The invention relates to a double-cone pumping device, designed to provide for flow of the liquid product only on the outer side of the rotating cones, making it compatible with mixing of particulate-containing liquid products; and specifically advanced for high pumping capacity in mixing-agitation applications in food processing. The double-cone pumping device comprises two cones that are axially symmetrically arranged with their large bases abutting, and rotatable around the axis, and an axial shaft that connects to driving means. The invention also relates to a use of this pump in processing of liquid food.

A GMK-reactor includes —a housing, —a hollow base attached to the housing; an inverse taper narrowing downward and attached to the top of housing, —a supporting tube passing through the base including an upper portion situated inside the housing and a bottom discharge opening, —a number of washers of predetermined shapes mounted on an outer surface of the upper portion of the supporting tube such that outer edges of the washer and the inner sidewalls of the housing form predetermined gaps therebetween, and —a number of inlets tangentially attached to the base for introducing a substance and a liquid thereinto forming a circulating suspension therein. The suspension flow, under external pressure, takes a vortex, laminar or turbulent form, rises along inner sidewalls of the housing, enters the gaps, changing its direction at the inverse taper, thus forming a cavitation zone, providing for grinding, or/and mixing of the suspension.

A mixing system and mixing method are provided. The mixing system includes a tank assembly, a container positioned within the tank assembly, a mixer disposed within a compartment of the container, a linear motor, and a shaft having a first end secured to the mixer and an opposing second end secured to the linear motor. The linear motor provides a variable stroke length for the shaft. The mixing method includes providing a tank assembly having a linear motor, positioning a mixing assembly including a mixing bag in the tank assembly, combining two or more components in a compartment of the mixing bag, attaching a mixing shaft extending from a mixer disposed within the mixing bag to the linear motor, and raising and lowering the mixing shaft to mix the two or more components. A stroke length of the mixing shaft during the raising and lowering is varied.

The present invention relates to a method for preparing an aqueous or hydro-alcoholic colloidal solution of metal chalcogenide amorphous nanoparticles notably of the Cu.sub.2ZnSnS.sub.4 (CZTS) type and to the obtained colloidal solution. The present invention also relates to a method for manufacturing a film of large-grain crystallized semi-conducting metal chalcogenide film notably of CZTS obtained from an aqueous or hydro-alcoholic colloidal solution according to the invention, said film being useful as an absorption layer deposited on a substrate applied in a solid photovoltaic device.

Techniques or processes for efficiently producing concrete using dynamic feedback are disclosed. A concrete plant can use a control system to manage concrete production based on the dynamic feedback. The dynamic feedback can control mixing of concrete ingredients so as to yield uniform particle distribution for the concrete ingredients. The dynamic feedback can also avoid overflow situations as well as yield improved loading of the resulting concrete into a concrete transport vehicle (e.g., concrete truck).

A method of mixing a rubber composition includes a carbon introduction step and a uniform dispersion step. In the carbon introduction step, on the basis of a deviation between a rate of temperature increase of the rubber mixture (R) and a target value, at least one of a ram pressure (Pr) and a rotational speed (N) of the mixing rotor (2) is PID controlled so that the ultimate temperature of the rubber mixture (R) at the conclusion of the step is within a tolerance range. In the uniform dispersion step, the ram pressure (Pr) or the rotational speed (N) of the mixing rotor (2) is adjusted to reduce a deviation between a value based on successively detected data associated with a predetermined control target and a target value.

Disclosed are systems and methods for continuously producing dry water from silica and water and from silica, sodium bicarbonate, and water.

The subject of the invention is a flow disperser for mixing substances, in particular for breaking up, dissolving and emulsifying liquids and/or powders. A flow disperser comprising a casing equipped with a perforated inner stator and a rotating drive shaft with a fixed impeller according to the invention is characteristic in that the impeller (4) with the swirling baffle (5) divides the mixing area into two mixing chambers (6) and (7), wherein the inlet port of the mixture ingredients (8) for the mixing chamber (6) is located in the axis of the casing (1) with the fixed impeller (4) and the outlet (9) of the product is made in the side surface of the casing (1) in the mixing chamber (7).

A mixing method, a controller and a mixing device for mixing components in a mixing vessel are provided. The mixing method includes providing a mixing impeller in the mixing vessel; accelerating the mixing impeller from an inactive state to a rotating state in which the mixing impeller rotates at a first desired speed in a first rotation direction; rotating the mixing impeller at the first desired speed for a first time t.sub.steady,1 in the first rotation direction; changing the rotation direction of the mixing impeller, so that the mixing impeller rotates in a second rotation direction at a second desired speed; and rotating the mixing impeller at the second desired speed for a second time t.sub.steady,2.

A method is provided for monitoring a flow behavior of mixed components without requiring additional instrumentation or sampling. The method is carried out by determining ratios of the power required to rotate a mixing impeller at different rotational speeds and then comparing the ratios. Characteristics about the mixed components are determined based on differences between the ratios.