Embodiments of the present technology may include a method of forming an emulsion. The method may include flowing an oil stream and an aqueous stream into a coiled tube to form a mixture of an oil phase and an aqueous phase in the coiled tube. The method may also include flowing the mixture in the coiled tube against gravity and under laminar conditions. A plurality of beads may be disposed within the coiled tube. The method may further include mixing the oil phase and the aqueous phase in the coiled tube until the emulsion is formed.

The present invention relates to a method and device for emulsifying emulsion explosive: an oil phase and a part of a water phase having undergone split-flow enter a first stage coarse emulsion mixer; after mixing, the mixture together with a part of the water phase having undergone second stage split-flow enters a second stage coarse emulsion mixer; the obtained mixture together with a part of the water phase having undergone third stage split-flow enters a third stage coarse emulsion mixer for mixing; forming a coarse emulsion matrix after multiple stages of mixing, and finally completing emulsification after mixing in a multi-stage fine emulsion mixer. The method and device mix the water phase with the oil phase multiple times according to a desired ratio, thus greatly reducing the stored explosive, with no mechanical stirring or shearing, with no heat accumulation, and with low pressure, without requiring matrix pumping, thus enhancing safety.

A method of producing organic pigment microparticles includes: Step 1 of precipitating organic pigment microparticles by mixing an organic pigment raw material liquid in which an organic pigment raw material is mixed with a solvent, and a precipitation solvent for precipitating the organic pigment microparticles from the organic pigment raw material liquid in a thin film fluid formed by introducing the organic pigment raw material liquid and the precipitation solvent in a space between at least two processing surfaces which are disposed so as to face each other, being capable of approaching to and separating from each other, at least one of which rotates relatively to the other; and Step 2 of coating at least a part of the organic pigment microparticles with an oxide coating; wherein the oxide coating is optically colorless and transparent, and Step 1 and Step 2 are performed out continuously in the thin film fluid.

Object: To provide a method for manufacturing a polymer, which is a method for forming a polymer having a homogeneous copolymer composition and a narrow molecular weight distribution.

Resolution Means: A method for manufacturing a polymer using a microreactor including a flow path capable of mixing a plurality of liquids to perform radical polymerization of a monomer component containing two or more types of monomers in the presence of a polymerization initiator; wherein the microreactor includes a first inlet port configured to feed the monomer component and an additional inlet port located downstream of the first inlet port; and the method includes feeding the monomer component through the first inlet port and the additional inlet port.

Organopolysiloxane emulsions which are stable and of large particle size are produced in controllable fashion using a cylindrical mixer having multiple inlets and axially displaced rotor stator units.

Embodiments of the present technology may include a system for forming an emulsion. The system may include a coiled tube. The coiled tube may have a first end and a second end. The second end may be located at a position higher than the position of the first end. The system may also include a plurality of beads disposed within the coiled tube. The system may further include a first inlet fluidly connected to the coiled tube. The first inlet may be configured to deliver a first fluid to the first end before the second end. In addition, the system may include a second inlet fluidly connected to the coiled tube. The second inlet may be configured to deliver a second fluid to the first end before the second end.

The invention relates to an apparatus for aerating a pasty product. The apparatus comprises a housing (1) with an inlet (4) for the pasty product to be aerated and an outlet (5) for the aerated product. The apparatus comprises at least a first set of a rotor and a stator (21) and a second set of a rotor and a stator (22). The apparatus further comprises a gas injector (6) for injecting, upstream of the first set of a rotor and a stator (21), a gas into the pasty product to be aerated. The apparatus further comprises an intermediate mixing chamber (7) provided in the housing between the first and the second sets of a rotor and a stator (21, 22). A secondary product introduction means protrudes into the intermediate mixing chamber (7) so as to issue into said intermediate mixing chamber (7). A method for aerating a pasty product is also provided.

The present invention is concerned with improved swirl burners, particularly, but not limited to, swirl burners used in fuel cell systems.

A system forms a cosmetic composition. The system includes a dispensing arrangement in selective fluid communication with a plurality of dispensing dosing receptacles mounted on a movable carousel. The dispensing arrangement is configured to selectively dispense a plurality of the booster compositions together with a base composition corresponding to a formulation corresponding to a compatibility profile and consumer skin conditions to form a stable composition having efficacious concentrations of active ingredients into a receiving receptacle.

A chemical treatment apparatus for diluting and activating a polymeric material can include a mixing chamber having a first end, a second end, a first baffle plate positioned between the first end and second end, a high shear mixing zone positioned between the first end of the mixing chamber and the first baffle plate, and a low shear mixing zone positioned downstream from the high shear agitation zone between the second end of the mixing chamber and the first baffle plate. The volume ratio of the high shear mixing zone to the low shear mixing zone can be in the range of 1:2 to 1:10. A method and system for diluting and activating polymeric materials are also disclosed.