This disclosure relates generally to mixing apparatus. More particularly, this disclosure relates to apparatus for mixing solid materials.
Mixing is an important but poorly understood aspect in petrochemical, food, ceramics, fertilizer and pharmaceutical processing and manufacturing. Segregation and mixing phenomenon occur in most systems of powdered or granular solids and have a significant influence on their behavior. Deliberate mixing of granular solids is an essential operation in the production of industrial powder products usually constituted from different ingredients.
The importance of granular mixing to the U.S. economy is tremendous as the production of products ranging from semiconductors to polymers and ceramics increasingly depend on reliable granular flow and uniform granular mixing. For example, the annual cost of inefficient industrial mixing in the U.S. has been estimated to be as high as one trillion dollars. The efficiency of all pharmaceutical products depends on their blend homogeneity. Therefore, inconsistency in the mixture can be extremely detrimental.
Commonly used conventional mixers can be divided into two distinct categories: rotary blenders and convective blenders. While the rotary blenders rely upon the action of gravity to cause the powder to cascade and mix within a rotating vessel, the convective blenders employ an impeller, paddle, blade, or screw which stirs the powder inside a static mixing vessel. Convective blenders exhibit variations in both impeller and vessel geometries, while rotary blenders which rotate around one axis, differ mainly in the geometry of the vessel.
Single axis rotary blenders (mixers) are some of the most common batch mixers used in the pharmaceutical, food, agriculture, and polymer industries. Such equipment finds use in a myriad of applications such as dryers, kilns, coaters, mills and granulators. In most of the rotary mixers, the radial mixing (convection) is faster than the axial mixing (dispersion) of powders. This slow dispersive process hinders the overall granular mixing performance in many blending, drying and coating applications. The double cone mixer's performance is least effective among all types of rotary mixers, e.g., cylindrical drum mixers, v-blenders, or tote-blenders.
There is provided a multi-dimensional rotary mixer comprising a stand, a frame mounted to the stand, and a mixing vessel mounted to the frame. The frame is rotatable around a first axis of rotation and the mixing vessel is rotatable around a second axis of rotation, the second axis of rotation being substantially orthogonal to the first axis of rotation.
The mixer may further comprise a first drive motor coupled to the frame to rotate the frame about the first axis of rotation and a second drive motor mounted to the frame and coupled to the mixing vessel to rotate the mixing vessel about the second axis of rotation. The first and second drive motors may be stepper motors.
The mixer may further comprise a control system in electrical communication with the first and second drive motors.
The stand may comprise first and second support members, each of which has a first end adapted to being attached to a base.
The mixer may further comprising first and second axle segments that define the first axis of rotation. Each of the axle segments includes an outer end portion rotatably mounted to one of the support member and an inner end portion mounted to the frame.
The mixing vessel may comprise oppositely disposed first and second outer portions, each having a conical shape or a conical-frustum shape forming an apex, the apexes of the outer portions defining the second axis of rotation.
The mixing vessel also comprises a cylindrical middle portion disposed intermediate the first and second outer portions.
The present disclosure may be better understood and its numerous objects and advantages will become apparent to those skilled in the art by reference to the accompanying drawings in which:
a, 4b and 4c illustrate the effect of varying the rotational speed of the mixing vessel on the intensity of segregation of the particles over time;
a, 6b and 6c illustrate the mixing efficiency of a mixing vessel rotated about a single axis; and
a, 7b, and 7c illustrate the mixing efficiency of the subject multi-dimensional rotary mixer.
With reference to the drawings wherein like numerals represent like parts throughout the several figures, a multi-dimensional rotary mixer in accordance with the present disclosure is generally designated by the numeral 10.
With reference to
The two outer portions 48, 50 of the mixing vessel 12 may have a conical shape or a conical-frustum shape, with the apexes 52, 54 of the outer portions 48, 50 defining a second axis of rotation 56 (Y axis in the example) that is orthogonal to the first axis of rotation 36. A cylindrical middle portion 58 may be disposed intermediate the two outer portions 48, 50, as shown in
In the example shown in
With reference to
By rotating the mixing vessel 12 around the two orthogonal axes 36, 56 of the mixing vessel 12, the axial mixing rate is improved to be substantially equal to the radial mixing rate, manifesting a significant improvement of overall mixing compared to mixers that rotate around only a single axis, as shown in
Further experimentation has shown that changing the fill level of the mixer vessel 12 between 10% to 40% had little effect on the mixing of the particles. With reference to
Incorporation of dual axis rotation reduces the axial mixing time by 60 to 90% in comparison to single axis rotation. A manufacturer using a mixer of the subject disclosure on an industrial scale can save large amounts of resources (time, manpower, energy) because of reduced processing (mixing) time.
It will be appreciated that various of the above-disclosed and other features and functions, or alternatives thereof, may be desirably combined into many other different systems or applications. Also that various presently unforeseen or unanticipated alternatives, modifications, variations or improvements therein may be subsequently made by those skilled in the art which are also intended to be encompassed by the following claims.
This application claims the benefit under 35 U.S.C. §119(e) of U.S. Provisional Patent Application Ser. No. 61/270,943 filed Jul. 15, 2009.
Number | Date | Country | |
---|---|---|---|
61270943 | Jul 2009 | US |