According to some aspects, described herein is an automated droplet-based reactor that utilizes oscillatory motion of a droplet in a tubular reactor under inert atmosphere. In some cases, such a reactor may address current shortcomings of continuous multi-phase flow platforms.

A method of manufacturing a microfluidic system or microfluidic device having at least one channel includes providing a base sheet, providing a deformable intermediate layer, providing a cover film, and laminating the base sheet, the intermediate layer and the cover film so that a back surface of the intermediate layer is attached to a front surface of the base sheet and a back surface of the cover film is attached to a front surface of the intermediate layer opposite to the back surface thereof, thereby forming a laminate comprising the base sheet, the intermediate layer and the cover film. Further, the method includes applying pressure to the front surface of the intermediate layer through the cover film so as to deform the intermediate layer, thereby forming the at least one channel. The invention also relates to a microfluidic system or microfluidic device) manufactured by this method.

A reactor system for high throughput applications includes a plurality of reactor assemblies, each reactor assembly including: a fluid source, which fluid source is adapted to provide a pressurized fluid to the flow-through reactors, a flow splitter which flow splitter includes a planar microfluidic chip, which microfluidic chip has a chip inlet channel and a plurality of chip outlet channels, which microfluidic chip further includes a plurality of flow restrictor channels, where each flow restrictor channel extends from said chip inlet channel to an associated chip outlet channel, where the chip inlet channel and the chip outlet channels each have a diameter, where the diameter of the chip inlet channel is the same or less than the length of said chip inlet channel and where the diameter of each chip outlet channel is the same or less than the length of said chip outlet channel.

Provided is a microreactor which can be produced at a lower cost. The microreactor has a transfer means for transferring a liquid raw material using the pressure of a gas. The microreactor has a raw material tank for storing the liquid raw material. The transfer means for transferring a liquid raw material can transfer the liquid raw material stored in the raw material tank using the pressure of a gas in the raw material tank. A pipe which connects the raw material tank and the next device is preferably provided with a small diameter portion.

A photovoltaic apparatus comprising: at least one photovoltaic surface electrically connected to a set of photovoltaic electrodes; and a chemical reactor electrically connected to the set of photovoltaic electrodes. The chemical reactor enables N pairwise fluid contacts among k chemical fluids, with k2 and N4 and comprises: a reaction layer extending in a plane subtended by two directions; N chemical cells, each including two circuit portions, designed for enabling circulation of two of the k chemical fluids, respectively, the two circuit portions intersecting each other, thereby enabling one pairwise fluid contact for the two of the k chemical fluids; and a fluid distribution circuit comprising: k sets of inlet orifices sequentially alternating along lines parallel to one of the two directions; and k sets of outlet orifices sequentially alternating along lines parallel to the inlet orifices, and wherein, each circuit portion connects an inlet orifice to an outlet orifice.

A check-valve comprises: a thin sheet and a thick sheet; flow paths for flowing fluid which are formed by penetrating the thin sheet and the thick sheet; a flow-in chamber and a flow-out chamber which are connected to the flow paths; a partition sheet which is bonded to the thin sheet and the thick sheet while being sandwiched therebetween, and has a flexible inner flange which projects in cavities of the flow-in chamber and the flow-out chamber and does not close the flow-out valve chamber by flexing toward the flow-out valve chamber in a normal flow, and closes the flow-in valve chamber by flexing toward the flow-in valve chamber in a reverse flow; and a through-pass hole which is opened at the partition sheet and connects the both valve chambers.

A reactor system for high throughput applications includes a plurality of reactor assemblies, each reactor assembly including: a fluid source, which fluid source is adapted to provide a pressurized fluid to the flow-through reactors, a flow splitter which flow splitter includes a planar microfluidic chip, which microfluidic chip has a chip inlet channel and a plurality of chip outlet channels, which microfluidic chip further includes a plurality of flow restrictor channels, where each flow restrictor channel extends from said chip inlet channel to an associated chip outlet channel, where the chip inlet channel and the chip outlet channels each have a diameter, where the diameter of the chip inlet channel is the same or less than the length of said chip inlet channel and where the diameter of each chip outlet channel is the same or less than the length of said chip outlet channel.

A process for continuous preparation of halogenated alkoxyethane of general formula XCIHCCF.sub.2OR, where X is Cl or F and OR is C.sub.1-4 alkoxy, the process comprising a step of introducing in a plate reactor reaction components comprising (i) a compound of general formula XCIHCCYF.sub.2, where each of X and Y is independently Cl or F, (ii) a base, and (iii) a C.sub.1-4 alkanol, wherein (a) the plate reactor comprises a fluidic module defining one or more fluidic path(s) through which the reaction components flow as a reaction mixture, and (b) the halogenated alkoxyethane is formed at least upon the reaction components mixing, with the so formed halogenated alkoxyethane flowing out of the plate reactor in a reactor effluent, and (c) the base is one that forms a salt soluble in the alkanol during formation of the halogenated alkoxyethane.

The present disclosure generally relates to a flow reactor system (100) and a flow reaction method (200). The flow reactor system (100) comprises liquid pumps (110) for communicating liquid reagents based on a set of flow conditions, a fluid pump (200) for communicating a carrier fluid that is immiscible with the liquid reagents; a fluidic mixer (130) for mixing the liquid reagents into a liquid mixture, a measurement device (150) for measuring properties of liquid plugs (140) discharged from an outlet (136) of the fluidic mixer (130); and a control module configured for controlling the liquid pumps (110) and adjusting the flow conditions based on the measured properties of the liquid plugs (140), wherein the liquid plugs (140) are representative of different flow conditions.

The automated synthesis of clinically relevant amounts of 16-.sup.18F-fluoro-5-dihydrotestosterone (.sup.18F-FDHT) using a commercially available radiosynthesizer. Synthesis was performed in 90 minutes with a decay-corrected radiochemical yield of 295%. The specific activity was 4.6 Ci/mol (170 GBq/mol) at end of formulation with a starting activity of 1.0 Ci (37 GBq). The formulated .sup.18F-FDHT yielded sufficient activity for multiple patient doses and passed all quality control tests required for routine clinical use.