Coupling of local visualization and numerical approach for particle microfiltration optimization

The performance of the microfiltration process is controlled by the filter fouling due to the accumulation of solid matter forming a cake layer on the membrane surface. The objective of this work is to study the cake build up and growth at the particle level and to establish correlations with microfiltration performance measured at the process scale. A theoretical model coupling Navier–Stokes equation, convective/diffusion particle transport and deposit formation is developed to simulate a sequence of microfiltration in a confined geometry (Comsol Multyphysics^®). This model is used to make predictive simulations of cake growth during the filtration of diluted particles in the range of size of microorganism (5 μm). In the same time a specific filtration micro-system including an optical chamber and a microsieve (Aquamarijn^®) filtration membrane is designed in order to perform an experimental approach allowing in situ 3D-visualization of a deposit of model particles (polystyrene fluorescent microspheres) using Confocal laser scanning microscopy (CLSM). Based on image analysis, the cake building and properties (particle arrangement, thickness) are analyzed. These experimental data will be further used to improve the filtration model in order to obtain a predictive tool for process optimization.     

A superposable double-gradient droplet array chip for preparation of PEGDA microspheres containing concentration-gradient drugs

This article describes a superposable double-concentration-gradient droplet array chip, which allows a variety of concentration combinations of two components to be formed simultaneously. The concentration gradients generated from two layers of the chip could be arbitrarily superimposed by adjusting the center angle between the two bonding layers. With the aqueous phase flow rate of 1.0 μL min^?1 and the oil phase flow rate of 30.0 μL min^?1, the droplets about 58 μm in diameter were produced, and the coefficients of variation were below 6.0% for single channel and 5.7% for all the channels. Using a dual-32-channel superposable gradient droplet array chip, poly(ethylene glycol) diacrylate (PEGDA) microspheres containing concentration-gradient combinations of rhodamine B and fluorescein were fabricated to demonstrate the capability of PEGDA for encapsulating hydrophilic and hydrophobic substances, as well as the proper concentration-gradient distribution. Furthermore, PEGDA microspheres loaded with two anticancer drugs, hydrophilic doxorubicin hydrochloride and hydrophobic paclitaxel, of 17 concentration combinations were simultaneously prepared. The drug-induced apoptosis of human uterine cervix cancer cells was investigated using the dual-drug-loaded PEGDA microspheres. The optimum synergistic concentration combination of the two drugs was 12.5 μg mL^?1 for doxorubicin hydrochloride and 43.75 μg mL^?1 for paclitaxel according to the preliminary screening. The superposable double-gradient droplet array generator was demonstrated to be a promising platform for screening multiple drug combination in microcarriers.     

Droplets coalescence and mixing with identical and distinct surface tension on a wettability gradient surface

The influence of identical and distinct surface tensions on the coalescence and mixing of droplets after a direct collision on a wettability gradient surface (made from a self-assembled monolayer, SAM technique) was investigated. The results indicate that their mixing is driven sequentially by interior convection and diffusion; the convection endures less than 100 ms but dominates more than 60 % of the mixing. If the stationary droplet has a large surface tension (73.28 mN × m^?1), whether the moving droplet has a large surface tension (73.28 mN × m^?1) or a small surface tension (38.63 mN × m^?1), the mushroom-shaped mixing pattern is generated within the coalesced droplet that enhances the convective mixing and also significantly enlarges the interface for mass diffusion. The mixing index of these two cases was greater than 0.8 at 120 s after the collision. For the cases in which the stationary droplet with a small surface tension collided by the moving droplet with a large surface tension, a mixing pattern with a round-head shape developed, which was insufficient to benefit the mixing. When the stationary and moving droplets both had small surface tension, the moving droplet was unable to merge with stationary droplet and had poor mixing quality due to the small surface Gibbs energy of both stationary and moving droplets. For the collision of droplets of identical surface tension, the surface tension affects the coalescence behavior; for the collision of droplets with distinct surface tension, the coalescence behavior and mixing quality depend on the colliding arrangement of stationary and moving droplets.     

A microfluidic platform with permeable walls for the analysis of vascular and extravascular mass transport

The interface between the blood pool and the extravascular matrix is fundamental in regulating the transport of molecules, nanoparticles and cells under physiological and pathological conditions. In this work, a microfluidic chip is presented comprising two parallel microchannels connected laterally via an array of high aspect ratio micropillars, constituting the permeable vascular membrane. A double-step lithographic process combined with a replica molding approach is employed to realize 80 different arrays of micropillars exhibiting three cross-sectional geometries (rectangular, elliptical and curved); two orientations (normal and parallel) with respect to the flow; and a variety of width and gap sizes, respectively, ranging from 10 to 20 μm and 2 to 5 μm. As compared to conventional rectangular structures, the curved pillars provide higher bending stiffness, lower adhesive interactions, and smaller intra-channel separation distances. Specifically, 10-μm-wide curved pillars, laying parallel to the flow, offered the highest mechanical stability. To assess vascular permeability, the extravascular channel was filled with a hyaluronic acid hydrogel, while fluorescent Dextran molecules and calibrated polystyrene beads were injected in the vascular channel. Membrane permeability was observed to reduce with the molecular weight of Dextran and diameter of the beads, ranging from about 6 × 10^?5 to 2 × 10^?5 cm/s for 40 and 250 kDa Dextran and up to zero for 1.5 μm beads. The presented data demonstrate the potential of the proposed microfluidic chip for analyzing the vascular and extravascular mass transport, over multiple spatial and temporal scales, in a variety of diseases involving differential permeation across vascular walls.     

Electrochemical determination of glutamic pyruvic transaminase using a microfluidic chip

The activity of glutamic pyruvic transaminase (GPT) is an important clinical evidence for some acute diseases such as acute hepatopathy and myocardial infarction. Thus, there is a demand for rapid determination of GPT in small formats at point-of-need. Herein, we describe a novel method of electrochemical determination of GPT with microfluidic technique. GPT activity was indirectly determined via the electrochemical (EC) detection of nicotinamide adenine dinucleotide (NADH) produced from the GPT transdeamination reaction. A type of microfluidic chip was developed, in which a passive mixer comprising 100 sub-ribs and a three-electrode strip for EC were integrated. To verify the response to NADH, a series of NADH concentrations varying from 19 µM to 5 mM were calibrated with cyclic voltammetry within the microfluidic chip. And a linear relationship with R ² 0.9982 between the peak current and the concentration of NADH was obtained. Then, the GPT activity was determined using the chips containing and not containing a ribs-type mixer. And a linear relationship which contained two sections between the GPT activity and the peak current was obtained. The chip with a ribs-type mixer exhibited the sensitivity of 0.0341 μA U^?1 L in the range of 10–50 U L^?1 and 0.0236 μA U^?1 L in the range of 50–250 U L^?1. And the detection limit of the chip with a ribs-type mixer was 9.25 U L^?1. The complete detection process of GPT activity within the microfluidic chip was realized, and the time-consuming problem was remarkably improved too.     

Selective and in-situ determination of carbonate and oxide particles in aqueous solution using laser-induced breakdown spectroscopy (LIBS) for wearable information equipment

Laser-induced breakdown spectroscopy (LIBS) has been applied for quantitative analysis of Al₂O₃, CaCO₃ and MgO particles suspended in water. In the single elemental system, the plasma emission intensities of Al, Ca and Mg were linearly increased with concentration of elements in the range of 1.0×10^?5–1.0×10^?3  M, 1.0×10^?4–2.0×10^?3 M and 8.0×10^?5 –4.0×10^?3 M, respectively. We also investigated the concentration dependence of breakdown spectra for suspended mixtures of Al₂O₃, CaCO₃ and MgO particles. The emission lines, such as Al I, Ca I, Ca II and Mg I, were appeared in the LIBS spectrum simultaneously, and each emission peak could be deconvoluted. The plasma emission intensities of Al, Ca and Mg in the multielemental system were also linearly increased with their concentrations in the range of 1.0×10^?5–1.0×10^?3 M, 1.0×10^?4–2.0×10^?3 M and 4.0×10^?4–2.0×10^?3 M, respectively. LIBS was found to be available for quantitative and qualitative measurement of the concentrations of Al₂O₃, CaCO₃ and MgO particles suspended in water. The present results suggest that LIBS is a potentially useful tool for in-situ analysis on particles composition and concentrations for environmental monitoring by the wearable information equipments.     

Development and characterization of a microthermoelectric generator with plated copper/constantan thermocouples

This work reports the development and the characterization of a microthermoelectric generator (μTEG) based on planar technology using electrochemically deposited constantan and copper thermocouples on a micro machined silicon substrate with a SiO₂/Si₃N₄/SiO₂ thermally insulating membrane to create a thermal gradient. The μTEG has been designed and optimized by finite element simulation in order to exploit the different thermal conductivity of silicon and membrane in order to obtain the maximum temperature difference on the planar surface between the hot and cold junctions of the thermocouples. The temperature difference was dependent on the nitrogen (N₂) flow velocity applied to the upper part of the device. The fabricated thermoelectric generator presented maximum output voltage and power of 118 mV/cm² and of 1.1 μW/cm², respectively, for a device with 180 thermocouples, 3 kΩ of internal resistance, and under a N₂ flow velocity of 6 m/s. The maximum efficiency (performance) was 2 × 10^?3 μW/cm² K².     

Quantitative analysis of microfluidic mixing using microscale schlieren technique

In this study, we discuss the employment of microscale schlieren technique to facilitate measurement of inhomogeneities in a micromixer. By mixing dilute aqueous ethanol and water in a T-microchannel, calibration procedures are carried out to obtain the relation between the concentration gradients and grayscale readouts under various incident illuminations, concentrations of aqueous ethanol solution, and knife-edge cutoffs. We find that to broaden measuring range with minimal error, the luminous exitance should be tuned to have a reference background with an average grayscale readout of 121, and dilute aqueous ethanol solution with a mass fraction of 0.05 should be used along a 50 % cutoff. For concentration gradients greater than 6.8 × 10^?3 or below ?2.5 × 10^?2 μm^?1, the calibration curves show great linearity. Correspondingly, the discernable limit of our microscale schlieren system is 2.3 × 10^?5 μm^?1 for a positive refractive index gradient and ?8.6 × 10^?5 μm^?1 for a negative refractive index gradient. Once the relation between concentration gradients and grayscale readouts is known, the concentration distribution in a microfluidic can be reconstructed by integrating its microscale schlieren image with appropriate boundary conditions. The results prove that the microscale schlieren technique is able to provide spatially resolved, noninvasive, full-field measurements. Since the microscale schlieren technique is directly linked to the measurement of a refractive index gradient, the present method can be easily extended to other scalar quantifications that are related to the variation of refractive index.     

Dean flow focusing and separation of small microspheres within a narrow size range

Rapid, selective particle separation and concentration within the bacterial size range (1–3 μm) in clinical or environmental samples promises significant improvements in detection of pathogenic microorganisms in areas including diagnostics and bio-defence. It has been proposed that microfluidic Dean flow-based separation might offer simple, efficient sample clean-up: separation of larger, bioassay contaminants to prepare bioassay targets including spores, viruses and proteins. However, reports are limited to focusing spherical particles with diameters of 5 μm or above. To evaluate Dean flow separation for (1–3 μm) range samples, we employ a 20 μm width and depth, spiral microchannel. We demonstrate focusing, separation and concentration of particles with closely spaced diameters of 2.1 and 3.2 μm, significantly smaller than previously reported as separated in Dean flow devices. The smallest target, represented by 1.0 μm particles, is not focused due to the high pressures associated with focussing particles of this size; however, it is cleaned of 93 % of 3.2 μm and 87 % of 2.1 μm microparticles. Concentration increases approaching 3.5 times, close to the maximum, were obtained for 3.2 μm particles at a flow rate of 10 μl min^?1. Increasing concentration degraded separation, commencing at significantly lower concentrations than previously predicted, particularly for particles on the limit of being focused. It was demonstrated that flow separation specificity can be fine-tuned by adjustment of output pressure differentials, improving separation of closely spaced particle sizes. We conclude that Dean flow separation techniques can be effectively applied to sample clean-up within this significant microorganism size range.     

Submicron polymer structures with X-ray lithography and hot embossing

This article describes the process chain for replication of submicron structures with varying aspect ratios (AR) up to 6 in polymethylmethacrylate (PMMA) by hot embossing to show the capability of the entire LIGA process to fabricate structures with these dimensions. Therefore a 4.7 μm thick layer of MicroChem 950k PMMA A11 resist was spin-coated on a 2.3 μm Ti/TiO _x membrane. It was patterned with X-ray lithography at the electron storage ring ANKA (2.5 GeV and λ _c ≈ 0.4 nm) at a dose of 4 kJ/cm³ using a Si₃N₄ membrane mask with 2 μm thick gold-absorbers. The samples were developed in GG/BDG and resulted in AR of 6–14. Subsequent nickel plating at 52°C resulted in a 200 μm thick nickel tool of 100 mm diameter, which was used to replicate slit-nozzles and columns in PMMA. Closely packed submicron cavities with AR 6 in the nickel shim were filled to 60% during hot embossing.     

One-step rapid fabrication of paper-based microfluidic devices using fluorocarbon plasma polymerization

In this work, we demonstrated an all-dry, top-down, and one-step rapid process to fabricate paper-based microfluidic devices using fluorocarbon plasma polymerization. This process is able to create fluorocarbon-coated hydrophobic patterns on filter paper substrates while maintaining the trench and detection regions intact and free of contamination after the fabrication process, as confirmed by attenuated total reflectance–Fourier transform infrared spectroscopy and X-ray photoelectron spectroscopy. We have shown that the processing time is one critical factor that influences the device performance. For the device fabricated with a sufficiently long processing time (180 s), the sample fluid flow can be well confined in the patterned trenches. By testing the device with an 800 μm channel width, a sample solution amount as small as 4.5 μL is sufficient to perform the test. NO₂ ^? assay is also performed and shows that such a device is capable for biochemical analysis.     

On-chip manipulation and trapping of microorganisms using a patterned magnetic pathway

We demonstrate on-chip manipulation and trapping of individual microorganisms at designated positions on a silicon surface within a microfluidic channel. Superparamagnetic beads acted as microorganism carriers. Cyanobacterium Synechocystis sp. PCC 6803 microorganisms were immobilized on amine-functionalized magnetic beads (Dynabead^® M-270 Amine) by 1-ethyl-3-(3-dimethylaminopropyl)carbodiimide (EDC)–N-hydroxysulfosuccinimide coupling chemistry. The magnetic pathway was patterned lithographically such that half-disk Ni₈₀Fe₂₀ (permalloy) 5 μm elements were arranged sequentially for a length of 400 micrometers. An external rotating magnetic field of 10 mT was used to drive a translational force (maximum 70 pN) on the magnetic bead carriers proportional to the product of the field strength and its gradient along the patterned edge. Individual microorganisms immobilized on the magnetic beads (transporting objects) were directionally manipulated using a magnetic rail track, which was able to manipulate particles as a result of asymmetric forces from the curved and flat edges of the pattern on the disk. Transporting objects were then successfully trapped in a magnetic trapping station pathway. The transporting object moves two half-disk lengths in one field rotation, resulting in movement at ~24 μm s^?1 for 1 Hz rotational frequency with 5 μm pattern elements spaced with a 1 μm gap between elements.     

On-chip encapsulation via chaotic mixing

A microfluidic device for production of uniform size capsules with a prescribed membrane thickness is described. It is versatile, novel and suitable for various polymerization reactions. Parameters such as polymerization time and reagent concentrations can be precisely tuned to control the membrane properties. The device features a part which allows to overcome the diffusion barrier by initiating interfacial polymerization via chaotic mixing. It also allows the termination of the reaction and the collection of the resulting capsules. We observe different typical dynamical phenomena occurring in capsules during their flow along the microchannel, namely wrinkling of the membrane, parachute and bullet shapes and bursting of the capsules due to strong hydrodynamical flow. In addition to production, the monitoring of capsule dynamics in flow gave a possibility to estimate the elastic surface modulus \(E_{{\rm S}}\) and the membrane thickness t. We found that \(E_{{\rm S}}\) can be as low as 6 × 10^?3 N m^?1 and that the thickness can be below 100 nm. This microfluidic device is therefore capable of producing uniform size capsule solutions with suitable membrane properties for the controlled release of drugs, and as a model system of red blood cells for microhydrodynamics experiments.     

Mesoporous silicon-based miniature fuel cells for nomadic and chip-scale systems

We report here the fabrication of a new miniature fuel cell for nomadic applications and chip-scale power supply based on a Nafion^®-filled porous silicon self-supported membrane. Combining advantages of Nafion^® for its great proton conduction and silicon for an easier integration and standard microfabrication techniques, this solution enables the integration of gas feed and electrical contacts into the membrane etching process thanks to simple KOH wet etching processes and metal sputterings. The encapsulation is also possible. Compared to simple Nafion^® membranes, this technique may reduce the lateral water diffusion through the membrane. Experiments have been carried out at room temperature and gas feed H₂ is provided by the electrolysis of a NaOH solution. A long-term power density of 18 mW cm^?2 has been achieved after stabilization with a maximum current density of 101 mA cm^?2 and an open circuit voltage of 0.8 V.     

A patterning technique of lead zirconate titanate thin film by ultraviolet-light

The patterning technique of Pb(Zr, Ti)O₃ (PZT) thin film is an essential process in device fabrication processes for application in microsensors and microactuators. In this paper, a novel pattern technique is proposed for PZT thin film by UV photolysis processes. PZT thin films were first spin coated on the substrate and exposed by UV light for photolysis step. The UV photolysis step defined exposed and unexposed area by mask, and the pattern will be transferred to PZT thin film. After photolysis, PZT films were placed in non-ionic surfactant to remove unexposed area. Finally, PZT films were sintered at 650 °C in the furnace for crystallization. Experimental results showed that remnant polarization of patterned PZT film by UV photolysis was 21.4 μc cm^?2, which was compared to 17.24 μc cm^?2 by hot plate prolysis. Coercive fields were 45 and 104 kV cm^?1 by UV photolysis and hot plate prolysis, respectively. Dielectric loss was 0.027 by UV photolysis which was much smaller than 0.043 by hot plate prolysis. PZT thin films patterned by UV photolysis showed satisfactory geometries.     

Variation in aerosol black carbon concentration and its emission estimates at the mega-city Delhi

Simultaneous measurements of aerosol black carbon (BC) mass concentration using an Aethalometer Model AE-42 and mixing layer height (MLH) using a monostatic sonic detection and ranging (SODAR) system were carried out from January 2006 to January 2007 at the mega-city Delhi. The BC concentration generally had a typical diurnal variation with morning and late-afternoon/night peaks. The average BC concentration during the whole period of observation was fairly high at 14.75 μg m^?3. The BC concentration nearly doubled during cloudy-sky conditions compared to that during clear-sky conditions. The seasonal variation showed a maximum average concentration during the winter (25.5 μg m^?3) and a minimum during the monsoon season (7.7 μg m^?3), with post- and pre-monsoon values at 13.7 and 9.4 μg m^?3, respectively. The average BC concentrations were strongly affected by the ventilation coefficient, a product of average wind speed (WS) and average MLH, and were found to be strongly anticorrelated. A simple model of BC concentration along with the MLH and WS was applied to estimate the average BC emission, which was found to vary in the range 11?000–17?000 kg of BC per day. The maximum emission during the day averaged every hour for different months lay in the range 1000–2100 kg h^?1. The mean monthly emission varied in the range 0.35–0.52 Gg per month, giving rise to an annual estimated emission of 4.86 Gg in the year 2006 over Delhi.     

An effective PDMS microfluidic chip for chemiluminescence detection of cobalt (II) in water

A microfluidic chip for the chemiluminescence detection of cobalt (II) in water samples, based on the measurement of light emitted from the cobalt (II) catalysed oxidation of luminol by hydrogen peroxide in basic aqueous solution, is presented. The microfluidic chip was designed and fabricated from polydimethylsiloxane using micro-molding method. Optimized reagents conditions were found to be 5.0 × 10^?4 mol/L luminol, 1.0 × 10^?2 mol/L hydrogen peroxide, and 8.0 × 10^?2 mol/L sodium hydroxide. The system can perform fully automated detection with a reagent consumption of only 2.4 μL each time. The linear range of the cobalt (II) ions concentration was 1.0 × 10^?10–1.0 × 10^?3 mol/L and the detection limit was 5.6 × 10^?11 mol/L with the S/N ratio of 3. The relative standard deviation was 4.6 % for 1.0 × 10^?5 mol/L cobalt (II) ions (n = 10).     

MEMS design and fabrication of an electrostatic vibration-to-electricity energy converter

This paper presents a micro electrostatic vibration-to-electricity energy converter based on the micro-electromechanical system. For the 3.3 V supply voltage and 1 cm² chip area constraints, optimal design parameters were found from theoretical calculation and Simulink simulation. In the current design, the output power is 200 μW/cm² for the optimal load of 8 MΩ. The device was fabricated in a silicon-on-insulator wafer. Mechanical and electrical measurements were conducted. Residual particles caused shortage of the variable capacitor and the output power could not be measured. Fabrication processes are being refined to remove the back silicon substrate to eliminate residual particles and parasitic capacitance.     

Hyper-miniaturization of monodisperse alginate–TiO2 composite particles with densely packed TiO2 nanoparticles

We report a novel technique to fabricate alginate–TiO₂ composite particles with densely packed TiO₂ nanoparticles. Using a microfluidic device, monodisperse sodium alginate droplets containing low-density TiO₂ nanoparticles (1 or 5 w/v%) were formed in the oil phase. The sodium alginate droplets formed in the oil phase were subsequently placed on a Ca²⁺-loaded agarose-gel plate to induce shrinkage by water removal (from the droplets to the Ca²⁺-loaded agarose-gel plate) and gelation by Ca²⁺ transport (from the Ca²⁺-loaded agarose-gel plate to the droplets). Thus, the produced alginate–TiO₂ composite particles containing densely packed TiO₂ nanoparticles were significantly smaller than the microchannel. We also investigated the optimal conditions to successfully produce spherical composite particles by varying the oil phases, surfactants, calcium concentrations and gel strength of the agarose-gel plate. Moreover, our method could decrease the probability of channel clogging that often occurs when a colloidal suspension (e.g., nanoparticles) is used as the dispersed phase. This method facilitates the stable production of monodisperse alginate–inorganic composite particles for a wide range of applications.     

A large-area,all-plastic,flexible electroosmotic pump

A large-area, fabric-like pump would potentially have applications, for example, in controlling water transport through a garment, such as a rain jacket, regardless of the external temperature and humidity. This paper presents an all-plastic, flexible electroosmotic pump, constructed from commercially available materials: A polycarbonate membrane combined with the electrochemically active polymer poly(3,4-ethylenedioxythiophene) polystyrene sulfonate that actively transports water using an electric potential that can be supplied by a small battery. By using electrochemically active polymer electrodes instead of metal electrodes, the electrochemical reaction that drives flow avoids the oxygen and hydrogen gas production or pH changes associated with water electrolysis. We observe a water mass flux up to 23 mg min^?1 per cm² polycarbonate membrane (porosity 10–15%), at an applied potential of 5 V, and a limiting operating pressure of 0.3 kPa V^?1, similar to previously reported membrane-based electroosmotic pumps.