there is a co-existence of the two regimes for intermediate Reynolds. In addition to their lateral migration, under certain conditions, particles can also align in the flow direction to form trains of evenly spaced particles. This work has thus been devoted to the statistical study on the quantification and localization of the train formation and configuration. It has been shown that the formation of trains is controlled by the flow configuration in the wake of the particles, and that the train characteristics, i.e., the fraction of particles in trains and the interparticle distance, are functions of the particle Reynolds number. Finally, preliminary results on flows of bidisperse suspensions have been obtained. To conclude, the perspectives and future developments of this work are presented
Carpenter, James David. "Microchannel plates in astronomy and planetary science." Thesis, University of Leicester, 2006. http://hdl.handle.net/2381/7983.
Full textGreen, James Alexander. "Mixing in surface tension driven microchannel flows." Thesis, University of Hertfordshire, 2006. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.440160.
Full textChen, Siyu S. M. Massachusetts Institute of Technology. "Bubble dynamics on structured surface in microchannel." Thesis, Massachusetts Institute of Technology, 2013. http://hdl.handle.net/1721.1/81595.
Full textCataloged from PDF version of thesis.
Includes bibliographical references (p. 69-70).
Surface enhancement is a potential way to improve the performance of flow boiling in microchannels, which is considered to be one of the most promising cooling methods to solve thermal management challenges faced by future semiconductor products. Considerable research has been done on examining the functions of engineered surfaces. However, the mechanism of how these surfaces improve the flow boiling performance is still unclear. In this thesis, bubble dynamics on micropillar array surfaces were studied. A surface energy based model is presented to predict the bubble morphology on pillar array surfaces. The results showed that bubbles tend to stay on top surfaces of pillars at solid fractions greater than 0.162, keeping liquid films underneath the bubbles. On the other hand, on surfaces at solid fraction less than 0.162, bubbles tend to propagate within the pillar unit cells. A flow loop with good degassing and a fluid temperature control system was designed and built for various flow boiling experiments. Five different types of silicon micropillar array surfaces were fabricated. Moreover a setup for observing bubble dynamics in microchannels under flow boiling conditions was developed. Experiments were performed to investigate the bubble dynamics on silicon micropillar array surfaces. Bubble departure modes were observed. The bubble departure size of direct departing mode was found to be independent with flow rate while departure size of sliding mode decreased with increasing of the flow rate. Three potential methods to create single nucleation sites for improved studies of bubble dynamics were also presented in this thesis. An experimental setup to investigate behavior of a single bubbles created by air injection on micropillar array was presented. Single 10-30 [mu]m injection holes were fabricated on micropillar array surfaces by laser cutter. The experimental results show that structured surfaces have higher bubble departure sizes than that for a plain surface. The surfaces with solid fractions greater than 0.162 had larger departure sizes than that of surfaces with solid fractions smaller than 0.162 at mass flow rates above 250 kg/m²s while departure sizes of the higher solid fraction surfaces become smaller than that of lower solid fraction surfaces when flow rates decreased below 200 kg/m²s. The similarity between the departure sizes obtained by air injection experiments and flow boiling experiments suggest that air injection experiments could provide useful information on understanding the vapor bubble departure behavior on micropillar array surfaces. Silicon micropillar array surfaces may have larger bubble departure sizes than plain surfaces, however, the surfaces with solid fractions greater than 0.162 are suggested for boiling due the a large amount of liquid thin films may create for higher heat transfer rates.
by Siyu Chen.
S.M.
Phillips, Richard J. "Forced-convection, liquid-cooled, microchannel heat sinks." Thesis, Massachusetts Institute of Technology, 1987. http://hdl.handle.net/1721.1/14921.
Full textMICROFICHE COPY AVAILABLE IN ARCHIVES AND ENGINEERING
Bibliography: v.2, leaves 286-291.
by Richard J. Phillips.
M.S.
Talebi, Mohammadmahdi [Verfasser]. "Local Sensing in Microchannel Boiling / Mohammadmahdi Talebi." München : Verlag Dr. Hut, 2021. http://d-nb.info/1240540027/34.
Full textKulkarni, Amit S. "Effects of surface roughness in microchannel flows." [Gainesville, Fla.] : University of Florida, 2004. http://purl.fcla.edu/fcla/etd/UFE0003400.
Full textKuravi, Sarada. "Numerical Study of Encapsulated Phase Change Material (EPCM) Slurry Flow in Microchannels." Doctoral diss., University of Central Florida, 2009. http://digital.library.ucf.edu/cdm/ref/collection/ETD/id/4093.
Full textPh.D.
Department of Mechanical, Materials and Aerospace Engineering;
Engineering and Computer Science
Mechanical Engineering PhD
Cetin, Murat. "Design And Experimental Investigation Of Microchannel Heat Exchanger." Master's thesis, METU, 2010. http://etd.lib.metu.edu.tr/upload/12611856/index.pdf.
Full textEllob, Mohamed. "Process intensification : hydrocarbon cracking using a microchannel reactor." Thesis, University of Newcastle Upon Tyne, 2009. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.500964.
Full textDavies, Colin John Stephen. "MRI studies of complex fluids and microchannel flows." Thesis, University of Cambridge, 2009. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.598355.
Full textLackritz, Neal M. "MERLIN : a multiprocessor design for a MicroChannel architecture." Thesis, Massachusetts Institute of Technology, 1989. http://hdl.handle.net/1721.1/14287.
Full textSon, Sungmin. "Suspended microchannel resonators for ultralow volume universal detection." Thesis, Massachusetts Institute of Technology, 2008. http://hdl.handle.net/1721.1/44867.
Full textIncludes bibliographical references (leaves 32-33).
Universal detectors that maintain high sensitivity as the detection volume is reduced to the sub-nanoliter scale can enhance the utility of miniaturized total analysis systems ([mu]-TAS). Here the unique scaling properties of the suspended microchannel resonator (SMR) are exploited to show universal detection in a 10 pL analysis volume with a density detection limit of ~1 ([mu]g/cm³ (10 Hz bandwidth) and a linear dynamic range of six decades. Analytes with low UV extinction coefficients such as polyethylene glycol (PEG) 8 KDa, glucose, and glycine are measured with molar detection limits of 0.66 ([mu]M, 13.5 ([mu]M, and 31.6 ([mu]M, respectively. To demonstrate the potential for real-time monitoring, gel filtration chromatography was used to separate different molecular weights of PEG as the SMR acquired a chromatogram by measuring the eluate density. This work suggests that the SMR could offer a simple and sensitive universal detector for various separation systems from liquid chromatography to capillary electrophoresis. Moreover, since the SMR is itself a microfluidic channel, it can be directly integrated into ([mu]-TAS without compromising overall performance.
by Sungmin Son.
S.M.
Chivengwa, Tapiwa. "Microchannel flow fields for polymer electrolyte fuel cells." Master's thesis, University of Cape Town, 2015. http://hdl.handle.net/11427/13674.
Full textLee, Man. "Forced convection heat transfer in integrated microchannel heat sinks /." View abstract or full-text, 2006. http://library.ust.hk/cgi/db/thesis.pl?MECH%202006%20LEE.
Full textTurkakar, Goker. "Numerical Simulation And Analytical Optimization Of Microchannel Heat Sinks." Master's thesis, METU, 2010. http://etd.lib.metu.edu.tr/upload/12612377/index.pdf.
Full textC under a constant pumping power requirement. Taking the objective function as the total thermal resistance, the optimum geometries have been obtained for the mentioned metal-polymer heat sinks as well as more conventional silicon ones. The results of the optimization code agreed very well with available ones in the literature. In the optimization study, the Intel Core i7-900 Desktop Processor Extreme Edition Series is considered as a reference processor which is reported to dissipate 130 W of heat and to have chip core dimensions of 1.891 cm ×
1.44 cm. A dimensional optimization study has been performed for various copper and silicon microchannel heat sinks to cool down this processor. To the best of the author&rsquo
s knowledge, this study contributes to the literature in that, as opposed to the available analytical microchannel optimization studies considering constant thermophysical properties at the fluid inlet temperature, the properties are evaluated at the area weighted average of the fluid inlet and iteratively calculated outlet temperatures. Moreover, the effects of the thermal and hydrodynamic entrance regions on heat transfer and flow are also investigated.
Ulu, Ayse Gozde. "Experimental Investigation Of Uninterrupted And Interrupted Microchannel Heat Sinks." Master's thesis, METU, 2012. http://etd.lib.metu.edu.tr/upload/12614227/index.pdf.
Full textm channel widths. Two different versions of interrupted channels are tested
with single interruption and with 7 interruptions. Distilled water is used as the working fluid and tests are conducted at volumetric flow rates in a range of 0.5-1.1 lpm. Thermoelectric foils are used to supply uniformly distributed heat load to the heat sinks such that for all the tests the heat removed by water is kept constant at 40 W. Pressure drop and temperature increase are measured along the channels of different configurations for a number of different flow rates. For the interrupted channels thermal boundary layers re-initialize at the leading edge of each interrupted fin, which decreases the overall boundary layer thickness. Also the flow has been kept as developing, which results in better heat transfer performance. Due to the separation of the flow into branches, secondary flows appear which improves the mixing of the stream. Advanced mixing of the flow also enhances the thermal performance. In the experiments, it is observed that interruption of channels improved the thermal performance over the uninterrupted counterparts up to 20% in average Nusselt number, for 600 micron-wide channels. The improvement of average Nusselt number between the single interrupted and multi interrupted channels reached a maximum value of 56% for 500 micron-wide channels. This improvement did not cause a high pressure drop deviation between the uninterrupted and interrupted microchannels even for the maximum volumetric flow rate of 1.1 lpm. Highest pressure drop through the channels was measured as 0.07 bar, which did not require to change the pump. In the tests, maximum temperature difference between the inlet of the fluid and the base of the channel is observed as 32.8°
C, which is an acceptable value for electronic cooling applications.
Schindhelm, Eric R., J. C. Green, Oswald H. W. Siegmund, Camden Ertley, Brian T. Fleming, Kevin C. France, Walter M. Harris, Alex Harwit, Stephan R. McCandliss, and John V. Vallerga. "Microchannel plate detector technology potential for LUVOIR and HabEx." SPIE-INT SOC OPTICAL ENGINEERING, 2017. http://hdl.handle.net/10150/626502.
Full textBennett, Christopher James. "Solitary and transitional waves in two-layer microchannel flows." Thesis, University of Birmingham, 2015. http://etheses.bham.ac.uk//id/eprint/5922/.
Full textStockslager, Max A. "Measuring single-cell density using serial suspended microchannel resonators." Thesis, Massachusetts Institute of Technology, 2017. http://hdl.handle.net/1721.1/111934.
Full textCataloged from PDF version of thesis.
Includes bibliographical references (pages 42-43).
Cells adjust their composition during important physiological processes, including cell cycle progression, apoptosis, and disease. Due to differences in the densities of water and the various macromolecules which compose cells, changes in cellular composition are reflected by changes in cell density. Previously, methods have been described for measuring density at the single-cell level using suspended microchannel resonators by weighing the same cell in fluids of different densities. Here we describe a high-throughput version of this approach, in which cells are weighed sequentially in three cantilevers containing fluids of different densities. The system design and operation are described, measurement uncertainty is characterized, and single-cell density measurements are compared to those obtained using existing techniques. As a demonstration, we use the system to characterize the biophysical response of CD8' T cells during activation. We find that single-cell density distinguishes between the phenotypically distinct human CD8' T cells of healthy vs. chronic lymphocytic leukemia donors, suggesting possible utility as a lymphocyte transformation assay. In summary, the system as described is capable of measuring single-cell density with improved throughput, and the approaches used here for on-chip fluid exchange are applicable to other SMR devices where it is desirable to weigh a cell in multiple fluids, e.g., to measure single-cell growth rate before and after drug or media perturbations..
by Max A. Stockslager.
S.M.
Von, Muhlen Marcio Goldani. "Label-free buoyant mass assays with suspended microchannel resonators." Thesis, Massachusetts Institute of Technology, 2010. http://hdl.handle.net/1721.1/62389.
Full textCataloged from PDF version of thesis.
Includes bibliographical references (p. 105-112).
Improved methods are needed for routine, inexpensive monitoring of biomarkers that could facilitate earlier detection and characterization of complex diseases like cancer. Development of new assay formats based on microfluidic, label-free platforms enable radical reductions in assay complexity and reagent requirements with the potential for such applications. Suspended microchannel resonators (SMRs) are highly sensitive, batch-fabricated microcantilevers with embedded microchannels that can measure mass with femtogram precision. Biomolecules such as proteins and nucleic acids are denser than water, and their presence can thus be quantified by their buoyant mass, or increase in mass relative to the solution they displace. This thesis presents two approaches to conducting label-free, buoyant-mass immunoassays with SMRs with potential for clinical applications. The sensor surface can be functionalized to bind targets directly, or individually weighed polystyrene beads can be used as mobile supports. As in other label-free detection methods, biomolecular measurements in complex media such as serum are challenging due to high background signals from non-specific binding. We demonstrate that carboxybetaine-derived polymers developed to adsorb directly onto SMR SiO2 surfaces act as ultra-low fouling and functionalizable surface coatings. Coupled with a reference microcantilever, this approach enables detection of activated leukocyte cell adhesion molecule (ALCAM), a model cancer biomarker, in undiluted serum with a limit of detection of 10 ng/mL. Decoupling the complexity of surface modifications from the sensor precludes the need for specialized reagents. Monodisperse, micron-scale polystyrene beads are widely available and can be used as mobile supports, with the mean mass of a bead population quantifying target binding onto bead surfaces. Inherent mass variability in the bead population is masked by matching solution density to bead density. We demonstrate that by weighing hundreds of beads in 30 min, mean mass can be estimated with a resolution of 100 attograms. A proof-of-principle assay is demonstrated that quantifies IgG binding onto functionalized beads at 5.20 femtograms per bead.
by Marcio Goldani von Muhlen.
Ph.D.
Alexander, Brentan R. "Design of a microbreather for two-phase microchannel devices." Thesis, Massachusetts Institute of Technology, 2008. http://hdl.handle.net/1721.1/44919.
Full textThis electronic version was submitted by the student author. The certified thesis is available in the Institute Archives and Special Collections.
Includes bibliographical references (p. 50-52).
Multiphase flows in microchannels are encountered in a variety of microfluidic applications. Two-phase microchannel heat sinks leverage the latent heat of vaporization to offer an efficient method of dissipating large heat fluxes in a compact device. In microscale methanol-based fuel cells, the chemical reactions produce a two-phase flow of methanol solution and carbon dioxide gas. Differences in the underlying physics between microscale and macroscale systems, however, provide a new set of challenges for multiphase microscale devices. In thermal management devices, large pressure fluctuations caused by the rapid expansion of vapor are prevalent in the flow channels. In fuel cells, the gaseous carbon dioxide blocks reaction sites. In both of these cases, dry-out is a problem that limits device performance. We propose a design for a microscale breather that uses surface chemistry and microstructures to separate gas from a liquid flow to improve two-phase microchannel performance. To better understand the physics and governing parameters of the proposed breather, we have designed and fabricated test devices that allow cross-sectional visualization of the breathing events. We have conducted various experiments to examine the effects of device channel hydraulic diameters ranging from 72 [mu]m to 340 [mu]m and liquid inlet flow rates ranging from 0.5 cm/s to 4 cm/s on the maximum gas removal rate. We demonstrated a maximum breather removal rate of 48.1 [mu]l/min through breather ports with a hydraulic diameter of 4.6 [mu]m connected to a microchannel with a hydraulic diameter of 72 [mu]m, and a liquid inlet flow velocity of 0.5 cm/s. A model was developed that accurately predicts the exponential dependence of the maximum gas removal rate on a non-dimensional ratio of the pressure across the breather ports compared to the pressure drop in the main channel caused by the venting bubble.
(cont.) These results serve as design guidelines to aid in the development of more efficient and sophisticated breathing devices. The successful implementation of a microchannel with an efficient breather will allow for new technologies with higher heat removal capacities or chemical reaction rates that can be effectively used by industry.
by Brentan R. Alexander.
S.M.
Zandi, Matthew A. "Single Position Focusing of Cells in a Microchannel System." University of Cincinnati / OhioLINK, 2015. http://rave.ohiolink.edu/etdc/view?acc_num=ucin1428066046.
Full textTruter, Lara. "Development of a zeolite washcoating technique for microchannel reactors." Master's thesis, University of Cape Town, 2011. http://hdl.handle.net/11427/10855.
Full textSkog, Torkel. "CuPGS Laminate Core for a Matrix Microchannel Heat Exchanger." Thesis, Luleå tekniska universitet, Institutionen för system- och rymdteknik, 2019. http://urn.kb.se/resolve?urn=urn:nbn:se:ltu:diva-76914.
Full textShiao, Shin-Duan, and 蕭心端. "Experimental Study of Microchannel Geometry on the Microchannel Heat Sink Performance Enhancement." Thesis, 2006. http://ndltd.ncl.edu.tw/handle/77817152086764854254.
Full text國立中興大學
機械工程學系所
94
In this study,performances of two types of microscale heat sinks based on the modifications from the conventional parallel channel heat sink (PCHS) are studied experimentally。By referring the walls that separating the channels in PCHS as the plate fins,the first type of modified heat sinks involves placing obstacles alternatively on the plate fins. As a result,the original parallel channels in PCHS become winded。This type of heat sink is referred to as the obstructive channel heat sink (OCHS)。It is intended to enhance the heat transfer coefficient by the flow disruption in this heat sink design。In the second type of heat sink,the plate fins are cut into segments and arranged in staggered form。This results in the plate fins in the original parallel heat sink been modified to a staggered arranged pin fin array and the heat sink is referred as the pin fin heat sink (PFHS)。Since the transverse fluid flow in pin fin array is allowed,the PFHS is designed to have two inlets and two outlets to enhance heat transfer coefficient。The heat sink base plate temperature uniformity,thermal resistance,and pressure drop across the heat sink are the three parameters used to evaluate the performances of the heat sinks studied。For all these three parameters,the experimental results show that the PFHS can provide best temperature uniformity,lowest thermal resistance and lowest pressure drop among the three heat sink designs in this study。
Huang, Yu Hsiang, and 黃友相. "Laminar Heat Transfer in Microchannel." Thesis, 1999. http://ndltd.ncl.edu.tw/handle/33228770672319143894.
Full textLi, Chi-hung, and 李奇翃. "Biomolecular Adsorption in the Microchannel." Thesis, 2014. http://ndltd.ncl.edu.tw/handle/63123549499748252059.
Full text國立臺灣科技大學
機械工程系
102
The protein adsorption is a critical factor in influencing the performance of a biochip which is used for disease detection. In this study, numerical simulation was used to estimate the protein adsorption rate in terms of the flowing velocity, design of the inlet, the length of the microchannel. To validate the simulation results, the microfluidic devise was fabricated with a micromilling machine and the PDMS casting technique. Then the microchannel was sealed with another piece of glass with the surface plasma treatment and used for experiments. Multiple experiments were conducted either with a confocal microscope or a fluorescence microscope, but the results were not steady enough to compare or even conclude with the simulation result. Therefore modification of the experiments will be made to improve the quality of the experiments, then validate the simulation results.
Yen, Hung-Yu, and 顏鴻宇. "Capillary Phenomena in a Microchannel." Thesis, 2013. http://ndltd.ncl.edu.tw/handle/76515072230750919342.
Full text國立臺灣大學
化學工程學研究所
101
This work investigate capillary phenomenon in different types of microchannels. Capillary rise can be described by Jurin’s Law under specific scale and the results are consistent with Surface Evolver simulation. However, capillary rise can also be studied via the energy minimization method, thus the capillary rise in the stepped tube and in composite tube are examined to model the water transportation in trees. In the process of increasing the tube height, liquid level increases with the tube height. The highest liquid level is determined by the radius of the top opening which is consistent with the effective volume theory. According to this result, we propose that the height of water transportation in trees is determined by the radius of the stomas. The simulation results of the capillary rise in a composite tube also coincide the effective volume theory. And the results of capillary rise in composite tube indicate that the highest liquid level is restricted by the max radius on the top opening of the composite tube. The liquid drop captured at the capillary end, which is observed in capillary valve and pendant drop technique, is also investigated theoretically and experimentally in this thesis. Because of contact line pinning of the lower meniscus, the lower contact angle is able to rise from the intrinsic contact angle ( ) so that the external force acting on the drop can be balanced by the capillary force. In the absence of contact angle hysteresis (CAH), the upper contact angle remains at . However, in the presence of CAH, the upper contact angle can descend to provide more capillary force. The coupling between the lower and upper contact angles determines the equilibrium shape of the captured drop. In a capillary valve, the pinned contact line can move across the edge as the pressure difference exceeds the valving pressure, which depends on the geometrical characteristic and wetting property of the valve opening. When CAH is considered, the valving pressure is elevated because the capillary force is enhanced by the receding contact angle. For a pendant drop under gravity, the maximal capillary force is achieved as the lower contact angle reaches 180˚ in the absence of CAH. However, in the presence of CAH, four regimes can be identified by three critical drop volumes. The lower contact angle can exceed 180˚ and therefore the drop takes on the shape of a light bulb, which does not exist in the absence of CAH. The comparisons between Surface Evolver simulations and experiments are quite well.
Tu, Kuan-Hsu, and 凃冠旭. "Condensation Heat Transfer Enhancementin Microchannel." Thesis, 2013. http://ndltd.ncl.edu.tw/handle/61905943294136803719.
Full text國立臺灣大學
機械工程學研究所
101
The microchannel evaporator with two-phase heat transfer achieves a high heat transfer coefficient, and low working fluid demands; therefore, is considered to have high potential. Thus, the use of microchannel condenser that uses two-phase heat transfer is seen as a cooling component with very high potential. By making it a porous structure that creates a 3D porous network, resulting in advantages such as large evaporation area, high capillary force, and high permeability, the heat transfer performance of the microchannel condenser is expected to increase significantly. This study used copper to manufacture both the flat-plate microchannel condenser and porous microchannel condenser, with 30 microchannels of width and depth 500μm×155μm; Using water as working fluid, with mass flux range of 65~95 kg/m2 s, for heat transfer performance test. This study first investigates the effect of copper powder size and the structure’s base thickness of a porous microchannel condenser on heat transfer performance, then compares its heat transfer performance, pressure drop, and flow patterns to those of flat-plate microchannel condenser. Comparing experimental results for heat transfer performance to heat transfer correlation of the conventional channel showed that the MAE is still large. With regard to pressure drop, compare with the correlation of microchannel developed recently, it correlated with our result, indicating a certain degree of reliability. For flat-plate microchannel condenser, from flow visualizations of flows, 5 most common types of flow in condensation process can be seen clearly: droplet flow, annular flow, injection flow, slug flow, and bubbly flow. Heat transfer coefficient and pressure drop is positive correlative with increasing mass flux. When mass flux increases, the flow velocity increases, and the liquid-vapor interface shear stress increases, resulting in thinning of the liquid film, and the annular flow region increases; the heat transfer performance was thus enhanced accordingly. Heat transfer coefficient is 23~79kw/m2k. The overall pressure drop was also enhanced due to increased flow rate of the working fluid and elongation of the two-phase region. For porous microchannel condenser, manufacturing parameters such as the base thickness range of 150~300μm and copper powder diameter range of 1~150μm was investigated. Experimental results showed that highest heat transfer coefficient was achieve with base thickness of 150μm and powder diameter of 88μm; heat transfer coefficient is 43~161kw/m2k, on average, the heat transfer coefficient of porous microchannel condenser was increased by 110% compared to that of flat-plate microchannel condenser. The absorption of condensed water build up by a porous microchannel structure allows for the thinning of the condensed liquid film and the annular flow region is more extended, therefore its heat transfer performance is better than that of a regular flat-plate microchannel condenser. Concerning pressure drop, the overall pressure drop is greater than that for flat-plate microchannel condenser, with a greatest enhancement value of 15kpa. To summarize this study, porous microchannel effectively enhance the heat transfer performance of condenser, It is highly potential for the high-power thermal management application.
Chung, Kun-Zhi, and 鍾昆志. "Decomposition of hydrogen iodide in microchannel." Thesis, 2010. http://ndltd.ncl.edu.tw/handle/16334133895192271472.
Full textLin, Hung-chun, and 林鴻鈞. "Electroosmotic Flows in a Square Microchannel." Thesis, 2005. http://ndltd.ncl.edu.tw/handle/34202341015506051500.
Full text國立中山大學
機械與機電工程學系研究所
93
Experiments were performed using a microparticle image velocimetry (MPIV) for full field velocity distributions of electroosmotically driven flows in a 40 mm long microchannel with a square cross section of 200 µm × 200 µm. Electroosmotic flow bulk fluid velocity measurements were made in a range of streamwise electric field strengths from 5 to 25 kV/m. A series of seed particle calibration tests can be made in a 200 µm x 200 µm x 24000 µm untreated PDMS channel incorporating MPIV to determine the electrophoretic mobilities in aqueous buffer solutions of 1 TAE, 1 TBE, 10 mM NaCl, and 10 mM borate, respectively. A linear/nonlinear (due to Joule heating) flow rate increase with applied field was obtained and compared with those of previous studies. A parametric study, with extensive measurements was performed with different electric field strength and buffer solution concentration under a constant zeta potential at wall for each buffer. The characteristics of electroosmotic flow in square microchannels were thus investigated. Finally, a composite correlation of the relevant parameters was developed within accuracy for 99% of the experimental data.
Chen, Yu-Tang, and 陳育堂. "Fabrication and Analysis on Microchannel Structures." Thesis, 2004. http://ndltd.ncl.edu.tw/handle/61864081139843190767.
Full text淡江大學
機械與機電工程學系
92
Micro shaping techniques have been realized for various applications. In this dissertation, polymer micro manufacturing techniques are proposed to fabricate different profile microchannel structures. Besides, air flow through microtubes with diameters of 0.287 and 0.409 mm was investigated experimentally. Polymethylmethacrylate (PMMA) was dipped into methyl for two hours to fully generate the physical-chemical change. The PMMA swelling appeared through the mass transfer effect. This polymer swelling process was implemented to form the 3D micro venturi tube into a curved nozzle with the throat size successfully reduced to 100m. This dissertation presents an economical fabrication process for micro venturi tubes for future analysis in micro technologies. Additionally, a novel technique for fabricating microchannels in SU-8 by inserting optical-fibers as sacrificial moulds is also proposed in this dissertation. The embedded circular microchannels, with inner diameters of 36, 80, and 125μm (i.e., the diameters of optical-fibers), have been made successfully using a low-temperature fabrication process; where the SU-8 transparent negative-bone photo-resist is selected as the structure layer built in multilayers. Preliminary results show that the microchannels fabricated with the proposed technique have an average surface roughness (Ra) of the inner wall less than 10nm and roundness deviation less than 8.5%. This new fabrication technique of microchannel manufacture provides a new approach in selecting SU-8 for the structure material containing microchannels. Moreover, the air flow through microtubes with diameters of 0.287 and 0.409 mm was investigated experimentally. The experimental results indicate that the friction factor obtained from the Fanno-line flow function shows good conformity with the Poiseuille (f = 64/Re) and Blasius equations (f = 0.316/Re0.25) in both laminar and turbulent flow. These results illustrate the continuity and coherence in the study. Therefore, Fanno-line flow analysis can predict the general trends of the experimental results, enabling approximate analysis for many engineering application. Furthermore, the maximum pressure loss coefficient of micro nozzle / diffuser without “separation”, and the designs for the optimum profile of micro nozzle / diffuser are numerically analyzed in this dissertation. The SU-8 negative bone photo-resist is then introduced for the molding structure of micro nozzle / diffuser, and Polydimethyl-siloxane (PDMS) is used for the structure of micro nozzle / diffuser by copy. A low-temperature bonding technique using glass to bounding is introduced in this dissertation. Through the measurement of the pressure and flow, the analysis and investigation of fluid dynamics characteristics are then achieved. This dissertation consists of numerous existing as well as future allocations, especially in the pumps without valves where the micro nozzle / diffuser is the major structure. In sum, the theoretical analysis and design basis can then be formulated for the reference and application need in the fabrication of micro nozzle / diffuser from this study.
Hwang, Chen-yu, and 黃振彧. "Computation of Gaseous Flows in Microchannel." Thesis, 2007. http://ndltd.ncl.edu.tw/handle/98579110067504277835.
Full text國立成功大學
航空太空工程學系碩博士班
95
In the last decade, the microelectromechanical system(MEMS) field has significant and impressive progress. For the microchannel flows, a lot of experimental and theoretical results have been presented, but it still exists some problems which are worthwhile to study. In this thesis, the numerical computations are performed to investigate the gaseous flow behaviors in the microchannels. First the unstructured tetrahedral and prismatic meshes are created in the flow domain, the four-step Runge-Kutta time integration scheme and finite volume upwind method are adopted to solve the unsteady three-dimensional Navier-Stokes equations in he Cartesian coordinate system. To efficiently treat the geometric problem, the CATIA software is introduced to generate geometric shape, surface triangular grids and prismatic meshes. Then the mesh generation technique presented by Liu and Hwange is utilized to finish the distribution of tetrahedrons. To investigate the low speed flows, the approach for solving the pressure, which was presented by Rossow, is adopted in this study. On the unstructured tetrahedral/prismatic meshes, the above approach is extended to solve the three-dimensional inviscid and laminar flow. To evaluate this numerical method, the inviscid flows around sphere and passing through the converging-diverging nozzle with circular crosssection are investigated first. For the different Mach number, the comparision between the computed pressure coefficient and velocity distributions on the surface of sphere and the results from the potential flow theory is performed. Also the history of convergence is studied. About the nozzle flow, the pressure and velocity distributions along the nozzle axis are compared with those from the isentropic flow. Secondly, the computation of pipe flow is processed. For the comparision between the present results and the analytical solution for the poiseuille flow (such as entrance length and poiseuille number), the accuracy of current numerical approach for solving the laminar flow is confirmed. Finally, the present solution procedure is applied to study the trapezoidal microchannel. For the different value of Knudsen number and Mach number, the distribution of Poiseuille number and pressure distribution are computed and compared with the related data in the other literature.
SU, BO-YU, and 蘇柏瑜. "Magnetohydrodynamic Effect in a Circular Microchannel." Thesis, 2019. http://ndltd.ncl.edu.tw/handle/2aw584.
Full text明志科技大學
化學工程系碩士班
107
The main purpose of this paper is to investigate the application of a magnetic field to control the flow rate of the solution in the annular microfluidic channel. The annular microchannel used in the experiment includes three slots. The first type consists of an ITO conductive film with 1.20 cm in inner diameter and a graphite carbon electrode with of 0.80 cm in inner diameter to form a channel with 0.20 cm in width. The other two trenches are made up of 0.10 cm and 0.20 cm wide channels made of white gold rings with outer diameters of 1.80 cm, 1.50 cm and 1.20 cm. The working fluid in the experiment is a mixed solution of potassium ferricyanide and potassium ferrocyanide at 0.5 M, 0.6 M, 0.7 M, and 0.8 M. Polystyrene microspheres are added to the solution to facilitate testing of the flow rate. This experiment used several magnets with various magnetic flux densities to change the magnetic field. The flow rate changes with various magnetic field strengths and concentrations were measured by cross-testing of different concentrations of working fluid.
Chen, Chia-Yung, and 陳家勇. "Thermal fluid analysis of compressible microchannel flow." Thesis, 2002. http://ndltd.ncl.edu.tw/handle/29612527353265423501.
Full text國立中央大學
機械工程研究所
90
This numerical study analyzed the thermal-flow characteristics of the compressible laminar flow over the microchannel (dh < 4μm). The channel wall is assumed as non-slip flow condition. Two flow regimes were considered: 1) Ma=0.07~0.21, Re=1~10; 2) Ma=(3~12)×10-4, Re=(1.2~8.9)×10-3. Numerical results show that the compressible laminar flow has abrupt velocity jump near the channel entrance, and the fully developed flow can never be achieved no matter how long the channel is. In addition, further increases inlet velocity, more significant increasing of velocity at the outlet is predicted. The predicted velocity of present non-slip flow has a flat profile, which is similar to the solution of the slip flow simulation, and the velocity distribution is flatter as the flow approaches the outlet. Near the inlet, velocity profiles have a concave shape due to the viscosity heating at wall. For the heating wall case, the Nusselt number is inversely proportional to the wall temperature. When the wall temperature is higher, the flow needs longer channel to reach a constant Nusselt number. Comparing with the incompressible flow, nonlinear pressure distribution is obtained due to the compressibility effect. Both pressure and velocity gradient reach the maximum value at the outlet. Furthermore, enforcing higher pressure ratio (inlet value to outlet value), more significant nonlinear level of pressure distribution is observed. Because of the channel size effect, even the inlet velocity is very low (Main~10-3), numerical results reveal that a slight velocity difference makes a huge dissimilar pressure distribution in microchannel.
Chiu, Yi-Shan, and 邱義善. "Investigation of Heat Transfer on Microchannel Evaporator." Thesis, 2007. http://ndltd.ncl.edu.tw/handle/24616800940770022083.
Full text國立臺灣大學
機械工程學研究所
95
Microchannles provide a large heat transfer surface area per unit flow volume. Phase change in microchannel evaporator makes it desirable for three reasons:(1) high critical heat flux (2) high heat transfer coefficient (3) low coolant flow rate. Therefore, they are well suited for high heat flux removal and high temperature uniformity cooling applications. Present research successfully established a reliable microchannel evaporator experimental system to investigate heat transfer behavior in microchannels and enhance heat transfer performance by sintered porous structure. The working liquid used is refrigerant R-134a, operating pressure is 8 bar, and mass flux ranges from 222 to 464kg/m2s. The microchannel evaporator was fabricated from oxygen-free copper, and top platform was cut to form 62 parallel rectangular 225μm×660μm microchannels. The top platform of porous microchannel evaporator was sintered to form 62 parallel rectangular 210μm×660μm microchannels. The thickness of porous surface structure is 96μm, and the porosity is 54%. The average particle size is 30μm. The results reveal that flow boiling pressure drop is primarily affected by mass velocity and heat flux, which increases with increasing mass velocity and heat flux. The predictability of separated flow model is much better than homogeneous equilibrium model on flow boiling pressure drop in microchannel, and the lowest MAE is 10.6%. Flow boiling in microchannel can be classified either as boiling-dominated region or convection-dominated region. In boiling-dominated region, the heat transfer coefficient increases with increasing heat flux. In convection-dominated region, the heat transfer coefficient decreases with decreasing vapor quality. These two region are separated by the peak value of heat transfer coefficient, and this separation will change if mass velocity differs. The heat transfer data closely match with some previous correlations, and the lowest MAE is 13.6%. The critical heat flux is primarily affected by mass velocity, which increases with increasing mass velocity. The CHF data also closely match with some previous correlations, and the lowest MAE is 2.6%. As for heat transfer enhancement, in the same volume flow rate 167 ml/min, the heat transfer coefficient and CHF of porous microchannel evaporator is enhanced by 2-3.8 times and 19-23% respectively.
Chen, Hong-Ren, and 陳弘仁. "Design and Fabrication of the Microchannel System." Thesis, 2001. http://ndltd.ncl.edu.tw/handle/58397027681977147649.
Full text國立成功大學
航空太空工程學系
89
The objective of this present work applied MEMS technology to fabricate a micro-channel for the study of inside flow and heat transfer process. Due to the complexity of the rarefied gas heat transfer, we would like to focus our attention in a simplified case where the size of the channel is close to the mean free path of the gas. By performing some experiments to this micro-channel we can study the heat transfer inside a channel with different gas flows at the slip or transition regime with the bottom wall of a channel heated uniformly. The entire fabrication of the micro-channel system was to employ MEMS techniques to integrate micro-channel, micro-sensors and micro-heaters together within the suspended insulation system of a 1cm x 1cm chip. The channels were designed with 4000μm in length, 40μm in width and 0.8μm in height. The chip can heat uniformly the bottom wall and provide measurements of the temperature and pressure distributions along the flow direction. The Kn number of the gas in this channel falls between 0.053 and 0.154 from the calculation. Therefore, one can study the rarefied gas flow heat transfer under both the slip-flow and the transition-flow regimes. All of the sensors and the heaters were made of polysilicon doped with different concentrations of boron or phosphorous, which results in different electric resistance. To achieve a better insulation, the channel was made of low thermal conductivity material, silicon oxide, to reduce the heat loss. The entire fabrication process was made with the equipments in NDL. Followings are summarized results of current achievements: 1) Develop a fabrication procedures that can be fitted to the requirements set by IC processing laboratory. 2) Develop a new planarization process for poly-Si sacrificial layer. 3) Develop wet etching process for poly-Si sacrificial layer removal. 4) Develop photolithography process on surface with large size and deep ditches. Through years of revisions and adjustments the design and fabrication in the current chip has been greatly simplified. Many problems encountered during fabrication such as thick film stress, wet-etching contamination or step coverage effects etc. have also been overcame. Therefore, one has achieved the goals to establish the primary techniques for heat transfer application in MEMS and to develop experimental methods for micro-scale flow and heat transfer study successfully.