A method for producing a chemical reactor, wherein the chemical reactor comprises one or more effective channels which comprise pillar structures, an input connected to one of the effective channels to allow fluid/gas into the effective channels and an output connected to one of the effective channels to remove at least one component of the liquid/gas. The method comprises obtaining an initial design of the reactor, further introducing into the initial design at least a structured area positioned adjacent to an effective channel of the one or more effective channels located at the edge of the initial design, the structured area not being fluidly connected to one of the effective channels, to obtain a further design and the production of the reactor according to the further design.

A microfluidic synthesis platform includes a microfluidic chip holder that has a computer controlled heating element and cooling element therein. A microfluidic chip is mountable in the microfluidic chip holder. The microfluidic chip is formed by a hydrophobic substrate having patterned thereon a hydrophilic reaction site and a plurality of hydrophilic channels or pathways extending outward from the hydrophilic reaction site and terminating at respective loading sites on the substrate, wherein the hydrophilic channels or pathways are tapered with an increasing width in an inward direction toward the hydrophilic reaction site. A fixture is provided for holding a plurality of non-contact reagent dispensing devices above the microfluidic chip at locations corresponding to the loading sites of the plurality of hydrophilic channels or pathways, the fixture further holding a moveable collection tube disposed above the hydrophilic reaction site of the microfluidic chip for removing droplets containing reaction products.

The invention belongs to the technical field of metal micro-forming, and in particular relates to a method for inflating micro-channels. The present invention is aimed at the problems of low process flexibility, single product type, and non-closed structure of the micro-channel when preparing metal micro-channels by micro-plastic forming of ultra-thin metal strips. The present invention uses a method combining numerical simulation and bond rolling experiment to analyze the effect of the hydrogen pressure and bond strength of the metal composite ultra-thin strip after bond rolling on the pore diameter of the micro-channel, and the corresponding relationship between the micro-channel pore diameter and the titanium hydride content, heating temperature, and bond strength of the metal composite ultra-thin strip is obtained. The present invention has no special requirements on molds, wide selection of metal materials, low requirements for equipment capabilities; closed tubular micro-channel products with different pore diameters and different distributions can be prepared according to requirements, with rich product categories and high process flexibility.

A microfluidic synthesis platform includes a microfluidic chip holder that has a computer controlled heating element and cooling element therein. A microfluidic chip is mountable in the microfluidic chip holder. The microfluidic chip is formed by a hydrophobic substrate having patterned thereon a hydrophilic reaction site and a plurality of hydrophilic channels or pathways extending outward from the hydrophilic reaction site and terminating at respective loading sites on the substrate, wherein the hydrophilic channels or pathways are tapered with an increasing width in an inward direction toward the hydrophilic reaction site. A fixture is provided for holding a plurality of non-contact reagent dispensing devices above the microfluidic chip at locations corresponding to the loading sites of the plurality of hydrophilic channels or pathways, the fixture further holding a moveable collection tube disposed above the hydrophilic reaction site of the microfluidic chip for removing droplets containing reaction products.

A micro-channel reaction apparatus includes a first mixing device and a first jetting device. The first mixing device includes a first inflow channel and a second inflow channel respectively used to direct a first fluid and a second fluid into the micro-channel reaction apparatus. The first jetting device includes a first tapering portion and a first flared portion, wherein one end of the first tapering portion is connected to the first inflow channel and the second inflow channel; another end of the first tapering portion is connected to the first flared portion; and the first tapering portion has a contract ratio of inner diameter ranging from 0.1 to 0.75.

Provided in some aspects are methods for light-controlled in situ surface patterning of a substrate comprising a step of blocking or ablating oligonucleotide molecules in a boundary region separating a plurality of spot regions, and attaching oligonucleotides to oligonucleotide molecules in a first one or more of the spot regions.

A method for producing a chemical reactor, wherein the chemical reactor comprises one or more effective channels which comprise pillar structures, an input connected to one of the effective channels to allow fluid/gas into the effective channels and an output connected to one of the effective channels to remove at least one component of the liquid/gas. The method comprises obtaining an initial design of the reactor, further introducing into the initial design at least a structured area positioned adjacent to an effective channel of the one or more effective channels located at the edge of the initial design, the structured area not being fluidly connected to one of the effective channels, to obtain a further design and the production of the reactor according to the further design

A method of synthesising an organic high explosive includes the steps of i) providing a first solution A, ii) providing a second solution B, wherein the admixture of solution A and solution B are selected such that they are capable upon formation of the admixture of reacting together to provide an organic high explosive, and iii) causing the solution A and B to be mixed and passed through a flow reactor to create an admixture, wherein the flow reactor includes a pipe, wherein the internal diameter of the pipe is selected such that it is less than the critical diameter of the organic high explosive, thereby preventing detonation of the formed organic high explosive in said flow reactor.