Abstract: An exhaust aftertreatment system is provided. In one embodiment, the system includes a catalyst, and injector positioned upstream from the catalyst, and a fluid-spray atomizer positioned between the catalyst and the injector. The fluid-spray atomizer includes a plurality of horizontal slats, wherein each horizontal slat is a different size and a smaller horizontal slat is nested at least partially inside a larger horizontal slat.

Abstract: A layer multiplier (100) is disclosed. It comprises an inlet (102) for a flow of multilayered flowable material, a distribution manifold (104) into which the inlet debouches, a number>2 of separate splitting channels (106) extending from the distribution manifold, a recombination manifold (108) into which the splitting channels debouch, an outlet in one end of the recombination manifold, and the distribution manifold is arranged in an opposing relationship with the recombination manifold.

Abstract: The present invention is directed to an apparatus for mixing gaseous mixture components. The present invention likewise relates to a correspondingly applied method and to the use of an apparatus according to the invention for mixing components of the exhaust gas of internal combustion engines with a reducing agent and to a correspondingly designed reactor.

Abstract: A mixing apparatus is disclosed. The mixing apparatus comprises a mixing device having a constant flow area. The mixing device is configured to create a shearing environment. Several types of mixing apparatus are disclosed. Methods for producing aqueous fuel emulsions with consistently uniform dispersed phase particle sizes using a mixing apparatus are also disclosed.

Abstract: The present invention provides ballast water treatment equipment which can decompose fungicide included in ballast water and reduce the amount of use of fungicide adsorbing material by passing through the ballast water.

Abstract: The invention is a column contact apparatus for contacting gas with liquid in an upflow in a column container, containing two or more stages of honeycomb structural bodies in the column container in a vertical direction, a space portion formed between the respective stages of the honeycomb structural bodies and a flow-aligning portion as back-flow prevention means provided in the space portion between the respective stages such that the flow-aligning portion is not brought into contact with the honeycomb structural bodies, the flow-aligning portion including a plurality of holes with hole diameters of 0.5 mm to 8 mm.

Abstract: An exhaust treatment system includes an exhaust conduit for conveying exhaust gases from an engine of a vehicle. An aftertreatment device is disposed in the exhaust conduit. A flow device is disposed upstream of the aftertreatment device. The flow device includes a base having a first surface and an oppositely disposed second surface. The base defines a plurality of openings. A plurality of flow deflectors is engaged to the base at the plurality of openings. Each flow deflector includes a first deflector that extends outwardly from the first surface of the base and a second deflector that extends outwardly from the second surface of the base. The first and second deflectors define a passage. Flow of exhaust gases through the passage cause exhaust gases to swirl about a longitudinal axis of the exhaust conduit.

Abstract: A mixing apparatus includes a housing having an inner chamber, an inlet, and an outlet; an outlet conduit having a first and second end, the second end providing communication between the inner chamber and the outlet; and one or more dispersion members configured to mix one or more fluids, the one or more dispersion members extending between the outlet conduit and the housing. The dispersion members include a plate having a first and second side, a first opening in the plate for receiving an outlet conduit of the mixing device, and a plurality of second openings in the plate. The plurality of second openings has a first and second side. The first and second sides of the plurality of second openings have chamfered edges.

Abstract: The present invention relates to an emulsification method and an emulsification apparatus, capable of attaining easy control of particle size and particle size distribution, and simple scale-up and maintenance, and providing an emulsifying amount sufficient for industrial production. Namely, the method comprises continuously and successively passing two or more types of liquids which are substantially immiscible with each other through two or more mesh members disposed at certain intervals in the presence of an emulsifier to thereby perform emulsification, and the emulsification apparatus as an apparatus for carrying out the method comprises liquid feed pumps for feeding two or more types of liquids which are substantially immiscible with each other, and a cylindrical flow passage to which the two or more types of liquids are fed by the liquid feed pumps, the cylindrical flow passage including a predetermined number of wire gauzes disposed therein at a predetermined interval.

Abstract: A microchannel structure including a dispersed-phase introduction channel which communicates with a dispersed-phase introduction inlet; a continuous-phase introduction channel which communicates with a continuous-phase introduction inlet; a discharge channel which communicates with a discharge outlet; a fine-particle formation channel; and a plurality of branch channels for dispersed-phase introduction which are microchannels; wherein one end of the fine-particle formation channel in a fluid traveling direction communicates with the continuous-phase introduction channel whereas the other end thereof communicates with the discharge channel; and wherein a side part of the dispersed-phase introduction channel and side part of the fine-particle formation channel communicate via the plurality of branch channel for dispersed-phase introduction.

Abstract: A method and apparatus for mixing at least one fluid stream with a large gas stream flowing in a gas duct, especially for introducing reducing agent into flue gas containing nitrogen oxides. The gas stream is directed against at least one disk-shaped mixer element on an inlet side that is inclined at an angle counter to the direction of flow of the gas stream, wherein eddy-type whirls form at the mixer element. A swirled fluid stream is admixed with the large gas stream downstream of the mixer element.

Abstract: A static mixer includes first and second tubular housings which define elongated internal cavities. Dividers divide each internal cavity into a plurality of separate and sequential flow paths for the fluid mixture. Each separate flow path extends between the opposite ends of each housing, reverses direction substantially adjacent to an end of each housing, and conducts the fluid mixture in a direction opposite of the fluid mixture conducted by one of a preceding or succeeding flow path.

Abstract: A static continuous flow mixer, with or without reaction, is provided with basic cells, which are individually provided with an individualized chamber (1). The basic cells are also provided with at least two connecting channels (2), at least two of them being oblique relatively to the resulting direction (x) of the flow in the mixer, and with at least two additional apertures (0) for connection with the exterior. The cells interconnect successively in the space, forming a network. The mixer promotes convective processes. The dimensions (Dj, li, di, ?), the geometry of the chambers (spherical or cylindrical) and of the channels (cylindrical or prismatic) may vary, as well as their quantity.

Abstract: A micromixing apparatus includes a mixing microchannel formed in a top surface of a substrate having a channel length and a variable channel width defined by a first sidewall surface and an opposing second sidewall surface. The channel width varies from a minimum channel width h to a maximum channel width H in a ratio of H:h?1.1:1.0. A first inlet is for injecting a first fluid into the mixing microchannel and a second inlet for injecting a second fluid into the mixing microchannel. The first and second fluid flow in a flow direction in the mixing microchannel along the channel length. The first sidewall surface includes first curved surface portions and the second sidewall surface includes a second curved surface portions. The plurality of first curved surface portions and plurality of second curved surface portions are non-overlapping to provide the variable channel width.

Abstract: A pouring insert is provided for insertion into a container outlet, for example a bottleneck, for aerating liquids pored from the container. This is achieved by a combination of a hollow, tapering jacket with a hollow pipe axially disposed within it. The jacket features a plurality of elongated slots penetrating the jacket and allowing for liquid/air flow therethrough. The invention furthermore relates to a bottle pourer having a spout and the pouring insert described herein. The invention also relates to the use of the pouring insert and of the bottle pourer for aerating wine. Finally, the present invention relates to a method of manufacturing the pouring insert by injection molding.

Abstract: A micromixer is fabricated using a selective high intensity focused ultrasound foaming technique. The micromixer employs a 3D porous region for effective mixing. The 3D porous micromixer can achieve sufficient mixing results with a short mixing length for flows with a Reynolds number as low as 0.1. The fabrication process of the micromixer is rapid, low-cost, and biocompatible. The pore size of the micromixer can be controlled by adjusting the selective high intensity focused ultrasound foaming parameters. The micromixer has potential for use in lab-on-a-chip and micro-total-analysis devices.

Abstract: A mixing or dispersing element (1, 10, 30, 40, 50, 60, 70) includes a passage (2) in which an insertion element (3, 4. 33, 34) is arranged which contains a foam structure. A static mixing element (5, 6, 35, 36) for macro mixing or predispersing or macro dispersing is arranged in the passage (2) in addition to the insertion element (3, 4, 33, 34) for micro mixing or dispersing. Furthermore, a method is described of producing a dispersion using such a mixing or dispersing element.

Abstract: Flow deflector that is capable of changing the flow direction of a fluid during passage through a duct. The duct is formed by an inner and outer duct, which creates an annular region in the duct. The flow deflector forces the fluid passing through the annular region of the duct to flow inside the inner duct, while the fluid passing through the inner duct is forced to flow through the annular region. Reactor tubes for catalytic reactors are formed by assembling tubes comprising said flow deflector and having a catalyst arranged in the inner tube.

Abstract: An energy-saving static stirring apparatus for automatically stirring a fluid includes a deflector adapted for stationary placement in a container that holds a fluid for boiling. The deflector may include at least one friction contact point for frictionally engaging the container to prevent movement of the deflector. An inner portion of the deflector may be configured for placement proximate to a center of the container. An outer portion of the deflector may be configured for placement proximate to a side of the container. One or more deflector ramps define one or more vent openings to impart lateral movement to heated fluid currents and/or vapor bubbles moving upwardly away from a heat source below the container and to redirect the fluid currents and/or vapor bubbles into a swirling motion that stirs the fluid without movement of the deflector.

Abstract: The invention comprises embodiments of devices and methods involving mixers and/or swirlers that better combine or optimize important factors such as mixing and turbulent mixing intensity and/or natural liquid, vapor and gas-specific mixing and turbulent mixing and/or cost-efficient application possibilities and/or precise controllability of numerous substances and amounts. Throughflow plates provided with special hole arrangements and matching mixing and/or turbulent mixing aids, such as funnels, enable better control, regulation and optimization of flow speeds, mixing and/or turbulent mixing intensities and combinations and complex mixing and/or turbulent mixing processes. The invention is suitable for efficient mixing and/or turbulent mixing of liquids and/or mixtures of liquids and solids and/or vapors and/or gases. Many applications are conceivable, e.g. in water treatment, the food and beverages industry, medicine, pharmaceuticals, biology, physics and chemistry.

Abstract: A carrier fluid and an added input fluid are mixed together in a static mixer to create an emulsified output fluid mixture. The static mixer comprises a plurality of mixing chambers whose cross-sectional size expand considerably relative to an inlet, a series of bent and curved baffle plates which divert, rotate, divide, reverse and otherwise create turbulence in the combined flow, and inlet chamber in which the added input fluid is dispensed upstream into the carrier fluid, and a number of other structural mixing elements which, through turbulence, abrupt pressure drops and velocity changes, subdivide the added input mixture into very small volumetric quantities evenly dispersed within the carrier fluid to create a homogeneous output fluid mixture.

Abstract: A method for collapsing a microbubble includes applying stimulation to the microbubble during the gradual decrease of the its size. As a result, the microbubble floating in a solution that decreases in size due to the natural dissolution of a gas contained in the microbubble and disappears after a while, has the speed of its size decrease enhanced and causes the microbubble to disappear.

Abstract: The present invention relates to a hole-jetting type reactor and its applications, in particular to a process for the production of isocyanates by the phosgenation of aliphatic or aromatic diamines or triamines in the gas phase using this reactor. The present invention achieves a good mixing and reacting result of the gas-phase phosgenation reaction at a high temperature by improving the mixing of reactants in the reactor to reduce the possibility of forming swirls and eliminate negative pressure produced at a local jet area, which can finally reduce back-mixing and formation of solid by-products.

Abstract: One aspect of the present invention relates to a mixing system for use in a chemical-process column. The mixing system includes a heavy-reactant mixing surface arranged perpendicular to a flow of reactant through the chemical-process column. The mixing system also includes an aperture formed in the heavy-reactant mixing surface. A pre-distributor is coupled to an underside of the mixing system and fluidly coupled to the aperture.

Abstract: An agitation system including a motor that is capable of measuring the torque output of the motor required to mix a suspension. The motor is attached to an agitator which is placed in a suspension to be measured. The agitator is placed in the suspension and the agitation system is turned on for a period of time. This period determined by the type of agitator used and the characteristics of the suspension. When the suspension is well mixed and the torque measurement on the agitator becomes stable, the agitation system is stopped. The suspension is allowed to sit without agitation for a period of time and the agitation system is started again. After a period of time the agitation system is started and the amount of torque needed to begin turning the agitator is measured.

Abstract: A mixing apparatus is disclosed. The mixing apparatus comprises a mixing device having a constant flow area. The mixing device is configured to create a shearing environment. Several types of mixing apparatus are disclosed. Methods for producing aqueous fuel emulsions with consistently uniform dispersed phase particle sizes using a mixing apparatus are also disclosed.

Abstract: A microfluidic device that comprises several microchannel structures in which there are an inlet port, an outlet port and there between a structural unit comprising a fluidic function. The structural unit can be selected amongst units enabling a) retaining of nl-aliquots comprising constituents which has been defined by mixing of aliquots within the microfluidic device (unit A), b) mixing of aliquots of liquids (unit B), c) partition of larger aliquots of liquids into smaller aliquots of liquids and distributing the latter individually and in parallel to different microchannel structure of the same microfluidic device (unit C), d) quick penetration into a microchannel structure of an aliquot of a liquid dispensed to an inlet port of a microchannel structure (unit D), and e) volume definition integrated within a microchannel structure (unit E).

Abstract: A microchannel structure is provided wherein supplied fluids are prevented from transuding via a lamination interface into channels for a mixture or reaction product. A method is further provided for producing an emulsion having a uniform particle size under a high pressure condition by using the microchannel structure. The microchannel structure comprises one or more layers having notches to constitute channels, laminated and pressed between a pair of frames having an outside communicating hole to constitute a channel, so as to form microchannels to mix/react fluids, channels to supply the fluids to the microchannels, and a channel to discharge the fluids from the microchannels, wherein a channel for discharging a transudation fluid is provided to recover a fluid having transuded at a lamination interface so as not to let it enter into the channels including the microchannels and discharge it to the outside.

Abstract: A fluid conditioner for a fluid traveling through a conduit, the conduit having a longitudinal axis and substantially circular cross-section. The fluid conditioner includes a static mixing element and a straightener plate. The plate is affixed to a substantially rectangular member located downstream of the static mixing element and oriented substantially perpendicularly to the longitudinal axis of the conduit, the plate substantially covering the cross-section of the conduit having a plurality of openings to facilitate the passage of the fluid within the conduit.

Abstract: A mixing apparatus is disclosed. The mixing apparatus comprises a mixing device having a constant flow area. The mixing device is configured to create a shearing environment. Several types of mixing apparatus are disclosed. Methods for producing aqueous fuel emulsions with consistently uniform dispersed phase particle sizes using a mixing apparatus are also disclosed.

Abstract: To improve reaction efficiency by increasing a contact area of first and second reactants per unit volume, without reducing dimensions of the inlet paths for the first and second reactants in a layer-thickness direction, a channel includes a first inlet path having the first reactant, a parallel second inlet path separated from the first inlet path and having the second reactant, a junction channel for causing the first and second reactants to join as separate laminar flows, and a parallel reaction channel connected with a downstream side of the junction channel for permitting the laminar flows of the first and second reactants to react at a contact interface thereof. A dimension of the reaction channel in the layer-thickness direction perpendicular to the contact interface is set to be smaller than the sum of the dimensions of the first inlet path and the second inlet path in the layer-thickness direction.

Abstract: Interaction between two different species of particles in a fluid stream is promoted by generating turbulent eddies in the fluid stream. The turbulent eddies are designed to be of such size and/or intensity that the two species of particles are entrained into the eddies to significantly different extents. Consequently, the different species of particles follow different trajectories, and the likelihood of collisions or interactions between the particles is increased. Optimum collision rates will occur for a system which maintains a Stokes Number (St) much less than 1 for one species, and or order 1 or greater for the other species. The invention has particular application in air pollution control, by promoting agglomeration of fine pollutant particles in air streams into larger particles to thereby facilitate their subsequent removal from the air streams.

Abstract: An exhaust mixer (16) is provided for use in an engine exhaust system (10) downstream from an additive injector (14). The mixer (16) includes a first wall structure (20), and a second wall structure (22) carrying a set of mixer vanes (30), the second wall structure (22) being cone shaped and extending radially outwardly from the first wall structure (20).

Abstract: A channel forming body of a reactor has a base plate, a first sealing member bonded to one surface of the base plate and a second sealing member bonded to the other surface of the base plate. A plurality of first inlet grooves forming first inlet paths and a plurality of reaction grooves forming reaction grooves are formed in parallel and side by side in one surface of the base plate. A plurality of second inlet grooves forming second inlet paths are formed in parallel and side by side in the other surface of the base plate. A plurality of junction holes forming junction channels penetrate the base plate from the one surface to the other surface between corresponding ones of the respective first and second inlet grooves and the reaction grooves corresponding to the inlet grooves to connect downstream ends of the inlet grooves and upstream ends of the reaction grooves.

Abstract: A fluid conditioner for a fluid traveling through a conduit, the conduit having a longitudinal axis and substantially circular cross-section. The fluid conditioner includes a static mixing element and a straightener plate. The preferred static mixer is one having a flat generally rectangular central portion having first and second sets of ears affixed on opposite sides of the central portion. The sets of ears include first and second ears bent respectively in upward and downward directions relative to the plane of the central portion wherein each pair of ears located diagonally opposite one another across the central portion are bent in the same direction relative to the plane of the central portion.

Abstract: A flow plug of varying thickness has a plurality of holes formed therethrough. The plug fits in a conduit such that a fluid flow in the conduit passes through the plug's holes. Each hole is defined by a parameter indicative of size in terms of the cross-sectional area thereof. A ratio of hole length-to-parameter is approximately the same for all of the holes.

Abstract: A high efficiency mixing device for mixing first and second fluids within a conduit. A biscuit element is positioned at the upstream end of the conduit having a longitudinal axis that coincides with the longitudinal axis of the conduit. The biscuit element is provided with a plurality of openings including a central opening positioned along the longitudinal axis and a plurality of additional openings spaced proximate to the central opening. The openings are provided with primary mixing elements which induce a rotational angular velocity to a first fluid passing therethrough of the same rotational sign. Second fluid feed ports are positioned within each of the openings for introducing a second fluid to the first fluid as the first fluid passes through the openings and into the conduit. Secondary and tertiary mixing elements are optionally located downstream of the biscuit element to enhance the mixing of the first and second fluids.

Abstract: A dispersion apparatus for dispersing a treating agent into a fluid treatment system that includes a flow duct in which a fluid stream flowing through the duct is mixed with the treating agent. The apparatus is based on a multi-pipe lance positioned in the stream flow, where each pipe supplies a minimum of feed discharge nozzles (typically one to four), and the individual pipes branch off from the same location. Use of the multi-pipe lance, in combination with a suitable baffle, results in better overall dispersion/distribution of the injected medium by surface area. By improving the surface area distribution, better utilization of the injected sorbent can be achieved. The baffle acts to generate a low pressure zone on its downstream side and creates a high-intensity turbulence plume in the fluid. The orifices of the pipe are located to inject the treating agent into the turbulence plume to better distribute and intermix the injected treating agent into the surrounding fluid.

Abstract: A blending apparatus for blending a first fluid stream having a first density and a second fluid stream having a second fluid density, the first density being greater than said second density, is discussed. The apparatus includes a first fluid director including a plurality of baffles affixed therein to create turbulence and shear in the first fluid, a cylindrical second fluid director, a primary mixing chamber receiving the first sheared fluid from the first fluid director and receiving the second fluid from the second fluid director, wherein the first fluid and second fluid are mixed in the primary mixing chamber to form a mixed primary fluid stream, and a secondary blending chamber comprising at least one static mixer and coaxially aligned with and receiving the mixed primary fluid stream from the primary mixing chamber.

Abstract: A process is described for the extraction of one or more substances from a fluid starting material with an appropriate extraction agent by use of a static micromixer for mixing the starting material with the extraction agent. The static micromixer is provided with disk-shaped components, the disk (1) being provided with at least one inlet opening (2) for introducing at least one fluid stream into a linking channel (3) disposed in the plane of the disk and at least one outlet opening (4) for removing the fluid stream into a mixing zone (5) disposed in the plane of the disk, the inlet opening (2) being connected with the outlet opening (4) in a communicating manner through a linking channel (3) disposed in the plane of the disk, and the linking channel (3) before opening into the mixing zone (5) being divided by microstructure units (6) into two or more part channels (7), and the widths of the part channels being in the millimeter to submillimeter range and being smaller than the width of the mixing zone (5).

Abstract: A method for processing a fluidic mixture in a multi-stage hydrodynamic cavitation device is disclosed. The fluidic mixture is introduced to an inlet and passed through a flowpath having at least ten cavitation zones. The fluidic mixture is exposed to cavitation inducing features in each of the at least ten cavitation zones to induce cavitation bubbles, which bubbles are then collapsed between every two adjacent of the at least ten cavitation zones. The multi-stage hydrodynamic cavitation device for processing the fluidic mixture has a generally cylindrical housing with an inlet, an outlet, a flowpath therebetween, and a plurality of cavitation zones along the flowpath. Two or more of the cavitation zones along the flowpath comprise a disk multi-jet nozzle having a plurality of through channels disposed across the surface thereof, wherein each channel includes expansions and contractions of its cross-sectional area along its length.

Abstract: Disclosed is a water saving device which provides the pressure and amount of water to be delivered that can satisfy the comfortable sense of water usage, regardless of whether the water may be supplied under the high pressure or low pressure or whether the water may be supplied in the larger or smaller amount. In accordance with the present invention, the water saving device comprises a hollow cylindrical body that is adapted to be attached to a water passage conduit or pipe. The hollow cylindrical body includes a first plate member disposed perpendicular to the direction of the water flowing through the water passage conduit or pipe. The first plate member has a plurality of first water passage holes formed thereon at regular intervals with regard to each other in the circumferential direction. A water guide member is further included.

Abstract: A dispersion lance is for use in combination with a fluid treatment system of the type which includes a flow duct in which a fluid stream is mixed with a treating agent. The dispersion lance includes a pipe mounted in the duct with its axis approximately transverse to the direction of the fluid stream flow, the pipe having a series of openings along its length for injecting a treating agent into the fluid stream. A baffle extends lengthwise along the pipe, the baffle having a cross-section the central portion of which is V-shaped, with the apex of the V facing upstream of the fluid stream flow, and with generally flattened wing portions extending from the legs of the V beyond the sides of the pipe in a direction where they transversely intersect the stream flow. The baffle acts to generate a low pressure zone on its downstream side which enhances turbulence in the fluid.

Abstract: Provided is an agitating vessel using baffles and an agitator having improved agitating capability and including the same, and more particularly, to an agitating vessel using baffles that has a simple structure in which a horizontal baffle is formed over a predetermine area and that is capable of significantly improving mixing performance of an agitator using a chaos fluid mixing theory, and an agitator having improved agitating capability and including the same. The agitating vessel 100 of the agitator 1000 mixing fluid includes: a body 110 having a space 111 formed in a hollow inner portion thereof so that fluid is stored therein; and a horizontal baffle 130 formed to have a plate shape in a vertical direction to a central shaft of the body 110.

Abstract: A device for processing fluids includes a number of fin layers with a number of plates separating the fin layers so that a fluid flow passage is defined through each fin layer. A first fluid inlet is in communication with a first end portion of the fluid flow passage, a first fluid outlet is in communication with a second end portion of the fluid flow passage, a second fluid inlet is in communication with the second end portion of the fluid flow passage and a second fluid outlet in communication with the first end portion of the fluid flow passage. The fluid flowing through the second inlet is subjected to a shearing action by the fin layers so that mass transfer to the fluid flowing through the first inlet occurs. The device may be used for both liquid-liquid processes, such as extraction, or gas-liquid processes, such as adsorption, absorption or desorption and reactions.

Abstract: In an air mixing arrangement wherein a primary fluid is introduced through an opening in a wall to be mixed with a secondary fluid flowing along the wall surface, the opening is airfoil shaped with its leading edge being orientated at an attack angle with respect to the secondary fluid flow stream to enhance penetration and dispersion of the primary fluid stream into the secondary fluid stream. The airfoil shaped opening is selectively positioned such that its angle of attack provides the desired lift to optimize the mixing of the two streams for the particular application. Embodiments of the arrangement can comprise a collar around the openings, multiple openings that comprise a larger opening and a smaller opening positioned downstream, pairs of openings and associated collars symmetric relationship, and nozzles on the inner side of the wall.

Abstract: Static mixers and fluid systems incorporating one or more of the static mixers. The static mixers include one or more channels that provide a fluid path through a body, wherein fluid flowing through each channel defines a downstream direction through the channel. The channel includes two or more sets of concatenated mixing elements arranged adjacent to each other across the width of the channel, wherein two sets of the mixing elements are offset from each other along the downstream direction of the channel.

Abstract: A water conditioner includes a plate located diametrically across a pipe and a plurality of posts in lines on, or substantially parallel to, the longitudinal axis of the plane and extending from either side thereof, to be close to the periphery of a pipe with which the water conditioner is located. There may also be a plurality of ribs extending from either side of the plate and adjacent the posts for providing a plurality of discreet paths through the water conditioner.

Abstract: A mixing unit, a mixing device, an agitation impeller and a pump mixer can mix a large amount of fluid while having significant mixing effects in a small space. There are also provided a mixing system that uses the pump mixer and achieves a continuous operation and a reaction device that uses the mixing unit and achieves an efficient operation. The mixing unit (1) includes: a stacked member (2) in which a plurality of mixing elements (21) are stacked; and a first plate (3) and a second plate (4) between which the stacked member (2) is sandwiched and which are arranged opposite each other.

Abstract: A fluid flow modification apparatus for creating turbulence in a moving fluid includes turbulence-creating elements arranged in a fractal configuration, each element having a first surface portion against which the fluid can flow and a second surface portion along which the fluid can flow, and further includes an insert for arrangement to obstruct the flow of fluid between adjacent second surface portions of at least two turbulence-creating elements. A support holds the turbulence-creating elements in the fluid to allow movement of the fluid relative to the turbulence-creating elements and the insert. The insert may be attachable to at least two turbulence-creating elements, such that the arrangement of the inserts is symmetrical about a centre point of the fluid flow field for improved mixing.