Abstract: A method of mixing viscous fluids is disclosed. The method comprises rotating a mixing apparatus in a container of fluid. The mixing apparatus comprises a cage located at the end of a shaft. The cage comprises a central circular disc with an outer edge and top and bottom sides. A number of vanes extend from each side of the plate, the vanes spacedly located near the outer edge of the plate. The free ends of the vanes are connected by a hoop to maintain their spaced relationship.

Abstract: An apparatus for quickly making multiple-phase microemulsion fuel including: a primary mixer for primarily mixing water, catalyst, emulsifying agent, stabilizer and little quantity of oil in the primary mixer for producing oil-in-water phase mixing liquid; and a secondary mixer having a turbine agitator rotatably mounted in the secondary mixer, an eddy-flow guiding device of calabash shape disposed around the turbine agitator for producing upwardly and downwardly curved eddy flows of a mixing solution in the secondary mixer fed with the mixing liquid supplied from the primary mixer and raw fuel oil, and a plurality of turbulence baffles radially secured in the secondary mixer for limiting the eddy flows of the mixing solution in the secondary mixer into a plurality of eddy-flow "sector zones" for accelerating a thorough mixing and emulsion of the fuel oil with the oil-in-water phase mixing liquid for quickly producing water-in-oil phase fuel oil for better combustion efficiency and less air pollution when bur

Abstract: A rotary mixer and disperser head consisting of a shaft to which is connected a mixing chamber that is to be disposed into a vat or the like for dispersing, dissolving or blending of solids liquids or gasses with other liquids. The mixing chamber has secured to its upper and lower ends a plurality of impeller blades that have an end thereof located outside the mixing chamber to direct material into the mixing chamber and out through openings in the side wall of the mixing chamber during the mixing and dispersing thereof. The shaft for rotating the mixing chamber is merely located at one end thereof and doesn't extend into the mixing chamber and thus does not impede the mixing action taking place therewithin. The specific location of the blades, their relationship relative to the mixing chamber and their configuration provide for a very efficient mixing operation.

Abstract: The present invention provides a mixing impeller including a plurality of blades circumferentially mounted to a frame around the mixing impeller with adjacent blades being opened from one another. The blades are secured to the frame in a manner such that at least part of each blade extends outwardly of the frame to guide discharge of fluid passing through the impeller away from the frame and substantially eliminate any turbulence that the frame might otherwise create. In addition, the frame has a rearwardly inwardly tapering configuration with each of the blades having the same inward rearward taper as that of the frame. This combination of features substantially reduces turbulance of the outward flow of liquid from the impeller relative to conventional impeller designs.

Abstract: A mixing device employs a rotating hollow column or pipe that is motor-driven for rotation, is open at both ends to, at its upper or outer end, receive an inflow of a mixing fluid, such a gas or liquid, and its opposite or lower end, to simultaneously receive a co-axial inflow of a fluid-like or flowable charge material that is to be thoroughly and substantially uniformly mixed with the counter in-flowing mixing fluid.

Abstract: An agitator comprises a vessel having an intake (101) through which a medium is introduced into the vessel, and rotating guide devices (12) for guiding and discharging the medium. The inner and outer defining surfaces of the vessel have a hyperbolic, conical shape and the cross-sectional area of the intake increases progressively towards the guide devices. The guide devices (12) extend horizontally towards the periphery of the vessel and are mounted on a horizontal rotatable bottom plate (11) which is driven for rotation from beneath.

Abstract: A rotary mixing and straining apparatus (10) for liquids (100) including a shaft member (16) secured on one end to a rotary power tool (15) and equipped on the other end with a mixing head unit (13) including a generally cylindrical open framework member (20) surrounded by a screen member (40) whereby the liquid (100) is forced outwardly through the screen member (40) by centrifugal forces and recirculated through the open top of the framework member (20).

Abstract: A cement paste generator produces a paste with improved workability. The cement paste generator includes a housing, a shaft and a series of blades and baffles which have critical dimensions.

Abstract: A rotary device for mixing viscous liquids within a container. A vertical rotary driven shaft is connected to a circular disc at its terminal end. Radial or tangential mixing vanes are connected to the top surface of the disc and a baffle plate or cover disc is located over the vanes to prevent vertical flow in the area of the vanes. A central flow passage is provided about the shaft. Fluid is driven laterally outwardly by the vanes and replacement fluid is pulled downwardly by a pumping action along the shaft and likewise driven laterally outwardly for mixing. A removable washer shaped flow restrictor is placed in the central flow passage, vertically supported by the inner ends of the vanes and held in place by the downward flow during rotation of the mixing device.

Abstract: The mixing apparatus has a plurality of pump impellers having one common axis and extending parallel to each other. Immediately adjacent pump impellers have opposite directions of rotation. The blading of the pump impellers is such that the currents of the mediums exiting the pump impellers have an as large as possible peripheral component. The medium currents exiting the adjacent pump impellers and having opposite senses of rotation are guided together and generate at the mutual point of contact an extremely high turbulence because the peripheral components of the exiting rotating currents of the mediums are directed oppositely to each other and eliminate each other practically immediately.

Abstract: The invention is related to a method for dispersing two phases in an extraction process so that each extraction step includes several mixing stages, and at each mixing stage the mixing is carried out by means of a vertical circulation and advantageously at least one mixing stage is provided with an intensified vertical circulation. According to the invention, the dispersing apparatus of one extraction step in an extraction process is formed of several mixers provided with circulation cylinders (11). Advantageously at least one of the mixers is provided with a dispersing pump (16).

Abstract: The invention relates to a method for dispersing the two liquid phases of a solvent extraction process well together, for controlling the desired type of dispersion and for raising the created dispersion to a level essentially higher than the liquid surface in the mixing tank. In the apparatus of the invention, to the circulation cylinder (6) of the mixer there is connected the heavy phase return conduit (27) and the light phase return conduit (29) entering from the settler of the same extraction step. In the top part of the mixer, coaxially with the turbine pump (9), there is installed the dispersion pump (12) where the dispersion rises to above the liquid surface (8) of the mixer through 2-24 rising pipes (15). The top ends of the rising pipes (15) are connected to the circular pipe (18), wherefrom the dispersion flow is conducted to the next stage through the collecting trough (22).

Abstract: Arrangement for the treatment of fluent, thin and highly viscous media, particularly for the fermentation of micro organisms, for mixing, pumping and the dissipation of the medium. The arrangement is based on a novel principle of bladeless mixing and pumping of fluent media of any kind and density. The main part of the arrangement is a hollow rotor with a bottom with at least a single inlet opening in the bottom. The rotor is rotated at a speed at which the treated medium due to centrifugal forces proceeds from one end of the rotor to the other one. The medium is discharged from the rotor through one or more outlet openings in the sides or in the top of the rotor; the medium is either only raised, or is also dissipated below or above the level of the fluent medium.

Abstract: The present invention concerns a way to achieve in liquid-liquid extraction in the step of dispersing two different solution phases the transformation of the desired phase, which may also be the phase with smaller volume, to become the continuous phase, with the aid of a primarily vertical circulation flow. The invention also concerns an apparatus serving this purpose, a circulation dispersion contactor, in which the smooth circulation of the dispersion is accomplished by the aid of a radial pump turbine designed for this particular purpose, or of an axial propeller, and of distribution/guide rings on the periphery of the contactor.

Abstract: This invention relates to an apparatus and method that provides by means of circulator/impeller configuration alone the generation of a stabilized vortex in a media wherein the vortex generated is stable in its dynamic formation over a wide range of rotational circulator/impeller speeds and increasing distances beneath the surface of the media.The apparatus and method include a charge carrying fluid media in a vessel or other containment device that is redirected within the vessel or containment device by fluid flow, by and through a circulator/impeller such that the fluid is forced to pass through an angle greater than 90 degrees but less than 180 degrees. The redirection being as a result of forces imparted to the fluid by virtue of the inventive geometry of the circulator/impeller and independent of vessel/containment device configuration or nearby wall confinements.

Abstract: There is provided a mixing device for low velocity and low shear mixing. The device is of special value for mixing of delicate materials, such as cell suspensions, microspheres and the like, as used in fermentors and the like. The device is based on the suction effect obtained by low velocity rotation of a cylinder provided with tangential openings.

Abstract: An apparatus is provided for blending and emulsifying a dry product with a viscous product, the latter being disposed to a predetermined level within a tank. The tank is provided with a dry product inlet disposed above the level of the viscous product. The apparatus includes a power actuated rotary agitator immersed within the viscous product and, when rotating at a predetermined speed, causes the viscous product to form a vortex into which the dry product is fed through the tank inlet. The agitator is provided with first and second disc members arranged in spaced, substantially parallel relation. One of the disc members is provided with an enlarged central opening. The disc members are interconnected to one another by a plurality of symmetrically arranged baffles. The periphery of at least one of the disc members is provided with a plurality of symmetrically arranged shear blades.

Abstract: A longitudinally extending housing with end closures forms a closed mixing chamber within the housing. A mixer that has a fluid material inlet at each end thereof with longitudinally spaced, opposed ends forming fluid material outlets and a central peripheral discharge from the mixer between the end outlets is supported on a rotatable shaft that extends through one of the end closures to position the mixer in the mixing chamber. Housing inlet means comprising a pair of conduits communicate fluid to the closed mixing chamber for discharging it thereinto adjacent, but spaced from the end fluid inlets of the mixer, and housing outlet means is aligned with the mixer to receive the central discharge therefrom. The diameter of the mixer is about one-half the diameter of the closed mixing chamber, and the length of the mixer is about one-third the longitudinal extent of the closed mixing chamber. The mixer is positioned substantially equidistant from the sides and ends of the mixing chamber.

Abstract: A mixer for mixing a body of receiving liquid with solids, liquids or gases introduced therein. The mixer includes a rotatable shaft, a thin disk-like member mounted for rotation on the shaft, and at least one thin annular ring mounted on the disk-like member spaced from, parallel to and concentric with it. The flow of liquid perpendicular to the annular ring through the inner opening thereof, when the mixer is immersed and rotating in the body of receiving liquid, is unimpeded by any structural member. The annular ring may be mounted on either side of the disk, and a plurality of annular rings may be employed. The annular ring or rings may be mounted on the disk-like member by at least three elongated support posts spaced equally around the outer perimeter of the disk, the transverse cross-section of each post being curvilinear, preferably circular, in shape. The mixer is disclosed for use in a tank.

Abstract: An apparatus for agitating and transforming settled sludges into slurries which are then capable of being pumped by conventional means. The apparatus comprises a housing immersible in the contents of a tank or chamber and containing separate variable drive means for an impeller and an impeller casing. The impeller casing forms an inlet to the impeller and has a plurality of radially directed outlet nozzles whereby rotation of the impeller effects circulation of the contents of the tank or chamber from the inlet to the outlets and rotation of the casing causes the discharge at the outlets to agitate the contents. The discharge at the outlets breaks up solid sediment at the bottom of the tank or chamber and a continuous recirculation of the contents results in the formation of a slurry.

Abstract: An arrangement for developing photographic layer carriers has at least one container for accommodating a treating medium and having an uninterrupted wall, a pump for circulating the treating medium in the container and having a first part formed by the uninterrupted wall of the container and a second part associated with the first part, and a magnetic force-transmitting element located outside the container and magnetically acting upon a rotary body of the pump so as to rotate the same.

Abstract: A motor-pump aggregate whose pump is a glandless centrifugal pump and is intended for use in a nuclear reactor plant has hollow coaxial pump and motor shafts which are sealingly coupled to each other. To this end, the first end portion of the pump shaft extends into the adjacent first end portion of the motor shaft and has an external conical shoulder for engagement with an internal conical seat of the first end portion of the motor shaft. A feather holds the first end portions against rotation relative to one another, and the shoulder is urged against the seat by a pair of threaded connectors one of which is anchored in a disc-shaped member in the region of the second end portion of the motor shaft and the other of which is anchored in the first end portion of the pump shaft. The disc-shaped member and the second end portion of the motor shaft have mating ring gears to ensure accurate and a reproducible centering.

Abstract: A mix for batch mixing a treatment agent and a particulate material comprises a mixing chamber having at least one mixing member rotatably mounted therein. Outlet means is positioned to receive the mixed batch of material from the mixing chamber. The mixing member may be rotated at a first speed of rotation effective to mix materials within the mixing chamber without discharging from the outlet means. The mixing member is also rotatable at a second speed of rotation effective to discharge the charge or batch of material through the outlet means after it has been treated during the initial mixing step. The rotation of the mixing member at a higher rate of speed at the second speed of rotation effects discharge through the outlet means by centrifugal force.

Abstract: A mixing device and method of mixing a liquid, vapor, or gas into a slurry of material in a vat in which the liquid, vapor, or gas is introduced into a stream of the slurry passing from the vat through a venturi at the diverging portion of the venturi, and in which the slurry with the entrained liquid, vapor, or gas is returned to the vat below an umbrella of a high velocity stream of slurry in the vat produced by an agitator so as to dissipate the heat of reaction between the two fluids.

Abstract: A jet impeller mixer-agitator having a shaft adapted for rotation by a power source, a hub communicating with the shaft and at least one hollow blade fixed to the hub, the hollow blade having a fluid entrance opening on the effective face of the blade and a fluid exit opening on the non-effective face of the blade with a fluid passage connecting the fluid entrance opening and the fluid exit opening so that upon rotation of the shaft the fluid is directly forced into the fluid entrance opening, through the fluid passage and out of the fluid exit opening.

Abstract: There is provided a mixing device for low velocity and low shear mixing. The device is of special value for mixing of delicate materials, such as cell suspensions, microspheres and the like, as used in fermentors and the like. The device is based on the suction effect obtained by low velocity rotation of a cylinder provided with tangential openings.