Abstract: The invention relates to a method of preparing a rheology product from a pseudomlaminar silicate comprising microfiber bundles. The inventive method comprises the following steps consisting in: grinding the pseudolaminar silicate mineral which is selected from sepiolite mineral, attapulgite mineral and combinations of same, with a pseudolaminar silicate concentration of at least 50%, moisture of less than 40% and a particle size of less than 1 mm; mixing the ground pseudolaminar silicate mineral with an aqueous solution of a dispersing component comprising at least one dispersing agent, in order to obtain a first mixture comprising between 35% and 85% water and between 0.1% and 7% dispersant in relation to the weight of the pseudolaminar silicate mineral; and intensively mixing the first mixture obtained in the second step until the dispersion of the pseudolaminar silicate microfibre bundles in order to obtain the rheology product in a dispersion homogeneously mixed with the dispersant and the water.

Abstract: A sand washing apparatus may be used for separating organic material from a mixture comprising sand and organic material. The apparatus may comprise: a wash chamber for accepting a mixture comprising sand and organic material, the chamber including a lower portion; and an agitator comprising a screw having two or more flights extending into the lower portion. A method for recovering sand from a mixture comprising sand and organic material may comprise the steps of: introducing a mixture comprising sand and organic material into a water-filled chamber having a net flow of water in an upwardly direction; allowing organic material from the mixture to ascend in a net upwardly direction and allowing sand from the mixture to descend in a net downwardly direction; subjecting at least a portion of the descending sand to a turbulence; and recovering sand that has descended past the turbulence.

Abstract: A disclosed sand washing apparatus may be used for separating organic material from a mixture comprising sand and organic material. The apparatus may comprise: a wash chamber for accepting a mixture comprising sand and organic material, an agitator, a collection chamber, and a conveyor configured to transport sand away from the collection chamber. The disclosed method for recovering sand from a mixture comprising sand and organic material may comprise the steps of: introducing the mixture into a chamber, allowing organic material to ascend while allowing sand to descend, subjecting a portion of the descending sand to a turbulence that creates a lifting action, and recovering sand that has descended past the turbulence.

Abstract: An apparatus (100, 100?, 100?) for separating organic material from inorganic material includes a container (1), a feeding apparatus (4), a charging apparatus (9), a lifting apparatus (21), a discharging apparatus (24) and a removal apparatus (7). The feeding apparatus (4) is located in the upper portion of the container (1), and it serves to introduce inorganic material polluted with organic material into the container (1). The charging apparatus (9) is located in the lower portion of the container, and it serves to introduce cleaning water into the container (1). The lifting apparatus (21) is located in the container (1), and it serves to substantially subject the inorganic and organic material to an upwardly directed component of movement. The lifting apparatus (21) and the charging apparatus (9) produce a fluidized layer (22) in the container (1) during operation of the apparatus (100, 100?, 100?). The fluidized layer (22) causes the organic material to be separated from the inorganic material.

Abstract: A process for extracting and purifying naturally occurring zeolite from ores in the presence of other mineral phases by using mechanical dispersion and differential suspension to remove a majority of the clay content of the ore. The process continues by removal of contaminants with a higher mass to surface area ratio than that of the desired zeolite product by employing the properties of demineralized water in combination with a countercurrent flow separation column. No chemical flocculating or flotation agents need be employed in the process.

Abstract: A process for extracting and purifying naturally occurring zeolite from ores in the presence of other mineral phases by using mechanical dispersion and differential suspension to remove a majority of the clay content of the ore. The process continues by removal of contaminants with a higher mass to surface area ratio than that of the desired zeolite product by employing the properties of demineralized water in combination with a countercurrent flow separation column. No chemical flocculating or flotation agents are employed in the process. The process separates the particulate compound by using the separation effect of an electrical double layer which forms when the mixture is hydrated in a low electrolyte medium.

Abstract: There is disclosed a process and plant for cleaning unwashed clay/sand or oil sands in which a vessel having a false floor of permeable material contains a column of liquid and sand to be cleaned in which an air and liquid mix is injected through the permeable material at a controlled pressure so that the air, water and sand clay mixture will mix together to fluidise the sand with the presence of small bubbles of air to create a turbulence and abrasion of the particles and to clean the sand.

Abstract: New systems for the purification of liquids containing suspended solids and/or dissolved solid materials basically include a conical flocculator unit and a conjoined conical clarifier unit. The flocculator has a cylindrical lower portion, frustum middle portion and large diameter cylindrical top portion while the clarifier is essentially a large diameter cylindrical top portion over a lower frustum portion. Water or other liquid to be purified enters the flocculator lower portion via opposed, unequally sized nozzles to assume a helical flow upward past a series of deflector plates positioned at the top of the lower flocculator portion while a sludge blanket forms therein. A double flume plus slot arrangement located at the junction of the flocculator with the clarifier separates solids from liquid as fluid flow from the flocculator passes into the clarifier where it is subjected to further separation of sludge from clarified liquid with part of the sludge being recycled to the flocculator.

Abstract: An apparatus is disclosed for gravity separation of comminuted solid particles. It has a transparent pipe (18) through which water flows upwards at a controlled velocity to float grains of a given size and specific gravity but to maintain lighter particles in a funnel on top of the pipe. The pipe is enclosed in a housing in which a water level can be raised or lowered to coincide with a mark on a scale indicative of the instant lowermost gravity of particles passing downwards through the pipe (18). The device is of a simple structure and provides the possibility of the readout of the specific weight of the accepted particles.

Abstract: An apparatus and method for separating particulate solid from a solid mixture based on the size of the particles which includes feeding a slurry of the particulate solid mixture into an upper vessel portion adapted to be filled with liquid such as the slurried particulate. The apparatus also includes a lower vessel portion having a cross-sectional area which is less than the cross-sectional area of the upper vessel portion and is sealingly connected for fluid communication with the upper vessel portion by an outwardly diverging wall located at the top of the lower vessel portion. The upper vessel portion has a free-settling region for separating particulate solids. The particulate containing slurry is met with an upwardly directed stream of fluidization fluid, e.g., water, in the lower vessel portion wherein a first fraction-containing solid particulate which has descended through the fluidization stream is directed from the apparatus by a means therefor.

Abstract: The present separation apparatus makes it possible at low cost continuously to separate a mixture according to the density of its constituent particles which have been graded to an upper limit of the particle size of any shape, and is particularly suitable for the separation of electrical storage battery waste. A separation medium, consisting preferably of a liquid and a gaseous flow medium, fed into a vertical separator column (1) via a mixing nozzle (10) flows through the column from the bottom upwardly. Above a constriction (7) adjacent a through-flow aperture (9) there is a baffle (15) which is movable transversely relative to the longitudinal axis (4) of separator column (1) to form a flow channel (20) leading to the through-flow aperture (9). The width of the flow channel (20) when the baffle (15) lies against the internal wall (1a) of the separator column (1) is just sufficiently large to let the particles through.

Abstract: An apparatus for separating minerals and the like from earth and the like which includes a tank including a tank having an upper portion and a lower portion having a frusto-conical formation. The lower tank portion terminates in a chamber from which extends an outlet for separated material. The top of the tank has an outlet and an inlet. The tank also includes an auger for causing a flow of liquid in the tank portions from within the chamber upwardly and into said lower and upper portions. The tank has baffle members and on the tank arcuate bar members connected to the auger for separating material. A fluid injection inlet is connected to said chamber for introducing fluid under pressure into the chamber and an outlet on said chamber separated material. The tank also includes a bypass conduit on the outside of the tank and leading into the tank at the juncture of the upper and lower tank portions for use with relatively light weight material to be separated.

Abstract: Refuse, particularly of the household type, is sorted according to density by the following consecutive operations: Sifting the refuse; comminuting the oversize obtained; separating the comminuted material by a gas stream into light and heavy material fractions; separating the heavy material fraction by a liquid stream into two fractions of different density; and separating the two fractions of different density into basic components.

Abstract: Metal contained within soil is separated therefrom by introducing the soil into a tank containing water which is quite turbulent, the turbulence being generated by the fact that the water is introduced into the tank in a swirl and also directly upwardly through the center of the swirl. Vibrator units on the sidewalls of the tank further add to the turbulence. Upon being introduced into the turbulent water, the soil quickly turns to mud which goes into suspension and the suspension so formed is buoyed upwardly by the incoming clean water which rises through the tank. The suspension overflows the tank and is directed to a settling basin where the mud is allowed to settle out. The clean water which remains is recirculated through the tank. The metal, on the other hand, being considerably heavier than the mud, passes downwardly through the tank where it is thoroughly washed by the incoming water. The washed metal passes out of the bottom of the tank and is elevated upwardly by a screw-type conveyor.

Abstract: A hydraulic classifier for sand has a vessel of circular cross section about a vertical axis and tapers downward to an aperture in its bottom. A rotor is slowly rotated on a hollow shaft coaxially mounted in the vessel. It includes a hollow member conically tapering from an annular lower orifice upwardly spaced from the bottom aperture toward a smaller upper orifice, a flow tube mounted on the shaft for receiving liquid upwardly discharged from the upper orifice of the hollow member for upward flow, agitating blades projecting radially outward beyond the flow tube above the hollow member, and a nozzle on the shaft below the hollow member for forcing cleaned sand through the bottom aperture of the vessel by means of a flushing medium. A washing nozzle directs a liquid washing medium radially inward toward the conical hollow member intermediate the orifices of the same whereby washing medium is deflected into the flow tube and draws additional liquid from the upper orifice.