The Application of Multi-dimensional Fluorescence Imaging to Microfluidic Systems

This thesis describes the application of multidimensional fluorescence imaging to microfluidic systems. The work focuses on time- and polarisation-resolved fluorescence microscopy to extract information from microchannel environments. The methods are applied to polymerase chain reaction (PCR) and a DNA repair enzyme, uracil DNA glycosylase (UDG). The fluorescence lifetimes Rhodamine B are calibrated over a thermal gradient using time correlated single photon counting. The dye is then introduced in solution into a novel microfluidic PCR device. Fluorescence lifetime imaging microscopy (FLIM) is then performed, and using the calibration curve, the temperature distributions are accurately determined. The device is subsequently optimised for efficient DNA amplification. A line-scanning FLIM microscope is used to characterise a rapid microfluidic mixer via a fluorescence quenching experiment. Fluorescein and sodium iodide are mixed in a continuous flow format and imaged in 3-D. The spatial distributions of the fluorescence lifetimes are converted to the concentrations of sodium iodide to quantify mixing. Computational fluid dynamic (CFD) simulations are validated by comparison to the quantitative concentrations obtained experimentally. The binding reaction between UDG and a hexachlorofluorescein (HEX) labelled DNA strand is characterised spectrally. As well as an increase in fluorescence polarisation anisotropy, a 700 ps increase in the fluorescence lifetime is measured. Confocal microscopy shows the same spectral properties when the reaction is performed in both simple and rapid microfluidic mixers. In the latter experiment, a concentration series allows the determination of kinetics, which agree with conventional stopped-flow data. A two-colour two-photon (2c2p) FLIM microscope is developed and applied to the UDG-DNA system. An oligonucleotide containing 2-aminopurine, a reporter of DNA base flipping, and HEX is mixed with UDG in a microfluidic Y-mixer. The 2c2p excitation allows FLIM of both fluorophores and hence detection of binding and base flipping. Comparison to CFD with known kinetic rate constants confirms the experimental observations

Population balances combined with computational fluid dynamics : a modeling approach for dispersive mixing in a high pressure homogenizer

High pressure homogenization is at the heart of many emulsification processes in the food, personal care and pharmaceutical industry. The droplet size distribution is an important property for product quality and is aimed to be controlled in the process. Therefore a population balance model was built in order to predict the droplet size distribution subject to various hydrodynamic conditions found in a high pressure homogenizer. The hydrodynamics were simulated using Computational Fluid Dynamics and the turbulence was modeled with a RANS k–e model. The high energy zone in the high pressure homogenizer was divided into four compartments. The compartments had to be small enough to secure nearly homogeneous turbulent dissipation rates but large enough to hold a population of droplets. A population balance equation describing breakage and coalescence of oil droplets in turbulent flow was solved for every compartment. One set of parameters was found which could describe the development of the droplet size distribution in the high pressure homogenizer with varying pressure drop. An improvement of 65% was found compared to the same model containing just one compartment. The compartment approach may provide an alternative to direct coupling of CFD and population balances

Mass Transfer

This book covers a wide variety of topics related to advancements in different stages of mass transfer modelling processes. Its purpose is to create a platform for the exchange of recent observations, experiences, and achievements. It is recommended for those in the chemical, biotechnological, pharmaceutical, and nanotechnology industries as well as for students of natural sciences, technical, environmental and employees in companies which manufacture machines for the above-mentioned industries. This work can also be a useful source for researchers and engineers dealing with mass transfer and related issues

Magnetic field stimulation of magnetic nanoparticles for the intensification of scalar transport

Dans cette thèse, le transport de scalaires dans des ferrofluides / ferrogels est étudié théoriquement et expérimentalement. L’intérêt principal est de quantifier expérimentalement le processus de transport de masse dans des ferrofluides / ferrogels exposés à un champ magnétique externe et de comprendre les mécanismes sous-jacents à ces processus à la lumière de simulations ferrohydrodynamiques (FHD). Nous visons également à utiliser les phénomènes de transport améliorés, identifiés dans les ferrofluides pour des applications de génie de la réaction chimique, par le biais d'études expérimentales sur le mélange / micromélange en micro-canal. L’introduction présente les principes de base de la dynamique des ferrofluides et des nanoparticules magnétiques (NPM) du point de vue de la mécanique des fluides et de la physique des colloïdes. Le cadre de ferrohydrodynamique, englobant les équations du mouvement des ferrofluides en relation avec la relaxation magnétique, y est expliqué. La littérature récente pertinente au transport de scalaires et au mélange dans les ferrofluides est examinée et les mécanismes d'intensification de transport de masse dans le ferrofluides excités par divers types de champs magnétiques sont discutés. Le première chapitre présente des observations expérimentales et des simulations numériques sur le transport de scalaires dans un ferrofluide de type Brownien au repos mais soumis à un champ magnétique rotatif (CMR). Les expériences de transport de masse ont été conduites dans un mélangeur capillaire en T excité transversalement par un champ magnétique uniforme. Une augmentation significative du transport de masse a été observée en présence de CMR dans une direction normale à l'axe de rotation du champ magnétique. Un tel contrôle directionnel par CMR a permis de mettre en évidence le caractère anisotrope du flux de masse puisque la diffusion moléculaire était le seul mécanisme de transport agissant dans une direction parallèle à l'axe du capillaire. Le rôle de l'advection du ferrofluide induite par CMR (écoulement spin-up) quant à l'amélioration du transport de masse a été examiné à la lumière de la solution de l'équation d’advection-diffusion et de la comparaison des prédictions numériques de FHD avec les résultats expérimentaux. Une analyse comparative systématique des simulations numériques par rapport aux observations expérimentales a révélé que la diffusivité effective dans le ferrofluide peut être représentée par un tenseur diagonal dont les composantes sont fonction de la fréquence du CMR et de la concentration des NPM.Dans cette thèse, le transport de scalaires dans des ferrofluides / ferrogels est étudié théoriquement et expérimentalement. L’intérêt principal est de quantifier expérimentalement le processus de transport de masse dans des ferrofluides / ferrogels exposés à un champ magnétique externe et de comprendre les mécanismes sous-jacents à ces processus à la lumière de simulations ferrohydrodynamiques (FHD). Nous visons également à utiliser les phénomènes de transport améliorés, identifiés dans les ferrofluides pour des applications de génie de la réaction chimique, par le biais d'études expérimentales sur le mélange / micromélange en micro-canal. L’introduction présente les principes de base de la dynamique des ferrofluides et des nanoparticules magnétiques (NPM) du point de vue de la mécanique des fluides et de la physique des colloïdes. Le cadre de ferrohydrodynamique, englobant les équations du mouvement des ferrofluides en relation avec la relaxation magnétique, y est expliqué. La littérature récente pertinente au transport de scalaires et au mélange dans les ferrofluides est examinée et les mécanismes d'intensification de transport de masse dans le ferrofluides excités par divers types de champs magnétiques sont discutés. Le première chapitre présente des observations expérimentales et des simulations numériques sur le transport de scalaires dans un ferrofluide de type Brownien au repos mais soumis à un champ magnétique rotatif (CMR). Les expériences de transport de masse ont été conduites dans un mélangeur capillaire en T excité transversalement par un champ magnétique uniforme. Une augmentation significative du transport de masse a été observée en présence de CMR dans une direction normale à l'axe de rotation du champ magnétique. Un tel contrôle directionnel par CMR a permis de mettre en évidence le caractère anisotrope du flux de masse puisque la diffusion moléculaire était le seul mécanisme de transport agissant dans une direction parallèle à l'axe du capillaire. Le rôle de l'advection du ferrofluide induite par CMR (écoulement spin-up) quant à l'amélioration du transport de masse a été examiné à la lumière de la solution de l'équation d’advection-diffusion et de la comparaison des prédictions numériques de FHD avec les résultats expérimentaux. Une analyse comparative systématique des simulations numériques par rapport aux observations expérimentales a révélé que la diffusivité effective dans le ferrofluide peut être représentée par un tenseur diagonal dont les composantes sont fonction de la fréquence du CMR et de la concentration des NPM. Dans le deuxième chapitre, nous avons exploité le concept de diffusion effective anormale anisotrope dans les ferrofluides pour expliquer les variations de la dispersion axiale observées expérimentalement pour un écoulement de Poiseuille en présence de CMR. Les résultats expérimentaux ont montré que la distribution des temps de séjour (DTS) en présence de CMR est moins asymétrique avec un temps de percée de plus en plus retardé lorsque la fréquence de CMR et/ou la concentration en nanoparticules magnétiques augmente(nt). La solution de l'équation d'advection-diffusion couplée aux équations de transport de quantité de mouvement sous champ magnétique rotatif signale une faible contribution de l'advection dans le phénomène observé. Les simulations numériques ont également montré que la réduction de la dispersion axiale était le résultat d'une diffusivité effective anisotrope anormale dans le ferrofluide suggérant une échelle de mélange de l’ordre de quelques nanomètres dictée par l’effet de la rotation du champ magnétique sur la matrice liquide porteuse non-magnétique des NPM. Dans le troisième chapitre, les propriétés de transport de masse du ferrofluide identifiées ont ensuite été examinées pour des applications de mélange et de micromélange via des techniques réactionnelles. Une étude comparative a été menée pour évaluer l'efficacité du mélange entre des fluides magnétiques et non magnétiques dans un mélangeur de type T capillaire, cylindrique et soumis à des champs magnétiques statique (CMS), oscillant (CMO) et rotatif. En utilisant la réaction modèle de Villermaux-Dushman, nous avons mis en évidence la sensibilité de la sélectivité de cette réaction au micromélange et au transfert de masse au niveau moléculaire. Les résultats ont montré une réduction substantielle de la résistance au transport à l’échelle nanométrique avec des effets mesurables sur la distribution des produits lorsque le mélange est stimulé par un cham magnétique rotatif. Dans le chapitre quatre, nous étendons le concept de mélange NPM/CMR aux ferrogels, préparés en ensemençant des (dipôles durs) nanoparticules de cobalt-ferrite dans un hydrogel de polyacrylamide. L'analyse quantitative des données d’aimantation a révélé l'existence de NPM hydrodynamiquement libres, donc sensibles à la relaxation brownienne, ainsi que des NPM mécaniquement bloquées dans la structure du ferrogel. Un ferrogel contenant des MNP hydrodynamiquement libres engendre des diffusivités effectives d’un soluté passif largement supérieures à la diffusion moléculaire intrinsèque mesurée pour le même soluté au sein de la structure de ferrogel en absence de champ magnétique rotatif. Les résultats expérimentaux et théoriques de cette thèse pourraient ouvrir la voie à l’utilisation de MNP/ferrofluide stimulés par champ magnétique pour la conception et le développement de systèmes micro-fluidiques et de matériaux magnétiques multifonctionnels dotés de propriétés de transport contrôlables à distance.Dans le deuxième chapitre, nous avons exploité le concept de diffusion effective anormale anisotrope dans les ferrofluides pour expliquer les variations de la dispersion axiale observées expérimentalement pour un écoulement de Poiseuille en présence de CMR. Les résultats expérimentaux ont montré que la distribution des temps de séjour (DTS) en présence de CMR est moins asymétrique avec un temps de percée de plus en plus retardé lorsque la fréquence de CMR et/ou la concentration en nanoparticules magnétiques augmente(nt). La solution de l'équation d'advection-diffusion couplée aux équations de transport de quantité de mouvement sous champ magnétique rotatif signale une faible contribution de l'advection dans le phénomène observé. Les simulations numériques ont également montré que la réduction de la dispersion axiale était le résultat d'une diffusivité effective anisotrope anormale dans le ferrofluide suggérant une échelle de mélange de l’ordre de quelques nanomètres dictée par l’effet de la rotation du champ magnétique sur la matrice liquide porteuse non-magnétique des NPM.. Dans le troisième chapitre, les propriétés de transport de masse du ferrofluide identifiées ont ensuite été examinées pour des applications de mélange et de micromélange via des techniques réactionnelles. Une étude comparative a été menée pour évaluer l'efficacité du mélange entre des fluides magnétiques et non magnétiques dans un mélangeur de type T capillaire, cylindrique et soumis à des champs magnétiques statique (CMS), oscillant (CMO) et rotatif. En utilisant la réaction modèle de Villermaux-Dushman, nous avons mis en évidence la sensibilité de la sélectivité de cette réaction au micromélange et au transfert de masse au niveau moléculaire. Les résultats ont montré une réduction substantielle de la résistance au transport à l’échelle nanométrique avec des effets mesurables sur la distribution des produits lorsque le mélange est stimulé par un cham magnétique rotatif. Dans le chapitre quatre, nous étendons le concept de mélange NPM/CMR aux ferrogels, préparés en ensemençant des (dipôles durs) nanoparticules de cobalt-ferrite dans un hydrogel de polyacrylamide. L'analyse quantitative des données d’aimantation a révélé l'existence de NPM hydrodynamiquement libres, donc sensibles à la relaxation brownienne, ainsi que des NPM mécaniquement bloquées dans la structure du ferrogel. Un ferrogel contenant des MNP hydrodynamiquement libres engendre des diffusivités effectives d’un soluté passif largement supérieures à la diffusion moléculaire intrinsèque mesurée pour le même soluté au sein de la structure de ferrogel en absence de champ magnétique rotatif. Les résultats expérimentaux et théoriques de cette thèse pourraient ouvrir la voie à l’utilisation de MNP/ferrofluide stimulés par champ magnétique pour la conception et le développement de systèmes micro-fluidiques et de matériaux magnétiques multifonctionnels dotés de propriétés de transport contrôlables à distance.The solution of advection-diffusion equation coupled to FHD equations of motion predicted weak contribution of advection in the observed phenomenon. The numerical simulations showed that the reduced axial dispersion is the outcome of anomalous anisotropic effective diffusivity in ferrofluid exposed to external uniform RMF. In chapter three, the identified mass transport properties of ferrofluid were further examined for (micro)-mixing applications in reaction engineering. A comparative study was conducted to evaluate the mixing efficiency between magnetic and non-magnetic fluids in a cylindrical capillary T-type mixer subjected to static (SMF), oscillating (OMF) and rotating magnetic fields. By using a probe reaction set (the Villermaux-Dushman reaction) with sensitive selectivity to mass transfer rate, mixing at molecular level was also investigated. The results showed substantial elimination of mass transfer rate influence on product distribution of chemical reactions when the mixing process is intensified with RMF. In chapter four, we extend the concept of mixing by MNP/RMF to ferrogels, prepared by seeding hard-dipole cobalt-ferrite MNP in polyacrylamide hydrogels. Quantitative analysis of magnetization data indicated the existence of hydrodynamically free MNPs, susceptible to Brownian relaxation along with mechanically blocked ones. A ferrogel consisting of hydrodynamically free MNP exhibits effective diffusivities higher than the intrinsic molecular diffusion of passive solute within the ferrogel structure. The experimental and theoretical findings in this thesis may open the way for application of magnetic field-stimulated MNP/ferrofluid for design and development of microfluidic systems and multifunctional magnetic materials with remote-controllable transport properties.In this PhD thesis, the transport of scalars in ferrofluids/ferrogels is theoretically and experimentally studied. The major interest is to experimentally quantify mass transport process in ferrofluids/ferrogels exposed to external magnetic fields and also to understand the mechanisms underlying the observed enhanced mass transport processes through ferrohydrodynamic (FHD) simulations. We also aim at utilizing the identified enhanced transport phenomena in ferrofluids for reaction engineering applications through experimental studies on mixing/micromixing in microchannels. The introduction presents the basic principles and fundamentals of ferrofluid and magnetic nanoparticles (MNP) dynamics from fluid mechanics and colloidal physics perspectives. The framework of ferrohydrodynamics (FHD), encompassing the ferrofluid equations of motion in connection with magnetic relaxation is explained. The recent literature relevant to the subject of scalar transport and mixing in ferrofluids is reviewed and the mechanisms of rate intensification of mass transport in ferrofluid subjected to various types of magnetic fields are discussed. The first chapter reports experimental observations and numerical simulations on the transport of scalars in quiescent Brownian ferrofluids under rotating magnetic field (RMF). The mass transport experiments were conducted in a cylindrical capillary T-mixer in presence/absence of transverse uniform RMF. Significant enhancement in mass transport was observed in presence of RMF in a direction normal to rotation axis of magnetic field. RMF directional control of mass flux enhancement was anisotropic since the molecular diffusion was the only detected transport mechanism in a direction parallel to the capillary axis. The significance of RMF driven ferrofluid advection (spin-up flow) in mass transport enhancement was examined in the light of the solution of advection-diffusion equation and subsequent comparison of numerical predictions with experimental results. Systematic analysis of numerical simulations compared to experimental observations unveiled that the effective diffusivity in ferrofluid consists of a diagonal tensor whose components are a function of RMF frequency and MNP concentration. In the second chapter, we exploited the concept of anisotropic anomalous effective diffusion in ferrofluids to explain the experimentally observed variations of axial dispersion in ferrofluid capillary Poiseuille flow in presence of external RMF. The experimental results showed that residence time distribution (RTD) in presence of RMF is more symmetric with retarded breakthrough time when frequency of RMF and magnetic nanoparticles (MNP) concentration are increased

Liquid-liquid Dispersion in Batch and In-line Rotor-Stator Mixers

This two-part dissertation investigates the behavior of batch and in-line rotor-stator mixers separately. In the first study, water was dispersed into viscous oil using a batch Silverson L4R rotor-stator mixer. The flow regime was determined by reference to published Power number data and by qualitative differences in drop size data. Drop breakup in laminar flow was analyzed by comparison to published single drop breakup experiments in idealized flow fields. The breakup mechanism in laminar flow was similar to that for simple shear flow and equal to about twice the nominal shear rate in the rotor-stator gap. Drop breakup in turbulent flow followed a mechanistic correlation for mean drop size for drops less than the Kolmogorov microscale, but still large enough that both inertial and viscous effects were manifest. Surfactants decreased drop size with Marangoni effects observed near the CMC for laminar, but not for turbulent flow. Below phase fractions of 0.05, d32 increased in a log-linear fashion with phase fraction for all conditions tested including: laminar and turbulent flow, presence of surfactant, and hydrophobically treated high-shear surfaces. The significant effect of phase fraction was caused by the flow structure being locally laminar near the drops, and was permitted by sufficiently low fluid viscosities which promoted film drainage. Above phase fractions of 0.1, drop sizes plateaued. This was attributed to decreasing coalescence rate and efficiency, along with increasing breakup. In the second study, the power consumption of an IKA 2000/4 in-line pilot scale rotor-stator mixer was measured with a purpose-built torque meter. The power spent by the mixer on pumping was insignificant compared to viscous dissipation. A constant power number was obtained for turbulent flow using constant power per stage with an empirically determined effective diameter for each generator type. For conditions where mean drop size was close to equilibrium, as determined by flowrate independence, previously reported mean drop size data were calculated using the well-known inertial subrange scaling law along with the power draw measurements of the present study. The maximum local energy dissipation rate was found to be nine times the average energy dissipation rat

Modeling of the Flow Dynamics through Incompressible Porous Media in Solid-Liquid Filtration

Solid-liquid filtration is a long-standing engineering practice and has been widely used in the chemical, process and mineral industries. Current models are semi-empirical in nature; thus, they require significant experimental and/or computational resources in order to determine the empirical quantities. In contrast, this dissertation provides a model to predict the dynamic behavior for both the liquid and solid phase of a filtration process without the requirement of empirical parameters. Instead, the model relies solely on the to-be-captured particle size distribution of contaminants as well as the pore size distribution of the filtration media. The new algorithm is capable of describing filtration based on both “steric” capture of contaminants as well as capture within dead-end pores in the material. This dissertation shows the performance of the model in modeling beds comprised of high void fraction materials (diatomaceous earth) that is used for the removal of multi-modal mixtures of contaminant. By formally accounting for the complex pore size distribution, the predict flow dynamics that are much closer to experimental results than the predictions of the traditional Kozeny-Carmen (K-C) model and show that this approach is viable for both statically formed and evolving (dynamic) beds. In an effort to understand the relationship between flow dynamics and pore size distribution more fully, a dynamic filter cake model is proposed that continuously modifies the pore size distribution as contaminants (polydispere spheres) are deposited. This dissertation also describes a simulation model capable of describing the capture of spherical particles within dead-end pores. A 3D discrete element method-lattice Boltzmann method (DEM-LBM) coupling approach is applied to investigate the particle capture under conditions of different particle size and pore structures. Both the pressure drop and the fluid density are examined to indicate this capture performance. The predicted flow dynamics of this new model match the dynamic experimental results remarkably well, setting the stage for a priori prediction of filtration times, flow-rates, particle capture, and pressure requirements from simple measurements of the size distribution of both the filter media pores as well as the contaminant particles/droplets

Volume II: Mining Innovation

Contemporary exploitation of natural raw materials by borehole, opencast, underground, seabed, and anthropogenic deposits is closely related to, among others, geomechanics, automation, computer science, and numerical methods. More and more often, individual fields of science coexist and complement each other, contributing to lowering exploitation costs, increasing production, and reduction of the time needed to prepare and exploit the deposit. The continuous development of national economies is related to the increasing demand for energy, metal, rock, and chemical resources. Very often, exploitation is carried out in complex geological and mining conditions, which are accompanied by natural hazards such as rock bursts, methane, coal dust explosion, spontaneous combustion, water, gas, and temperature. In order to conduct a safe and economically justified operation, modern construction materials are being used more and more often in mining to support excavations, both under static and dynamic loads. The individual production stages are supported by specialized computer programs for cutting the deposit as well as for modeling the behavior of the rock mass after excavation in it. Currently, the automation and monitoring of the mining works play a very important role, which will significantly contribute to the improvement of safety conditions. In this Special Issue of Energies, we focus on innovative laboratory, numerical, and industrial research that has a positive impact on the development of safety and exploitation in mining

Magnetic bead-based DNA extraction and purification microfluidic chip

This thesis was submitted for the degree of Doctor of Philosophy and awarded by Brunel University.A magnetic bead-based DNA extraction and purification device has been designed to be used for extraction of the target DNA molecules from whole blood sample. Mixing and separation steps are performed using functionalised superparamagnetic beads suspended in the cell lysis buffer in a circular chamber that is sandwiched between two electromagnets. Non-uniform nature of the magnetic field causes temporal and spatial distribution of the beads within the chamber. This process efficiently mixes the lysis buffer and whole blood in order to extract DNA from target cells. Functionalized surface of the magnetic beads then attract the exposed DNA molecules. Finally, DNA-attached magnetic beads are attracted to the bottom of the chamber by activating the bottom electrode. DNA molecules are extracted from the magnetic beads by washing and re-suspension processes. The numerical simulation approach has been adopted in order to design the magnetic field source. The performance of the magnetic field source has been investigated against different physical and geometrical parameters and optimised dimensions are obtained with two different magnetic field sources; integrated internal source and external source. A new magnetic field pattern has been introduced in order to efficiently control the bulk of magnetic beads inside the mixing chamber by dynamic shifting of magnetic field regions from the centre of the coils to the outer edge of the coils and vice versa. A Matlab code has been developed to simulate beads trajectories inside the designed extraction chip in order to investigate the efficiency of the magnetic mixing. A preliminary target molecule capturing simulation has also been performed using the simulated bead trajectories to evaluate the DNA-capturing efficiency of the designed extraction chip. The performance of the designed extraction chip has been tested by conducting a series of biological experiments. Different magnetic bead-based extraction kits have been used in a series of preliminary experiments in order to extract a more automation friendly extraction protocol. The efficiency of the designed device has been evaluated using the spiked bacterial DNA and non-pathogenic bacterial cell cultures (B. subtilis, Gram positive bacteria and E. coli, Gram negative bacteria) into the blood sample. Excellent DNA yields and recovery rates are obtained with the designed extraction chip through a simple and fast extraction protocol

The Application of Fluorescence Lifetime Imaging Microscopy to Quantitatively Map Mixing and Temperature in Microfluidic Systems

The technique of Fluorescence Lifetime Imaging Microscopy (FLIM) has been employed to quantitatively and spatially map the fluid composition and temperature within microfluidic systems. A molecular probe with a solvent-sensitive fluorescence lifetime has been exploited to investigate and map the diffusional mixing of fluid streams under laminar flow conditions within a microfluidic device. Using FLIM, the fluid composition is mapped with high quantification and spatial resolution to assess the extent of mixing. This technique was extended to quantitatively evaluate the mixing efficiency of a range of commercial microfluidic mixers employing various mixing strategies, including the use of obstacles fabricated within the channels. A fluorescently labelled polymer has been investigated as a new probe for mapping temperature within microfluidic devices using FLIM. Time Correlated Single Photon Counting (TCSPC) measurements showed that the average fluorescence lifetime displayed by an aqueous solution of the polymer depended strongly on temperature, increasing from 3 ns to 13.5 ns between 23 and 38 oC. This effect was exploited using FLIM to provide high spatial resolution temperature mapping with sub-degree temperature resolution within microfluidic devices. A temperature-sensitive, water-soluble derivative of the rhodamine B fluorophore, effective over a wide dynamic temperature range (25 to 91 oC) has been used to map the temperature distribution during the mixing of fluid streams of different temperatures within a microchannel. In addition, this probe was employed to quantify the fluid temperature in a prototype microfluidic system for DNA amplification. FLIM has been demonstrated to provide a superior approach to the imaging within microfluidic systems over other commonly used techniques, such as fluorescence intensity and colourimetric imaging