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US4663137A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for producing cerium oxide particulates

Assignee: Rhone Poulenc Specialites Chimiques
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Filing: 1985-02-20
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Granted: 1987-05-05
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Expires: 2005-02-20
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Abstract

Abstract Morphologically improved cerium oxide particulates useful, e.g., as catalysts/catalyst supports, and having a B.E.T. specific surface of at least 85±5 m 2 /g, measured at a temperature ranging from 350° C. to 450° C., are prepared by hydrolyzing an aqueous solution of a cerium (IV) salt in an acidic medium, filtering the precipitate of hydrolysis which results, washing and optionally drying said precipitate, and then calcining same.

Inventors

  • 👤 Jean-Yves Chane-Ching
  • 👤 Jean-Yves Dumousseau

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 19:11
CPC Classifications
C; C01; C01F; C01F17/00; B; B01; B01J; B01J23/00; B01J23/10; C01F17/20; C01F17/206; C01F17/224; C01F17/235; C01F17/276; C01P; C01P2002/00; C01P2002/70; C01P2002/77; C01P2004/00; C01P2004/01; C01P2004/03; C01P2004/30; C01P2004/32; C01P2006/00; C01P2006/12; C01P2006/13

Claims Analysis

Total Claims: 18
Claim 1
Independent Claim 68 words
A process for the preparation of ceric oxide particulates having a B.E.T. specific surface of at least 85±5 m 2 /g, measured at a temperature ranging from 350° C. to 450° C., comprising hydrolyzing an aqueous solution of a cerium (IV) salt in a nitric acid medium, filtering the precipitate of hydrolysis which results, washing in an organic solvent and optionally drying said precipitate, and thence calcining same.
Claim 2
Dependent Claim 68 words
A process for the preparation of ceric oxide particulates having a B.E.T. specific surface of at least 85±5 m 2 /g, measured at a temperature ranging from 350° C. to 450° C., comprising hydrolyzing an aqueous solution of a cerium (IV) salt in a nitric acid medium, filtering the precipitate of hydrolysis which results, washing in an organic solvent and optionally drying said precipitate, and thence calcining same.
Claim 3
Dependent Claim 30 words
The process as defined by claim 1, said aqueous solution of a cerium (IV) salt comprising an aqueous solution of ceric nitrate or an aqueous solution of ammonium ceric nitrate.
Claim 4
Dependent Claim 28 words
The process as defined by claim 1, wherein the concentration of cerium salt in said solution, expressed as cerium (IV), ranges from 0.3 to 2 moles per liter.
Claim 5
Dependent Claim 16 words
The process as defined by claim 1, said medium of hydrolysis comprising distilled or de-ionized water.
Claim 6
Dependent Claim 21 words
The process as defined by claim 1, said medium of hydrolysis having an acidity ranging from 10 -2 to 1.0 N.
Claim 7
Dependent Claim 15 words
The process as defined by claim 5, said acidity emanating from the commencement of hydrolysis.
Claim 8
Dependent Claim 19 words
The process as defined by claim 5, said acidity emanating by nitric acid addition to the medium of hydrolysis.
Claim 9
Dependent Claim 16 words
The process as defined by claim 5, said acidity emanating by addition of a ceric nitrate.
Claim 10
Dependent Claim 22 words
The process as defined by claim 8, said ceric nitrate solution added having an acidity of from 0.3 N to 1 N.
Claim 11
Dependent Claim 42 words
The process as defined by claim 1, wherein the amount of the aqueous solution of cerium (IV) salt and the medium of hydrolysis is such that the equivalent final concentration of cerium (IV) therein ranges from 0.2 to 0.8 mole per liter.
Claim 12
Dependent Claim 23 words
The process as defined by claim 1, wherein the temperature of the hydrolysis reaction medium ranges from about 70° C. to 100° C.
Claim 13
Dependent Claim 19 words
The process as defined by claim 1, wherein the temperature of the hydrolysis reaction medium is its reflux temperature.
Claim 14
Dependent Claim 33 words
The process as defined by claim 11, wherein the temperature of the hydrolysis reaction medium is maintained for from 1 to 24 hours following addition of the solution of the cerium (IV) salt.
Claim 15
Dependent Claim 18 words
The process as defined by claim 1, said precipitate being washed at least once with an organic solvent.
Claim 16
Dependent Claim 14 words
The process as defined by claim 14, said organic solvent comprising ethanol or isopropanol.
Claim 17
Dependent Claim 34 words
The process as defined by claim 1, said calcining being carried out at a temperature of from 300° C. to 600° C. for a period of time of about 30 minutes to ten hours.
Claim 18
Dependent Claim 17 words
The process as defined by claim 16, said calcining temperature ranging from 350° C. to 450° C.

References Cited (Backward Citations)

SU833525A1 Cited
US4529410A Cited
EP0033843A1 Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1990-05-04 1990-11-03 1991-05-05 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1994-05-04 1994-11-03 1995-05-05 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1998-05-04 1998-11-03 1999-05-05 $7700.00 Window Closed / Lapsed

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