997 resultados para Particle Image Velocimetry –mittaustekniikka
Resumo:
Numerous types of acute respiratory failure are routinely treated using non-invasive ventilatory support (NIV). Its efficacy is well documented: NIV lowers intubation and death rates in various respiratory disorders. It can be delivered by means of face masks or head helmets. Currently the scientific community’s interest about NIV helmets is mostly focused on optimising the mixing between CO2 and clean air and on improving patient comfort. To this end, fluid dynamic analysis plays a particularly important role and a two- pronged approach is frequently employed. While on one hand numerical simulations provide information about the entire flow field and different geometries, they exhibit require huge temporal and computational resources. Experiments on the other hand help to validate simulations and provide results with a much smaller time investment and thus remain at the core of research in fluid dynamics. The aim of this thesis work was to develop a flow bench and to utilise it for the analysis of NIV helmets. A flow test bench and an instrumented mannequin were successfully designed, produced and put into use. Experiments were performed to characterise the helmet interface in terms of pressure drop and flow rate drop over different inlet flow rates and outlet pressure set points. Velocity measurements by means of Particle Image Velocimetry were performed. Pressure drop and flow rate characteristics from experiments were contrasted with CFD data and sufficient agreement was observed between both numerical and experimental results. PIV studies permitted qualitative and quantitative comparisons with numerical simulation data and offered a clear picture of the internal flow behaviour, aiding the identification of coherent flow features.
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Mixing is a fundamental unit operation in the pharmaceutical industry to ensure consistent product quality across different batches. It is usually carried out in mechanically stirred tanks, with a large variety of designs according to the process requirements. A key aspect of pharmaceutical manufacturing is the extensive and meticulous cleaning of the vessels between runs to prevent the risk of contamination. Single-use reactors represent an increasing trend in the industry since they do not require cleaning and sterilization, reducing the need for utilities such as steam to sterilize equipment and the time between production batches. In contrast to traditional stainless steel vessels, single-use reactors consist of a plastic bag used as a vessel and disposed of after use. This thesis aims to characterize the fluid dynamics features and the mixing performance of a commercially available single-use reactor. The characterization employs a combination of various experimental techniques. The analysis starts with the visual observation of the liquid behavior inside the vessel, focusing on the vortex shape evolution at different impeller speeds. The power consumption is then measured using a torque meter to quantify the power number. Particle Image Velocimetry (PIV) is employed to investigate local fluid dynamics properties such as mean flow field and mean and rms velocity profiles. The same experimental setup of PIV is exploited for another optical measurement technique, the Planar Laser-Induced Fluorescence (PLIF). The PLIF measurements complete the characterization of the reactor with the qualitative visualization of the turbulent flow and the quantitative assessment of the system performance through the mixing time. The results confirm good mixing performances for the single-use reactor over the investigated impeller speeds and reveal that the filling volume plays a significant role in the fluid dynamics of the system.
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This study develops an automated analysis tool by combining total internal reflection fluorescence microscopy (TIRFM), an evanescent wave microscopic imaging technique to capture time-sequential images and the corresponding image processing Matlab code to identify movements of single individual particles. The developed code will enable us to examine two dimensional hindered tangential Brownian motion of nanoparticles with a sub-pixel resolution (nanoscale). The measured mean square displacements of nanoparticles are compared with theoretical predictions to estimate particle diameters and fluid viscosity using a nonlinear regression technique. These estimated values will be confirmed by the diameters and viscosities given by manufacturers to validate this analysis tool. Nano-particles used in these experiments are yellow-green polystyrene fluorescent nanospheres (200 nm, 500 nm and 1000 nm in diameter (nominal); 505 nm excitation and 515 nm emission wavelengths). Solutions used in this experiment are de-ionized (DI) water, 10% d-glucose and 10% glycerol. Mean square displacements obtained near the surface shows significant deviation from theoretical predictions which are attributed to DLVO forces in the region but it conforms to theoretical predictions after ~125 nm onwards. The proposed automation analysis tool will be powerfully employed in the bio-application fields needed for examination of single protein (DNA and/or vesicle) tracking, drug delivery, and cyto-toxicity unlike the traditional measurement techniques that require fixing the cells. Furthermore, this tool can be also usefully applied for the microfluidic areas of non-invasive thermometry, particle tracking velocimetry (PTV), and non-invasive viscometry.
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En ambientes fluviales, la interacción del flujo con la geometría del cauce y con los sedimentos del lecho define una dinámica turbulenta compleja en permanente evolución. El nivel de complejidad del flujo aumenta ante la presencia de estructuras hidráulicas (pilas de puentes, protecciones contra erosión, etc.). La mayoría de los ríos, o canales naturales, presentan confluencias y bifurcaciones, en donde se genera una convergencia (o divergencia) del flujo con el resultado de un ambiente hidrodinámico complejo en la cercanía de las uniones (Kenworthy y Rhoads 1995). Bajo estas condiciones no es posible extrapolar las soluciones tradicionales básicas de las ecuaciones de gobierno desarrolladas para canales rectos y uniformes. Algunas investigaciones experimentales realizadas en estos sistemas son las de Best (1988), Rhoads y Sukhodolov (2001), Richardson et al. (1996); Richardson y Thorne (1998, 2001); Parsons et al. (2004); Szupiany et al. (2005).Por otro lado, la zona costera en ambientes marítimos se caracteriza por la existencia de diversos procesos dinámicos, entre los que se destacan la acción de olas, corrientes, interacción olas-corrientes, transporte de sedimentos y cambios batimétricos. Estos se manifiestan en una alteración morfodinámica de la playa generando superficies potenciales de erosión. Así, el diseño de las protecciones costeras (ya sean continuas, como escolleras o muros verticales; o discontinuas como espigones o diques externos) sometidas al clima marítimo bajo distintas condiciones de olas y mareas, alteran los patrones de circulación y de transporte afectando la morfodinámica en su zona de influencia y plantean, por ejemplo, la necesidad de ajustes de los coeficientes de estabilidad y pesos de los bloques de roca de las escolleras. Los problemas generados, son especialmente complejos ya que deben considerarse para su estudio, los niveles de turbulencia, la transmisión del oleaje sobre o a través de la estructura, difracción alrededor de la misma, refracción y shoaling sobre un fondo dinámico, reflexión en la estructura, etc. (Alsina et al., 2007) Revisiones bibliográficas previas muestran que, en ambos ambientes (fluvial y marítimo), es necesario optimizar las técnicas experimentales existentes para que ellas permitan caracterizar con precisión los flujos turbulentos complejos presentes. El objetivo general propuesto en esta investigación es contribuir a mejorar el conocimiento de los procesos hidrodinámicos de flujos turbulentos naturales con y sin la presencia de estructuras hidráulicas que den lugar a formaciones complejas (3D). Para alcanzar este objetivo se propone realizar una recopilación de antecedentes y un análisis crítico detallado de los equipos de ultima generación para mediciones de flujo con alta frecuencia y resolución disponibles en el Laboratorio de Hidráulica (LH) de la Universidad Nacional de Córdoba (UNC): ADV 3D (Acoustic Doppler Velocimeter de Sontek) y laser PIV 2D (Particle Image Velocimeter de Dantec). A estos equipamientos se le agrega un moderno equipo de generación bidimensional de oleaje con absorción dinámica (adquiridos a HR Ltd. en 2007 por el CAI 085 del FONTAR). Finalmente se prevé utilizar este equipamiento durante el desarrollo de experimentos y mediciones los cuales se realizarán sobre modelos físicos fluviales y costeros diseñados y construidos con y sin estructuras que interactúen con flujo turbulentos complejos. Los resultados obtenidos en este proyecto permitirá alcanzar una mejor comprensión de los procesos hidrodinámicos de los flujos turbulentos complejos, lo cual es necesario y de gran utilidad para realizar un manejo apropiado de los ambientes fluviales y marítimos, teniendo como campo directo de aplicación el correcto diseño de estructuras hidráulicas, asistiendo a la toma de medidas correctivas en sistemas naturales sometidos a procesos erosivos o de sedimentación, y contribuyendo de esta forma al manejo ambientalmente sustentable de los recursos.
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Työn tavoitteena oli kehittää sekoituskyvyn empiirinen monimuuttujafunktio eräälle dynaamiselle linjasekoittimelle. Monimuuttujafunktio oli tarkoitus kehittää sekoittimen kierrosnopeuden, virtaavien materiaalien ja tilavuusvirtausten perus-teella. Työn kirjallisuusosassa tarkasteltiin pääosin dynaamisia linjasekoittimia ja niiden toimintaperiaatteita sekä sekoituskyvyn määrittämiseen soveltuvia mittausmene-telmiä. Sekoitettavien aineiden epähomogeenisuus määritettiin mittaamalla termoelemen-teillä sekoittimen jälkeisen virran lämpötilavaihtelut. Sekoitettavina aineina käy-tettiin kolmea erilaista seosta: vesi-vesi-, kuitususpensio-vesi- ja karboksyylime-tyyliselluloosa-vesiseoksia. Muita muuttujia kokeissa olivat neljä eri sekoittimen kierrosnopeutta, neljä eri päävirran tilavuusvirtausta ja kolme päävirran sekäsii-hen lisättävän sivuvirran suhdetta. Monimuuttujafunktiokehitettiin vain kuitususpensio-vesiajojen pohjalta muilla seoksilla tehtyjen koeajojen osittaisen epäonnistumisen vuoksi. Hallitsevaksi pa-rametriksi monimuuttujafunktiossa osoittautui sekoittimen kierrosnopeus. Osittai-nen epäonnistuminen kokeissa johtui osaksi termoelementtien käytön sopimatto-muudesta sekoituskyvyn määrittämiseen ja osaksi sekoitettavien aineiden valin-nasta. Jatkotutkimuksiaajatellen muista sekoituskyvyn mittaamiseen käytettävissä olevista menetelmistäkäyttökelpoisimmaksi arvioitiin sähkötomografia.
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Työssä tutkittiin leijupetikiteyttimen toimivuutta sulfatiatsolikiteiden kasvunopeuksien mittaamisessa. Sulfatiatsoli on lääkeaine, jota käytetään antibioottina. Kirjallisuusosassa on käsitelty kiteytyksen perusteita sekä olosuhteiden vaikutuksia kidemorfologiaan. Koska kyseessä on lääkeaine, on työssä myös selvitetty tekijöitä, jotka vaikuttavat syntyvän kiteen polymorfimuotoon. Näitä ovat mm. siemenkiteen polymorfimuoto sekä käytetty liuotin. Kirjallisuusosassa on myös esitelty teollisia ja laboratoriomittakaavan leijupetikiteyttimiä. Kokeellisessa osassa on keskitytty testaamaan leijupetikiteyttimen toimintaa sekä etsimään sopivia olosuhteita kasvukokeiden suorittamiselle. Kokeissa tutkittiin ylikylläisyyden vaikutusta sulfatiatsolikiteen kasvuun. Kiteen kasvun seurantaan pyrittiin etsimään sopivia hiukkaskokoanalysaattoreita. Mittauksissa käytetyt laitteistot olivat PIA 4000 mod LUT on-line-videomikroskooppi ja laserdiffraktioon perustuva Coulter LS 130 off-line-partikkelikokoanalysaattori.
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Tässä työssä tutkittiin kahden erilaisen partikkelikokoanalysaattorin, PSyA:n ja PIA:n soveltuvuutta flokkuloinnin online-seurantaan. Kummallekin menetelmälle määritettiin raja-arvot, kuten lietteen maksimisakeus. Lisäksi tutkittiin flokkulanttiannostuksen, sekoitusnopeuden, sekoitusajan ja lietteen kiintoainepitoisuuden vaikutusta flokkikokojakaumaan. Kirjallisuusosassa tarkasteltiin kolloidisen suspension ominaispiirteitä, koaguloinnin ja flokkuloinnin teoriaa, flokkulaation kokeellista tutkimista sekä prosessin jatkuvatoimiseen seurantaan soveltuvia laitteita. Lisäksi esitettiin taustaa hydrometallurgisesta prosessista, johon työ liittyy. Flokkauskokeissa käytettiin jätevettä, jonka koostumus vastasi metalliteollisuuden peittausjätevesien tyypillistä koostumusta. Tutkittava jätevesimäärä käsiteltiin ensin kalkkimaidolla, jonka jälkeen saostunut kiintoaine flokattiin synteettisellä polymeeriflokkulantilla. Lietteen keskimääräinen kiintoainepitoisuus oli n. 10 g/l. Esikokeiden perusteella PSyA:lla voitiin mitata ilman laimennusta, mutta PIA:lla tuloksia ei saatu ilman laimentamista kiintoainepitoisuuteen n. 2,5 g/l. Kokeiden aikana havaittiin, että flokit muodostuivat erittäin nopeasti. Flokkien hajoaminen alkoi pian sen jälkeen, kun flokkulantin annostelu lopetettiin. Sekoitusnopeudella 40 r/min tai alle flokit alkoivat laskeutua astian pohjalle sekoituksesta huolimatta ja ne pysyivät pitempään koossa kuin suuremmilla sekoitusnopeuksilla. 5 - 10 minuutin kuluttua flokkulantin lisäämisestä saavutettiin tasapaino, jolloin flokkien kokojakauma ei enää muuttunut. Sekoitusnopeuksilla 80 r/min ja 120 r/min tasapainotilanteen koko-jakauma oli selvästi kapeampi kuin pienimmällä sekoitusnopeudella. Alkuperäisessä lietteessä flokit olivat suurempia kuin laimennetussa lietteessä. PSyA:lla jännepituusjakaumien määrittäminen oli varsin hidasta prosessissa tapahtuviin muutoksiin verrattuna, ja tuloksissa oli suurta hajontaa. PIA:lla saadut partikkelikokojakaumat sitä vastoin olivat johdonmukaisempia, vaikka suurimpien flokkien määrittäminen osoittautuikin epämääräiseksi. Menetelmän suurimmaksi puutteeksi todettiin soveltumattomuus sakeiden lietteiden analysointiin. Kumpikaan menetelmä ei ilman modifiointia sovellu tutkitun lietteen kaltaisten prosessilietteiden flokkuloinnin seurantaan.
Resumo:
We present an experimental study on the behavior of bubbles captured in a Taylor vortex. The gap between a rotating inner cylinder and a stationary outer cylinder is filled with a Newtonian mineral oil. Beyond a critical rotation speed (ω[subscript c]), Taylor vortices appear in this system. Small air bubbles are introduced into the gap through a needle connected to a syringe pump. These are then captured in the cores of the vortices (core bubble) and in the outflow regions along the inner cylinder (wall bubble). The flow field is measured with a two-dimensional particle imaging velocimetry (PIV) system. The motion of the bubbles is monitored by using a high speed video camera. It has been found that, if the core bubbles are all of the same size, a bubble ring forms at the center of the vortex such that bubbles are azimuthally uniformly distributed. There is a saturation number (N[subscript s]) of bubbles in the ring, such that the addition of one more bubble leads eventually to a coalescence and a subsequent complicated evolution. Ns increases with increasing rotation speed and decreasing bubble size. For bubbles of non-uniform size, small bubbles and large bubbles in nearly the same orbit can be observed to cross due to their different circulating speeds. The wall bubbles, however, do not become uniformly distributed, but instead form short bubble-chains which might eventually evolve into large bubbles. The motion of droplets and particles in a Taylor vortex was also investigated. As with bubbles, droplets and particles align into a ring structure at low rotation speeds, but the saturation number is much smaller. Moreover, at high rotation speeds, droplets and particles exhibit a characteristic periodic oscillation in the axial, radial and tangential directions due to their inertia. In addition, experiments with non-spherical particles show that they behave rather similarly. This study provides a better understanding of particulate behavior in vortex flow structures.
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Intact, enveloped coronavirus particles vary widely in size and contour, and are thus refractory to study by traditional structural means such as X-ray crystallography. Electron microscopy (EM) overcomes some problems associated with particle variability and has been an important tool for investigating coronavirus ultrastructure. However, EM sample preparation requires that the specimen be dried onto a carbon support film before imaging, collapsing internal particle structure in the case of coronaviruses. Moreover, conventional EM achieves image contrast by immersing the specimen briefly in heavy-metal-containing stain, which reveals some features while obscuring others. Electron cryomicroscopy (cryo-EM) instead employs a porous support film, to which the specimen is adsorbed and flash-frozen. Specimens preserved in vitreous ice over holes in the support film can then be imaged without additional staining. Cryo-EM, coupled with single-particle image analysis techniques, makes it possible to examine the size, structure and arrangement of coronavirus structural components in fully hydrated, native virions. Two virus purification procedures are described.
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A identificação e o monitoramento de microorganismos aquáticos, como bactérias e microalgas, tem sido uma tarefa árdua e morosa. Técnicas convencionais, com uso de microscópios e corantes, são complexas, exigindo um grande esforço por parte dos técnicos e pesquisadores. Uma das maiores dificuldades nos processos convencionais de identificação via microscopia é o elevado número de diferentes espécies e variantes existentes nos ambientes aquáticos, muitas com semelhança de forma e textura. O presente trabalho tem por objetivo o desenvolvimento de uma metodologia para a caracterização e classificação de microorganismos aquáticos (bactérias e microalgas), bem como a determinação de características cinemáticas, através do estudo da mobilidade de microalgas que possuem estruturas que permitem a natação (flagelos). Para caracterização e reconhecimento de padrões as metodologias empregadas foram: o processamento digital de imagens e redes neurais artificiais (RNA). Para a determinação da mobilidade dos microorganismos foram empregadas técnicas de velocimetria por processamento de imagens de partículas em movimento (Particle Tracking Velocimetry - PTV). O trabalho está dividido em duas partes: 1) caracterização e contagem de microalgas e bactérias aquáticas em amostras e 2) medição da velocidade de movimentação das microalgas em lâminas de microscópio. A primeira parte envolve a aquisição e processamento digital de imagens de microalgas, a partir de um microscópio ótico, sua caracterização e determinação da densidade de cada espécie contida em amostras. Por meio de um microscópio epifluorescente, foi possível, ainda, acompanhar o crescimento de bactérias aquáticas e efetuar a sua medição por operadores morfológicos. A segunda parte constitui-se na medição da velocidade de movimentação de microalgas, cujo parâmetro pode ser utilizado como um indicador para se avaliar o efeito de substâncias tóxicas ou fatores de estresse sobre as microalgas. O trabalho em desenvolvimento contribuirá para o projeto "Produção do Camarão Marinho Penaeus Paulensis no Sul do Brasil: Cultivo em estruturas Alternativas" em andamento na Estação Marinha de Aquacultura - EMA e para pesquisas no Laboratório de Ecologia do Fitoplâncton e de Microorganismos Marinhos do Departamento de Oceanografia da FURG. O trabalho propõe a utilização dos níveis de intensidade da imagem em padrão RGB e oito grandezas geométricas como características para reconhecimento de padrões das microalgas O conjunto proposto de características das microalgas, do ponto de vista de grandezas geométricas e da cor (nível de intensidade da imagem e transformadas Fourier e Radon), levou à geração de indicadores que permitiram o reconhecimento de padrões. As redes neurais artificiais desenvolvidas com topologia de rede multinível totalmente conectada, supervisionada, e com algoritmo de retropropagação, atingiram as metas de erro máximo estipuladas entre os neurônios de saída desejados e os obtidos, permitindo a caracterização das microalgas.
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Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)
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Micro-scale, two-phase flow is found in a variety of devices such as Lab-on-a-chip, bio-chips, micro-heat exchangers, and fuel cells. Knowledge of the fluid behavior near the dynamic gas-liquid interface is required for developing accurate predictive models. Light is distorted near a curved gas-liquid interface preventing accurate measurement of interfacial shape and internal liquid velocities. This research focused on the development of experimental methods designed to isolate and probe dynamic liquid films and measure velocity fields near a moving gas-liquid interface. A high-speed, reflectance, swept-field confocal (RSFC) imaging system was developed for imaging near curved surfaces. Experimental studies of dynamic gas-liquid interface of micro-scale, two-phase flow were conducted in three phases. Dynamic liquid film thicknesses of segmented, two-phase flow were measured using the RSFC and compared to a classic film thickness deposition model. Flow fields near a steadily moving meniscus were measured using RSFC and particle tracking velocimetry. The RSFC provided high speed imaging near the menisci without distortion caused the gas-liquid interface. Finally, interfacial morphology for internal two-phase flow and droplet evaporation were measured using interferograms produced by the RSFC imaging technique. Each technique can be used independently or simultaneously when.
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La determinación experimental in situ del escurrimiento superficial en cauces naturales (mediante aforos) en forma sistemática permite lograr una mayor eficiencia en la gestión del recurso hídrico en una cuenca determinada. Además, la determinación precisa de los caudales es relevante para el diseño sustentable de infraestructura hídrica (puentes, canalizaciones, etc.) debido en parte a que el sobredimensionamiento de las obras genera un impacto innecesario sobre el medio ambiente, además de que resulta antieconómico. Además, la subestimación de las obras a diseñar provoca fallos con resultados catastróficos con alto impacto sobre la sociedad y el medio ambiente, ya sea por la pérdida de vidas humanas como de bienes públicos y privados. En los últimos años se ha incrementado el instrumental disponible para la cuantificación experimental de caudales de agua superficial en cauces naturales con tecnología que permite caracterizar el flujo de agua con mayor resolución espacial y temporal. Específicamente, el empleo de la anemometría acústica basada en el efecto Doppler (que utiliza el principio físico del cambio de frecuencia ante el rebote acústico que produce una partícula transportada por el flujo) se ha tornado actualmente una práctica universal en hidráulica fluvial y está reemplazando a las metodologías convencionales como por ejemplo el uso de molinetes. El instrumento acústico utilizado comúnmente en el caso de mediciones en campo, es el ADCP (Acoustic Doppler Current Profiler). Por otra parte desde hace algunos años se están desarrollando metodologías experimentales que permiten medir el campo de velocidades del flujo en manera instantánea y con alta resolución espacial mediante el procesamiento digital de imágenes. Dentro de estos métodos se destaca el de velocimetría por seguimiento de partículas PTV (Particle Tracking Velocimetry) de reciente aplicación a nivel mundial en mediciones de campo. Sobre esta base, se considera un desafío tecnológico la implementación en nuestra provincia de estas modernas tecnologías, ya validadas en el ámbito de la Universidad Nacional de Córdoba para la obtención precisa de registros de caudales en cauces naturales. Mediante este proyecto de transferencia de los resultados de investigación y comunicación pública de la ciencia, el grupo de Investigación del CETA - FCEFyN -UNC realizará un "Programa de capacitación y actualización en modernas técnicas experimentales para medición de caudales de aguas superficiales en cauces naturales" que incluye los recientes avances observados en la temática. La Secretaría de Recursos Hídricos del Ministerio de Agua, Ambiente y Energía de la Provincia de Córdoba será beneficiada y se fortalecerá en una de sus principales funciones que es: "procurar el fortalecimiento de redes de mediciones o monitoreo sistemático a través de programas de cooperación técnica y presupuestaria con entidades provinciales y nacionales -públicas o privadas-, prestatarias de obras y servicios públicos y los usuarios del agua, manteniendo un sistema de información provincial sobre las variables meteorológicas y el recurso hídrico con el objeto de procesar su flujo en forma permanente".
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Dilatant faults often form in rocks containing pre-existing joints, but the effects of joints on fault segment linkage and fracture connectivity is not well understood. We present an analogue modeling study using cohesive powder with pre-formed joint sets in the upper layer, varying the angle between joints and a rigid basement fault. We analyze interpreted map-view photographs at maximum displacement for damage zone width, number of connected joints, number of secondary fractures, degree of segmentation and area fraction of massively dilatant fractures. Particle imaging velocimetry helps provide insights on deformation history of the experiments and illustrate the localization pattern of fault segments. Results show that with increasing angle between joint-set and basement-fault strike the number of secondary fractures and the number of connected joints increases, while the area fraction of massively dilatant fractures shows only a minor increase. Models without pre-existing joints show far lower area fractions of massively dilatant fractures while forming distinctly more secondary fractures.
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Recent developments have made researchers to reconsider Lagrangian measurement techniques as an alternative to their Eulerian counterpart when investigating non-stationary flows. This thesis advances the state-of-the-art of Lagrangian measurement techniques by pursuing three different objectives: (i) developing new Lagrangian measurement techniques for difficult-to-measure, in situ flow environments; (ii) developing new post-processing strategies designed for unstructured Lagrangian data, as well as providing guidelines towards their use; and (iii) presenting the advantages that the Lagrangian framework has over their Eulerian counterpart in various non-stationary flow problems. Towards the first objective, a large-scale particle tracking velocimetry apparatus is designed for atmospheric surface layer measurements. Towards the second objective, two techniques, one for identifying Lagrangian Coherent Structures (LCS) and the other for characterizing entrainment directly from unstructured Lagrangian data, are developed. Finally, towards the third objective, the advantages of Lagrangian-based measurements are showcased in two unsteady flow problems: the atmospheric surface layer, and entrainment in a non-stationary turbulent flow. Through developing new experimental and post-processing strategies for Lagrangian data, and through showcasing the advantages of Lagrangian data in various non-stationary flows, the thesis works to help investigators to more easily adopt Lagrangian-based measurement techniques.