In-line rotor-stator disperser and reaction process

US10406506B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-10406506-B2
Application numberUS-201415033214-A
CountryUS
Kind codeB2
Filing dateOct 29, 2014
Priority dateNov 1, 2013
Publication dateSep 10, 2019
Grant dateSep 10, 2019

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  4. Key dates

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  5. First independent claim

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  6. CPC / IPC classifications

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  7. Citations and related patents

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Abstract

Official abstract text for this publication.

The present invention is directed to a special device for fast mixing and precipitation reactions of chemical substances. In particular, the present invention presents a reactor which allows an extremely fast mixing of at least two liquid streams containing highly concentrated dissolved materials from which solid metal compound particles are formed when at least two reactant streams meet, to which optionally a further stream, advantageously containing a dispersion or suspension, may be added.

First claim

Opening claim text (preview).

What is claimed is: 1. A reactor device for the fast reaction and precipitation of chemical substances comprising: a housing defining an inlet zone; one stator disc comprising one or more stator rings of spaced apart teeth with openings to the bottom, concentrically located within the inlet zone and fixed to the reactor device; one rotor disc comprising one or more rotor rings of spaced apart teeth with openings to the top, configured for rotation about an axis of rotation relative to the stator disc and concentrically located within the inlet zone; the spaced apart teeth of the one or more stator rings and the spaced apart teeth of the one or more rotor rings being alternatingly adjacent to each other in radial direction; the one or more stator rings engaging the one or more rotor rings from the top in such a way that the openings of the spaced apart teeth build the only communication of the inlet zone to a collector zone in communication with an outlet of the reactor device; a first inlet located eccentrically at a first radial location for supply of a first reactant material to the inlet zone; at least one further inlet located eccentrically at a radial location, different from the radial location of the other inlet for supply of at least one further reactant material to the inlet; the outlet being configured for the removal of the product collected in the collector zone; wherein the first inlet for supply of a first reactant material and the at least one further inlet for supply of a further reactant material are located such that the reactant materials hit the spaced apart teeth of a radial interior most positioned rotor ring after being supplied through the inlets and prior contact with the interior most positioned stator ring, and wherein the first inlet and the at least one further inlet are configured such that the first reactant material and the at least one further reactant material make contact on respective, different teeth of the radial interior most positioned rotor ring prior to coming into mixing, reacting contact. 2. The reactor device according to claim 1 , wherein the spaced apart teeth of an exterior stator ring have a distance to each other of 0.5-5 mm. 3. The reactor device according to claim 1 , wherein the spaced apart teeth of an interior rotor ring have a distance to each other of 0.5-5 mm. 4. The reactor device according to claim 1 , wherein the spaced apart teeth, of the stator ring and the rotor ring have a shape selected from the group consisting of rectangular, rhombic, trapezoid and round shape. 5. The reactor device according to claim 1 , wherein the spaced apart teeth of the stator rings and the spaced apart teeth of the rotor rings are alternatingly adjacent to each other in the radial direction and have an interstitial spacing of between 0.05-2 mm. 6. The reactor device according to claim 1 , wherein the first inlet for supply of a first reactant material and the at least one further inlet for supply of at least one further reactant material are located as to be diametrically opposed on a circle encircling a central axis of the rotor disc. 7. The reactor device according to claim 1 wherein the first inlet for supply of a first reactant material and the at least one further inlet for supply of at least one further reactant material have outlet conduit sections that each extend along a vertical axis as to extend in relative parallel fashion. 8. The reactor device according to claim 1 wherein the first inlet for supply of a first reactant material and the at least one further inlet for supply of at least one further reactant material have outlet conduit sections that are arranged to supply respective reactant material into the reactor device at radially eccentric locations. 9. The reactor device according to claim 1 wherein the first inlet for supply of a first reactant material and the at least one further inlet for supply of at least one further reactant material have outlet conduit sections that are arranged relative to the rotor disc as to have the first reactant material and the at least one further reactant material initially supplied to the rotor disc at eccentric locations on the rotor disc such that initial mixing is carried out with circular and radial, centrifugal motion generated by the rotor disc. 10. The reactor device according to claim 1 wherein the first inlet for supply of a first reactant material and the at least one further inlet for supply of at least one further reactant material have outlet conduit sections that extend below an upper surface of the stator disc. 11. The reactor device according to claim 1 wherein, in addition to the first inlet for supply of a first reactant material and the at least one further inlet for supply of at least one further reactant material reactant at eccentric locations on the rotor disc, there is provided a third inlet configured to supply an additional reactant material along a rotation axis of the rotor disc. 12. The reactor device of claim 1 wherein said first inlet and said at least one further inlet are radially spaced from the axis of rotation as to be closer to the rotor ring than the axis of rotation. 13. Process for fast reaction and precipitation of chemical substances, comprising supplying at least two materials to the reactor device of claim 1 through the first and at least one further inlet, and collecting the product from the outlet of the reactor device. 14. Process according to claim 13 , wherein supplying the at least two materials results in the produced product being a metal compound particle of an anion selected from the group consisting of hydroxide, oxy-hydroxide, oxide, and mixtures thereof and of a metal cation selected from the group consisting of aluminum, zirconium, copper, iron, cobalt, nickel, manganese, barium, rare earths, and mixtures thereof. 15. Process according to claim 13 , wherein supplying the at least two materials results in a production of a viscous suspension of precursors for catalyst materials having a viscosity of >50 Pa×s. 16. A reactor device for fast reaction and precipitation of a chemical substance comprising: a housing defining an inlet zone; one stator disc comprising one or more stator rings of spaced apart teeth defining openings to the bottom, concentrically located within the inlet zone and fixed to the reactor device; one rotor disc comprising one or more rotor rings of spaced apart teeth defining openings to the top, configured for rotation about an axis of rotation relative to the stator disc and concentrically located within the inlet zone; the spaced apart teeth of the one or more stator rings and the spaced apart teeth of the one or more rotor rings are alternatingly adjacent to each other in the radial direction; the one or more stator rings being arranged to engage the one or more rotor rings from the top in such a way that the openings of the spaced away teeth build the only communication of the inlet zone to a collector zone in communication with an outlet of the reactor device; a first inlet located eccentrically at a first radial location for supply of a first reactant material to the inlet zone; at least one further inlet located eccentrically at a radial location, different from the radial location of the other inlet for supply of at least one further reactant material to the inlet zone; the outlet being configured for the removal of product collected in the collector zone; wherein the first inlet for supply of a first reactant material and the at least one further inlet for supply of a further reactant material are located su

Assignees

Inventors

Classifications

  • B01J23/63Primary

    with rare earths or actinides · CPC title

  • moved by stirrers or by rotary drums or rotary receptacles {or endless belts} · CPC title

  • forming a thin film · CPC title

  • Compounds containing zirconium, with or without oxygen or hydrogen, and containing two or more other elements · CPC title

  • characterised by a specific device · CPC title

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What does patent US10406506B2 cover?
The present invention is directed to a special device for fast mixing and precipitation reactions of chemical substances. In particular, the present invention presents a reactor which allows an extremely fast mixing of at least two liquid streams containing highly concentrated dissolved materials from which solid metal compound particles are formed when at least two reactant streams meet, to wh…
Who is the assignee on this patent?
Umicore Ag & Co Kg
What technology area does this patent fall under?
Primary CPC classification B01J23/63. Mapped technology areas include Operations & Transport.
When was this patent published?
Publication date Tue Sep 10 2019 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).