B01F27/93

PROCESSING APPARATUS, SHEET MANUFACTURING APPARATUS, AND PROCESSING METHOD
20190203414 · 2019-07-04 ·

A processing apparatus includes a deinking material supply portion that supplies a deinking material to defibrated fibers, and an agitating portion that agitates a mixture of the deinking material and the fibers. The agitating portion includes a chamber and a rotary blade that rotates in the chamber.

Gas-liquid dispersion impeller assembly with annular-sector-shaped concave blades

The invention discloses an agitation device comprising an impeller, an agitating shaft and a power device. The impeller includes a disc, a hub and concave blades. Each blade consists of a concave surface which extends radially and has an annular sector-like shape, the projections of the upper and lower portions of the blade in the horizontal plane are two annular sectors, and the radian of the annular sector obtained by the projection of the upper portion is larger than that of the lower portion, and the annular sector-like shape and the rotation direction of blades are the same, so that each portion of the blades directly faces an incoming flow, the utilization efficiency of blades is increased and the impeller has low energy consumption and high gas-liquid dispersion efficiency. The device is efficient and energy-saving, has low power consumption, high mixing performance and high gas holdup and mass transfer performance.

Cavitation Pump
20190176108 · 2019-06-13 · ·

A cavitation device is supplied by a disc pump with fluids for mixing. A cavitation rotor, having an array of cavities on its cylindrical surface, is fixed to a shaft for rotation by a motor. The disc pump and the cavitation device are beneficially in the same housing. At least one disc is spaced from and attached to the rotor near the inlet end of the cylindrical housing, so it will rotate with the rotor. A central hole in the (at least one) disc permits fluid to enter the space between the disc and the rotor; it is flung toward the peripheral space between the rotor and the cylindrical housing, where it is subjected to cavitation, and then passed to an outlet. The shaft may pass through one or both of the end walls of the cylindrical housing. The cavitation pump is especially useful for mixing oil field fluids.

Yogurt maker and method for using the same

The present disclosure discloses a yogurt maker and its method of use for using the same. A vertical upwardly extending mixing container protrusion is set at the bottom of the mixing container of the yogurt maker and a mixing head is detachably sleeved on the mixing container protrusion, and the rotation of the mixing head is driven by a power device so that the mixing head can mix the mixture in the mixing container well. At the same time, a temperature sensor is installed at the bottom of the mixing container to monitor the temperature of the mixing container, so as to ensure constant heat preservation conditions in different environments. The mixing device can be detached easily, which eliminates hygienic blind spots and ensures that the yogurt maker can be cleaned easily after making yogurt.

Yogurt maker and method for using the same

The present disclosure discloses a yogurt maker and its method of use for using the same. A vertical upwardly extending mixing container protrusion is set at the bottom of the mixing container of the yogurt maker and a mixing head is detachably sleeved on the mixing container protrusion, and the rotation of the mixing head is driven by a power device so that the mixing head can mix the mixture in the mixing container well. At the same time, a temperature sensor is installed at the bottom of the mixing container to monitor the temperature of the mixing container, so as to ensure constant heat preservation conditions in different environments. The mixing device can be detached easily, which eliminates hygienic blind spots and ensures that the yogurt maker can be cleaned easily after making yogurt.

DEVICE AND METHOD FOR WORKING ON AND PROCESSING CHOCOLATE AS WELL AS USING A UNIVERSAL MACHINE THEREFORE
20190110494 · 2019-04-18 ·

The invention provides a device (1) for processing and treating chocolate, with a container (2) and stirring means (3) arranged therein, wherein the container (2) has a processing interior (2a) with a cylindrical wall (4) and an outwardly curved bottom (5) and is set up obliquely, i.e., the center axis (ZA) of the cylindrical wall (4) is inclined with respect to the vertical, and wherein the stirring means (3) comprises at least one stirring arm (7), which is rotatable about this center axis (ZA), while projecting from the center axis (ZA) of the cylindrical container (4) at least also in the radial direction, and a conching tool (6), which is rotatably arranged at or near the bottom (5) or the lowest vertical point of the container (2) about a an axis of rotation (DA), and wherein the conching tool (6) rotates faster than the stirring arm (7) during operation. In a method according to the invention for processing and treating chocolate, it is provided that a starting mass or an intermediate product of chocolate is filled in an inclined cylindrical container (2) and rotating therein along with at least one stirring arm (7), which rotates about this center axis (ZA), while projecting from the center axis (ZA) of the cylindrical container (2) at least also in the radial direction, as well as processed simultaneously by means of a rotatable conching tool (6), which rotates faster than the at least one stirring arm (7) about an axis of rotation (DA), which is inclined relative to the center axis (ZA) of the cylindrical container (2). Furthermore, the invention provides for the use of a universal machine for processing and treating nutritional and food products, processing and treating chocolate, wherein the universal machine comprises a container (2) and stirring means (3) arranged therein, and wherein the container (2) has a processing interior (2a) with a cylindrical wall (4) and an outwardly curved bottom (5), and arranged obliquely, i.e. the center axis (ZA) of the cylindrical wall (4) is inclined with respect to the vertical, and wherein the stirring means (3) comprise at least one stirring arm (7), which is rotatable about the center axis (ZA) of the cylindrical wall (4), while projecting from the center axis (ZA) of the cylindrical container (2) at least also in the radial direction, and wherein it is further provided that the stirring means (3) comprise a conching tool (6) rotatably arranged at or

Cavitation pump

A cavitation device is supplied by a disc pump with fluids for mixing. A cavitation rotor, having an array of cavities on its cylindrical surface, is fixed to a shaft for rotation by a motor. The disc pump and the cavitation device are beneficially in the same housing. At least one disc is spaced from and attached to the rotor near the inlet end of the cylindrical housing, so it will rotate with the rotor. A central hole in the (at least one) disc permits fluid to enter the space between the disc and the rotor; it is flung toward the peripheral space between the rotor and the cylindrical housing, where it is subjected to cavitation, and then passed to an outlet. The shaft may pass through one or both of the end walls of the cylindrical housing. The cavitation pump is especially useful for mixing oil field fluids.

Nanobubble generation system using friction

The present disclosure relates to a nanobubble generation system using friction in which a frictional force is applied to bubbles included in a gas-liquid mixed fluid so that the atomization of the bubbles is induced and nanobubbles are generated. The nanobubble generation system includes: a chamber including an inlet, an outlet, and an internal space S configured to atomize bubbles included in a gas-liquid mixed fluid; one or more strikers each including a plurality of protrusions provided on a body thereof to simultaneously apply impact to the gas-liquid mixed fluid that flows into the chamber and swirl the fluid in order to cause the gas-liquid mixed fluid to rub against an inner wall of the chamber, the strikers being provided on the driving shaft; a plurality of friction elements provided on the driving shaft in order to apply frictional force to the gas-liquid mixed fluid; and a driving mechanism including the driving shaft and configured to rotate the striker and the friction elements, wherein the friction elements are arranged on the driving shaft to be spaced apart from each other at a predetermined interval, and peripheral surfaces of bodies of the friction elements directly face the inner wall of the chamber with a predetermined distance therebetween.

Polymerization Reaction Device for High Viscosity Resin

A polymerization reaction device of a high viscosity resin includes a cylindrical reactor having an inlet formed at an upper part and a discharge port formed at a lower part; and an impeller rotatably arranged inside the reactor and configured to mix materials in the reactor. The materials in the reactor are mixed by the impeller and polymerized into the high viscosity resin, and the polymerized high viscosity resin is discharged to an outside of the reactor through the discharge port by applying an inert gas. A ratio of a diameter of the discharge port to a diameter of the reactor may be set such that 80% or more of the high viscosity resin is discharged from the reactor from a time point when the applying of the inert gas starts to a time point when the inert gas reaches the discharge port.

Polymerization Reaction Device for High Viscosity Resin

A polymerization reaction device of a high viscosity resin includes a cylindrical reactor having an inlet formed at an upper part and a discharge port formed at a lower part; and an impeller rotatably arranged inside the reactor and configured to mix materials in the reactor. The materials in the reactor are mixed by the impeller and polymerized into the high viscosity resin, and the polymerized high viscosity resin is discharged to an outside of the reactor through the discharge port by applying an inert gas. A ratio of a diameter of the discharge port to a diameter of the reactor may be set such that 80% or more of the high viscosity resin is discharged from the reactor from a time point when the applying of the inert gas starts to a time point when the inert gas reaches the discharge port.