Method for reducing hexavalent chromium in oxidic solids

US9725364B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-9725364-B2
Application numberUS-201314411618-A
CountryUS
Kind codeB2
Filing dateJul 5, 2013
Priority dateJul 6, 2012
Publication dateAug 8, 2017
Grant dateAug 8, 2017

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  1. Title

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  2. Abstract

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  4. Key dates

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  5. First independent claim

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Abstract

Official abstract text for this publication.

Process for reducing hexavalent chromium in oxidic solids, which comprises the steps: a) mixing of the oxidic solid containing Cr(VI) with a carbon-containing compound which is liquid in the range from 20 to 100° C., b) treatment of the mixture obtained after a) in an indirectly heated reactor at a temperature of from 700° C. to 1100° C., particularly preferably at a temperature of from 800° C. to 1000° C., under a protective atmosphere, c) cooling of the reaction product obtained after b) to at least 300° C., preferably at least 150° C., under a protective atmosphere.

First claim

Opening claim text (preview).

What is claimed is: 1. A process for reducing hexavalent chromium in oxidic solids, the process comprising: a) mixing an oxidic solid containing Cr(VI) with a carbon-containing compound to form a mixture, wherein the carbon-containing compound is a compound that is liquid at temperatures from 20° C. to 100° C., b) treating the mixture obtained after a) in an indirectly heated reactor at a temperature of 700° C. to 1100° C. under a protective atmosphere to form a reaction product, and c) cooling of the reaction product obtained after b) to a temperature of 300° C. or less under a protective atmosphere to form a reduced process product. 2. The process according to claim 1 , wherein the oxidic solid contains a proportion of less than 15% by weight of calcium oxide. 3. The process according to claim 1 , wherein the oxidic solid is a chrome ore residue. 4. The process according to claim 1 , wherein the carbon-containing compound comprises a polyhydroxy compound. 5. The process according to claim 1 , wherein, instead of vaporizing, the carbon-containing compound decomposes at temperatures of ≧150° C. 6. The process according to claim 1 , wherein the carbon-containing compound comprises glycerol, polyethylene glycol having a molar mass of from 380 to 420, or a mixture of the two in a mass ratio of from 4:1 to 15:1, based on the mass of Cr(VI). 7. The process according to claim 1 , wherein carbon of the carbon-containing compound is used in a molar ratio to Cr(VI) of from 5:1 to 35:1. 8. The process according to claim 1 , wherein: the carbon-containing compound comprises glycerol, polyethylene glycol having a molar mass of from 380 to 420, or a mixture of the two; and carbon of the carbon-containing compound is used in a molar ratio to Cr(VI) of from 9:1 to 23:1. 9. The process according to claim 1 , further comprising conducting step a) in a continuously operating mixing apparatus. 10. The process according to claim 1 , further comprising conducting step b) in a continuously operating indirectly heated reactor. 11. The process according to claim 1 , further comprising conducting step c) in a continuously operating cooling apparatus. 12. The process according to claim 1 , wherein the oxidic solid has a water content. 13. The process according to claim 1 , further comprising in step a), adding auxiliaries which improve the processability of the mixture produced, wherein the auxiliaries are selected from the group consisting of silicas, silicates, aluminates, and aluminosilicates. 14. The process according to claim 1 , wherein the oxidic solid contains up to 80,000 ppm of Cr(VI). 15. The process according to claim 3 , wherein the chrome ore residue contains up to 10,000 ppm of Cr(VI). 16. The process according to claim 3 , wherein the chrome ore residue comprises a mixture of chrome ore residue and other residue, with the mixture containing up to 20 000 ppm of Cr(VI). 17. The process according to claim 1 , wherein the process product has a Cr(VI) content of <640 ppb.

Assignees

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Classifications

  • Hydraulic lime cements; Roman cements {; natural cements} · CPC title

  • Compositional purity · CPC title

  • C01G37/00Primary

    Compounds of chromium · CPC title

  • by treating with halogens, sulfur or compounds thereof; by carburising, by treating with hydrogen (hydriding) · CPC title

  • Compositions of bituminous materials, e.g. asphalt, tar, pitch · CPC title

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What does patent US9725364B2 cover?
Process for reducing hexavalent chromium in oxidic solids, which comprises the steps: a) mixing of the oxidic solid containing Cr(VI) with a carbon-containing compound which is liquid in the range from 20 to 100° C., b) treatment of the mixture obtained after a) in an indirectly heated reactor at a temperature of from 700° C. to 1100° C., particularly preferably at a temperature of f…
Who is the assignee on this patent?
Lanxess Deutschland Gmbh
What technology area does this patent fall under?
Primary CPC classification C01G37/00. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Aug 08 2017 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).