The invention includes a system for producing a nitrogen fixation product, where the system includes a nitrogen gas source providing nitrogen gas; a delivery system for the nitrogen gas in fluid communication with the nitrogen gas source, wherein the delivery system delivers the nitrogen gas into a plasma reactor, and wherein the plasma reactor energizes the nitrogen gas as a plasma to produce activated nitrogen species; a secondary reactant source providing a secondary reactant in a secondary reactant stream that is separated from the nitrogen gas, wherein the secondary reactant stream is directed to contact the activated nitrogen species in a reaction zone, and wherein contact between the activated nitrogen species and the secondary reactant produces a reaction that yields the nitrogen fixation product. The invention also includes methods of the use of such a system for producing a nitrogen fixation product.

The invention includes systems for producing a selective oxidation product that include an oxidant gas source providing an oxidizing agent; a delivery system for the oxidizing agent in fluid communication with the oxidant gas source, wherein the delivery system delivers the oxidizing agent into a plasma reactor, and wherein the plasma reactor energizes the oxidizing agent as a plasma to produce activated oxidant species; a secondary reactant source providing a secondary reactant in a secondary reactant stream that is separated from the oxidant gas, wherein the secondary reactant stream is directed to contact the activated oxidant species in a reaction zone, and wherein the contact between the activated oxidant species and the secondary reactant in the reaction zone produces a reaction that yields the selective oxidation product.

In order to provide a dispersion method and a dispersion apparatus capable of mixing a material to be processed and a dispersion medium having no affinity with each other using a single apparatus without using a dispersant, there are provided a quantitative supply mechanism quantitatively supplying a material to be processed, a suction stirring mechanism primarily including a suction stirring pump in which the material to be processed and a dispersion medium are subjected to negative pressure suction by a negative pressure suction force generated by rotation of a rotating blade and the suctioned material to be processed and the dispersion medium are stirred and mixed by the rotating blade and are allowed to pass through a throttle passage to cause cavitation, and a plasma generating mechanism generating a plasma in bubbles formed due to cavitation in a mixed liquid of the material to be processed and the dispersion medium.

The present disclosure relates generally to electrocatalytic process for conversion of a hydrocarbon reactant, comprising: introducing the hydrocarbon reactant into an acidic solution in a presence of a catalyst, wherein the catalyst includes a d° transition metal-oxo moiety; and applying an electrical input to the catalyst to convert the hydrocarbon reactant into a product. The present disclosure also relates to a catalyst for conversion of a hydrocarbon reactant, comprising a d° transition metal-oxo moiety and a sulfonic moiety bonded to the d° transition metal.

The present invention relates to a microfluidic or millifluidic device (1) comprising: —a support (2) made at least partially of a dielectric material, the support (2) comprising a first inlet (21a) adapted to be connected to a first reservoir containing gas, a second inlet (21b) adapted to be connected to a second reservoir containing liquid, an outlet (22) adapted to be connected to a receiver container containing gas and/or liquid, and a main microchannel or millichannel (3) present in the dielectric material allowing the liquid and the gas to flow from the inlets towards the outlet, —one or several ground electrode(s) (4) embedded in said dielectric material and extending along the main microchannel or millichannel (3), and —one or several high-voltage electrode(s) (5) embedded in said dielectric material and extending along the main microchannel or millichannel (3), wherein the high-voltage electrode(s) (5) and the ground electrode(s) (4) are located on opposite sides of the main microchannel or millichannel (3) so as to be able to generate an electric field inside the main microchannel or millichannel (3). The present invention relates also to a method for generating a plasma in a continuous manner using such a microfluidic or millifluidic device (1).

The present invention discloses high pressure flow reactor vessels and associated systems. Also disclosed are processes for producing thiol compounds and sulfide compounds utilizing these flow reactor vessels.

A system and method for performing plasma reactions creating a plasma area in a gas adjacent to a liquid. An embodiment of the plasma reactor includes a housing with an internal reaction chamber, first and second inlet paths to the reaction chamber, and electrodes for producing an electric field. The system may optionally further include a pre-ionization electrode and pre-ionization electric field for pre-ionizing a feed gas prior to entry into a reaction chamber. The reactor uses plasma to ionize gas adjacent with the liquid. The ionized gas reacts with the liquid to form an effluent. Exemplary uses of the plasma reactor include ionic injection, gas dissociation, liquid re-formation, and liquid dissociation. An alternative embodiment provides a system and method for infusion of gaseous particles into liquid by applying an electric field at power levels lower than the voltage required to form a plasma to gas adjacent to liquid.

A method for bonding a fluid to a substance includes filling a first pressure vessel with the fluid and pressurizing the first pressure vessel to a first pressure. The fluid is the circulated through an electric arc formed within the first pressure vessel, thereby creating a treated fluid. Within a second pressure vessel, the substance is exposed to a magnetic field, thereby forming a polarized substance. The treated fluid and polarized substance are combined under a second pressure within a third pressure vessel, thereby exposing the treated fluid to the polarized substance at a pressure sufficient to achieve a bond.

The present invention provides a low pressure generating plasma reactor closed loop process, comprising: feeding a fresh feed gas flow and a fresh feed absorption liquid flow to a plasma reactor closed loop comprising a condenser, a liquid loop, a recycle gas loop, and a plasma generator; converting feed gas to reactive plasma products in the plasma generator; quenching and absorbing the reactive plasma products into an absorption liquid circulating in the liquid loop where the reactive plasma products react to form liquid reaction products, thereby generating low pressure in the closed loop; monitoring the composition and low pressure of the recycle gas loop and, if the pressure increases, adjusting the composition of the fresh feed gas flow and/or fresh feed absorption liquid flow to bring the composition of the feed gas towards stoichiometric ratio with the absorbed reactive plasma products; extracting circulating absorption liquid, containing the liquid reaction products, from the plasma reactor closed loop as a product flow. The present invention also provides a low pressure generating plasma reactor closed loop system, comprising a plasma generator, a condenser, a recycle gas loop, a liquid loop, and a pump.

A reactor for performing a gas/liquid biphasic high-pressure reaction with a foaming medium, comprising an interior formed by a cylindrical, vertically oriented elongate shell, a bottom and a cap, wherein the interior is divided by internals into a backmixed zone and a zone of limited backmixing, wherein the backmixed zone and the zone of limited backmixing are consecutively traversable by the reaction mixture, wherein the backmixed zone comprises means for introducing gas and liquid and a gas outlet and also comprises at least one mixing apparatus selected from a stirrer, a jet nozzle and means for injecting the gas, and the zone of limited backmixing comprises a reaction product outlet, a first cylindrical internal element which in the interior extends in the longitudinal direction of the reactor and which delimits the zone of limited backmixing from the backmixed zone, backmixing-preventing second internal elements in the form of random packings, structured packings or liquid-permeable trays arranged in the zone of limited backmixing and a riser tube whose lower end is arranged within the backmixed zone and whose upper end opens into the zone of limited backmixing so that liquid from the backmixed zone can ascend into the zone of limited backmixing via the riser tube, wherein flow into the zone of limited backmixing enters from below. The reactor is configured such that the high-pressure reaction space is optimally utilized and contamination of workup steps or subsequent reactions arranged downstream of the high-pressure reaction with foam is substantially avoided. The invention further relates to a process for performing a continuous gas/liquid biphasic high-pressure reaction in the reactor.