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Process for depositing alumina onto a substrate and alumina regeneration

Assignee: Pechiney SA
•
Filing: 1976-11-24
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Granted: 1981-06-30
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Expires: 1996-11-24
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Abstract

Abstract A process for the concurrent deposition and regeneration of alumina onto a substrate from an aqueous sodium aluminate solution comprising immersing the substrate in an aqueous sodium aluminate solution of which the composition is controlled and adjusted by passage through a regeneration circuit where alumina is added to make up for the quantity deposited. The invention may be used in the production of adsorbents for the lead present in the exhaust gases of internal combustion engines.

Inventors

  • 👤 Bernard P. H. Hue
  • 👤 Henri A. Mercier

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-09 09:47
CPC Classifications
B; B01; B01J; B01J37/00; B01J37/02; B01J37/03; B01D; B01D53/00; B01D53/02; B01J20/00; B01J20/02; B01J20/0203; B01J20/0218; B01J20/0225; B01J20/0229; B01J20/04; B01J20/041; B01J20/06; B01J20/08; B01J20/30; B01J20/3078; B01J20/32; B01J20/3202; B01J20/3204; B01J20/3231; B01J20/3234; B01J20/3236; B01J20/34; B01J20/3433; C; C23; C23D; C23D5/00; C23D5/10

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 195 words
A process of concurrently depositing and regenerating alumina for physical deposition on a metal substrate consisting essentially of immersing the substrate in a circulating aqueous bath solution of alkali metal aluminate containing about 62 g of Na 2 O per liter and approximately 96 g of Al 2 O 3 per liter; agitating and heating the bath to a temperature of 80° to 100° C., the agitation insuring homogeneity of the bath; maintaining the bath rejuvenated by evaporating the aluminate solution to concentrate the same as to bring the Na 2 O content to 280-290 g per liter, condensing the evaporated water and returning the water condensate to the aluminate bath, heating the concentrated aluminate solution close to to its boiling point and adding alumina to regenerate the same, filtering the regenerated aluminate solution to remove any deposits of impurities and to eliminate any decomposition seeds from the regenerated aluminate solution, adding water in a quantity substantially equivalent to that which has been evaporated and necessary for keeping the concentration of the aluminate solution at 62 g of Na 2 O per liter, and returning the thus regenerated aluminate solution to the original aluminate solution.
Claim 2
Dependent Claim 195 words
A process of concurrently depositing and regenerating alumina for physical deposition on a metal substrate consisting essentially of immersing the substrate in a circulating aqueous bath solution of alkali metal aluminate containing about 62 g of Na 2 O per liter and approximately 96 g of Al 2 O 3 per liter; agitating and heating the bath to a temperature of 80° to 100° C., the agitation insuring homogeneity of the bath; maintaining the bath rejuvenated by evaporating the aluminate solution to concentrate the same as to bring the Na 2 O content to 280-290 g per liter, condensing the evaporated water and returning the water condensate to the aluminate bath, heating the concentrated aluminate solution close to to its boiling point and adding alumina to regenerate the same, filtering the regenerated aluminate solution to remove any deposits of impurities and to eliminate any decomposition seeds from the regenerated aluminate solution, adding water in a quantity substantially equivalent to that which has been evaporated and necessary for keeping the concentration of the aluminate solution at 62 g of Na 2 O per liter, and returning the thus regenerated aluminate solution to the original aluminate solution.
Claim 3
Dependent Claim 14 words
A process according to claim 1 wherein the alkali metal aluminate is sodium aluminate.
Claim 4
Dependent Claim 17 words
A process according to claim 1 wherein the temperature of the bath is from about 88°±2° C.
Claim 5
Dependent Claim 21 words
A process according to claim 1 wherein the substrate is maintained in the bath from about 5 to about 40 hours.
Claim 6
Dependent Claim 39 words
A process according to claim 1 wherein the substrate is a metal wool of ferritic stainless steel to be utilized as an adsorbent of lead present in the exhaust gases of an internal combustion engine in a clean-air catalyst.
Claim 7
Dependent Claim 30 words
A process according to claim 1 wherein said substrate is heated under calcining conditions to a temperature of 530°-550° C. subsequent to removal from the bath to obtain anhydrous alumina.

References Cited (Backward Citations)

US2791516A Cited
US2941902A Cited
US3025188A Cited
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US3231520A Cited
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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-06-29 1984-12-29 1985-06-30 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-06-29 1988-12-29 1989-06-30 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-06-29 1992-12-29 1993-06-30 $7700.00 Window Closed / Lapsed

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