Abstract:
A full continuous flow synthesis process of fluorine-containing aromatic hydrocarbon compounds. Aromatic amine and hydrogen fluoride are respectively pumped into thermostats A and B, then flow into micro-channel reactor C for salt forming reaction whose temperature is kept constant; sulfuric acid solution of nitrosylsulfuric acid is pumped into thermostat D; after keeping the temperature constant, the sulfuric acid solution of nitrosylsulfuric acid and salt forming product flowing out from the micro-channel reactor C flow into micro-channel reactor E for diazotization reaction; the obtained product flows into micro-channel reactor F for thermal decomposition reaction, is cooled in cooler G, then enters three-phase separator H for continuous separation, fluorine-containing aromatic hydrocarbon crude product is subjected to continuous alkaline washing, drying and rectification to obtain fluorine-containing aromatic hydrocarbon finished product, and mixture of hydrofluoric acid and sulfuric acid is continuously distilled to obtain hydrogen fluoride and sulfuric acid.
Abstract:
The present disclosure is directed to systems and methods for reforming a hydrocarbon fuel to increase the cetane value of the hydrocarbon fuel. The system includes a microstatic mixer and a microchannel reactor downstream of the microstatic mixer. The microchannel reactor includes a microchannel with an NHPI catalyst coated onto the walls of the microchannel. A hydrocarbon fuel and an oxygen-containing gas are combined and mixed in the microstatic mixer to produce a combined stream and the combined stream is passed through the microchannel. The microchannel reactor includes a heat transfer system. The hydrocarbon fuel and oxygen-containing gas are contacted in the microchannel in the presence of the catalyst at a reaction temperature sufficient to produce a reformed hydrocarbon fuel having a cetane value greater than a cetane value of the starting hydrocarbon fuel.
Abstract:
The present disclosure is directed to systems and methods for reforming a hydrocarbon fuel to increase the cetane value of the hydrocarbon fuel. The system includes a microstatic mixer and a microchannel reactor downstream of the microstatic mixer. The microchannel reactor includes a microchannel with an NHPI catalyst coated onto the walls of the microchannel. A hydrocarbon fuel and an oxygen-containing gas are combined and mixed in the microstatic mixer to produce a combined stream and the combined stream is passed through the microchannel. The microchannel reactor includes a heat transfer system. The hydrocarbon fuel and oxygen-containing gas are contacted in the microchannel in the presence of the catalyst at a reaction temperature sufficient to produce a reformed hydrocarbon fuel having a cetane value greater than a cetane value of the starting hydrocarbon fuel.
Abstract:
The invention generally provides systems and methods for producing a chemical product. In certain embodiments, the invention provides systems that include a chemical product production unit. The chemical production unit includes a plurality of microfluidic modules configured to be fluidically coupled to each other in an arrangement that produces a chemical product from an input of a plurality of starting reagents that react with each other due to conditions within the plurality of microfluidic modules through which the starting reagents flow. The system also includes a droplet dispenser fluidically coupled to the chemical product production unit that forms and dispenses droplets of the chemical product.
Abstract:
A method of manufacturing core-shell particles comprises: filling a buffer into a rotor, which is extended in a longitudinal direction, and is accommodated so as to be spaced apart from an inner wall side of a non-rotational hollow cylinder extended in a longitudinal direction and then discharging air to outside; rotating the rotor after terminating the filling; forming a core-shell precursor by supplying raw materials from a first storage and a second storage, which comprise a material forming a core, into an interior of the cylinder in which the rotor rotates; supplying a shell material for coating the core to the interior of the cylinder in which a core-type precursor is formed; separating a liquid comprising core-shell particles formed through the supplying into a solid and a liquid; and drying the core-shell particles obtained through the separating.
Abstract:
Aspects of the present disclosure relate to reconfigurable chemical synthesis systems and related components and methods. In some embodiments, the described systems comprise one or more fluidic connector units, wherein each fluidic connector unit comprises a plurality of flexible conduits. In certain cases, a system comprising one or more fluidic connector units is configured to synthesize a first chemical compound by providing a plurality of fluidic connections between a plurality of fluid outlets (e.g., outlets of chemical reagent sources, outlets of pumps) and a plurality of fluid inlets (e.g., inlets of reaction modules, inlets of pumps) through the plurality of flexible conduits. In certain cases, the system is subsequently reconfigured by resetting the system (e.g., disconnecting each fluidic connection) and/or configuring the system to synthesize a second, different chemical compound (e.g., disconnecting one or more fluidic connections and providing one or more additional fluidic connections). According to some embodiments, in order to avoid tangling the flexible conduits during reconfiguration of the system, the fluidic connections are disconnected according to certain inventive methods described herein. In certain embodiments, fluidic connections are disconnected in reverse order relative to the order in which they were formed (e.g., the newest fluidic connection is disconnected first, the oldest fluidic connection is disconnected last). In certain embodiments, certain fluidic connections are targeted for disconnection, and additional fluidic connections are disconnected if they overlap the targeted fluidic connections and were formed more recently than the targeted fluidic connections. The fluidic connection and/or disconnection steps may, in some embodiments, be performed by a robotic manipulator.
Abstract:
Apparatus for manufacturing particles has at least one reactor and a method for manufacturing particles using the same. A first reactor has a hollow main body extending in the lengthwise direction, first and second raw material inlets formed at the one side end of the main body, a reactant outlet formed at the other side end of the main body, and a mixer formed inside the main body to mix materials fed from the first and second raw material inlets. A second reactor of the apparatus connected to one side of the first reactor has a non-revolving hollow cylinder extending in the lengthwise direction, a revolving body extending in the lengthwise direction, a driver portion, a reactant inlet formed on the outer circumference at one side end of the cylinder and connected to the reactant outlet of the first reactor.
Abstract:
Microfluidic methods and systems are provided for continuous flow synthesis and active loading of liposomes, which include a liposome formation region configured to form a population of liposomes and a microdialysis region downstream from the liposome formation region and configured to form a transmembrane gradient for active drug loading of the liposomes. Microfluidic methods and systems for high throughput production of liposomes are also provided featuring high aspect ratio microchannels.
Abstract:
In various implementations, methanol is produced using a (CO+H2) containing synthesis gas produced from a combined PDX plus EHTR or a combined ATR plus EHTR at a pressure of 70 bar to 100 bar at the correct stoichiometric composition for methanol synthesis so that no feed gas compressor is required for the feed to the methanol synthesis reactor loop.
Abstract translation:在各种实施方案中,使用由组合的PDX加EHTR或组合的ATR plus EHTR产生的(CO + H 2)的合成气在70巴至100巴的压力下以合适的化学计量组成用于甲醇合成来生产甲醇,使得不 进料气压缩机是进料到甲醇合成反应器回路所必需的。
Abstract:
A method for preparing a high-quality epoxidized fatty acid ester with a micro-reaction device, including: respectively pumping an aqueous hydrogen peroxide solution and a carboxylic acid at the same time into a first micro-mixer; after the reaction in the first micro-reactor, respectively pumping the output material and an unsaturated fatty acid ester into a second micro-mixer;completely mixing them and then introducing the mixture into a second micro-reactor; and after a complete reaction, water-rinsing the organic phase part of the resultant reaction liquid and drying the same to obtain the epoxidized fatty acid ester.