According to this disclosure, there is provided a pyrolysis reaction system and a direct non-oxidative methane coupling process using the same by which it is possible to reach the selectivity for good C.sub.≤10 hydrocarbons and at the same time to inhibit coke from being generated while a good methane conversion is maintained during direct conversion of methane into C.sub.2+ hydrocarbons through non-oxidative pyrolysis.

A reactor for performing a reaction between two immiscible fluids of different density, 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, a zone of limited backmixing preferably arranged below the backmixed zone and a plug-flow zone which are at least consecutively traversable by one of the fluids, wherein the backmixed zone comprises at least one inlet and the plug-flow zone comprises an outlet and the backmixed zone comprises at least one mixing apparatus selected from a stirrer, a jet nozzle and means for injecting the fluid of lower density, a first cylindrical internal element which in the interior extends in the longitudinal direction of the reactor, which delimits the zone of limited backmixing from the plug-flow zone and which comprises a first passage to the backmixed zone and a second passage to the plug-flow zone, a second internal element which delimits the backmixed zone from the plug-flow zone such that there is no direct fluid connection between the backmixed zone and the plug-flow zone, and backmixing-preventing third internal elements in the form of random packings, structured packings or liquid-permeable trays arranged in the zone of limited backmixing. The reactor allows an optimal residence time distribution in the reaction of the two immiscible fluids of different density. The invention further relates to a process for performing a continuous reaction in the reactor.

A process for isolating lignin from an alkaline process stream of thickened black liquor which is introduced continuously into a lower region of at least one circulation reactor having two reactor zones in concentric arrangement, liquid level of the alkaline process stream in the interior of the reactor is at a level with an upper end of an inner tubular reactor zone, a CO.sub.2-containing gas is blown continuously from the bottom into the inner tubular reactor zone of the reactor, wherein the CO.sub.2-containing gas is absorbed by the alkaline process stream in the inner circulation reactor zone and offgas is drawn off with residual amounts of the CO.sub.2 at the top of the reactor, the process is run at 1 atm, and thickened black liquor with a reduced lignin content together with precipitated lignin present are drawn off optionally after settling at the base of the reactor.

Disclosed is a reactor for solution polymerization process using a metallocene catalyst for preparing polyolefin. The reactor includes: a reaction vessel for mixing a hydrocarbon-based solvent and an olefin monomer to produce polyolefin; a feed inlet installed at a lower portion of the reaction vessel to feed a feed including an unreacted monomer, a solvent, and a catalyst into the reaction vessel; a guide pipe having a cylinder shape being open at respective ends, installed along a central axis of the reaction vessel, and dividing an internal space of the reaction vessel into an up-flow region where a reaction mixture flows upward and a down-flow region where the reaction mixture flows downward; a swirling flow-inducing blade attached to the exterior surface of the guide pipe, causing the reaction mixture in the reaction vessel to rise along the exterior surface of the guide pipe while forming a swirling flow.

The present disclosure provides device comprising a cylindrical reaction vessel having one or more permeable cylindrical membranes disposed therein separating the cylindrical reaction vessel into at least a first portion and a second portion, wherein the one or more permeable cylindrical membranes are configured to permit first reactants from a first solution in the first portion or reactants from a second solution in the second portion to percolate or seep to a reaction zone proximate a surface of the one or more cylindrical membranes. A lifting device (mechanism) located above the first portion of the cylindrical reaction vessel configured to continuously draw a preform two-dimensional polymer tube formed by continuous reaction of the first and second reactants out from the reaction zone.

A support structure for a structured catalytic packing is disclosed. The support structure is in a fixed position relative to the reactor tube containing it. It supports catalyzed casings that are free to move relative to the support structure. The support structure and casings are inserted in the reactor tube such that the support structure is located proximate the longitudinal axis of the tube and the casings are located between the support structure and the reactor tube wall. The support structure comprises a central support tube or rod proximate to, and impervious or perforated discs perpendicular to, the longitudinal axis of the reactor tube, and may comprise spacers separating the discs.

A water gas shift (WGS) reactor system includes a housing; a reaction tube disposed in the housing, wherein a reaction channel is defined within the reaction tube and a cooling fluid channel is defined between the housing and the reaction tube; a catalyst disposed in the reaction channel, the catalyst configured to catalyze a hydrogen generation reaction; and a heat transfer material disposed in the reaction channel.

Apparatus for converting feed gas (28) into a product gas (29), comprising at least one reactor (1) with a reaction chamber (15) bounded by the inner wall of an outer tube (4) closed at a first outer end and an inner tube (14) received coaxially in this outer tube (4) and provided at both its outer ends with openings, which reactor (1) is provided with an inlet chamber (11) and with an outlet chamber (10), wherein a first wall (31) of the outlet chamber (10) encloses the outer tube (4) and extends therefrom, and a second wall (12) of the outlet chamber (10) lying opposite the first wall (31) encloses the outer tube (4) and extends therefrom, and the inlet chamber (11) is bounded by the second wall (12) of the outlet chamber (10) and a third wall (47) which lies opposite this second wall (12), encloses the outer tube (4) and extends therefrom.

A method for preparing a dispersion of nanoparticles of a solid organic dye or pigment in a liquid carrier, the method comprising continuously mixing: at least one solution or slurry containing a reactant precursor for the solid organic dye or pigment in an organic or other solvent with the liquid carrier in a counter current mixing reactor whereby to obtain reaction of the reactant precursor and formation of the solid organic dye or pigment as a dispersion of nanoparticles in the liquid carrier and solvent mixture; optionally, removing unreacted reactant precursor and/or by-product from the dispersion when present; and optionally, concentrating the dispersion.

Disclosed is an LED light source photocatalytic tubular reactor and application thereof. The LED light source photocatalytic tubular reactor comprises an LED light source, a temperature control chamber and a transparent reaction pipeline; the transparent reaction pipeline is located in the temperature control chamber; at least one side of the temperature control chamber is a light-transmitting plate; the LED light source provides a light source for the transparent reaction pipeline through the light-transmitting plate; and the transparent reaction pipeline has a diameter-to-length ratio of the inner diameter to the length of 0-0.1, but not 0. The LED light source continuous photocatalytic tubular reactor of the present disclosure can eliminate the scaling up effect, increase the yield and allow continuous production with an advantage of easy to use and low cost. The tubular reaction device of the present disclosure can also realize automatic control, which can effectively reduce personnel costs and improve production safety.