A microfluidic device includes a channel through which a reaction solution flows. The channel passes through a reaction section having a plurality of temperature zones set at predetermined different temperatures. The channel includes, at least in the reaction section, a region where a cross-sectional area decreases in a feeding direction of the reaction solution.

A process for producing polymer-supported metal nanoparticles involves confinement of metal nanoparticles in polymeric nanotubes or nanosheets in an aqueous environment using hydrophobic reactants. Metal nanoparticles supported in the polymeric nanotubes or nanosheets are substantially monodisperse and have an average particle size of 4 nm or less. The polymer-supported metal nanoparticles are useful in fuel cells, sensors, bioanalysis, biological labeling or semi-conductors, especially as catalysts.

A catalytic microscale reactor with spiral reactor geometry may have a high surface area to volume ratio, high catalytic surface area, high heat transfer surface area, long residence time, and high single pass conversion. The catalytic surface may be treated with microsphere spacer particles which serve to maintain the space between them at an engineered distance without the need for precise manufacturing techniques. The design of the reactor may allow for a catalyst surface to be removed, uncoiled, refurbished, and recoiled in an automated continuous process. An automated continuous process may be suitable both for initially preparing a new catalytic surface as well as refurbishing a fouled catalytic surface and may reduce the time and cost to prepare a new surface.

A channel assembly is disclosed, which may comprise a microfluidic channel. Methods of manufacture are also disclosed as are detectors and detector components which may comprise such a channel assembly. An example is a detection apparatus comprising: a detector for detecting a substance of interest; and a pneumatic system comprising a microfluidic channel assembly comprising a first microfluidic channel for dispensing vapour to the detector, wherein the first microfluidic channel comprises a groove in a surface of a polymer body and a wall of the first channel is provided by a film bonded to the surface of the body over the groove.

Disclosed herein are methods for preparing nanomaterials, such as nanoparticles. The methods can involve jet-mixing two or more precursor solutions to form the nanomaterials. By rapidly mixing the precursor solutions, nanomaterials of improved quality and uniformity can be prepared in high yield (e.g., in yields of at least 85%). The methods are also scalable, and allow for the continuous production of nanomaterials. Also provided are jet-mixing reactors that can be used to prepare nanomaterials using the methods described herein.

The present invention refers to a system for the process of synthesis of zeolite nanoparticles in continuous flow wherein the processes of mixing, aging and crystallization are integrated, to reduce the synthesis time. The system has a microfluidic device of the 3D crossing channels micromixer type, consisting of microchannels built in series, used to generate the reaction mixture; buffer system with addition of seeds; and a heated tubular reactor which, in turn, is used for crystallization, which takes place through a continuous hydrothermal process.

A pressure sensor (100) for a measuring system (10) measuring concentrations of gaseous and/or aerosol components of a gas mixture with a reaction carrier (14), with a flow channel (42). The flow channel (42) forms a reaction chamber (46) with a reactant (48), that enters into an optically detectable reaction, and with a measuring device (12) with a gas port unit (5) connecting an inlet channel (16) and an outlet channel (18) to the flow channel (42) and a gas delivery unit (28). The pressure sensor (100) measures a pressure difference of a gas mixture flowing through the gas delivery assembly unit (2) and/or the flow channel (42) of the reaction carrier (14) and has an elastic element (102), which is configured to undergo deformation as a function of the pressure difference. A measuring method, a measuring device and a reaction carrier for such a measuring system are also provided.

A continuous acoustic chemical microreactor system is disclosed. The system includes a continuous process vessel (CPV) and an acoustic agitator coupled to the CPV and configured to agitate the CPV along an oscillation axis. The CPV includes a reactant inlet configured to receive one or more reactants into the CPV, an elongated tube coupled at a first end to the reactant inlet and configured to receive the reactants from the reactant inlet, and a product outlet coupled to a second end of the elongated tube and configured to discharge a product of a chemical reaction among the reactants from the CPV. The acoustic agitator is configured to agitate the CPV along the oscillation axis such that the inner surface of the elongated tube accelerates the one or more reactants in alternating upward and downward directions along the oscillation axis.

The present disclosure provides a microchannel device including a first base having a defining surface that defines a flow channel and containing a polymer that contains a fluorine atom and a second base having a defining surface that defines the flow channel together with the defining surface of the first base, having solvent resistance, and coming into contact with the first base, in which an arithmetic average roughness Ra of a surface of the first base, exposed by peeling the second base from the first base, is 1 μm or more, and provides a use application thereof.

There is provided a master for micro flow path creation, a transfer copy, and a method for producing a master for micro flow path creation by which transfer copies having an area with high hydrophilicity can be easily mass-produced, the master for micro flow path creation including: a base material; a main concave-convex portion provided on a surface of the base material and extending in a planar direction of the base material; and a fine concave-convex portion provided on a surface of the main concave-convex portion and having a narrower pitch than the main concave-convex portion. The fine concave-convex portion has an arithmetic average roughness of 10 nm to 150 nm and has a specific surface area ratio of 1.1 to 3.0.