Copper cha zeolite catalysts

US2016101411A1 · US · A1

Patent metadata
FieldValue
Publication numberUS-2016101411-A1
Application numberUS-201514973353-A
CountryUS
Kind codeA1
Filing dateDec 17, 2015
Priority dateFeb 27, 2007
Publication dateApr 14, 2016
Grant date

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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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Abstract

Official abstract text for this publication.

Zeolite catalysts and systems and methods for preparing and using zeolite catalysts having the CHA crystal structure are disclosed. The catalysts can be used to remove nitrogen oxides from a gaseous medium across a broad temperature range and exhibit hydrothermal stable at high reaction temperatures. The zeolite catalysts include a zeolite carrier having a silica to alumina ratio from about 15:1 to about 256:1 and a copper to alumina ratio from about 0.25:1 to about 1:1.

First claim

Opening claim text (preview).

1 - 17 . (canceled) 18 . A catalyst comprising a copper ion-exchanged aluminosilicate zeolite having a CHA crystal structure, the zeolite having a mole ratio of silica to alumina from about 20 to about 40 and an atomic ratio of copper to aluminum from about 0.25 to about 0.50. 19 . The catalyst according to claim 18 , wherein the catalyst contains ion-exchanged copper and an amount of non-exchanged copper sufficient to maintain NOx conversion performance of the catalyst in an exhaust gas stream containing nitrogen oxides after hydrothermal aging of the catalyst. 20 . The catalyst according to claim 18 , wherein the mole ratio of silica to alumina is about 25 to about 40. 21 . The catalyst according to claim 18 , wherein the mole ratio of silica to alumina is about 25. 22 . The catalyst according to claim 18 , wherein the mole ratio of silica to alumina is about 26. 23 . The catalyst according to claim 18 , wherein the mole ratio of silica to alumina is about 27. 24 . The catalyst according to claim 18 , wherein the mole ratio of silica to alumina is about 28. 25 . The catalyst according to claim 18 , wherein the mole ratio of silica to alumina is about 29. 26 . The catalyst according to claim 19 , wherein the mole ratio of silica to alumina is about 30. 27 . The catalyst according to claim 19 , wherein the zeolite having the CHA structure is SSZ-13. 28 . The catalyst according to claim 18 , wherein the atomic ratio of copper to aluminum is about 0.30. 29 . The catalyst according to claim 18 , wherein the atomic ratio of copper to aluminum is about 0.33. 30 . The catalyst according to claim 18 , wherein the atomic ratio of copper to aluminum is about 0.38. 31 . The catalyst according to claim 18 , wherein the atomic ratio of copper to aluminum is about 0.44. 32 . The catalyst according to claim 18 , wherein the atomic ratio of copper to aluminum is about 0.46. 33 . The catalyst according to claim 18 , wherein the atomic ratio of copper to aluminum is about 0.40. 34 . The catalyst according to claim 18 , further comprising a binder. 35 . The catalyst according to claim 34 , wherein the binder is ZrO 2 . 36 . The catalyst according to claim 19 , wherein the zeolite contains at least about 2.00 weight percent copper, expressed as copper oxide. 37 . An exhaust gas treatment system comprising the catalyst of claim 18 and further comprising a catalyzed soot filter. 38 . The exhaust gas treatment system of claim 37 , wherein said catalyzed soot filter is upstream of said catalyst. 39 . The exhaust gas treatment system of claim 37 , further comprising a diesel oxidation catalyst. 40 . The exhaust gas treatment system of claim 39 , wherein the diesel oxidation catalyst is upstream of the catalyst comprising the zeolite having the CHA crystal structure. 41 . A catalyst article comprising a substrate having deposited thereon the catalyst according to claim 18 . 42 . The catalyst article according to claim 41 , wherein the substrate is metal or ceramic. 43 . The catalyst article according to claim 42 , wherein the substrate is a honeycomb substrate. 44 . The catalyst article according to claim 43 , wherein the honeycomb substrate is a flow through substrate. 45 . The catalyst article according to claim 43 , wherein the honeycomb substrate is a wall flow substrate.

Assignees

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Classifications

  • Wall flow filters · CPC title

  • Copper and noble metals · CPC title

  • Processes characterised by a specific catalyst · CPC title

  • Ammonium compounds · CPC title

  • Other types characterised by their X-ray diffraction pattern and their defined composition {(C01B39/023, C01B39/026, C01B39/06 take precedence)} · CPC title

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What does patent US2016101411A1 cover?
Zeolite catalysts and systems and methods for preparing and using zeolite catalysts having the CHA crystal structure are disclosed. The catalysts can be used to remove nitrogen oxides from a gaseous medium across a broad temperature range and exhibit hydrothermal stable at high reaction temperatures. The zeolite catalysts include a zeolite carrier having a silica to alumina ratio from about 15:…
Who is the assignee on this patent?
Basf Corp
What technology area does this patent fall under?
Primary CPC classification B01J29/723. Mapped technology areas include Operations & Transport.
When was this patent published?
Publication date Thu Apr 14 2016 00:00:00 GMT+0000 (Coordinated Universal Time) (A1). 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).